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TW201142104A - Impulse type shock wave fast dyeing machine - Google Patents

Impulse type shock wave fast dyeing machine Download PDF

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Publication number
TW201142104A
TW201142104A TW99116240A TW99116240A TW201142104A TW 201142104 A TW201142104 A TW 201142104A TW 99116240 A TW99116240 A TW 99116240A TW 99116240 A TW99116240 A TW 99116240A TW 201142104 A TW201142104 A TW 201142104A
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Taiwan
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nozzle
tube
disposed
downstream
passage
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TW99116240A
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Chinese (zh)
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TWI439595B (en
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Zhao-Cheng Jiang
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Zhao-Cheng Jiang
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Abstract

An impulse type shock wave fast dyeing machine utilizes high speed airstream ejected by a co-constructed spray nozzle to drive textiles that does not only perform the free expansion moving with full width and fully generate periodic intense flutter, but also disperses the hydraulic atomized grains or micro-particles or single-molecular dyes or an treatment agent in tremendous high speed airstream by the impact effect principle. The fabric textiles 3 are directly hit to repeatedly and continuously produce powerfully elastic collision and non-elastic collision and shock wave effect on the surface of the fabric textiles 3. It does not only goad the dyes or the treatment agent to obtain the energies of speed-up permeation and fast diffusion on the fabric textiles 3, but also facilitates transforming the non-active molecules, which absorb enough energies, into activated molecules. A great quantity of high energy particles produced from high speed airstream can also be treated with anhydrous processing by utilizing corona discharge effect, thereby achieving the purpose of fast cleaning production.

Description

201142104 六、發明說明: 【發明所屬之技術領域】 本發明涉及一種衝動式爆震波快速染色機,簡稱爆震波染色機,其係 由噴霧式可開幅氣力振動加速染色機所改良的機型,屬於高效率、多功能、 多用性、環保型之染色與加工處理機。 【先前技術】 在節能減碳呼聲中,為了降低全球氣候暖化及變遷的衝擊,促使許多 ® 特殊加工技術領域應用於纖維織物加工處理上,其中爆震波、電化學、低 溫等離子技術、二氧化碳超臨界流體技術、生物酶加工技術、超聲波、輻 射能、微波…等清潔染整加工技術以其方便、迅速、有效、安全以及適用 性廣、節約染料、降低環境汙染、節約能源和便於實現電子計算機控制的 自動化等_ ’目前均在世界各地積極發展巾。但是,大部分的技術發展 方向,均朝單一性、專用型機種為發展主流,有關多功能、一機多用性的 _ 高效率環保型機種,迄今還未有所聞。因此,更激勵了前項發明案「喷霧 式氣力開幅振動加速染色機」〔註:該案以獲得二十餘國發明專利其中包 括中華民國(申請日:1997/2/25、申請號:86102237)、中國大陸(申請日: 1997/04/29、申請號:Zl97 1 82145.3)、美國(申請日:1997/03/31、申請號: 828,884)加拿大(申請曰:1997/04/29、申請號:2,288,214)、歐盟(申請曰: 1997/4/29、申請號:97917988.4)、印度(申請日:1997/5/28、申請號: 1126/MAS/97)、曰本(申請曰:1997/4/29、申請號:10546452)、韓國(申請 曰:1999/10/28、申請號:997009996)等〕,再度有了更明確更具體更 堅定的改善方向和創新動力來源,為期盼能以更完善的新思維及理念參與 201142104 節能減碳,以協助染整產業在急迫的時刻中,順利達成清潔生產目標。 眾所周知,紡織品染整生產一直是以水為介質進行各種濕處理加工, 歷來是工業生產巾的汙雜放大戶之―,在全;械化魏—再升高的壓力 下,同時也迫使國際紡織品市場掀起綠色旋風,這意味著環保紡織品將成 為未來產品之主要訴求,相反的,對不易制環保技術水平的染整產業而 言’無疑是件嚴峻的挑戰。為了確保染整產紐得永續發展,以長遠觀點 來看,採用清潔的生產技術或設施已被認為是唯一途徑。 事實上,氣候暖化及變遷的問題已到了刻不容緩的地步,對染整產業 而言’更須減腳步賴的思維及無加以_,重败換新設施或建立 新製程及新方法為目標。 因此’本發明為了達到更佳的節能、節水、清潔生產設施,特別將纖 維織物與㈣或處理鑛聚集巾在高能職動場巾,以促進所有參與的反 應物,均能在極短時_及在有限哺财,藉由高能的絲場侧,、帶 來更快速及更纽率的加讀理,同耗概溫轉子體之纽技術領域 也涉入於本發明中’以便促使纖_物在某些加^序中,除了達到無水 加工之目的外S可以獲得更佳、更寬廣的卫軸作空間和獲得最佳的產 品處理效果。 目前染整生產設施,大多仍是以單向性(註:是指在—個時間内不能同 時處理其他工序作業者)的濕加工為线,*但_大量的水,也同時浪費 大量的能源’並且嚴重汙純境,其處高亦造成不必要的難 損失,也帶給生態極大的危害。 θ 目前纺織品市場均傾向少量、多樣、多雜、精緻的清潔生產為訴求 201142104201142104 VI. Description of the Invention: [Technical Field] The present invention relates to an impulse detonation wave fast dyeing machine, referred to as a detonation wave dyeing machine, which is a machine improved by a spray type openable pneumatic vibration accelerating dyeing machine. It is a dyeing and processing machine with high efficiency, versatility, versatility and environmental protection. [Prior Art] In the energy-saving and carbon-reduction call, in order to reduce the impact of global warming and change, many of the special processing technologies are applied to the processing of fiber fabrics, including detonation wave, electrochemical, low-temperature plasma technology, and carbon dioxide super Clean fluidization and processing technologies such as critical fluid technology, biological enzyme processing technology, ultrasonic, radiant energy, microwave, etc. are convenient, rapid, effective, safe and applicable, saving dyes, reducing environmental pollution, saving energy and facilitating the realization of electronic computers. Control automation, etc. _ 'There are currently active development of towels around the world. However, most of the technological development directions are mainly for the development of single-purpose and special-purpose models. The versatile and multi-purpose _ high-efficiency and environmentally-friendly models have not been heard so far. Therefore, it has further motivated the "Injection-type pneumatic open-end vibration accelerating dyeing machine" of the previous invention [Note: The case obtained more than 20 invention patents including the Republic of China (application date: 1997/2/25, application number: 86102237), Mainland China (application date: 1997/04/29, application number: Zl97 1 82145.3), United States (application date: 1997/03/31, application number: 828,884) Canada (application number: 1997/04/29, Application No.: 2,288,214), EU (application number: 1997/4/29, application number: 97917988.4), India (application date: 1997/5/28, application number: 1126/MAS/97), transcript (application: 1997/4/29, application number: 10546452), South Korea (application number: 1999/10/28, application number: 997009996), etc., once again have a clearer, more specific and firmer direction of improvement and source of innovation, for a period of time Hope to participate in 201142104 energy-saving and carbon reduction with more perfect new thinking and ideas, to help the dyeing and finishing industry to achieve clean production goals in an urgent moment. As we all know, textile dyeing and finishing production has always been carried out with water as a medium for various wet processing, which has always been the pollution-producing household of industrial production towels. Under the pressure of full and mechanical Wei-re-emerging, it also forces international textiles. The market has set off a green whirlwind, which means that environmentally friendly textiles will become the main appeal of future products. On the contrary, it is undoubtedly a serious challenge for the dyeing and finishing industry that is not easy to make environmental protection technology. In order to ensure the sustainable development of dyeing and finishing, in the long run, the adoption of clean production techniques or facilities has been considered the only way. In fact, the problem of climate warming and change has reached an urgent point. For the dyeing and finishing industry, it is even more necessary to reduce the mentality and lack of reliance on the new facilities or new processes and new methods. Therefore, in order to achieve better energy-saving, water-saving, and clean production facilities, the invention particularly in the case of fiber fabrics and (4) or processing mineral gathers in high-energy field wipes to promote all participating reactants, can be in a very short time _ And in the limited feeding, with the high-energy silk field side, bringing faster and more favorable rate reading, the technical field of the same-temperature temperature rotor body is also involved in the invention 'in order to promote the fiber _ In some additions, in addition to achieving the purpose of waterless processing, S can obtain a better and wider space for the axis and obtain the best product treatment effect. At present, most of the dyeing and finishing production facilities are still unidirectional (Note: refers to those who can not handle other process operators at the same time) as a line, * but _ a large amount of water, but also a large amount of energy is wasted 'And it is seriously polluted, and its high position also causes unnecessary hard loss, and it also brings great harm to the ecology. θ At present, the textile market tends to be small, diverse, complex, and delicate for clean production. 201142104

V 方向因此’批量(間歇式)環保型染色設施將成為生產主流,對一般習用的 没施而言,無論是無式、束幅式的氣流染色機或是較傳統时射式液流 染色機’對織物進行染色或其他加工處理時還有些問題迄今仍絲能獲得 有效解決例如.再雛料、左右異色前後異色以及其他線條痕等等 不均染、動力帶布輪與作動喷嘴之間速度未同步、布速移動速度不夠快、 擦傷或碰撞及勾紗、作動喷嘴之射喷作用力過大使織物纖維發生斷紗、喷 嘴及過濾器於處理過程中容易造成阻塞的問題,或是布身未達到豐厚感、 生物酶處辦鱗*佳、處料間太慢、設施魏*足使加卫工序受到限 制、能源使用過大的問題和水f源過度浪費的問題而造成大量的汗水處 理成本’也會因為動力帶布輪的設施,而造成公安問題,或是手感不佳的 問題然而上述提及的各種問題中,除了人為的疏失外,絕大多數是因為 設施設計製造不良所引起的,其巾主要均發生在於纖_物與染液或 處理液與空氣流進行作功及熱傳分佈不均所造成的,例如管差異色就是由 春多管的處理槽設施中所發生的,因為一般習用染色機均為多槽型所構成, 因此,在染液或空氣流的分配方法也都採用一分為二,再分為四再分為 八的方式完成分支式佩的健,其最大缺點為分割造成過多之τ形接頭, 依據流體動力學上的探討,流體難於精峰分成兩個鱗之—半,在引進管 路上會有任何偏向-邊之情形,誤差將越分越大,並導致原來設定的流量 產生變化’並且因分流不均所造成的不均關題,依絲能解決。因此, 為了達到理想清錄整生產目標,±述這朗題有必要同時解決,因為每 當問題發生時所造成重修、重染的過程,都會帶來更大量能源及水資源的 耗費,同時也會増加生產成本的負荷。 201142104 追麟色理論發展迄今,大多數染色理論被認為,染料對纖維的上染 過程可分為以下四個階段: i染料在驗情染液流動逐漸靠近纖維界面嘴階段染料的性質和 狀態與上染性能基本無關’無論是溶解態的染料分子還是懸浮態的 染料顆粒都-樣隨染液流動,其遷移速度決定於染液流速。 2·由於液體與纖維界面存在難以流動的動力邊界層(滯流層),染料進 入動力邊界層及靠近齡表面到—定距離前,主要靠自身的擴散接 近纖維。這階段染料的遷移速度不僅和染液流速有關,還和染料的 擴散速度有關,溶娜_料分子比料態及聚錢的雜擴散快 的多,因此,染料的溶解度和分散狀態對這階段染料的遷移速度有 較大的影響。 3·染料擴散到距纖維表面一定距離後’染料與纖維之間存在足夠大的 分子作用力,染料被迅速吸附到纖維表面。這個階段染料的遷移速 度’主要取決於染料分子與纖維分子的結構和性能,即染料與纖維 之間的作用力,也和界面溶液的性質有關,其中染料的溶解度和分 散狀態有較大影響。所以,此階段染料與纖維之間作用力越大,染 料溶解愈好,吸附速度越快。 4.染料被吸附到纖維表面之後,在纖維内外產生染料濃度差或内外染 料化學位差’由菲克定律(Fick’s law)可知,染料將從纖維表面向纖 維内部擴散遷移。這時的遷移速度主要取決於纖維的化學及物理微 結構,也和染料分子結構及濃度有關。纖維無定形區的比例大,孔 隙大或自由容積大’纖維表面染料濃度高,染料向纖維内遷移速度 201142104 就快。因此,此階段染料的遷移速度直接和纖維被溶脹或增塑程度 以及染料在纖維表面的漠度有關。 由上述可知,上染速度除了決定於染料和纖維的分子結構外,還和染 料在溶液巾的轉度及麟脹或增塑程度有關。事實上,雜與纖維 之間的相互作用關係,並非需要大量工作液才能獲得溶解或快速上染,倘 若在進行染色時,使染料溶解在過量的工作液中,同時會受到過量的工作 液阻斷祕錢理猶齡在短雜的接賴會,使纽接觸機率變少 外,也失去快速上染或處理的目的,它還會使絕大多數輸入能量轉換為工 作液分子的旋轉動能,以及來自工作液分子内部各個原子振動的能量,此 外,還有功液分子之間會職與上染或加工處理無關的各種相互作用力。 為了使染料在染色時有一定的溶解度,在合成生產染料時總是在染 料分子中引人數量的極性基’以增加染料的溶解度。但引人水溶性離 子基後’除了少數情況下可提高祕和纖維的結合外,在完成上染過程後 反而會帶來許Μ題’例如在纖維上通過水化溶解降低_品的染色濕牢 度’染液巾絲的水雜祕很難脫色淨化處理,給汙水處理增加困難等。 對於難溶性的分散染料來說,其分子中不具有離子基團,在常壓1〇〇 c下由於溶解度低,纖維溶脹或增塑程度低,上染速度很慢,很難進行 木色而J1作液巾的染料,必須依靠大量的分散劑幫助,才能呈懸浮體狀 刀放於工作液巾’這樣不但需要大量的分制懸浮體的穩定性也不容易 保持’並會對染色和汙水處理都帶來問題。因此,適當提高分散染料的溶 解度,不僅減少分散臟不用分散舰可轉持祕錄穩定性,還有利 於上染。 m. 9 201142104 而對於疏水性的合賴維來說,在水巾报難溶脹,因絲料在纖維内 擴散也雜’通巾染色需魏高的溫度’例如聚目旨齡必須在高溫高壓染 色溫度達靴’若能增加這些纖維的溶脹或增塑程度就可加快染料在纖 維中的擴散速度,或降低染色溫度。 另外有天賊,較_,由於魏結構_,容㈣成極多空腔 並充滿空氣,因此當溶液滲入時不易產生相對運動,即會發生滞留現象而 導致染料不易滲人,因此通常需要較長_間才能獲得上染;而羊毛纖維 則由於其表面存在鱗片層,對染料上染有储侧,習用染色通常需達到 沸染的方絲進行,染色_也較長,因此,純減大,對麟損傷大。 另外,由於反雜祕通常在高溫及祕驗巾讀錢纽應,使反應 性染料的染著效率降低…般染色結束後,染色殘液中染料未吸盡,或染 色織物在後處理中洗下來的浮色,這都會造成嚴重的水汗染。 總之,染料上染纖_首要條件之—是_必須紅作液中溶解,只 有分解成單分子狀的染料才能迅速吸附於纖維,並擴散進入纖維内部,染 料晶體顆粒和體積較大義料聚集體是無法擴散進人纖軸部,如果利用 本發明所「高能波誠高鎌子職生的_力學_」,就能在極小 液量、高濃度的工作液中提高難溶細溶解度,加快纖維對染料的吸附 速度’又對_繪伽_,加_梅巾峨散速度,從而 可以加快整個上魏度。只要選關畴與_分子有較高的結合力,則 不僅有很好的上染力’而且有較高的染色牢度。 所以’為了提高祕速率,馳染色時間,除了降低用水量外,選擇 適用的染色設備’加強染液與織娜目對運動及選擇好纖維翻的染料, 201142104 配套染色助劑、染色介質之外’纖維織物本身的化學結構及物理微結構也 是必須考慮的關鍵因素。若纖維織物預先經過良好的前處理或改性預處理 或同時進行邊改性—邊染色,加快染料向纖維表面吸附速度及向纖維内 部擴散速度,就可以大幅提高染色速度,縮短染色_或降低染色溫度, 提高生產效率、達到節能減碳的清潔生產之目的。 【發明内容】 本發明所稱的爆震波染色機,是指錢色或其他加卫處理時其可利 用一共構式喷嘴_规域個,促錢液、處魏或歧溫等離子體, 紐他處理介質...等,均能分散在高速輕中賊維織物形成齊頭 齊^的方式針在-個高能義場的領域巾,讓所有倾的反應物都能 獲得所需的活化能(aetivatiQn啊y),進而在最短的時_,_最經濟的 清潔生產目的。Therefore, the V-direction (bulk (intermittent)) environmentally-friendly dyeing facility will become the mainstream of production. For general use, whether it is a non-type, beam-type airflow dyeing machine or a more traditional time-flow liquid dyeing machine 'There are still some problems in dyeing or other processing of fabrics. So far, it can be effectively solved, for example, the unevenness of the material, the color difference before and after the different colors, and other line marks, etc., the speed between the power belt cloth wheel and the actuating nozzle. Unsynchronized, fast speed of cloth speed, scratches or collisions, and hooking, excessive jetting force of the nozzle, causing yarn breakage of the fabric fibers, nozzles and filters are likely to cause blockage during processing, or cloth body It does not reach a sense of richness, the scale of the enzymes is good, the space between the materials is too slow, the facilities are weak, the maintenance process is limited, the energy use is too large, and the water source is excessively wasted, resulting in a large amount of sweat treatment costs. 'There will be public security problems or poor hand feelings due to the power belt pulley facilities. However, in addition to the man-made mistakes, Most of them are caused by poor design and manufacturing of the facilities. The main causes of the towels are caused by the interference between the fiber and the dye solution or the treatment liquid and the air flow, and the uneven distribution of heat transfer. In the multi-tube treatment tank facility, since the conventional dyeing machine is composed of a multi-groove type, the method of distributing the dye liquor or the air stream is also divided into two, and then divided into four sub-divided. Eight ways to complete the branch-type Pei Jian, its biggest disadvantage is that the division causes too many τ-shaped joints. According to the fluid dynamics discussion, the fluid is difficult to divide the peak into two scales - half, there will be any bias in the introduction pipeline - In the case of the side, the error will be more and more divided, and the original set flow will change, and the unevenness caused by the uneven flow can be solved by the wire. Therefore, in order to achieve the goal of ideal inventory and production, it is necessary to solve this problem at the same time, because the process of rebuilding and re-dying every time the problem occurs will bring more energy and water resources, and also Will increase the load of production costs. 201142104 The development of chasing color theory So far, most dyeing theories are believed that the dye-to-fiber dyeing process can be divided into the following four stages: i dyes in the test dye liquor flow gradually approaching the fiber interface mouth stage dye properties and state and The dyeing performance is basically irrelevant 'whether the dissolved dye molecules or the suspended dye particles flow with the dye solution, and the migration speed is determined by the dye liquor flow rate. 2. Since there is a hard-flowing kinetic boundary layer (stagnation layer) at the interface between the liquid and the fiber, the dye enters the kinetic boundary layer and close to the surface of the age to a certain distance, and is mainly close to the fiber by its own diffusion. The migration speed of the dye at this stage is not only related to the flow rate of the dye solution, but also related to the diffusion speed of the dye. The dissolution of the material is much faster than that of the material state and the money. Therefore, the solubility and dispersion state of the dye are at this stage. The migration speed of the dye has a large influence. 3. The dye diffuses to a certain distance from the surface of the fiber. There is a large enough molecular force between the dye and the fiber, and the dye is quickly adsorbed onto the surface of the fiber. The migration speed of the dye at this stage depends mainly on the structure and properties of the dye molecules and the fiber molecules, that is, the interaction between the dye and the fiber, and also on the properties of the interface solution, in which the solubility and dispersion state of the dye have a large influence. Therefore, the greater the force between the dye and the fiber at this stage, the better the dye dissolves and the faster the adsorption speed. 4. After the dye is adsorbed to the surface of the fiber, a difference in dye concentration inside or outside the fiber or a chemical difference between the inside and outside of the dye is produced. As is known from Fick's law, the dye will diffuse from the surface of the fiber to the inside of the fiber. The rate of migration at this time depends mainly on the chemical and physical microstructure of the fiber and also on the molecular structure and concentration of the dye. The proportion of the amorphous region of the fiber is large, the pore size is large or the free volume is large, and the dye concentration on the fiber surface is high, and the migration speed of the dye into the fiber is as fast as 201142104. Therefore, the rate of migration of the dye at this stage is directly related to the degree of swelling or plasticization of the fiber and the indifference of the dye on the surface of the fiber. From the above, it can be seen that the dyeing speed is determined not only by the molecular structure of the dye and the fiber, but also by the degree of rotation of the dye in the solution towel and the degree of swelling or plasticization. In fact, the interaction between the fibers and the fibers does not require a large amount of working fluid to obtain dissolution or rapid dyeing. If the dye is dissolved in an excess of working fluid during dyeing, it will be subjected to excessive working fluid resistance. The secret of the money is still in the short-term connection, which makes the contact probability of the New Zealand less, and also loses the purpose of rapid dyeing or processing. It also converts most of the input energy into the rotational kinetic energy of the working fluid molecules. And the energy from the vibration of each atom in the working fluid molecule, in addition, there are various interaction forces that are not related to the dyeing or processing of the working fluid molecules. In order to impart a certain solubility to the dye during dyeing, a number of polar groups are always introduced in the dye molecules during the synthesis of the dye to increase the solubility of the dye. However, after introducing a water-soluble ionic group, it can improve the binding of secret fibers and fibers in a few cases, but after the completion of the dyeing process, it will bring about a problem. For example, the syrup is reduced by hydration dissolution on the fiber. The degree of fastness of the dyed liquid towel is difficult to decolorize and purify, and it is difficult to treat sewage. For the poorly soluble disperse dye, there is no ionic group in the molecule, and the solubility is low at normal pressure 1 〇〇c, the degree of swelling or plasticization of the fiber is low, the dyeing speed is very slow, and it is difficult to carry out wood color. J1 as a dye for liquid towel, must rely on a large amount of dispersing agent to be placed in a working liquid towel as a suspension knife. This not only requires a large number of stable suspensions, but also is difficult to maintain and will stain and stain. Water treatment brings problems. Therefore, appropriately increasing the solubility of the disperse dye not only reduces the dispersion of the dirty, but also the stability of the secret transfer, and is also advantageous for dyeing. m. 9 201142104 And for the hydrophobicity of the Laiwei, it is difficult to swell in the water towel, because the silk material spreads in the fiber, and the 'temperature of the towel needs to be high, 'for example, the concentration must be high temperature and high pressure. Dyeing temperature up to the shoe's ability to increase the degree of swelling or plasticization of these fibers can accelerate the diffusion rate of the dye in the fiber, or reduce the dyeing temperature. In addition, there are thieves, more than _, because of the Wei structure _, Rong (four) into a lot of cavities and filled with air, so when the solution infiltrates, it is not easy to produce relative motion, that is, the retention phenomenon will cause the dye to be difficult to infiltrate, so it is usually necessary to compare In the long _ to get the dyeing; while the wool fiber has a scale layer on the surface, the dye is dyed with the storage side, the conventional dyeing usually needs to reach the boiling dyed square wire, and the dyeing _ is also longer, therefore, the pure reduction The damage to the lining is large. In addition, since the anti-hybrid usually reads the money at high temperature and secret rubbing, the dyeing efficiency of the reactive dye is lowered. After the dyeing is finished, the dye in the dyeing residue is not exhausted, or the dyed fabric is washed in the post-treatment. The floating color that comes down will cause severe sweating. In short, dyeing on the dye _ the first condition - is _ must be dissolved in the red liquid, only the dye broken down into a single molecule can be quickly adsorbed to the fiber, and diffused into the fiber, dye crystal particles and larger aggregates It is impossible to diffuse into the fiber shaft portion. If the "_Mechanical_" of the high-energy wave high-grade scorpion is used in the present invention, it is possible to increase the solubility of the hardly soluble solution in the working fluid of a very small liquid amount and a high concentration, and accelerate the fiber pair. The adsorption speed of the dye is also _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ As long as the selection domain has a higher binding force with the _ molecule, it has not only good dyeing power but also high color fastness. Therefore, in order to improve the secret rate, in addition to reducing the water consumption, in addition to reducing the water consumption, choose the appropriate dyeing equipment to enhance the dyeing and weaving of the dye and select the fiber to turn the dye, 201142104 supporting dyeing auxiliaries, dyeing media 'The chemical structure and physical microstructure of the fiber fabric itself are also key factors that must be considered. If the fiber fabric is pre-treated by a good pre-treatment or modification pre-treatment or simultaneously modified and dyed to accelerate the adsorption speed of the dye onto the fiber surface and the diffusion rate into the fiber, the dyeing speed can be greatly improved, and the dyeing can be shortened or reduced. Dyeing temperature, improve production efficiency, and achieve the goal of clean production of energy saving and carbon reduction. SUMMARY OF THE INVENTION The so-called detonation wave dyeing machine of the present invention refers to a co-construction nozzle _ domain, which promotes money liquid, Wei or differential temperature plasma, in the color of money or other processing. The treatment medium, etc., can be dispersed in a high-speed light thief, and the woven fabric is formed in the same manner as the high-energy field, so that all the reactants can obtain the desired activation energy ( AetivatiQn y), and in the shortest time _, _ the most economical clean production purpose.

在加工處理時,共構式喷嘴所喷出的高速流動的空氣、蒸氣、染料、 處理劑、低溫等離子體與_織物發生接觸碰撞時,均可姻正在轉向正 在往下墜_維織物’其所構成_端_,獲得—個較大的衝擊 姊衝動力,進行高效率能量轉換;當在進行過程中,染液和處理液則是 以咖的方式呈細粒狀或微粒狀或是以單分子方式分散在高速的空氣流 中,以直接近距離的方式與正在進行轉向的纖維織物發生衝擊,使 的纖維織物表面連續反覆不斷獲得強力的彈性碰撞(註:是指空氣或— 體)及非彈性碰撞(註:是指工作液或染料或是處理劑還包括等離子、 ^中在料舰撞中时促__得高效糾城料, 外’蝴暢__糊_他崎(ea= 11 201142104 而彈性碰撞則可促使纖維織物的下側端面與反射作用基板間形成一股高速 推動的空氣流外,亦可促使織物的上下端面間的空氣靜壓力發生壓力差, 使織物上側端面上的静壓力大於下側端面的靜壓力,進而促使移動中的纖 維織物在通過反射作動板時,均能利用該壓力差的作用,不斷產生周期性 的強烈波動運動,並可同時進行自由擴布的效果者。 §在進行濕式加工處理時,倘若纖維織物表面所吸附的液膜積量足夠 厚,高速空氣流的速度能量足夠大,即可促使波動中的纖維織物表面邊界 區域產生大量的空穴,引發出爆震波(shock wave)效應。而在乾式操作時, 高速的空氣流也可以利用電暈放電(coronadischarge)或是次輝光放電(gl〇w discharge),使部分高速的空氣流的空氣分子發生電離,來產生高速流動的 低溫等離子體(low temperature plasma),其除了賴物獲得高能粒子的 處理效果外,亦可獲得無水加工處理所帶來更多的生態利益。 在加工處理過程巾,掉落在集布槽⑽麟織物,可以糊動量慣性 的作用力及找流在快速驅離的作訂,所產生_間職侧,引發氣 擊效應’進而產生強力的鶴縣,促賊賴物在掉落集布制過程中, 均能利用擺動的機制’將附著在纖維織物表面上的殘留工作液及剝落的游 離纖維和其他不純_物體’進行強継魏肺分離,及同時完成摺疊 作業’使_織物表_工舰及着_和其他不純固形物體,能直接 由集布槽下财排出σ導人紐勒,經由精密筛絲進行顧和收集, 其可促使集布彻的纖輯物麟較料的狀態,_做_織物在進 行下-循環周期與染液或處理液接觸時,不會受到殘留工作液液膜屏障的 阻擔。經由過濾'的工作液’在循雜送的過程巾,可藉無泵加料裝置,進 12 201142104 行染料或處理劑的補給’使無泵加料裝置内的高溶度溶解染料或處理劑, 均能在循環輸送管的純巾,由加壓循觀浦的吸入口投入 ’使南濃度的 冷解染料或處糊’均能在有限量賴環工作射,獲得極小浴比及高均 度的混σ操作方式。gj此,使纖賴物再度與紐或處職進行接觸時, 均能獲得較高的位能和動能,同時也提高濃度梯度、溫度梯度以及化學親 和梯度’並促進染液或處理液進行快速滲透和擴散效果,所以有利於快速 加工處理之進行;另外除了可促使集布槽内的集疊織物在相互壓擠的作用 ♦力降到最低外’也能促使纖維織物在導布管内在進行快速移動時使所產 生拉張力降到最低。而在操作時,經由加壓循浦加壓的染液或處理液, 可利用輸送管路系統上的交流式液流佈流器的作用,使每一個液壓霧化喷 嘴,均能喷出均壓、均量、均溫、均速的霧化液滴❶ 而經由鼓風機加壓的空氣流’均能利用輸送管路系統上的交流式氣流 佈流裝置’以進行90度轉向形成矩形的佈流,再導入各自的分配管中,氣 流可藉分配管之擴散結構的作用,將運動中的氣流之動能轉變為靜壓力 能,其可促使空氣流在通過每一個氣浮喷嘴及每一個共構式噴嘴時均能 獲得較大的膨脹加速效率及均壓、均量、均溫、均速的分配效果如此除 了可防止纖輯物發生左右異色及獨染造成各式各樣的色花外,亦可促 進所有其他加工處理作業’獲得各式各樣均㈣手敍外觀。在操作時, 處理槽内的回流空氣,亦可利用交流式氣流回流裝置,進行橫向面的八佈 回流,以促使處理槽内部的氣流不致產生過度擾動現象,進而可獲得較穩 定較規律性的循環流動。 本發明特別涉及在導布管下側方橫跨於通路左右側壁間的水平管壁端 ί sa 13 201142104 面上,沿著通路方向,在上游和中游區段上,所設置的氣浮喷嘴及在下游 區段的截斷面上,所設置的-排橫跨於左右兩側壁,以並聯排列組合的共 構式喷嘴’以及在共構式喷嘴口的下游方肖,位於導布管通路出口的下側 方與集布槽上游落布區段入口的内側方空間,所設置的一u型迴轉板而 該u型迴轉板的上游側端以階梯式方式搭接固定在共構式喷嘴口的下側 方,使U型迴轉板上游外側端面構成一平直的反射作用基板在u型迴轉 板的下游外側端面上’位於集布槽上游落布區段的内外側方所設置的一分 離柵網’因此’在進行染色或其他加工處理時,處理制賴環空氣及工 作液和備料桶_液或處雌,可麵各自管路系統與鼓風機和加壓循環 栗浦相互連通’來提供增壓空氣及加歸液或處理液,經由共構式喷嘴喷 出,同時也可使部分的增壓空氣分別經由氣浮喷嘴喷出。在操作時,纖維 織物可借助氣料対出微量的空氣流,便能將_織物雜,使大部分 的動力能#,均難中在共構式喷嘴細,在_迴轉板的作用下,可促 使喷出的同妙氣歧變方向触反向排出,_促使纖輯物獲得強大 的驅動力n在操作時,共構式喷嘴可作域賴環鶴的主要動力 源’其可秉棄傳統式動力帶布輪的運作方式’同時也可改善前案發明的多 k式導向喷嘴’目卫作氣流能量過度分散,以達到高能級的加工處理問 題在操作時’同時可利用共構式喷嘴上所提供的液壓霧化喷嘴機構和電 暈或輝光放電機構’進行相互交變的工序,以獲得相辅相成的處理模式, 使各類纖維織物在進行加工時均可獲得更廣泛,更寬闊的工藝創作空間。 本發明的主要目的在於提供一種衝動式爆震波快速染色機在進行染 色或其他加工處理過程時’纖維織物可依照加工工藝需求利用共構式嗔嘴 201142104 喷出高速濕熱或乾熱的空該、高速均勻分散㈣料分子、高速均勻分散 處理液分子、高速流動·溫等離子體,或是其他高速均句分散的微粒子, 使所有的噴出介質’均能形成齊⑽方式集中在—個高能量的波動場中與 纖維織物反覆;ί;斷的發生碰撞,使得這些料的反應物與纖維織物,在極 短時p以财序的運動方式進行高鱗的能量健除了能使所有參 與的反應物,魏獲得所需要的活魏量之外,概做纖_物在最短 的時間’以最節能、最省水、最少義料、最少的處理劑之下,獲得清潔 生產為目的。 本發明的主要目的在於提供—種衝動式爆震波快速染色機在進行染 色或其他加J1處理時’其可藉由強力的波動侧或經波動所引發的爆震 波效應,促錢液或處理液形成低黏度、低阻力、高位能、高渗透高擴 散性的環境下與纖_物進行小液量、高濃度、高效力的濕加卫處理目的 者。本發撕說轉驗效應,是賊賴物在進行加卫處辦可以利 用间速空氣流的制產生高能級麟,在波_過程巾波峰區域會形成一 壓縮區’而在波谷域則形成—稀疏^進而促使纖輯物表面積上的 任何-質點’持、續不斷發生錢的魏區和顧區的波動錢動的壓縮 區内’會促使該區域的纖維織物表面外_空氣分子之平均距離縮短密 度變大,而在稀内,找分子的平均距離會增大,密度聰小,倘若 纖維織物㈣驗紐度足触,離生的波動力足触,其會使纖維織 物表面所_的i條分子同樣受__與稀疏區較變侧當稀疏 區負壓力降低達_和蒸汽壓之臨界值以下時,工作液分預的平=距離 就會增大到超過紐距離,從而破壞工分子或賊_物之間引力結 15 201142104 構的完整性,因此,導致纖維織物表面及纖維内外孔隙或纖維組織内外間 隙區域引發空穴(是指一種非常微小的空泡核),而一旦空穴形成,會一直 增長至負壓力達到極大值,導致生成大量的空化泡(註:是指一種密度極低 的蒸氣泡或空氣泡),而當相繼而來的壓縮區内,會使大部分的空化泡受到 壓擠發生贿破滅,進而產生爆震波效應,在此_㈣震波效應,是指 空化泡被擠壓破滅的過程,它是集中纖維織物的波動能量和外圍的壓力環 抚所產生的壓縮波能量共同合成的作用力,在空化環境中進行無障礙的射 流運動。因此,當空化泡崩潰破滅時,作用力會由外向内,瞬間產生一個 鲁 爆震波衝向空化泡中心,當纖維織物表面或組織耕受到爆震波經過或衝 擊時’會使齡賴表面上雜_外邊界區酬有介㈣紐壓力和粒 子的振動速度發生急細變化’且在滅的時間内在纖絲面的極小空間 上或在纖維無定賴中’會產生極高的溫度和極大賴力因此,在進行 染色或其他加工處理時’染液或處理液可藉空化泡的破滅所產生的爆震 波’在纖維表面或在纖维無定形區内產生強大的衝擊力,進而促使染液或 處理液在纖維中獲得加速滲透及快速擴散的能量外,亦可促使纖維織物表鲁 面上非活化的”子魏足夠能量轉化為活化分子,並導賴維分子組織產 生溶脹或增_效果,以達職速染色或其他加工處理之目的者。 本發明的主要目的在於提供-種衝擊式爆震波快速染色機,在進行染 色或其他加工處理時’其可利用高能的波動場所引發的爆震波效應,對纖 維織物進行改性,或是一邊改性一邊染色。 〃根據纖維微觀結構’無論是天然纖維素纖維或合成纖維都是由碳原子 與氫原子、氧原子、氮原子、氣原子相互連結構成長鏈狀分子所形成而 16 201142104 % 這些都屬於大分子的化合物,並都包括了結晶區和無定形區,而在纖維的 結晶區,分子會有規律地排列,分子之間的作用力較強,其分子結構緊密, 使得染料分子難以進入;而纖維的無定形區,分子無序排列,分子間的作 用力較弱,分子結構比較鬆散,存在一定的空隙。因此在染色或其他加工 處理時’染料或處理劑分子只能進入纖維的無定形區,如果是乾燥或常溫 下’染料分子也難以進入。 另外根據染色理論來說’無論染料是按孔道擴散的模型,還是按自由 籲體積擴散模型進行染色,無非都是加大無定形區的空隙,即增大纖維内外 部的比表面積’才得以使上染過程順利進行,因此凡是有利於纖維無定形 區空隙的加大和纖維内外比表面積增大的因素,都有利於染色或其他加工 處理過程的順利進行。而根據材料力學來說,任何材料的損傷和破壞都源 於材料中醜力過錢巾及原始雜和狀之起點,峨維高分子物無定 形區的空隙正是提供了這種可能1此,每當纖維織物受到強力的快速波 動及空化泡生成或破滅的作用下’必然會產生微晶之間的錯位或造成部分 纖維分子斷裂或重組,使纖維内部的比表面積加大,無絲區的空隙增加。 因此,可麟_改性之目的,也可同賴得―歧性―絲色之目的者。 本發明的主要目的在於提供-種衝擊式爆震波快麵色機其在進行 染色前處理時’纖維織物可利用高速流動的低溫等離子體的作用,進行無 水退槳或去除不純物或是進行纖維織物改質及改性。本發明所說的高速流 動的低溫等離子體,是指氣體壓力可在一大氣壓力的條件下,以大量高速 流動的空氣或其他氣體為介質,在通過共構式噴嘴時,可經由共構式嗔嘴 的喷射管通路上所設置的電極尖端與環形妹之間,由電暈放電或次輝光 I S. 1 17 201142104 放電的方式產生。在放電時’因電極尖端經施加-高電壓,使電極尖端與 裒形電乾發生不平衡的電~,在電極尖端表面曲率較大的地方,由於電力 線集中,使電壓等電位面健集,因此,在高電場高電壓的作用下,使自 由電子在電場巾獲得能量魏高能級的電子,迫使高能電子從電極尖端的 地方釋放辣,朝著環形软方向加速,使高能電子在通往環形電乾的途 中.、《Ρ/;的同速空氣流發生猛烈碰撞,在碰撞過程中,因高能級電子的能 量很大’會使空氣分子或原子外圍的電子發生解離,生成含有各式各樣的 高能活性粒子’耻,在精無水加卫處理時,其可共構式喷嘴喷出 # 含有電子、離子、自由基、激發原子或分子和未反應的分子等,而這些高 能活性粒仅間除了錄生相互反應個並伴有輻概外,大部分均會與 纖維織物表面發生劇烈的撞擊使能量獲得消散,因此,在消散過程中它 們對纖維織物3表面的作用不僅會產生相當的自由基,還會對纖維織物表 面進行氧化作用’進而促使非極性纖維織物表面增加大量的極性基團外, 也可利用高速流_低溫等離子體,將纖維織物表面上所含的天祕質以 及在纺織加工中施加的漿料和油汙等雜質進行去除,使纖維織物具有良好鲁 的吸濕、滲透效果’以滿足後續加工卫序,因為—般傳統前處理工序長, 化學藥品用量大’用水量較高,·生產效率較低,耗能高廢水排放量 大。因此,利用高速流動的低溫等離子體處理時,具有良好的去雜清潔作 用’可取代某些前處理化學濕加工工序,或經高速流動的低溫等離子體表 面處理後’能採用較溫和的前處理工序即可縮短處理時間、減少化學助劑 用量、降低處理溫度’從而提高生產效率,降低水魏的_及汗染,同 時也能達到節能減碳之目的。因此’在前處理加工中,若能利用高速流動 18 201142104 的低溫等離子體技術,其具有重大的環保效益和經濟效益。 本發明的主要目的在於提供—種衝動式爆震波快速染色機,其可藉由 -機多功性的技術領域機構進行各織_物染色外,它還可崎各種纖 維織物進行改性處理、退漿處理、精煉處理、漂白處理、生物酶處理、分 織處理、鬆_理、退色處理、賴處理、蓬鬆處理、柔軟處理、原纖化 處理、伸縮處理、消紋處理、修色處理等加工處理,達到方便快速有 效、安全及節_料、節_劑、節約能源、節約水資源以清潔生產的 方式降低環境汙染及便於實現自動化控制為目的者。 本發明的主要目的在純供—種衝動式爆震波快速染色機在進行染 色或其他加工處理時,其中,織物的循環移動動力,僅藉由一排共構式喷 嘴所驅動,其可秉棄傳統機械式㈣力帶布輪之_方式,啊,織物也 可藉由共構式嘴嘴所喷出的高速空氣流,自動完成摺疊作業,因此,也可 秉棄傳統機械式的動力擺布方式,因此,織物在快速的循環移動中,不再 受到動力料輪和動力擺布裝置的鱗衝擊關傷,也不再受職維織物 與動力帶布輪職生的移動速度不連續現⑽發生,麵,可獲得更簡便 的操控及均速移動之目的者。 本發明的主要目的在於提供一種衝動式爆震波快速染色機在進行染 色或其他加處理時’其中,纖維織物在進人鮮槽前,除了可藉助氣力 的擺動完成摺疊作業外,亦可藉由纖維織物瞬間所引發的氣擊效應產生強 力的擺動魏,迅速_著於纖輯物表__工作液,及雜纖維以 及未反應的浮色染料或是其它固形物體進行強制性的驅離,使進入集布槽 的疊集織物均能全面獲得脫液降污及降低相互麟的重力,促使附著雜 201142104 維織物中殘留的工作液降到最低,以獲取最小液量的操作,因此,除了可 利於快速處理之進行外’亦可創造最小的操作液量和高濃度的處理為目的 者0 本發明的主要目的在於提供__纖擊魏震波快速染色機在進行染 色或其他加工處理時’其中’纖維織物可在乾態環境下,高速流動的 低恤等離子體’進行·、精煉、表面改質聚合和接枝因此,除可提 供無水加J1處理外,更可提供齡齡在加工時’獲得更寬_創作工藝 空間為目的者。 本心明的主要目的在於提供__種衝擊式爆肢快速染色機,其在進行 染色或八他加工處理時’染料和處理劑可預先泵人無泵加料裝置的容器 内來對應處理槽内多變的壓力環境,染料和處理劑可利用位能的作用獲 得门精度的觀’其除可不受到處理動的升溫或升壓的環賴化,影響 補”。所A的〜$值外’亦可省下在高揚織小液量触送電能為目的者。 本發明的主要目的在於提供—纖擊式爆紐快速染色機,其中在導 端處可不須設置動力帶布輪,在導布管出口端也可不須設置機 械式擺布裂置。gj此,在操作時,除了可提供較安全_業環境,讓操作 人貝不再*_力帶布輪所帶麵㈣壓触或傷㈣,亦可提供纖維織 又J動力帶布輪的所產生的滑動性磨擦,以及不同步所造成的纏車 織物在通過導布管時,也不必再受到機械式擺布裳置的作用,使移 動速度不再麵_為目的者。 【實施方式] 參看圖一至圖七 本發明的衝動式爆震波快速染色機包括有處理槽i、 201142104 集布槽2、纖維織物3、導布管11、工作門孔12、反射作用基板13、U型 迴轉板14、導向板15、鼓風機16、液滴收集板18、備料桶19、無泵加料 裝置20、内侧分離柵網21、外側分離柵網22、滑條23、網孔板24、上游 落布區段31、分流口 42、通路口 43、回流口 46、弧型分流管61、匯流通 路管62、氣流輸送管路系統71、液流加壓循環泵浦72、加料泵浦73、上 游入口處111、下游出口處112、共構式喷嘴121、氣浮喷嘴122、楔形間隙 通路15卜氣流回流管160、空氣加熱器161、氣流過濾器162、交流式氣 _ 流佈流裝置163、右進斜歧管164、左進斜歧管165、匯流口 166、共構式 分配管167、氣浮分配管168、空氣流量調節閥169、染液回流管170、分 配口 172、交流式液流佈流器173、右進歧管174、左進歧管175、均壓分 配管176、分流孔178、喷流口 179、收集導流溝槽181、導流管182、工作 液收集板184、交流式氣流回流裝置19〇、單斜匯流管191、丁字型的匯流 回流管192、廢氣排出口及控制閥門200、新鮮空氣導入口及控制閥門2〇1、 流量調節閥203、加壓循環液流輸送管210、蒸氣輸入口及控制閥門211、 ® 其他氣體導入口及控制閥門212、工作液回收及排出口閥門214、循環通路 22卜環狀形電靶1211、喷射管1212卜更換式電擊棒12122、高壓電源連 接端子12123、接地連接端子12124、液壓霧化喷嘴1216、液壓霧化喷嘴口 12161、滑動閥桿12164、閥座12165、彈簧活塞12167、作動流體入口 12169。 清同時參照圖-至圖三’為處理槽i的構造,其可以單槽式或並聯排 列組成多槽式的處理槽1,在使用於高溫高壓時一般為圓形狀,而使用於常 溫常壓時可不受抗壓結構的限制,外形則可配合處理量及特殊加工需求或 依照環境場地任意加南或增長處理槽i的容積空間。例如:圖二所示,為 [S.1 21 201142104 加高型的機種,其可獲得較大的處理量。例如圖三所示,為加長型的機種,* 其可對應特別容易發生摺痕的纖維織物3,其在外型及構造上為了對應無水 - 加工環境,並能使纖維織物3移動順暢,以及材料成本的種種考量下在 實行時較適於圓形狀來達到最佳使用目的及最小的占地空間。如圖一所 示,是適用於高低溫或高低壓者,其形體則以英文字母中的〇字為設叶, 因此,處理槽1内的集布槽2及導布管11兩者間則可沿著槽壁内側空間形 成,構成一環形狀的循環通路。其中導布管U則設在集布槽2的正上方, 以一同軸向配置。為便於說明,在此以順時鐘為纖維織物3循環移動方向,鲁 在九點鐘方向為處理槽1之前端,在三點鐘方向則為處理槽丨之後端,處 理槽1底部最低部位為六點鐘方向設有染液回流管17〇,在處理槽i内中央 處空間部位設有一氣流回流管160,在處理槽丨前端槽壁上設有工作門孔 12。 另外該導布管11上游入口處m則設在處理槽i前端槽壁内側空間與 工作門孔12轉’與集布槽2下游出口相互連通,並位於工作門孔12近 處,而該導布管11的下游出口處則位於處理槽i的後端,位於與集布 φ 槽2上游相互連通’使導布管η與集布槽2前後兩端分別相互連通並構成 -條寬闊賴環通路。其可提供纖_物3在通路上以自由擴幅或開幅的 方式進行染色或其他加工處理。在導布管u下方橫跨於通路左右兩側的水 平皆壁端面上’沿著通路方向,在上游和中游區段,均設有多數的氣浮喷 嘴122 ’在下游區段的截斷面上,則設有一排橫跨於通路左右兩側壁間,以 並聯排列組合的共構式喷嘴12卜請同時參照圖四A、B所示為共構式喷嘴 121的構造。在共構式喷嘴121的膨膜加速喷射管通路上的入口處1213上 22 201142104 游部位,並設有一液壓霧化喷嘴1216,該液壓霧化喷嘴1216由一閥座12165 和一滑動閥桿12164所組成。為了達到精確的流量值,在正常情況下保持 預設最佳開度,其喷射流量係由閥座12165與滑動閥桿12164之間隙截面 積和液體壓力大小所決定。在滑動閥桿12164上並設有一彈簧活塞UK? 機構’當液壓霧化喷嘴口阻塞時,其可利用空麗或液壓流體經由作動流體 入口 12169導入彈簧活塞12167機構的氣室内,使彈簧活塞12167機構中 的氣缸壓力大於彈簧彈力,滑動閥桿12164可立即往後滑動,使間隙截面 籲積變大,進而可將滯留在液壓霧化喷嘴口 i施的游離纖維或其他固形物 進行排除》在操作過程中,若要増大喷霧流量,其可藉由氣虹施加壓力大 小與彈簧彈力之間取得平衡點,即可麟所需㈣霧流量。 請參關-、圖四A,在操作時,液壓霧化喷嘴1216可經由交流式液 流佈流器173與輸送管路系統21〇、17〇於加壓循環果浦72互相連接藉 由加壓循環泵浦72對染液或處理液施加壓力,將染液或處理液導入能產生 強大剪斷力的液壓霧化喷嘴口 12161中喷出而霧化,染液或處理液通常在 釀加壓至5_咖上即可獲得良好的霧化效果,在壓力越高溫度越高的情況 下霧化效果會大幅紐高’為使霧化的綠或處理液歸運航量提高衝 擊力’喷霧角度則控制在較小角度的範圍内進行霧化,使破碎解離成微粒 狀的染液或處理液均能充分分散在噴射管12121内與正在膨服加速的高速 空氣流齡’使霧化綠或處理液在通過共構式喷嘴口 ΐ2ιι時,均能再度 進行破碎解轉献λΙ、的錄’使鱗輯物3發生衝料,在齡織物3 表面積上,均能獲得均量的染液或處理液及均衡的衝擊力。為了達到更完 善的清潔生產目的,在液壓霧化喷嘴口 12161通路的中央處也可另行加設 I S1 23 201142104 一更換式電擊棒12122,請參閱圖 四B所示,該電擊棒12122設在液壓霧化 喷嘴1216的滑動閥桿12164中央部位上與絕緣體的滑動閥桿麵構成一 體’另-端觀伸至雜霧树嘴㈣體外财呈—高壓電職接端子 12123,其可經由電纜線於處理槽丨外部的高壓電源設施5互相連接。在共 構式喷嘴m通路上的喷射管12121管壁則改用一絕緣體贿使共構式 喷嘴口 1211構成-環狀型妹1211設置在絕緣體的喷射管中其於共構During the processing, when the high-speed flowing air, vapor, dye, treatment agent, low-temperature plasma and the _ fabric are sprayed and collided by the co-structured nozzle, the marriage can be turned to fall down. Forming _ end _, obtaining a large impact slamming power for high-efficiency energy conversion; when in the process, the dyeing liquid and the treatment liquid are fine-grained or granular or in a single way Molecularly dispersed in a high-speed air stream, impacting the fiber fabric that is being steered in a direct close-up manner, so that the surface of the fiber fabric continuously and continuously obtains a strong elastic collision (Note: means air or body) Inelastic collision (Note: refers to the working fluid or dye or treatment agent also includes plasma, ^ in the ship hits the __ to get efficient remedies, outside 'butter __ paste _ akisaki (ea = 11 201142104 The elastic collision can promote the formation of a high-speed air flow between the lower end surface of the fiber fabric and the reflective substrate, and also promote the pressure difference between the air static pressure between the upper and lower end faces of the fabric. The static pressure on the upper end surface is greater than the static pressure on the lower end surface, so that the moving fiber fabric can utilize the pressure difference to continuously generate periodic strong wave motion when passing through the reflection actuation plate, and can simultaneously perform The effect of free spreading. § In the wet processing, if the amount of liquid film adsorbed on the surface of the fiber fabric is sufficiently thick, the velocity energy of the high-speed air flow is large enough to promote the surface boundary region of the fiber fabric in the fluctuation. A large number of holes are generated, causing a shock wave effect. In dry operation, high-speed air flow can also use corona discharge or gl〇w discharge to make part of the high speed. The air molecules of the air stream are ionized to generate a low-temperature plasma of high-speed flow. In addition to the treatment effect of the high-energy particles, the water-processing can also obtain more ecological benefits. In the processing process towel, falling on the cloth groove (10) Lin fabric, you can paste the inertia force and find the flow Quickly drive away the order, the resulting _ inter-office side, causing the air-blown effect' to produce a strong crane county, to promote the thief in the process of falling distribution, can use the mechanism of the swing 'will adhere to the fiber Residual working fluid on the surface of the fabric and exfoliated free fiber and other impure _ objects 'strongly separate the Wei and the lungs, and at the same time complete the folding operation' to make the _ fabric table _ ship and _ and other impure solid objects can be directly Collecting the trough and discharging the σ lead to the New Zealand, through the precision of the sieve to carry out the collection, which can promote the state of the collection of the cloth and the material of the material, _ do _ fabric in the next - cycle cycle and dyeing Or when the treatment liquid is in contact, it will not be blocked by the residual working liquid membrane barrier. The filter can be fed through the filtered 'working fluid' in the process of feeding the waste, and the dye-free or treatment agent can be used. Replenishment 'Make high-solubility dissolving dyes or treatment agents in the pump-free feeding device, all in the pure towel of the circulating conveying pipe, and put the 'Southern concentration of cold-dissolving dye or paste' into the suction port of the pressurized pipe. Can shoot in a limited amount of Lai ring Σ obtaining a mixed mode of operation are extremely small bath ratio and high degree. Gj, in this way, when the fiber is in contact with the New Zealand or the service, it can obtain higher potential energy and kinetic energy, and also increase the concentration gradient, temperature gradient and chemical affinity gradient' and promote the dyeing liquid or treatment liquid to be fast. The effect of permeation and diffusion is beneficial to the rapid processing; in addition to the effect of the squeezing of the spliced fabrics in the grooving groove to minimize the force, the fiber fabric can be promoted in the guide tube. The tension generated is minimized when moving quickly. In operation, the dyeing liquid or the treatment liquid pressurized by the pressure can be used to make the pressure equalization of each of the hydraulic atomizing nozzles by the action of the alternating current flow distributor on the conveying pipeline system. Atomized droplets 均, average temperature, average temperature, and uniform velocity, and the air flow pressurized by the air blower can use the AC airflow device on the conveyor piping system to perform a 90-degree steering to form a rectangular flow. And then introduced into the respective distribution tubes, the air flow can transform the kinetic energy of the moving airflow into static pressure energy by the diffusion structure of the distribution tube, which can promote the air flow through each air-floating nozzle and each co-construction When the nozzle is used, it can obtain a large expansion acceleration efficiency and a distribution effect of equalizing, equalizing, equalizing, and equalizing speed. In addition to preventing various types of colored flowers caused by the left and right color and single dyeing of the fiber, It can also promote all other processing operations' to obtain a variety of (4) hand-appeared appearance. During operation, the return air in the treatment tank can also be reflowed in the lateral direction by using an alternating current flow recirculating device, so as to prevent the airflow inside the treatment tank from being excessively disturbed, thereby obtaining a more stable and regularity. Circulating flow. The invention particularly relates to a gas floating nozzle disposed on the upstream and midstream sections along the horizontal direction of the horizontal tube wall between the left and right side walls of the guide tube on the lower side of the guide tube. In the section of the downstream section, the arranged-displacement spans the left and right side walls, and the combined common-type nozzles in parallel and the downstream side of the common-purpose nozzle opening are located at the outlet of the duct. The inner side space of the lower side and the inlet of the upstream section of the collecting groove, a u-shaped rotating plate is provided, and the upstream side end of the u-shaped rotating plate is overlapped and fixed in a stepwise manner at the common nozzle opening. The lower side, the upstream outer end surface of the U-shaped rotating plate constitutes a flat reflective substrate on the downstream outer end surface of the u-shaped rotating plate, and a separating grid disposed on the inner and outer sides of the upstream segment of the collecting groove The net 'so' is used for dyeing or other processing, processing the air and working fluid and the preparation tank _ liquid or virgin, can be connected to the respective piping system and the blower and the pressurized circulation Lipu to provide increased Air pressure and return Or treatment liquid ejected through the nozzle configuration common, while allowing pressurized air via air flotation nozzle discharge portion, respectively. In operation, the fiber fabric can take out a small amount of air flow by means of the air material, so that the fabric can be mixed, so that most of the power energy is difficult to be fine in the co-structure nozzle, under the action of the _ slewing plate, It can promote the discharge of the same ambiguous gas in the opposite direction, _ stimulating the fiber to obtain a strong driving force. n In operation, the co-construction nozzle can be used as the main power source of the domain lagoon crane. The operation mode of the traditional power belt pulley wheel can also improve the multi-k guide nozzle of the invention in the previous case. The airflow energy is excessively dispersed to achieve high-energy processing problems. The hydraulic atomizing nozzle mechanism provided on the nozzle and the corona or glow discharge mechanism 'interact one another to obtain mutually complementary processing modes, so that various types of fiber fabrics can be obtained more widely and widerly. Craft creation space. The main object of the present invention is to provide an impulsive detonation wave fast dyeing machine in the process of dyeing or other processing. The fiber fabric can be sprayed with high-speed damp heat or dry heat according to the processing requirements of the co-construction nozzle 201142104. High-speed uniform dispersion of (four) material molecules, high-speed uniform dispersion of liquid molecules, high-speed flow and temperature plasma, or other high-speed uniform-dispersed particles, so that all the ejected media can be formed in a homogeneous manner (10) concentrated in a high-energy In the undulating field, it is repeated with the fiber fabric; ί; the collision of the break, so that the reactants of the material and the fiber fabric, in a very short time, the high-scale energy of the movement of the squama can make all the participating reactants In addition to the amount of live Wei required by Wei, it is aimed at obtaining clean production under the shortest time, with the most energy-saving, water-saving, least-material, and minimal treatment agent. The main object of the present invention is to provide an impulse detonation wave rapid dyeing machine that can perform a dyeing or other J1 treatment, which can be caused by a strong fluctuation side or a fluctuation wave-induced detonation wave effect, a money promoting liquid or a treatment liquid. It is formed into a low-viscosity, low-resistance, high-potential, high-permeability, high-diffusion environment and a small amount of liquid, high concentration, and high-efficiency wet-wet treatment. The hair-removing effect of the test is that the thief is able to use the system of inter-speed air flow to produce high-energy grade lining in the process of cultivating, and a compression zone is formed in the wave-wave region of the wave process, and is formed in the valley region. - Sparse ^ and then promote any of the "mass point" on the surface area of the fiber, and the continuation of the money in the Wei area and the volatility of the area of the volatility in the compression zone will promote the outer surface of the fiber fabric in the area _ the average of the air molecules The distance shortening density becomes larger, and in the thinning, the average distance of finding molecules will increase, and the density is small. If the fiber fabric (4) is full of touch, the free wave power is enough to touch, which will make the surface of the fiber fabric _ The i-molecular molecule is also affected by the __ and the sparse zone. When the negative pressure of the sparse zone is reduced by _ and the vapor pressure is below the critical value, the working fluid is pre-leveled = the distance is increased to exceed the New Zealand distance, thereby destroying The integrity of the structure between the numerator or the thief _ material 15 201142104, thus causing the surface of the fiber fabric and the inner and outer pores of the fiber or the inner and outer gap regions of the fiber tissue to induce holes (referring to a very tiny bubble nucleus), and once air The formation will continue to increase until the negative pressure reaches a maximum value, resulting in the formation of a large number of cavitation bubbles (note: a very low density of vapor bubbles or air bubbles), and when successive compression zones will make most of the The cavitation bubble is crushed and crushed, and then the detonation wave effect is generated. Here, the _ (four) seismic wave effect refers to the process in which the cavitation bubble is crushed and shattered. It is the wave energy of the concentrated fiber fabric and the peripheral pressure ring. The force generated by the combined compression wave energy is combined to perform an unobstructed jet motion in a cavitation environment. Therefore, when the cavitation bubble collapses, the force will be from the outside to the inside, and a Lu-Detonation shock wave will be instantaneously rushed toward the center of the cavitation bubble. When the surface of the fiber fabric or tissue is subjected to the shock wave passing or impacting, the surface will be on the surface. The heterogeneous-external boundary zone has a very high temperature and great change in the pressure of the four (4) New Zealand and the vibrational velocity of the particles, and in the extremely small space of the fibril surface or in the fiber in the time of extinction. Therefore, when dyeing or other processing is carried out, the "detonation wave generated by the dyeing liquid or the treatment liquid can be generated by the destruction of the cavitation bubble", which generates a strong impact force on the fiber surface or in the amorphous region of the fiber, thereby promoting The dyeing liquid or the treatment liquid can obtain the energy of accelerated penetration and rapid diffusion in the fiber, and can also promote the conversion of the non-activated "child" energy on the surface of the fiber fabric into the activated molecule, and lead to the swelling or increase of the molecular structure. _ effect, in order to achieve the purpose of dyeing or other processing. The main purpose of the present invention is to provide a kind of impact type detonation wave fast dyeing machine, in the dyeing or other addition When processing, it can use the detonation wave effect caused by high-energy wave places to modify the fiber fabric or dye while modifying. 〃 According to the fiber microstructure 'whether natural cellulose fiber or synthetic fiber is carbon The atoms are formed by the formation of chain molecules with hydrogen atoms, oxygen atoms, nitrogen atoms and gas atoms. 16 201142104 % These are macromolecular compounds, and both include crystalline and amorphous regions, and in the crystallization of fibers. In the region, the molecules are regularly arranged, the interaction between the molecules is strong, the molecular structure is tight, and the dye molecules are difficult to enter; while the amorphous regions of the fibers, the molecules are disorderly arranged, and the interaction between the molecules is weak, the molecules The structure is loose and there is a certain gap. Therefore, in the dyeing or other processing, the dye or the treatment agent can only enter the amorphous region of the fiber, and if it is dry or at room temperature, the dye molecules are difficult to enter. Say 'whether the dye is diffused by the channel or by the free-volume diffusion model, nothing more than It is to enlarge the voids in the amorphous region, that is, to increase the specific surface area of the fiber inside and outside, so that the dyeing process can be smoothly carried out, so that the factors which are favorable for the increase of the voids in the amorphous region of the fiber and the increase of the specific surface area of the fiber inside and outside, Both are conducive to the smooth progress of dyeing or other processing. According to the mechanics of materials, the damage and destruction of any material originates from the starting point of the ugly material in the material and the original miscellaneous shape, and the amorphous polymer is amorphous. The gap in the area provides this possibility. When the fabric is subjected to strong rapid fluctuations and the formation or collapse of cavitation bubbles, it will inevitably cause misalignment between the crystallites or cause partial breakage or reorganization of the fiber molecules. Therefore, the specific surface area inside the fiber is increased, and the void in the non-filament region is increased. Therefore, the purpose of the modification can also be related to the purpose of "disambiguation"-silk color. The main purpose of the present invention is to provide - The impact type detonation wave fast color machine can perform the pre-dyeing treatment. The fiber fabric can use the high-speed flow of low-temperature plasma to perform waterless unloading or removal. It was pure or modified, and for fabric modification. The high-speed flowing low-temperature plasma according to the present invention means that the gas pressure can be a medium with a large amount of high-speed flowing air or other gas under an atmospheric pressure, and can be co-constructed when passing through a co-structured nozzle. Between the electrode tip and the ring-shaped sister disposed on the nozzle path of the pout, it is generated by the discharge of corona discharge or sub-glow light I S. 1 17 201142104. During discharge, 'the voltage at the tip of the electrode is unbalanced due to the application of a high voltage. In the place where the curvature of the electrode tip surface is large, the voltage equipotential surface is concentrated due to the concentration of the power line. Therefore, under the action of high electric field and high voltage, the free electrons obtain the energy of the high-energy level in the electric field towel, forcing the high-energy electrons to release the spicy from the tip of the electrode, and accelerate toward the ring soft direction, so that the high-energy electrons lead to the ring. On the way of electric drying, "Ρ/; the same speed air flow violently collides, in the collision process, because the energy of high-level electrons is large" will dissociate the air molecules or electrons around the atom, resulting in various types The high-energy active particles are 'shameful, and when they are treated with no water, they can be co-constructed by nozzles. They contain electrons, ions, free radicals, excited atoms or molecules, and unreacted molecules. These high-energy active particles are only In addition to the mutual reaction of the recordings and the convergence, most of them will have a strong impact on the surface of the fabric to dissipate the energy. Therefore, in the process of dissipation Their effect on the surface of the fiber fabric 3 not only produces relatively free radicals, but also oxidizes the surface of the fiber fabric', thereby promoting the addition of a large number of polar groups on the surface of the non-polar fiber fabric, and also utilizing high-speed flow_low temperature plasma The impurities contained in the surface of the fiber fabric and the impurities such as slurry and oil stain applied in the textile processing are removed, so that the fiber fabric has a good lubricity and penetration effect to satisfy the subsequent processing order, because The traditional pre-treatment process is long, the chemical consumption is large, the water consumption is high, the production efficiency is low, and the energy consumption is high. Therefore, when using high-speed flow of low-temperature plasma treatment, it has a good de-cleaning effect, which can replace some pre-treatment chemical wet processing steps, or after high-speed flow of low-temperature plasma surface treatment, 'can adopt milder pre-treatment. The process can shorten the processing time, reduce the amount of chemical additives, and lower the processing temperature, thereby improving the production efficiency, reducing the water and the sweat, and at the same time achieving the purpose of energy saving and carbon reduction. Therefore, in the pre-processing, if the low-temperature plasma technology of high-speed flow 18 201142104 can be utilized, it has significant environmental and economic benefits. The main object of the present invention is to provide an impulsive detonation wave fast dyeing machine, which can be modified by various fabrics by means of a technical mechanism of the multi-functionality of the machine, and can also be modified by various fiber fabrics. Desizing treatment, refining treatment, bleaching treatment, biological enzyme treatment, weaving treatment, loosening, fading treatment, bleed treatment, fluffy treatment, soft treatment, fibrillation treatment, stretching treatment, fading treatment, color treatment, etc. Processing and processing, to achieve convenient, efficient and effective, and save the material, save the energy, save water, clean the production to reduce environmental pollution and facilitate the realization of automated control. The main object of the present invention is to use a purely supplied impulsive detonation wave fast dyeing machine for dyeing or other processing, wherein the cyclic moving power of the fabric is driven only by a row of co-structured nozzles, which can be discarded. The traditional mechanical (four) force belt cloth wheel _ way, ah, the fabric can also automatically complete the folding operation by the high-speed air flow sprayed by the co-form nozzle, therefore, can also abandon the traditional mechanical power arrangement Therefore, in the rapid cycle movement, the fabric is no longer affected by the scale impact of the power wheel and the power swing device, and the moving speed of the service fabric and the power belt cloth is no longer continuous (10). For easier manipulation and even speed movement. The main object of the present invention is to provide an impulse detonation wave fast dyeing machine for performing dyeing or other processing. In addition, before the fiber fabric is inserted into the fresh tank, the folding operation can be completed by the pneumatic swing. The air-shock effect caused by the moment of the fiber fabric produces a strong oscillating Wei, which is quickly escaping from the fiber surface __ working fluid, and the fiber and unreacted floating dye or other solid objects for forced detachment. The stacked fabrics entering the collecting trough can fully obtain the deliquescence and pollution reduction and reduce the gravity of the mutual lining, so as to minimize the residual working liquid in the 201142104 dimensional fabric to obtain the minimum liquid amount operation, therefore, in addition to For the purpose of rapid processing, it is also possible to create a minimum amount of operating liquid and high concentration. The main purpose of the present invention is to provide a __fibrillary Wei Zhenbo fast dyeing machine for dyeing or other processing. Among them, 'fibre fabric can be carried out in a dry environment, high-speed flow of low-shirt plasma', refining, surface modification polymerization and grafting. Providing an outer added anhydrous J1 processing, and more may be provided in the processing of old age '_ obtaining object creation process by a wider space. The main purpose of the present invention is to provide a __ type impact-type explosive limb rapid dyeing machine, which can be used in the processing tank of the pre-pumping pump-free feeding device in the dyeing or octah processing process. The variable pressure environment, the dye and the treatment agent can use the action of the potential energy to obtain the view of the door's accuracy, which can be affected by the temperature rise or the pressure increase of the process, which affects the compensation. It is also possible to save the purpose of high-powered small liquid amount of electric energy. The main object of the present invention is to provide a fiber-type explosion-proof fast dyeing machine in which a power belt cloth wheel is not required to be disposed at the guide end. The outlet end of the pipe does not need to be equipped with mechanical pendulum splitting. gj, in operation, in addition to providing a safer environment, let the operator be no longer *_ force belt cloth wheel (4) pressure contact or injury (4) The slidable friction generated by the fiber-woven and J-powered cloth wheels can also be provided, and the wrap-around fabric caused by the non-synchronization does not have to be mechanically placed to move when passing through the guide tube. Speed is no longer _ for the purpose. Embodiments Referring to Figures 1 to 7, the impulse detonation wave fast dyeing machine of the present invention comprises a treatment tank i, a 201142104 cloth collecting groove 2, a fiber fabric 3, a guide tube 11, a working door hole 12, a reflecting substrate 13, U Type rotary plate 14, guide plate 15, blower 16, droplet collection plate 18, preparation tank 19, pumpless charging device 20, inner separation grid 21, outer separation grid 22, slider 23, mesh plate 24, upstream Falling section 31, splitting port 42, passage port 43, return port 46, arc-shaped shunt pipe 61, bus path pipe 62, air flow conveying pipe system 71, liquid pressure circulation pump 72, feed pump 73, The upstream inlet 111, the downstream outlet 112, the common nozzle 121, the air flotation nozzle 122, the wedge gap passage 15, the airflow return pipe 160, the air heater 161, the air flow filter 162, the AC gas flow device 163, Right-inclined manifold 164, left-inclined manifold 165, manifold 166, co-construction distribution pipe 167, air flotation distribution pipe 168, air flow regulating valve 169, dye liquid return pipe 170, distribution port 172, AC liquid Flow distributor 173, right feed manifold 174, left feed manifold 175, Pressure distribution pipe 176, flow dividing hole 178, jet flow port 179, collecting guide flow groove 181, flow guiding pipe 182, working fluid collecting plate 184, alternating current airflow returning device 19, single oblique collecting pipe 191, T-shaped confluence Return pipe 192, exhaust gas discharge port and control valve 200, fresh air inlet port and control valve 2〇1, flow regulating valve 203, pressurized circulating fluid flow pipe 210, steam inlet port and control valve 211, ® other gas inlet And control valve 212, working fluid recovery and discharge valve 214, circulation passage 22, annular electric target 1211, injection tube 1212, replacement electric shock rod 12122, high-voltage power connection terminal 12123, ground connection terminal 12124, hydraulic atomization nozzle 1216. A hydraulic atomizing nozzle port 12161, a sliding valve stem 12164, a valve seat 12165, a spring piston 12167, and an actuating fluid inlet 12169. Referring to FIG. 3 to FIG. 3 simultaneously, the structure of the processing tank i can be arranged in a single tank or in parallel to form a multi-tank processing tank 1, which is generally round in shape when used at high temperature and high pressure, and is used for normal temperature and pressure. It can be free from the pressure-resistant structure, and the shape can be matched with the processing capacity and special processing requirements or the volume of the processing tank i can be increased according to the environment. For example, as shown in Figure 2, it is a [S.1 21 201142104 heightening type of machine, which can obtain a larger amount of processing. For example, as shown in FIG. 3, it is an elongated type of machine, which can correspond to a fiber fabric 3 which is particularly prone to creases, and which is suitable for the water-free processing environment in terms of appearance and structure, and enables the fiber fabric 3 to move smoothly, and the material. The various considerations of cost are more suitable for round shape in implementation to achieve the best use and minimum floor space. As shown in Fig. 1, it is suitable for high and low temperature or high and low pressure, and its shape is set by the 〇 word in the English alphabet. Therefore, between the collecting groove 2 and the guide tube 11 in the processing tank 1 It can be formed along the inner space of the groove wall to form a loop-shaped circulation passage. The guide tube U is disposed directly above the collecting trough 2, and is disposed in the same axial direction. For convenience of explanation, the direction of movement of the fiber fabric 3 is clockwise, and the direction of the groove is the front end of the processing tank 1 at the nine o'clock direction, and the rear end of the processing tank at the three o'clock direction. A dyeing liquid return pipe 17 is provided at a direction of six o'clock, and a gas flow return pipe 160 is disposed at a space in the center of the processing tank i, and a working door hole 12 is formed in the front wall of the processing tank. In addition, the upstream entrance portion m of the guide tube 11 is disposed in the inner space of the front end of the processing tank i and communicates with the working door opening 12 and the downstream outlet of the collecting trough 2, and is located near the working door hole 12, and the guide The downstream outlet of the pipe 11 is located at the rear end of the processing tank i, and is located in communication with the upstream of the collecting φ groove 2, so that the guiding pipe η and the front and rear ends of the collecting groove 2 are respectively connected to each other and constitute a wide strip. path. It provides for the dyeing or other processing of the fiber 3 on the passage in a freely expanding or opening manner. Below the guide tube u, across the horizontal wall end faces of the left and right sides of the passage, 'in the direction of the passage, in the upstream and midstream sections, a plurality of air-floating nozzles 122' are provided on the section of the downstream section. There is a row of co-structured nozzles 12 that are arranged in parallel in a row across the left and right side walls of the passage. Referring to Figures 4A and B, the configuration of the co-structured nozzles 121 is also shown. At the entrance of the constituting nozzle 121 of the co-structured nozzle 121, the inlet portion 1213 is on the portion 22 201142104, and a hydraulic atomizing nozzle 1216 is provided. The hydraulic atomizing nozzle 1216 is composed of a valve seat 12165 and a sliding valve stem 12164. Composed of. In order to achieve a precise flow rate, the preset optimum opening is maintained under normal conditions, and the injection flow rate is determined by the gap profile of the valve seat 12165 and the sliding valve stem 12164 and the magnitude of the liquid pressure. A spring piston UK is disposed on the sliding valve stem 12164. When the hydraulic atomizing nozzle is blocked, it can be introduced into the air chamber of the spring piston 12167 through the actuating fluid inlet 12169 by using the air or hydraulic fluid to make the spring piston 12167. The cylinder pressure in the mechanism is greater than the spring force, and the sliding valve stem 12164 can slide back immediately, so that the gap section becomes larger, and the free fiber or other solid matter retained in the port of the hydraulic atomizing nozzle can be excluded. During the operation, if the spray flow rate is to be increased, it can be balanced by the pressure applied by the gas rainbow and the spring force, so that the required (four) mist flow rate can be obtained. Please refer to - Figure 4A. During operation, the hydraulic atomizing nozzle 1216 can be interconnected with the delivery line system 21, 17 and the pressurized circulation Guopu 72 via the AC flow distributor 173 by pressurization. The circulating pump 72 applies pressure to the dyeing liquid or the processing liquid, and the dyeing liquid or the treatment liquid is introduced into the hydraulic atomizing nozzle opening 12161 capable of generating a strong shearing force to be sprayed and atomized, and the dyeing liquid or the processing liquid is usually pressurized. A good atomization effect can be obtained up to 5_ coffee. The higher the pressure, the higher the temperature will be, the atomization effect will be greatly increased. 'To make the atomized green or the treatment liquid return the air to improve the impact force' spray The angle is controlled to be atomized in a range of a small angle, so that the dyeing liquid or the treatment liquid disintegrated into fine particles can be sufficiently dispersed in the injection pipe 12121 and the high-speed air flow age that is being accelerated to accelerate the atomization green Or when the treatment liquid passes through the co-structured nozzle port 2 ι 2, it can be re-pulsed and dismantled, and the granules 3 can be granulated, and the average amount of dye solution can be obtained on the surface area of the aged fabric 3 Or treatment fluid and balanced impact. In order to achieve a more perfect cleaning production, an alternative type electric shock bar 12122 may be additionally installed at the center of the passage of the hydraulic atomizing nozzle port 12161. Referring to FIG. 4B, the electric shock bar 12122 is disposed at The central portion of the sliding valve stem 12164 of the hydraulic atomizing nozzle 1216 is integrally formed with the sliding valve stem surface of the insulator. The other end of the sliding valve stem 12164 is integrally connected to the misty tree mouth (four) in vitro. The high voltage electric service terminal 12123 can be connected via a cable. The high voltage power supply facilities 5 outside the processing tank are connected to each other. The wall of the injection pipe 12121 on the m-shaped path of the common nozzle is changed to an insulator brim to form a common nozzle port 1211. The ring-shaped sister 1211 is disposed in the injection tube of the insulator.

式喷嘴m形成-體,在環狀型電乾上並設有一接地連接端子i簡其可 經由電纜線於地表互相連接。The nozzles m are formed in a body, and a ring-shaped electric stem is provided with a ground connection terminal i which can be connected to each other via a cable.

因此’在操作時,液壓霧化喷嘴1216可利用交流式液流佈流器173的 作用,使每-液壓霧化喷嘴1216,喷出相同的流量值。因此,在操作時, 共構式喷嘴121可糊交流式氣流佈流裝置163的_,使每—共構式喷 嘴121和每-氣浮喷嘴122,噴出相同的流量值。因此,在操作時,其可利 用共構式喷嘴121作為帶動織物3進行循環移動的主要動力源,在染色或 其他加工時,可依纖_物3特性及加卫需求,將鼓風機16葉片的旋轉周 期增大或減小,即可獲得所需紅作线流量,同時也可彻氣浮分配管 入口處的調節閥169依據纖維織物3的單位面積重量,使氣浮噴嘴122噴 出適S的氣流’紐賴物3缺,讓鱗織物3獲得較平穩的氣流形成 一氣墊方式滑動,並促使纖維織物3與管壁間不發生磨擦接觸及擾動現象, 以促進纖維織物3在進行快速移動時的阻力降至最小。因此,在共構式噴 嘴121的作用下,會使喷出的高速空氣流,或是高速的霧化染液和處理劑, 或是高逮的低溫等離子體,或是高速的蒸氣流,或是其他氣體或液體,均 能以直接近距離方式喷向織物3下方表面上,在反射作用基板13的作用 24 201142104 下,可促使纖維織物3產生激烈的波動,在反射作用基板13的作用下,會 使高速空氣流受到反射作用基板13的端面牽引作用,由纖維織物3的下側 方朝向下游方向推進,因而引發壓力差的作用,進而促使纖維織物3產生 加速移動和波動運動,而在通過導布管U下侧方橫跨於通路左右__ 水平管壁端Φ上’辟通路方向在描和巾游區㈣纖_物3,會因纖維 織物3的加速移動作用,使纖維織物3上表面邊界的空氣受到牽引作用, 進而形成快速的流動的低壓區域,因此導致了纖維織物3在通過導布管n 時’使纖維織物3稍產生-垂直向下的壓力,而每#_織物3連續不 斷受到共構式喷嘴121推拉的驅動下,除了促使纖維織物3在共構式喷嘴 121的下游區段產生擴布效果外,同時也會牵動纖維織物3在快速通過導布 管11上游及巾舰段進行開幅狀的氣浮对轉,緊#在麟下方管壁端 面上沿著通路朝向共構式喷嘴121方向移動。 請同時參關-至圖三,在共構式喷嘴121喷出方_下游區段位 於導布管11通路出口的下側方與集布槽2上游落布區段31的入口内侧方 之間’設有-U型迴轉板14 ’該υ型迴轉板14的上游側端以階梯式方式搭 接固疋在共構式喷嘴121 α的下财’使υ型迴轉板14上游外侧端面構成 -平直的反射作用基板13,在υ型迴轉板14的下游外側端面上,在落布區 段31設有内側分離柵網W、外側分離柵網π,在導布管u通路的下游區 段,位於共構式喷嘴121的正上方,設有一導向板15,該導向板15的上游 側端搭接在導布管11上側方管壁上’其下游端則於集布槽2料區段Μ 的外側分離柵網22相互連接,其可藉由導向板15的作用,將導布管u通 路的下游區段空間形成-漸縮的楔型間隙151,當纖維織物3通過楔形間隙 I S.]. 25 201142104 151通路時’其可藉導向板15的下侧端面與纖維織物3上側端面所產生的 相對移動作用,促使導布管11内,將纖维織物3上方的空氣擠入楔形間隙 產生壓力,因此,使得通過共構式喷嘴121的纖維織物3再度獲得向下的 壓力作用,並可促使共構式喷嘴121在喷出高速空氣流與纖維織物3發生 衝擊時,可獲得較大反作用力,亦可促進纖維織物3在通過U型迴轉板14 時,使纖維織物3上側端面的空氣流不斷提供較大的靜壓空氣流,其可提 供纖維織物3在反射作用基板13與導向板15之間所產生的反射能量,均 能傳遞至纖維織物3上,進而增大波動能量及波動頻率。 · 在導布管11下游出口處與集布槽2上游落布區段31上,並設有一擺 布脫液機構。該擺布脫液機構系由上述說明的U型迴轉板14、導向板15、 内侧分離柵網21、外侧分離柵網22、液滴收集板18、工作液收集板184所 組成,其中在集布槽2通路上游側端的落布區段31的内外側壁上,各設有 一内側分離柵網21和外側分離栅網22,内側分離柵網21上游侧端設在u 型迴轉板14與液滴收集板18互相連接的部位處,以較直立的方式設在集 布槽2上游侧端位於落布區段31内侧方,其下游側端則與工作液收集板ι84 φ 的上游側端相互連接,在液滴收集板18之下游侧端,則設有一收集導流溝 槽181 ’在收集導流溝槽181的下側壁上和工作液收集板184最低部位,則 設有-導流管182,其可將收集的工作液導入集布槽2下方排出口 m排 出°外侧分離柵網22的上游側端則與導向板15的下游侧端相互銜接,其 下游側端則與集布槽2通路下側方的滑條23及網孔板24相互銜接,使集 布槽2外侧方與處理槽丨之内側壁間形成一空氣流的循環通路221其可引 導由外侧分離柵網22排出的空氣流由該循環通路221導入處理槽i前端的 26 201142104Therefore, in operation, the hydraulic atomizing nozzle 1216 can utilize the action of the alternating current flow distributor 173 to cause each of the hydraulic atomizing nozzles 1216 to eject the same flow rate value. Therefore, in operation, the co-configuration nozzle 121 can paste the _ of the alternating current flow device 163 to cause the same flow rate value to be ejected for each of the co-structure nozzles 121 and the per-air float nozzles 122. Therefore, in operation, it can utilize the co-structured nozzle 121 as the main power source for driving the fabric 3 to perform cyclic movement, and in the dyeing or other processing, the blower 16 blade can be selected according to the characteristics of the fiber 3 and the reinforcement requirement. When the rotation period is increased or decreased, the required red line flow rate can be obtained, and at the same time, the regulating valve 169 at the inlet of the air flotation distribution pipe can make the air floating nozzle 122 spray out according to the basis weight of the fiber fabric 3. The airflow 'New Zealand' is lacking, so that the scale fabric 3 obtains a smoother airflow to form an air-cushion sliding, and promotes no frictional contact and disturbance between the fiber fabric 3 and the pipe wall to promote the rapid movement of the fiber fabric 3 The resistance is minimized. Therefore, under the action of the co-structured nozzle 121, the high-speed air flow that is ejected, or a high-speed atomization dye solution and treatment agent, or a high-temperature low-temperature plasma, or a high-speed vapor stream, or Other gases or liquids can be sprayed directly onto the lower surface of the fabric 3 in a direct close manner. Under the action 24 201142104 of the reflective substrate 13, the fiber fabric 3 can be caused to fluctuate drastically under the action of the reflective substrate 13. The high-speed air flow is pulled by the end surface of the reflective substrate 13, and is advanced by the lower side of the fiber fabric 3 toward the downstream direction, thereby causing a pressure difference, thereby causing the fiber fabric 3 to generate accelerated movement and wave motion. The lower side of the guide tube U traverses the left and right sides of the passage __ the horizontal end of the horizontal tube Φ, and the direction of the passage is in the drawing and the towel area (four) fiber_object 3, which will cause the fiber fabric due to the accelerated movement of the fiber fabric 3. 3 The air at the upper surface boundary is subjected to traction, thereby forming a fast flowing low pressure region, thus causing the fiber fabric 3 to make the fiber fabric 3 slightly generated when passing through the guide tube n. The lower pressure, while each #_fabric 3 is continuously driven by the push-pull of the co-structured nozzle 121, in addition to causing the fiber fabric 3 to have a spreading effect in the downstream section of the co-structured nozzle 121, it also affects the fiber. The fabric 3 is rapidly rotated through the upstream of the guide tube 11 and the towel section to perform an open-air air-floating rotation, and the ## moves along the passage toward the co-structured nozzle 121 on the end surface of the tube wall below the collar. Please refer to the same as - to FIG. 3, between the lower side of the outlet of the common nozzle 121 and the inner side of the inlet of the upstream section of the collecting section 2 'Equipped with a U-shaped swivel plate 14' The upstream side end of the K-shaped swivel plate 14 is lapped in a stepwise manner and fixed to the upstream end face of the U-shaped revolving plate 14 The flat reflective substrate 13 is provided on the downstream outer end surface of the 回转 type rotary plate 14 with the inner separation grid W and the outer separation grid π in the falling section 31, and the downstream section of the guide tube u passage. Directly above the co-configuration nozzle 121, a guide plate 15 is provided, the upstream end of the guide plate 15 is overlapped on the side wall of the guide tube 11 and the downstream end thereof is in the material section of the collecting trough 2 The outer separating grids 22 of the crucibles are connected to each other, and the downstream section space of the duct u passages can be formed into a tapered wedge-shaped gap 151 by the action of the guide plates 15, when the fabric 3 passes through the wedge-shaped gaps Is . . . 25 201142104 151 passages, which can be generated by the lower end surface of the guide plate 15 and the upper end surface of the fiber fabric 3 The action of the movement causes the air in the guide tube 11 to squeeze the air above the fiber fabric 3 into the wedge-shaped gap to generate pressure, so that the fiber fabric 3 passing through the co-structured nozzle 121 is again subjected to downward pressure and can be promoted. The co-configuration nozzle 121 can obtain a large reaction force when the high-speed air stream is ejected and the fiber fabric 3 is impacted, and can also promote the air flow of the fiber fabric 3 on the upper end surface of the fiber fabric 3 when passing through the U-shaped revolving plate 14. Continuously providing a large static air flow, which can provide the reflected energy generated by the fiber fabric 3 between the reflective substrate 13 and the guide plate 15, can be transmitted to the fiber fabric 3, thereby increasing the wave energy and the fluctuation frequency. . · On the downstream exit of the guide tube 11 and the upstream distribution section 31 of the collecting trough 2, and a dispensing liquid removal mechanism is provided. The arranging mechanism is composed of the U-shaped rotating plate 14, the guide plate 15, the inner separating grid 21, the outer separating grid 22, the droplet collecting plate 18, and the working fluid collecting plate 184 described above. An inner separating grid 21 and an outer separating grid 22 are disposed on the inner and outer side walls of the falling section 31 on the upstream side end of the groove 2 passage, and the upstream side end of the inner separating grid 21 is disposed on the u-shaped rotating plate 14 and the droplet collecting At a portion where the plates 18 are connected to each other, the upstream side of the collecting groove 2 is located at the inner side of the falling cloth section 31 in an upright manner, and the downstream side end thereof is connected to the upstream side end of the working fluid collecting plate ι84 φ. At the downstream side end of the droplet collecting plate 18, a collecting guide groove 181' is provided on the lower side wall of the collecting guiding groove 181 and the lowest portion of the working fluid collecting plate 184, and a draft tube 182 is provided. The collected working fluid can be introduced into the lower discharge port m of the collecting trough 2, and the upstream side end of the outer separating grid 22 is connected with the downstream end of the guiding plate 15, and the downstream side end is connected to the collecting trough 2 The lower side slider 23 and the mesh plate 24 are connected to each other to form a collecting groove 2, a circulation passage 221 for forming an air flow between the outer side and the inner side wall of the treatment tank, which can guide the air flow discharged from the outer separation grid 22 to be introduced into the front end of the treatment tank i by the circulation passage 221 26 201142104

導布管11通路上。由外側分離栅網22所排出的液滴及游離纖維和其他不 純固形物體’則可經由處理槽!之内側壁收集,並沿著壁面流向下方排出 口 170排出’導入工作液收集槽213内。在操作時,共構式喷嘴121所喷 出的同速轉流會在纖輯物的下觸面航射作動紐13端面及口型迴 的作用下使空氣流沿著反射作動基板13端面及u型迴轉板外 側端面經由内側分離柵網21的上側方排丨,同時可牵動正在往集布槽a方 向墜落的纖維織物3 ’往内側分離柵網21移動,每當纖維織物受到内側分 離糖網21阻攔時’就會賴峨空氣雜酬分離她21翻的通路, 而使高速空氣流_產线較應發展舰魏,迫使__ 3快速往 外側分離柵網22方向雜㈣落雜段31正Τ謂猶展,因此,在内 側π離栅網21的纖維織物3會受到向下擴張氣流的作用,迫使纖維織物3 由内側分離_ 21上侧方往下_移動,线輯物3離細齡離拇網 21的上側方時,即内侧分離柵網21通路再度開啟,使受到υ型迴轉板14 作用的高处氣流,再度__分離柵網21的通路上排出,而上述的動 作在操作時會_反料_發生,因賴輯物3錢過㈣迴轉板Μ 時會因减空氣流的改變方向,使纖維織物3產生強力的擺動現象,在擺 動的過程中,每當纖維織物3在進行反向擺動的瞬間,它會促使附著在纖 維織物3表面上的殘留功液引發強大的拉張力與反向運動的纖維織物3 發生分離。因此’除了造成大量的殘留工作液辑生液滴的方式脫離 織表面伴隨工氣"IL由内側分離栅網21和外側分離栅網22通路離開集 布s的落布區#又31外’同時也能使掉入到集布槽2的纖維織物並可藉 由擺動作用順利完成摺疊的作業。 I S.1 27 201142104 在導布官11下側方橫跨於通路左右兩側的水平管壁的外側方空間沿 著通路方向在上游及中游區段相對於氣浮喷嘴122區域的人口處,設有一 · 氣浮分配管168 ’在氣浮分配管的上游入口處並設有一空氣流量調節閥 169。在共構式喷嘴12ι的入口處,位於氣浮分配管168的外側方空間,則 設有-共構式分配管167 ’在共構式分配管167的入口處,位於共構式分配 管的外侧方’並於處理槽i内接近中央部位,設有一交流式氣流佈流裝置 163 ’該交流式氣流佈流裝置163,請參_—、圖五、圖五A和圖五_ 示,其主要包括兩支相鄰對稱的左進斜歧管165和右進斜歧管164所組成,馨 以處理槽1橫向為準,左進斜歧管165從左至右,右進斜歧管164從右到 左,長度以導布管11之寬度同寬,若是在雙管導布管11者,則以雙管導 布‘ 11之寬度同寬,若是在四管導布管η者,則以四管導布管11之寬度 同寬,其長度可依據導布管11的多寡任意加寬或縮減,在斜歧管的斜側壁 上沿著通路方向,各設有一排並聯排列組合的分流口 42,在每一分流口 42 上各設有一弧型分流管61 ’弧型分流管61可經由幾何計算使上下錯列排列 的各個分流管構成一排同一方向的通路口 43均能藉由弧型分流管61的作 · 用,使每一弧型分流管61的下游端出口,形成一排並聯排列呈同一方向的 匯流口 166,在匯流口 166處的下游側端,設有一匯流通路管62,其上游 側端入口與匯流口 166相互連通’下游側端出口則與共構式分配管ι67及 氣浮分配管168相互連接連通。 請參照圖六,在相對於液壓霧化喷嘴1216的工作液入口 12162處的下 側方空間上’設有一交流式液流佈流器173,請參閱圖一和圖六所示為交流 式液流佈流器173的構造。其主要包括兩支相鄰排列對稱的左進歧管175 28 201142104 和右進歧管174 ’和-支均壓分gej管176,以處理槽丨橫向鱗,在均壓分 配管176的左右側方,左進歧管175從左至右,右進歧管174從右到左, 長度以導布管11之寬度同寬,若用在雙管導布管11者,則以雙管導布管 11之寬度同I:’若耻四管導布管u者,顺四管導布管1]L之寬度同寬, 其長度可依據導布管u的多寡任意加寬細減在左進歧管175和右進歧 g 174側壁上沿著下游方向,各設有一排分流孔178,在分流孔178與分流 孔178間保持^適當間隙,在兩支的分流孔178 μ,則以相對錯列排列方 式構成兩排不同方向或錯開的喷流口 179,在均壓分配管176上方側壁上, 相對於液壓霧化喷嘴之人口處12161,各設有-分配口 172其可藉由連通管 與液壓霧化噴嘴1216相互連接成一通路。 清同時參照圖-至圖三,在處理槽j中央部位位於工作液收集板184 的上側方另設有-交流式氣流回流裝置19〇,如圖七圖七α、圖七β所示, 為交流式氣細流裝置19〇的構造,其在結構讀线式驗佩裝置163 非常接近,主要包括兩支相鄰對稱的單斜匯流管191和-支Τ字型的匯流 回机e 192所組成’以處理槽i橫向為準,左側匯流管從左至右,右側匯 流管從右到左’長度轉布管u之寬度同寬,若是在雙管導布管U者, 則以雙g導布f 11之寬度同寬,若是在四管導布管U者麻四管導布 & 11之寬度同寬’其長度可依據導布管u的多寡任意加寬或縮減在單 斜匯流S 191的下方側壁上沿著通路彳向,各設冑—排鋪制組合的回 3在單斜匯流官的下游出口端則藉由⑽度的連通迴轉管194與τ 子里的回㈣192之左右兩側端相互連接連通使回流氣流均能在丁字型 中央出口處’再藉由回流輸送管⑽與鼓風機16相互連通。 29 201142104 請同時參照圖-至圖三’在回流輸送管160路上,並設有一氣流過遽 器162、一廢氣排出口及控制閥門2〇〇、一新鮮空氣導入口及控制間門肌、 在廢氣排出叹控制閥門2〇〇及新时氣導入口及控制間門2〇ι間並設有 一流量調節閥202,在加壓循環液流輸送管21〇上並設有一蒸氣輸入口及控 制閥門2H和-其他㈣導人口及控酬門212,在處理槽 設有-工作液收集槽213,及回收或· 口 214,其可暇程需要任意控制 各個導入或排出的閥門。 匕還包括-空氣加熱器⑹及一空氣過濾器162,其分別連接在空氣 輪送71和回流通路16〇 ±,與鼓風機16構成一通路。 在進行染色或其他加工處理,處理槽i内的循環空氣及工作液 士·’.、泉加料裝置2〇或備料桶w的染液或處理液,可經由各自管路系統與 =16和加料_ 73相互連通,可供增壓空氣及加壓染液或處理劑均 式噴嘴121的翻下喷出,同時也那_聰空氣分別經由 乳斤喷嘴122噴出者。 【圖式簡單說明】 圖一.其係為衝動式爆震波快速染色機的結構側面截面圖; H係為衝動式爆震波快速染色機的加高型的機種結構側面截面 目, θ ’、係為_式爆震波快速染色機的加長型賴觀構侧面截面 圖四A.其係為共構式喷嘴口的結構剖面圖; i ; 201142104 8Ε9Β :其係為加設有更換式電擊棒共構対嘴π的結構剖面圖; 圖五.其係為父流式氣流佈流裝置的立體圖; 圖五A:其係為交流式氣流佈流裝置的結構剖面圖; 圖五B.其係為雙管交流式氣流佈流裝置的結構剖面圖; 圖六·其係為交流式液流佈流器的結構剖面圖。 圖七:其係為交流式氣流回流裝置的立體圖; 圖七A:其係為交流式氣流回流裝置的結構剖面圖; • 圖七B:其係為雙管交流式氣流回流裝置的結構剖面圖。 【主要元件符號說明】 處理槽 1 集布槽 2 纖維織物 3 高壓電源設施 5 導布管 11 工作門孔 12 反射作用基板 13 u型迴轉板 14 導向板 15 鼓風機 16 液滴收集板 18 備料桶 19 無泵加料裝置 20 31 201142104 内側分離柵網 21 外側分離柵網 22 滑條 23 網孔板 24 上游落布區段 31 分流口 42 通路口 43 回流口 46 弧型分流管 61 匯流通路管 62 輸送管路系統 71 加壓循環泵浦 72 加料系浦 73 上游口處 111 下游出口處 112 擺布脫液機構 113 共構式喷嘴 121 氣浮喷嘴 122 楔形間隙通路 151 氣流回流管 160 空氣加熱器 161 氣流過渡器 162The guide tube 11 is on the passage. The droplets and free fibers and other impure objects discharged from the outer separation grid 22 can pass through the treatment tank! The inner side wall is collected and flows along the wall surface to the lower discharge port 170 to be discharged into the working fluid collecting tank 213. During operation, the co-rotating nozzle 121 ejects the same speed to flow the air flow along the end surface of the reflective substrate 13 and the lip-shaped back surface of the fiber. The outer end surface of the u-shaped rotating plate is drained via the upper side of the inner separating grid 21, and at the same time, the fiber fabric 3' falling toward the collecting groove a can be moved to the inner separating grid 21, and the fiber fabric is separated by the inner side. When the sugar net 21 blocks, it will separate the passage of her 21 turns, and make the high-speed air flow _ production line should develop the ship Wei, forcing __ 3 to quickly separate the grid from the outer side of the grid 22 (four) The segment 31 is said to be in a state of being, so that the fiber fabric 3 on the inner side of the grid 21 is subjected to the downwardly expanding airflow, forcing the fiber fabric 3 to be separated from the inner side by the upper side. 3, when the fineness is away from the upper side of the thumb net 21, that is, the inner separating grid 21 passage is opened again, so that the high-flow airflow which is subjected to the action of the squeezing type slewing plate 14 is discharged again on the passage of the detachment grid 21, and the above The action will happen when the operation is _ _ _ _ _ _ _ _ _ _ _ _ When the transfer plate Μ is changed, the direction of the air flow is changed, so that the fiber fabric 3 generates a strong swing phenomenon. During the swinging process, whenever the fiber fabric 3 is reversely swung, it promotes adhesion to the fiber fabric 3 The residual working fluid on the surface causes a strong tensile tension to separate from the reversely moving fabric 3 . Therefore, 'except for causing a large amount of residual working fluid to collect droplets, the detached surface is accompanied by the process gas"IL is separated from the distribution area of the cloth s by the inner separation grid 21 and the outer separation grid 22. At the same time, it is also possible to make the fiber fabric which has fallen into the collecting groove 2 and to perform the folding work smoothly by the swinging action. I S.1 27 201142104 The outer space of the horizontal pipe wall spanning the left and right sides of the passage on the side of the guide 11 is along the passage direction in the upstream and midstream sections relative to the population of the air flotation nozzle 122 area, An air flotation distribution pipe 168' is provided at the upstream inlet of the air flotation distribution pipe and is provided with an air flow regulating valve 169. At the entrance of the co-configuration nozzle 12i, located in the outer space of the air flotation manifold 168, a co-construction distribution tube 167' is provided at the inlet of the co-construction distribution tube 167 at the co-construction distribution tube The outer side is disposed in the processing tank i near the central portion, and is provided with an alternating current airflow device 163'. The alternating current airflow device 163, see _, Fig. 5, Fig. 5A and Fig. 5, It mainly consists of two adjacent symmetric left-inclined manifolds 165 and right-inclined inclined manifolds 164, which are in the lateral direction of the processing tank 1 and left-to-right oblique manifolds 165 from left to right and right into the oblique manifolds 164. From right to left, the length is the same width as the width of the guide tube 11, and if it is in the double tube guide tube 11, the width of the double tube guide cloth '11 is the same width, if it is in the four tube guide tube η, then The width of the four-pipe guide tube 11 is the same width, and the length thereof can be arbitrarily widened or reduced according to the number of the guide tubes 11, and a row of shunts arranged in parallel is arranged along the path direction on the oblique side wall of the oblique manifold. The port 42 is provided with an arc-shaped shunt pipe 61 on each of the split ports 42. The arc-shaped shunt pipe 61 can be made up by geometric calculation. Each of the shunt tubes arranged in the wrong row constitutes a row of the passages 43 in the same direction, and the outlets of the downstream end of each of the arc-shaped shunts 61 can be formed in parallel by the arrangement of the arc-type shunt tubes 61. The outlet port 166 in the same direction, at the downstream side end of the junction port 166, is provided with a confluence passage tube 62, the upstream side end inlet and the confluence port 166 are in communication with each other, and the downstream side end outlet is connected with the co-construction distribution tube ι67 and gas. The float distribution tubes 168 are connected to each other. Referring to FIG. 6, an AC flow distributor 173 is disposed on the lower side space at the working fluid inlet 12162 of the hydraulic atomizing nozzle 1216. Please refer to FIG. 1 and FIG. 6 for the AC flow cloth. The configuration of the flow device 173. It mainly comprises two adjacent symmetrically arranged leftward manifolds 175 28 201142104 and a right inlet manifold 174 ' and a branch equal pressure division gej tube 176 for processing the lateral transverse scales of the tank, on the left and right sides of the pressure equalization distribution pipe 176 Square, the leftward manifold 175 is from left to right, the right inlet manifold 174 is from right to left, and the length is the same width as the width of the guide tube 11, and if used in the double tube guide tube 11, the double tube guide is used. The width of the tube 11 is the same as I: 'If the four tube guide tube u is the same, the width of the four tube guide tube 1] L is the same width, and the length can be arbitrarily widened according to the number of the guide tube u. A pair of diverting holes 178 are respectively disposed on the side walls of the manifold 175 and the right inward g 174 along the downstream direction, and a proper gap is maintained between the diverting holes 178 and the diverting holes 178, and 178 μ in the diverging holes of the two branches are opposite The staggered arrangement constitutes two rows of differently or staggered spouts 179, on the upper side wall of the equalizing distribution pipe 176, with respect to the population portion 12161 of the hydraulic atomizing nozzle, each of which is provided with a distribution port 172 which can be connected The tube and the hydraulic atomizing nozzle 1216 are connected to each other to form a passage. Referring to FIG. 3 to FIG. 3 simultaneously, an AC-type airflow reflow device 19 is disposed on the upper side of the working fluid collecting plate 184 at the central portion of the processing tank j, as shown in FIG. 7 and FIG. The structure of the AC gas flow device 19A is very close to the structure read line type inspection device 163, and mainly comprises two adjacent symmetric single oblique flow tubes 191 and a branch-shaped confluent machine e 192. 'The lateral direction of the treatment tank i is the same, the left side of the confluence tube from left to right, the right side of the confluence tube from right to left 'the length of the distribution tube u is the same width, if it is in the double tube guide tube U, then double g guide The width of the cloth f 11 is the same width, if it is in the four tube guide tube U, the four tube guide cloth & 11 width and width 'the length can be arbitrarily widened or reduced according to the number of the guide tube u in the single oblique convergence S The lower side wall of the 191 is along the path of the passage, and the back 3 of each of the raft-distribution combinations is connected to the downstream end of the single-slope confluence by the (10) degree of the connecting rotary tube 194 and the back of the τ sub (four) 192 or so. The two ends are connected to each other so that the return airflow can be at the T-shaped central outlet and then by the return duct. Blower 16 communicate with each other. 29 201142104 Please also refer to the figure - to Figure 3 'on the return pipe 160, and is provided with a gas flow damper 162, an exhaust gas discharge port and a control valve 2 〇〇, a fresh air inlet and a control door muscle, The exhaust gas discharge sigh control valve 2〇〇 and the new gas inlet port and the control door 2〇1 are provided with a flow regulating valve 202, and a steam inlet port and a control valve are arranged on the pressurized circulating liquid flow pipe 21〇 2H and - other (4) population and control gate 212 are provided with a working fluid collection tank 213 and a recovery or port 214 in the treatment tank, which can arbitrarily control each of the introduced or discharged valves. The crucible further includes an air heater (6) and an air filter 162 connected to the air train 71 and the return passage 16〇, respectively, to form a passage with the blower 16. In the dyeing or other processing, the circulating air in the treatment tank and the dyeing liquid or treatment liquid of the working liquid, the spring feeding device 2 or the preparation tank w, can be fed through the respective piping system with =16 and feeding. _73 is connected to each other, and can be used for the pouring and discharging of the pressurized air and the pressurized dyeing liquid or the treating agent homogenizing nozzle 121, and at the same time, the _Cong air is ejected through the nipple nozzle 122, respectively. [Simple diagram of the diagram] Figure 1. It is a side profile view of the structure of the impulsive detonation wave fast dyeing machine; the H system is the side section of the heightened type of structure of the impulse detonation wave fast dyeing machine, θ ', system A side view of the elongated type of the _-type detonation wave fast dyeing machine. A. It is a structural sectional view of the co-structured nozzle opening; i; 201142104 8Ε9Β: the system is equipped with a replacement electric shock bar. Figure 5 is a perspective view of the parent flow airflow device; Figure 5A: is a structural cross-sectional view of the AC airflow device; Figure 5B. A cross-sectional view of the structure of the AC flow distribution device; Fig. 6 is a structural sectional view of the AC flow distributor. Figure 7: A perspective view of an AC flow recirculation device; Figure 7A: A cross-sectional view of the AC flow recirculation device; Figure 7B: A cross-sectional view of a dual-tube AC flow recirculation device . [Main component symbol description] Treatment tank 1 Distribution tank 2 Fiber fabric 3 High-voltage power supply facility 5 Guide tube 11 Working door hole 12 Reflecting substrate 13 U-shaped rotating plate 14 Guide plate 15 Blower 16 Droplet collecting plate 18 Preparation bin 19 Pumpless feeding device 20 31 201142104 Inner separating grid 21 Outer separating grid 22 Slider 23 Mesh plate 24 Upstream falling section 31 Splitting port 42 Access port 43 Return port 46 Arc type shunt pipe 61 Confluence path pipe 62 Pipe Road system 71 Pressurized circulation pump 72 Feeding line 73 Upstream port 111 Downstream exit point 112 Disengagement mechanism 113 Co-configuration nozzle 121 Air float nozzle 122 Wedge clearance path 151 Airflow return pipe 160 Air heater 161 Air flow transition 162

32 20114210432 201142104

交流式氣流佈流裝置 163 右進斜歧管 164 左進斜歧管 165 匯流口 166 共構式分配管 167 氣浮分配管 168 空氣流量調節閥 169 染液回流管 170 分配口 172 交流式液流佈流器 173 右進歧管 174 左進歧管 175 均壓分配管 176 分流孔 178 喷流口 179 收集導流溝槽 181 導流管 182 工作液收集板 184 交流式氣流回流裝置 190 單斜匯流管 191 T字型的匯流回流管 192 廢氣排出口及控制閥門 200 33 201142104 新鮮空氣導入口及控制閥門 201 流量調節閥 202 流量調節閥 203 加壓循環液流輸送管 210 蒸氣輸入口及控制閥門 211 其他氣體導入口及控制閥門 212 工作液收集槽 213 工作液回收或排出口閥門 214 工作液篩濾器 215 工作液熱交換器 220 循環通路 221 環狀形電靶 12111 喷射管 12121 更換式電擊棒 12122 高壓電源連接端子 12123 接地連接端子 12124 液壓霧化噴嘴 1216 液壓霧化噴嘴口 12161 工作液入口 12162 滑動閥桿 12164 閥座 12165 彈簧活塞 12167AC airflow device 163 Right-inclined manifold 164 Left-inclined manifold 165 Confluence port 166 Co-construction distribution pipe 167 Air flotation distribution pipe 168 Air flow regulating valve 169 Dyeing liquid return pipe 170 Distribution port 172 AC-type liquid flow cloth Flow 173 right feed manifold 174 left feed manifold 175 pressure equalization distribution tube 176 split hole 178 spray port 179 collect flow guide groove 181 guide tube 182 working fluid collection plate 184 AC flow return device 190 single oblique flow tube 191 T-shaped manifold return pipe 192 Exhaust gas exhaust port and control valve 200 33 201142104 Fresh air inlet port and control valve 201 Flow regulating valve 202 Flow regulating valve 203 Pressurized circulating fluid flow pipe 210 Vapor input port and control valve 211 Other Gas inlet and control valve 212 Working fluid collection tank 213 Working fluid recovery or discharge valve 214 Working fluid sieve filter 215 Working fluid heat exchanger 220 Circulation passage 221 Ring-shaped electric target 12111 Injection tube 12121 Replacement electric shock rod 12122 High-voltage power supply Connection terminal 12123 ground connection terminal 12124 hydraulic atomization nozzle 1216 hydraulic atomization Fluid inlet mouthpiece 12161 12162 12164 sliding stem valve spring piston 12167 12165

34 201142104 12169 作動流體入口34 201142104 12169 Actuating fluid inlet

3535

Claims (1)

201142104 七、申請專利範圍·· 1· 一種衝動式爆震波快速染色機,其至少由一個或多個並排組合的處理 槽⑴,並且與輸送管路系統(71)(160)(210)(170)相互連接連通,在每一 個處理槽(1)内各設有一個可提供紡織品集疊的集布槽(2)及可提供紡 織品加速移動的導布管(11),二者的前後兩端分別相互連通並構成一條 寬闊的循環通路,可供紡織品在通路上以擴幅的方式快速完成染色及 其他加工處理者,其特徵在於包括有: 一氣浮喷嘴(122) ’該氣浮喷嘴(122)係由多數小孔通路所組成,其鲁 裝置於沿著該導布管(11)通路的上游及中游區段的下方管壁上,該氣浮 喷嘴(122)藉由氣浮分配管(168)及氣流輸送管路系統(71)(16〇)與鼓風 機(16)相互連接連通; 一共構式噴嘴(121),該共構式噴嘴(121)係由一氣體噴射管(12121) 和一液壓霧化喷嘴(1216)所組成,其裝置於導布管(11)的下游區段的截 斷面上’接近導布管(11)出口處,以複數個並排組合的一排共構式喷嘴 (121) ’其可藉由一共構式分配管(167)及氣流輸送管路系統(71)(16〇)及鲁 液流輸送管路系統(210)(170)與鼓風機(16)和加壓循環泵浦(72)相互連 接連通。 2·如申請專利範圍第1項所述之衝動式爆震波快速染色機,其中該共構 式喷嘴(121)的喷射管(12121)中央通路上,入口處(1213)上游側端設有 一液壓霧化噴嘴(1216),在液壓霧化喷嘴口(12161)通路的中央處設有 一更換式電擊棒(12122),其中放電尖端位在液壓霧化喷嘴口(12161) 中央處,另一端則延伸至液壓霧化喷嘴(1216)體外側方,其經由電纜 36 201142104 線於尚壓電源設施5互相連接,在共構式喷嘴口(1211)上設有一環狀型 電靶(12111),其於共構式喷嘴口(1211)形成一共構體,其經由電纜線 於地表互相連接。 3. 如申請專利範圍第1項所述之衝動式爆震波快速染色機,更包括一反 射作動基板(13),其裝置於共構式喷嘴(丨21)的下游方向以階梯式方式 搭接固定於共構式喷嘴(121)的下側方上。 4· 如申請專利範圍第1項所述之衝動式爆震波快速染色機,更包括一u 型迴轉板(14) ’其裝置在共構式喷嘴(121)的下游方向,位於導布管(11) 通路出口的下侧方與集布槽(2)上游入口的内側方之間。 5. 如申請專利範圍第1項所述之衝動式爆震波快速染色機,另外包括有: 一 U型迴轉板(14),其設置在反射作動基板(13)的下游側方是由反 射作動基板(13)延伸構成的,以漸進方式構成一弧線形迴路; 一液滴收集板(18),其設置在U型迴轉板(14)下游側端; 一收集導流溝槽(181),其設置在液滴收集板(18)的下游側端; 一導流管(182),其設置在收集導流溝槽(181)的下側壁上; 一内側分離柵網(21),其設置在上游側端設在U型迴轉板(η)與液 滴收集板(18)互相連接的部位處,以垂直或接近垂直的方式設立在集 布槽(2)上游侧端的落布區段(31)内側處; 一外側分離柵網(22)的上游側端則設在導向板(15)的下游端,其下 游側端則與集布槽通路下側方的滑條(23)及網孔板(24)相互連接; 一工作液收集板(184),其設置在内侧分離柵網(21)下游側端,位 於集布槽(2)通路的上側方。 37 201142104 6. 一種衝動式爆震波快速染色機,其至少由一個或多個並排組合的處理 槽(1) ’並且輸送管路系統(71)(160)(210)(170)相互連接連通,在每一個 ~ 處理槽(1)内各設有一個可提供紡織品集疊的集布槽(2)及可提供纺織 品加速移動的導布管(11),二者的前後兩端分別相互連通並構成一條寬 闊的循環通路,可供紡織品在通路上以擴幅的方式快速完成染色及其 他加工處理者,其特徵在於包括有: 一氣浮喷嘴(122) ’該氣浮喷嘴(122)係由多數小孔通路所組成,其 裝置於沿著該導布管(11)通路的上游及t游區段的下方管壁上,該氣浮 _ 噴嘴(122)藉由氣浮分配管(168)及氣流輸送管路系統(71)(160)與鼓風 機(16)相互連接連通; 一共構式喷嘴(121),該共構式喷嘴(121)係由一氣體喷射管(12121) 和一液壓霧化喷嘴(1216)所組成,其中該共構式喷嘴(121)的喷射管 (12121) 中央通路上’入口處(1213)上游側端設有一液壓霧化嗔嘴 (1216),在液壓霧化喷嘴口(12161)通路的中央處設有一更換式電擊棒 (12122) ’其中放電尖端位在液壓霧化喷嘴口(12161)中央處,另一端則鲁 延伸至液壓霧化喷嘴體(1216)外側方,其經由電纜線於高壓電源設施5 互相連接’在共構式喷嘴口(1211)上設有一環狀型電起(12111),其於 共構式噴嘴口 (1211)形成一共構體,其經由電纜線於地表互相連接,該 共構式噴嘴(121)裝置於導布管(11)的下游區段的截斷面上,接近導布 管(11)出口處,以複數個並排組合的一排共構式喷嘴(121),其可藉由 一共構式分配管(167)及氣流輸送管路系統(71)(16〇)及液流輸送管路系 統(210)(170)與鼓風機(16)和加壓循環泵浦(72)相互連接連通。 38 201142104 7. 8. 如申請專利範圍第6項所述之衝動式爆震波快速染色機,更包括一u 型迴轉板(14),其裝置在共構式喷嘴(121)的下游方向,位於導布管(11) 通路出口的下側方與集布槽(2)上游入口的内側方之間。 如申請專利範圍第6項所述之衝動式爆震波快速染色機,更包括一反 射作動基板(13),其裝置於共構式喷嘴(121)的下游方向以階梯式方式 搭接固定於共構式喷嘴(121)的下側方上。 9. • 如申請專利範圍第6項所述之衝動式爆震波快速染色機,另外包括有: 一U型迴轉板(14) ’其設置在反射作動基板(13)的下游側方是由反 射作動基板(13)延伸構成的,以漸進方式構成一弧線型迴路; 一液滴收集板(18),其設置在U型迴轉板(14)下游側端; 一收集導流溝槽(181),其設置在液滴收集板(18)的下游側端; 一導流管(182),其設置在收集導流溝槽(181)的下側壁上; 一内側分離柵網(21),其設置在上游側端設在U型迴轉板(14)與液 • 滴收集板(18)互相連接的部位處,以垂直或接近垂直的方式設立在集 布槽(2)上游侧端的落布區段(31)内側處; 一外側分離柵網(22)的上游側端則設在導向板(15)的下游端,其下 游側端則與集布槽(2)通路下側方的滑條(23)及網孔板(24)相互連接; 一工作液收集板(184),其設置在内侧分離柵網(21)下游侧端》 10. 如申請專利範圍第6項所述之衝動式爆震波快速染色機,其中該交流 式液流佈流器(173)包括兩支相鄰排列對稱的左進歧管(175)和右進歧 管(174),和一均壓分配管(63),以處理槽(1)橫向為準,在均壓分配管 (63)的左右侧方,左進歧管(175)從左至右,右進歧管(174)從右到左, 39 201142104 長度以導布管(11)之寬度同寬,若用在雙管導布管(11)者,則以雙管導 布管(11)之寬度同寬’若用在四管導布管(11)者,則以四管導布管(11) 之寬度同寬,其長度可依據導布管(11)的多寡任意加寬或縮減,在左進 歧管(Π5)和右進歧管(174)侧壁上沿著下游方向,各設有一排分流孔 (81) ’在分流孔(81)與分流孔(81)間保持一適當間隙,在兩支的分流孔 (81)間,則以相對錯列排列方式構成兩排不同方向或錯開的喷流口 (44),在均壓分配管(63)上方側壁上,相對於液壓霧化喷嘴(12163)之入 口處’各設有一出口其可藉由連通管與液壓霧化喷嘴(12163)相互連接 成一通路。 11. 12. 如申請專利範圍第6項所述之衝動式爆震波快速染色機,其氣流輸送 管路系統更包括一交流式氣流回流裝置(190),該交流式氣流回流裝置 (190)與回流管路系統(16〇)於鼓風機(16)(17)互相連接連通。 一種衝動式爆震波快速染色機,其至少由一個或多個並排組合的處理 槽⑴,並且輸送管路系統(71)(160)(210)(170)相互連接連通,在每一個 處理槽(1)内各設有一個可提供紡織品集疊的集布槽(2)及可提供紡織 品加速移動的導布管(11),二者的前後兩端分別相互連通並構成一條寬 闊的循環通路,可供紡織品在通路上以擴幅的方式快速完成染色及其 他加工處理者,其特徵在於包括有: 一氣浮喷嘴(122),該氣浮喷嘴(122)係由多數小孔通路所組成,其 裝置於沿著該導布管(11)通路的上游及中游區段的下方管壁上,該氣浮 噴嘴(122)藉由氣浮分配管(168)及氣流輸送管路系統(71)⑽)與鼓風 機(16)相互連接連通; 201142104 一共構式喷嘴(121),該共構式喷嘴(121)係由一氣體噴射管(12121) ♦ 和一液壓霧化喷嘴(1216)所組成,其裝置於導布管(11)的下游區段的截 斷面上,接近導布管(11)出口處,以複數個並排組合的一排共構式喷嘴 (121) ’其可藉由一共構式分配管(167)及氣流輸送管路系統(71)(16〇) 及液流輸送管路系統(210)(170)與鼓風機(16)和加壓循環泵浦(72)相互 連接連通; 一交流式氣流佈流裝置(163),其設置在氣浮喷嘴(122)和共構式喷 • 嘴(121)與輸送管路系統(71)之間; 一交流式液流佈流器(173),其設置在液壓霧化喷嘴(1216)與輸送 管路系統(210)之間。 13.如申請專利範圍第12項所述之衝動式爆震波快速染色機,其中該共構 式喷嘴(121)的噴射管⑴⑵)中央通路上,人口處(1213)上游側端設有 一液壓霧化喷嘴(1216),在液壓霧化喷嘴口(12161)通路的中央處設有 -更換式電擊棒(12122),其中放電尖端位在液壓霧化喷嘴(12161)口中 釀央處,另-端則延伸至液壓霧化喷嘴體(m6)外側方,其經由電規線 於高壓電源設施5互相連接,在共構式噴嘴口(1211)上設有一環狀形電 靶(12111)並設有一連接端子⑽23),其於共構式喷嘴口⑽^形成一 共構體,其經由電纜線於地表互相連接。 U.如申請專利範圍第12項所述之衝動式爆震波快速染色機,更包括一 口 型迴轉板(M),其裝置在共構式喷嘴_的下游方向,位於導布管(11) 通路出π的下财與鮮槽⑵上游人口的内側方之間。 15·如中請專利範圍第12項所述之衝動式爆震波快速染色機,更包括一反 [S. 1 201142104 射作動基板(13),其裝置於共構式喷嘴(121)的下游方向以階梯式方式 搭接固定於共構式喷嘴(121)的下側方上。 16. 如申請專利範圍第12項所述之衝動式爆震波快速染色機,另外包括 有: 一U型迴轉板(14),其設置在反射作動基板(13)的下游側方是由反 射作動基板(13)延伸構成的,以漸進方式構成一弧線型迴路; 一液滴收集板(18),其設置在U型迴轉板(14)下游側端; 一收集導流溝槽(181),其設置在液滴收集板(18)的下游側端; _ 一導流管(182),其設置在收集導流溝槽(181)的下侧壁上; 一内側分離栅網(21),其設置在上游侧端設在U型迴轉板(14)與液 滴收集板(18)互相連接的部位處,以垂直或接近垂直的方式設立在集 布槽(2)上游侧端的落布區段25(21)内側處; 一外側分離柵網(22)的上游側端則設在U型迴轉板(14)的下游 端’其下游側端則與集布槽通路下側方的滑條(23)及網孔板(24)相互連 接; # 一工作液收集板(184),其設置在内侧分離栅網(21)下游側端。 17. 如申請專利範圍第12項所述之衝動式爆震波快速染色機,其中該交流 式氣流佈流裝置(16)包含兩支相鄰對稱的左進斜歧管(165)和右進斜歧 管(164)所組成’以處理槽⑴橫向為準,左進斜歧管(165)從左至右,右 進斜歧管(164)從右到左’長度以導布管(11)之寬度同寬,若是在雙管 導布管(11)者,則以雙管導布管(11)之寬度同寬,若是在四管導布管(11) 者’則以四管導布管(11)之寬度同寬,其長度可依據導布管(11)的多寡 42 201142104 任意加寬或縮減,在斜歧管的斜侧壁上沿著通路方向,各設有一排並 聯排列組合的分流口 (42),在每一分流口 (42)上各設有一弧型分流管 (61),弧型分流管(61)可經由幾何計算使上下錯列排列的各個分流管構 成一排同一方向的通路口(43)均能藉由弧型分流管(61)的作用,使每一 弧型分流管(61)的下游端出口,形成一排並聯排列呈同一方向的匯流 口 (166) ’在匯流口 (166)處的下游侧端,設有一漸擴的匯流通路管_, 其上游側端入口與匯流口(166)相互連通,下游側端出口則與共構式分 配管(167)及氣浮分配管(168)相互連接連通。 18.如申請專利範圍第12項所述之衝動式爆震波快速染色機,其中該鼓風 機(16)的吸入口上游通路上設有一新空氣導入口 (2〇1)及廢氣排出口 (200),以及處理槽(1)下側方最底處的處理液回收或排出口在各導入 及排出口上各設有一控制閥門,其可依製程需要任意控制。 19·如申請專利範圍第12項所述之衝動式爆震波快速染色機,另外包含有 -空氣熱交換器(161)及-空氣過絲(162),和—工作液熱交換器(22〇) 及-工作液篩漉器(215) ’其分別連接在氣體輸送管路系統(71)⑽)及 液流輸送管路系統(210)(170)上。 20.-種衝動式爆震波快速染色機,其至少由一個或多個並排組合的處理 槽⑴,並且輸送管路系統(71)(160)(210)(170)相互連接連通,在每一個 處理槽⑴内各設有-個可提供紡織品集疊的集布槽⑵及可提供纺織 品加速移動的導布管(11),二者的前後兩端分別相互連通並構成一條寬 闊的循環通路,可供紡織品在通路上以擴幅的方式快速完成染色及其 他加工處理者,其特徵在於包括有: 43 201142104 一氣浮喷嘴(122),該氣浮喷嘴(122)係由多數小孔通路所組成,其 裝置於沿著該導布管(11)通路的上游及中游區段的下方管壁上,該氣浮 喷嘴(122)藉由氣浮分配管(168)及氣流輸送管路系統(71)(160)與鼓風 機(16)相互連接連通; 一共構式噴嘴(121),該共構式喷嘴(121)係由一氣體喷射管(12121) 和一液壓霧化喷嘴(1216)所組成,其中該共構式喷嘴(121)的喷射管 (12121) 中央通路上,入口處(1213)上游側端設有一液壓霧化喷嘴 (1216),在液壓霧化噴嘴口(1216)通路的中央處設有一更換式電擊棒鲁 (12122) ’其中放電尖端位在液壓霧化喷嘴口(12161)中央處,另一端則 延伸至液壓霧化喷嘴體(1216)外側方,其經由電纔線於高壓電源互相 連接,在共構式喷嘴口(1211)上設有一環狀型電靶(12111),其於共構 式噴嘴口(1211)形成一共構體,其經由電纜線於地表互相連接,該共構 式噴嘴(121)裝置於導布管(η)的下游區段的截斷面上,接近導布管(11) 出口處,以複數個並排組合的一排共構式喷嘴(121),其可藉由一共構 式分配管(167)及氣流輸送管路系統(71)(16〇)及液流輸送管路系統馨 (210)(170)與鼓風機(16)和加壓循環泵浦(72)相互連接連通; 一交流式氣流佈流裝置(163) ’其設置在氣浮喷嘴(122)和共構式喷 嘴(121)與氣流輸送管路系統(71)之間; 一交流式液流佈流器(173),其設置在液壓霧化喷嘴(1216)與液流 輸送管路系統(210)之間。 21.如中請專利細第20項所述之衝動式爆震波快速染色機,更包括一u 型迴轉板(14) ’其裝置在共構式噴嘴(121)的下游方向,位於導布管(11) 44 201142104 通路出口的下側方與集布槽(2)上游入口的内侧方之間。 22·如申請專利範圍第20項所述之衝動式爆震波快速染色機,更包括一反 射作動基板(13) ’其裝置於共構式喷嘴(121)的下游方向以階梯式方式 搭接固定於共構式喷嘴(121)的下侧方上。 23. 如申請專利範圍第20項所述之衝動式爆震波快速染色機,另外包括 有: 一U型迴轉板(14),其設置在反射作動基板(13)的下游側方是由反 φ 射作動基板(13)延伸構成的,以漸進方式構成一弧線型迴路; 一液滴收集板(18),其設置在U型迴轉板(14)下游側端; 一收集導流溝槽(181),其設置在液滴收集板(18)的下游侧端; 一導流管(182),其設置在收集導流溝槽(181)的下側壁上; 一内侧分離柵網(21),其設置在上游側端設在U型迴轉板(14)與液 滴收集板(18)互相連接的部位處,以垂直或接近垂直的方式設立在集 布槽(2)上游側端的落布區段(31)内側處; 一外側分離栅網(22)的上游側端則設在導向板(15)的下游端,其下 游側端則與集布槽(2)通路下側方的滑條(23)及網孔板(24)相互連接; 一工作液收集板(184),其設置在内侧分離柵網(21)下游側端。 24. 如申請專利範圍第20項所述之衝動式爆震波快速染色機,其中該交流 式液流佈流器(173)包括兩支相鄰排列對稱的左進歧管(175)和右進歧 管(174),和一支均壓分配管(63),以處理槽(1)橫向為準,在均壓分配 管(63)的左右側方,左進歧管(175)從左至右,右進歧管(174)從右到左, 長度以導布管(11)之寬度同寬,若用在雙管導布管(11)者,則以雙管導 45 201142104 布s (11)之寬度同寬’若用在四管導布管⑼者,則以四管導布管⑽ 之寬度同寬,其長度可依據導布管⑼的多寡任意加寬或縮減,在左進 歧管⑽和右進歧管(174)側壁上沿著下游方向,各設有一排分流孔 _,在分流孔(17験分流孔⑽)間保持一適當間隙,在兩支的分流 孔(178)間,則以相對錯列排列方式構成兩排不同方向或錯開的嘴流口 (Π9) ’在均壓分配管(176)上方側壁上,相對於液壓霧化喷嘴⑽句之 工作液入口處(12161),各設有-出口(172)其可藉由連通管與液壓霧化 喷嘴(1216)相互連接成一通路。 25. 如申請專職圍第2G綱叙衝赋爆震波快速染色機,其中該 交流式氣流佈流裝置(163)包含兩支相鄰對稱的左進斜歧管(165)和右 進斜歧嘗(164)所組成,以處理槽(1)橫向為準,左進斜歧管(Ms)從左至 右,右進斜歧管(164)從右到左,長度以導布管(11)之寬度同寬,若是 在雙官導布管(11)者,則以雙管導布管(11)之寬度同寬,若是在四管導 布管(11)者,則以四管導布管⑼之寬度同寬,其長度可依據導布管⑽ 的多春任意加寬或縮減,在斜歧管的斜側壁上沿著通路方向,各設有 一排並聯排列組合的分流口(42),在每一分流口(42)上各設有一弧型分 流管(61),弧型分流管(61)可經由幾何計算使上下錯列排列的各個分流 管構成一排同一方向的通路口(43)均能藉由弧型分流管(61)的作用,使 每一孤型分流管(61)的下游端出口 ’形成一排並聯排列呈同一方向的 匯流口(166) ’在匯流口(166)處的下游侧端出口則分別與共構式分配管 (167)及氣浮分配管(168)相互連接連通’在氣浮分配管(168)入口處設有 一氣流調節閥門(169)。 46 201142104 26. 如申請專利範圍第20項所述之衝動式爆震波快速染色機,其輸送管路 系統更包括一交流式氣流回流裝置(19〇),該交流式氣流回流裝置 (190),主要包括兩支相鄰對稱的單斜匯流管(191)和一支τ字型的匯流 回流管(192)所組成,以處理槽(1)橫向為準,左側匯流管從左至右,右 側匯流管從右到左,長度以導布管(11)之寬度同寬,若是在雙管導布管 (11)者,則以雙管導布管(11)之寬度同寬,若是在四管導布管(11者, 則以四管導布管(11)之寬度同寬,其長度可依據導布管(11)的多寡任意 加寬或縮減,在單斜匯流管(191)的下方側壁上沿著通路方向,各設有 一排並聯排列組合的回流口(193),在單斜匯流管的下游出口端則藉由 180度的連通迴轉管(194)與Τ字型的回流管(192)之左右兩侧端相互連 接連通,使回流氣流均能在Τ字型中央出口處,再藉由回流輸送管 (160)與鼓風機(16)相互連通。 27. 如申請專利範圍第2〇項所述之衝動式爆震波快速染色機,其中該鼓風 機(16)的吸入口上游通路上設有一新空氣導入口 (2〇1)及廢氣排出口 (200),以及處理槽(1)下側方最底處的處理液回收或排出口在各導入 及排出口上各設有一控制閥門,其可依製程需要任意控制。 28. 如申請專利範圍第2〇項所述之衝動式爆震波快速染色機,另外包含有 一空氣熱父換器(161)及一空氣過渡器(162),和一工作液熱交換器(220) 及-工作液筛濾器(215),其分別連接在氣體輸送管路系統(71)(16〇)及 液流輸送管路系統(210)(170)上。201142104 VII. Patent Application Range··1· An impulse detonation wave fast dyeing machine, which is composed of at least one or more processing tanks (1) combined side by side, and with the conveying pipeline system (71) (160) (210) (170) Connected to each other, each of the processing tanks (1) is provided with a collecting groove (2) for providing textile stacking and a guiding tube (11) for providing accelerated movement of the textile, the front and rear ends of the two They are connected to each other and form a wide circulation passage for the textile to quickly complete the dyeing and other processing on the passage, and are characterized by: an air floating nozzle (122) 'the air floating nozzle (122) ) consisting of a plurality of small orifice passages disposed along the lower and downstream sections of the passage of the conduit (11), the air floatation nozzle (122) being supported by an air flotation tube ( 168) and the airflow conveying pipeline system (71) (16〇) and the blower (16) are connected to each other; a common configuration nozzle (121), the co-construction nozzle (121) is composed of a gas injection pipe (12121) and a hydraulic atomizing nozzle (1216), which is arranged downstream of the guide tube (11) On the section of the section, 'close to the exit of the duct (11), a plurality of side-by-side combined rows of co-construction nozzles (121) 'which can be connected by a common distribution tube (167) and airflow pipeline system (71) (16 〇) and the Lu fluid flow delivery piping system (210) (170) are in interconnected communication with the blower (16) and the pressurized circulation pump (72). 2. The impulsive detonation wave fast dyeing machine according to claim 1, wherein a hydraulic mist is provided on the central passage of the injection pipe (12121) of the co-structured nozzle (121) at the upstream end of the inlet (1213). The nozzle (1216) is provided with a replacement electric hammer (12122) at the center of the passage of the hydraulic atomizing nozzle (12161), wherein the discharge tip is located at the center of the hydraulic atomizing nozzle opening (12161), and the other end extends to The outer side of the body of the hydraulic atomizing nozzle (1216) is connected to the power supply device 5 via the cable 36 201142104, and a ring-shaped electric target (12111) is disposed on the common nozzle port (1211). The configuration nozzle opening (1211) forms a comon that is interconnected to the surface via a cable. 3. The impulse detonation wave fast dyeing machine according to claim 1, further comprising a reflection actuation substrate (13), the device being overlapped in a stepwise manner in the downstream direction of the co-structure nozzle (丨21) It is fixed to the lower side of the co-structured nozzle (121). 4. The impulse detonation wave fast dyeing machine described in claim 1 further comprises a u-shaped rotary plate (14) whose device is located downstream of the co-structured nozzle (121) and located at the guide tube ( 11) Between the lower side of the passage outlet and the inner side of the upstream inlet of the collecting tank (2). 5. The impulsive detonation wave fast dyeing machine according to claim 1, further comprising: a U-shaped rotating plate (14) disposed on the downstream side of the reflective actuation substrate (13) by reflection The substrate (13) is extended to form an arc-shaped circuit in a progressive manner; a droplet collecting plate (18) disposed at a downstream side end of the U-shaped rotating plate (14); a collecting guiding groove (181), It is disposed at the downstream side end of the droplet collecting plate (18); a guiding tube (182) disposed on the lower side wall of the collecting guiding groove (181); and an inner separating grid (21), which is disposed The upstream side end is provided at a portion where the U-shaped swivel plate (n) and the liquid droplet collecting plate (18) are connected to each other, and the falling portion of the upstream side end of the collecting groove (2) is set in a vertical or nearly vertical manner ( 31) the inner side; the upstream side end of an outer separating grid (22) is disposed at the downstream end of the guiding plate (15), and the downstream side end thereof is opposite to the sliding strip (23) and the net of the lower side of the collecting groove passage. The orifice plates (24) are connected to each other; a working fluid collecting plate (184) is disposed at the downstream side end of the inner separating grid (21) and located at the upper side of the collecting groove (2) passage. 37 201142104 6. An impulse detonation wave fast dyeing machine interconnected by at least one or more side-by-side combined treatment tanks (1)' and a delivery piping system (71) (160) (210) (170), Each of the processing tanks (1) is provided with a collecting groove (2) for providing textile stacking and a guiding tube (11) for providing accelerated movement of the textile, and the front and rear ends of the two are respectively connected to each other. And forming a wide circulation passage for the textile to quickly complete the dyeing and other processing on the passage, characterized in that it comprises: an air floating nozzle (122) 'The air floating nozzle (122) is composed of A plurality of small orifice passages are formed on the upstream of the passage of the conduit (11) and the lower wall of the t-tour section, the air float_nozzle (122) is provided by an air flotation distribution pipe (168) And the airflow conveying pipeline system (71) (160) and the blower (16) are connected to each other; a common configuration nozzle (121), the co-construction nozzle (121) is composed of a gas injection pipe (12121) and a hydraulic mist The nozzle (1216) is composed of a spray pipe (12121) of the common nozzle (121) on the central passage 'The upstream side of the inlet (1213) is provided with a hydraulic atomizing nozzle (1216), and at the center of the passage of the hydraulic atomizing nozzle (12161) is provided a replacement electric shock rod (12122) 'where the discharge tip is located in the hydraulic mist At the center of the nozzle opening (12161), the other end extends to the outside of the hydraulic atomizing nozzle body (1216), which is connected to each other via a cable at the high-voltage power supply facility 5 'on the common-purpose nozzle opening (1211) a ring-shaped electric device (12111), which forms a commiser at the common-type nozzle opening (1211), which is connected to each other via a cable line at a surface, and the common-structure nozzle (121) is disposed on the guide tube (11) On the section of the downstream section, close to the outlet of the duct (11), a plurality of side-by-side combined rows of co-constructed nozzles (121), which can be connected by a common distribution tube (167) and an air flow duct The road system (71) (16 〇) and the liquid flow delivery piping system (210) (170) are in interconnected communication with the blower (16) and the pressurized circulation pump (72). 38 201142104 7. 8. The impulse detonation wave fast dyeing machine according to item 6 of the patent application scope further comprises a u-shaped rotary plate (14), the device is located downstream of the co-structured nozzle (121), The guide tube (11) is between the lower side of the passage outlet and the inner side of the upstream inlet of the collecting duct (2). The impulse detonation wave fast dyeing machine according to claim 6 further includes a reflection actuation substrate (13), and the device is lapped and fixed in a stepwise manner in a downstream direction of the co-structure nozzle (121). The lower side of the configuration nozzle (121). 9. The impulsive detonation wave fast dyeing machine described in claim 6 of the patent application additionally includes: a U-shaped rotary plate (14) 'which is disposed on the downstream side of the reflective actuation substrate (13) by reflection The actuating substrate (13) is extended to form an arc-shaped circuit in a progressive manner; a droplet collecting plate (18) disposed at a downstream side end of the U-shaped rotating plate (14); and a collecting guiding groove (181) Provided at a downstream side end of the droplet collecting plate (18); a draft tube (182) disposed on the lower side wall of the collecting guiding groove (181); and an inner separating grid (21) The upstream side is disposed at a portion where the U-shaped rotating plate (14) and the liquid-collecting collecting plate (18) are connected to each other, and is disposed in a vertical or near-vertical manner at a feeding end of the upstream side of the collecting groove (2). The inner side of the segment (31); the upstream side end of the outer separating grid (22) is disposed at the downstream end of the guiding plate (15), and the downstream side end thereof is opposite to the sliding side of the lower side of the collecting groove (2) (23) and the mesh plate (24) are connected to each other; a working fluid collecting plate (184) disposed at the downstream side end of the inner separating grid (21)" 10. As claimed in claim 6 The impulsive detonation wave fast dyeing machine, wherein the AC flow distributor (173) comprises two adjacent symmetrically arranged leftward manifolds (175) and rightward manifolds (174), and a pressure equalization The piping (63) is based on the lateral direction of the treatment tank (1), on the left and right sides of the pressure equalization distribution pipe (63), the left inlet manifold (175) from left to right, and the right inlet manifold (174) from right to Left, 39 201142104 The length is the width and width of the guide tube (11). If it is used in the double tube guide tube (11), the width and width of the double tube guide tube (11) are used in the four tubes. For the guide tube (11), the width of the four-tube guide tube (11) is the same width, and the length can be arbitrarily widened or reduced according to the number of the guide tube (11), in the left-inward manifold (Π5) and On the side wall of the right-inward manifold (174), along the downstream direction, each row is provided with a row of diverting holes (81) 'to maintain a proper gap between the diverting holes (81) and the diverting holes (81), in the diverging holes of the two branches ( 81), in a relatively staggered arrangement, two rows of different directions or staggered jets (44) are formed on the upper side wall of the pressure equalizing distribution pipe (63) with respect to the inlet of the hydraulic atomizing nozzle (12163) 'Each one has an exit that can be connected The tube and the hydraulic atomizing nozzle (12163) are connected to each other to form a passage. 11. The impulse detonation wave fast dyeing machine according to claim 6, wherein the air flow conveying pipeline system further comprises an alternating current airflow returning device (190), and the alternating current airflow returning device (190) The return line system (16 〇) is connected to each other by a blower (16) (17). An impulse detonation wave fast dyeing machine comprising at least one or more processing tanks (1) combined side by side, and a conveying piping system (71) (160) (210) (170) connected to each other in each processing tank ( 1) each has a cloth collecting groove (2) for providing textile stacking and a guiding tube (11) for providing accelerated movement of the textile, and the front and rear ends of the two are respectively connected to each other to form a wide circulation path. The utility model can quickly complete the dyeing and other processing of the textile on the passage in a widening manner, and is characterized by comprising: an air floating nozzle (122), the air floating nozzle (122) is composed of a plurality of small hole passages, The device is disposed along the downstream wall of the passage of the conduit (11) and the lower wall of the midstream section, the air-floating nozzle (122) is provided by the air flotation distribution pipe (168) and the airflow conveying pipeline system (71) (10) The air blower (16) is connected to each other; The device is close to the guide cloth on the section of the downstream section of the guide tube (11) (11) At the exit, a plurality of rows of co-constructed nozzles (121) are combined side by side. 'There can be a co-construction distribution pipe (167) and an air flow conveying pipe system (71) (16 〇) and liquid flow. The delivery line system (210) (170) is in interconnected communication with the blower (16) and the pressurized circulation pump (72); an AC-type airflow device (163) is disposed at the air-floating nozzle (122) and Between the spray nozzle (121) and the transfer line system (71); an AC flow distributor (173) disposed between the hydraulic atomizing nozzle (1216) and the transfer line system (210) . 13. The impulsive detonation wave fast dyeing machine according to claim 12, wherein the spray pipe (1) (2) of the co-structured nozzle (121) is provided with a hydraulic atomization on the upstream side of the population (1213) in the central passage. The nozzle (1216) is provided at the center of the passage of the hydraulic atomizing nozzle port (12161) with a replacement electric shock bar (12122), wherein the discharge tip is located at the mouth of the hydraulic atomizing nozzle (12161), and the other end is Extending to the outside of the hydraulic atomizing nozzle body (m6), which is connected to each other via the electric gauge wire at the high voltage power supply facility 5, and a ring-shaped electric target (12111) is provided on the common nozzle opening (1211) and is provided with a connection. Terminals (10) 23), which form a common body at the common nozzle opening (10), which are interconnected to each other via a cable. U. The impulse detonation wave fast dyeing machine according to claim 12, further comprising a one-piece rotary plate (M), the device is located in the downstream direction of the co-structured nozzle _, and is located in the guide tube (11) passage Between the next fiscal and the fresh trough (2) between the inner side of the upstream population. 15. The impulsive detonation wave fast dyeing machine described in item 12 of the patent scope further includes an inverse [S. 1 201142104 shot actuation substrate (13), which is arranged downstream of the co-structure nozzle (121). It is lapped and fixed on the lower side of the co-structured nozzle (121) in a stepwise manner. 16. The impulsive detonation wave fast dyeing machine according to claim 12, further comprising: a U-shaped rotating plate (14) disposed on the downstream side of the reflective actuation substrate (13) by reflection The substrate (13) is extended to form an arc-shaped circuit in a progressive manner; a droplet collecting plate (18) disposed at a downstream side end of the U-shaped rotating plate (14); a collecting guiding groove (181), It is disposed at the downstream side end of the droplet collecting plate (18); _ a draft tube (182) disposed on the lower side wall of the collecting guiding groove (181); an inner separating grid (21), The upstream side end is disposed at a portion where the U-shaped swivel plate (14) and the liquid droplet collecting plate (18) are connected to each other, and is disposed in a vertical or near-vertical manner at a feeding portion at an upstream side end of the collecting groove (2). The inner side of the segment 25 (21); the upstream side end of the outer separating grid (22) is disposed at the downstream end of the U-shaped rotating plate (14), and the downstream side end thereof is opposite to the sliding side of the collecting groove path. (23) and the mesh plate (24) are connected to each other; # a working fluid collecting plate (184) disposed at the downstream side end of the inner separating grid (21). 17. The impulsive detonation wave fast dyeing machine of claim 12, wherein the alternating current flow device (16) comprises two adjacent symmetric left-inclined manifolds (165) and right-inclined The manifold (164) consists of 'the lateral direction of the treatment tank (1), the left forward oblique manifold (165) from left to right, and the right forward oblique manifold (164) from right to left 'length to the guide tube (11) The width is the same as the width. If it is in the double-tube guide tube (11), the width of the double-tube guide tube (11) is the same width. If it is in the four-tube guide tube (11), the four-tube guide is used. The width of the tube (11) is the same width, and the length thereof can be arbitrarily widened or reduced according to the number of the guide tube (11) 42 201142104, and a row of parallel arrangement is arranged along the path direction on the oblique side wall of the oblique manifold. The splitting port (42) is provided with an arc-shaped shunt tube (61) on each of the splitting ports (42), and the arc-shaped shunt tube (61) can geometrically calculate each of the shunt tubes arranged up and down in a row to form a row The passage openings (43) in the same direction can be formed by the action of the arc-shaped shunt tubes (61) so that the downstream end outlets of each arc-type shunt tube (61) are arranged in parallel in the same direction. The flow port (166)' is provided at the downstream side end of the manifold (166) with a diverging confluence passage tube_, the upstream side end inlet and the outlet port (166) are in communication with each other, and the downstream side end outlet is co-constructed The distribution pipe (167) and the air flotation distribution pipe (168) are connected to each other. 18. The impulse detonation wave fast dyeing machine according to claim 12, wherein a new air inlet port (2〇1) and an exhaust gas outlet port (200) are disposed in the upstream passage of the suction port of the blower (16). And the treatment liquid recovery or discharge port at the bottom of the lower side of the treatment tank (1) is provided with a control valve on each of the introduction and discharge ports, which can be arbitrarily controlled according to the process. 19. The impulsive detonation wave fast dyeing machine according to claim 12, further comprising an air heat exchanger (161) and an air filament (162), and a working fluid heat exchanger (22〇) And - the working fluid screen (215) 'is connected to the gas delivery line system (71) (10) and the liquid delivery line system (210) (170), respectively. 20. An impulsive detonation wave fast dyeing machine comprising at least one or more processing tanks (1) combined side by side, and a conveying piping system (71) (160) (210) (170) connected to each other, in each Each of the processing tanks (1) is provided with a collecting groove (2) for providing textile stacking and a guiding tube (11) for providing accelerated movement of the textile, and the front and rear ends of the two are respectively connected to each other to form a wide circulation passage. The utility model can quickly complete the dyeing and other processing by the textile on the passage, and is characterized in that: 43 201142104 an air floating nozzle (122), the air floating nozzle (122) is composed of a plurality of small hole passages The device is arranged on the lower wall of the upstream and midstream sections along the passage of the conduit (11), and the air-floating nozzle (122) is provided by an air flotation distribution pipe (168) and an air flow conveying pipeline system ( 71) (160) is connected to the blower (16); a common configuration nozzle (121) is composed of a gas injection pipe (12121) and a hydraulic atomizing nozzle (1216) , wherein the common nozzle (121) of the injection pipe (12121) is in the central passage, the inlet At the upstream end of the (1213), a hydraulic atomizing nozzle (1216) is disposed, and at the center of the passage of the hydraulic atomizing nozzle port (1216), a replacement electric shock rod (12122) is provided. The discharge tip is located at the hydraulic atomizing nozzle. At the center of the mouth (12161), the other end extends to the outside of the hydraulic atomizing nozzle body (1216), which is connected to each other via a power line at a high voltage power source, and a ring type electric power is arranged on the common nozzle port (1211). a target (12111) forming a comon at a co-configuration nozzle opening (1211) interconnected to the surface via a cable, the common-type nozzle (121) being disposed in a downstream section of the conduit (η) In the section of the section, close to the outlet of the duct (11), a plurality of rows of co-constructed nozzles (121) are arranged side by side, which can be connected by a common distribution tube (167) and an airflow pipeline system (71). (16〇) and the liquid flow conveying piping system Xin (210) (170) are connected to the blower (16) and the pressurized circulating pump (72); an AC type airflow device (163) 'its setting Between the air flotation nozzle (122) and the co-construction nozzle (121) and the airflow delivery piping system (71); an AC flow distributor ( 173), disposed between the hydraulic atomizing nozzle (1216) and the liquid delivery piping system (210). 21. The impulsive detonation wave fast dyeing machine described in the twentieth patent, further comprising a u-shaped rotary plate (14) 'the device is located downstream of the co-structured nozzle (121), located at the guide tube (11) 44 201142104 Between the lower side of the passage outlet and the inner side of the upstream entrance of the collecting tank (2). 22. The impulse detonation wave fast dyeing machine according to claim 20, further comprising a reflection actuation substrate (13) 'the device is lapped and fixed in a stepwise manner in the downstream direction of the co-structure nozzle (121) On the lower side of the co-structured nozzle (121). 23. The impulsive detonation wave fast dyeing machine according to claim 20, further comprising: a U-shaped rotary plate (14) disposed on the downstream side of the reflective actuation substrate (13) by inverse φ The projecting substrate (13) is extended to form an arc-shaped circuit in a progressive manner; a droplet collecting plate (18) disposed at a downstream side end of the U-shaped rotating plate (14); and a collecting guiding groove (181) ), which is disposed at the downstream side end of the droplet collecting plate (18); a draft tube (182) disposed on the lower side wall of the collecting guiding groove (181); and an inner separating grid (21), The upstream side end is disposed at a portion where the U-shaped swivel plate (14) and the liquid droplet collecting plate (18) are connected to each other, and is disposed in a vertical or near-vertical manner at a feeding portion at an upstream side end of the collecting groove (2). The inner side of the segment (31); the upstream side end of the outer separating grid (22) is disposed at the downstream end of the guiding plate (15), and the downstream side end thereof is opposite to the sliding side of the lower side of the collecting groove (2) (23) and the mesh plate (24) are connected to each other; a working fluid collecting plate (184) is disposed at the downstream side end of the inner separating grid (21). 24. The impulsive detonation wave fast dyeing machine of claim 20, wherein the alternating current flow distributor (173) comprises two adjacent symmetrically arranged leftward manifolds (175) and a right divergence. a tube (174), and a pressure equalization distribution tube (63), which is lateral to the treatment tank (1), on the left and right sides of the pressure equalization distribution tube (63), and the left inlet manifold (175) from left to right The right-inward manifold (174) is from right to left, and the length is the same width as the width of the guide tube (11). If it is used in the double-tube guide tube (11), the double-tube guide 45 201142104 cloth s (11 The width and width of the same width are used. If the four-tube guide tube (9) is used, the width of the four-tube guide tube (10) is the same width, and the length can be arbitrarily widened or reduced according to the number of the guide tube (9). On the side wall of the tube (10) and the right inlet manifold (174), there is a row of diverting holes _ in the downstream direction, and a proper gap is maintained between the diverting holes (17 験 diverting holes (10)), and the diverting holes in the two branches (178) Between the two rows of different directions or staggered nozzle openings (Π9) 'on the upper side wall of the pressure equalizing distribution pipe (176), relative to the working inlet of the hydraulic atomizing nozzle (10) (12161), each of which is provided with an outlet (172) which can be connected to each other by a communication pipe and a hydraulic atomizing nozzle (1216) to form a passage. 25. If applying for the full-scale 2G outline rushing detonation wave fast dyeing machine, the AC airflow device (163) comprises two adjacent symmetric left-inclined manifolds (165) and right-handed oblique (164) consists of the lateral direction of the treatment tank (1), the left-inclined manifold (Ms) from left to right, the right-inclined manifold (164) from right to left, and the length of the guide tube (11) The width is the same width. If it is in the double official guide tube (11), the width of the double tube guide tube (11) is the same width. If it is in the four tube guide tube (11), the four tube guide is used. The width of the tube (9) is the same width, and the length can be arbitrarily widened or reduced according to the spring of the guide tube (10). On the oblique side wall of the inclined manifold, a row of shunts (42) arranged in parallel are arranged along the direction of the passage. Each of the splitting ports (42) is provided with an arc-shaped shunt pipe (61), and the arc-shaped shunt pipe (61) can geometrically calculate the shunt pipes arranged in the upper and lower rows to form a row of the same direction of the access port ( 43) Both of the outlets of the downstream end of each of the isolated shunts (61) can be formed into a row of confluence ports (166) in parallel in the same direction by the action of the arc-shaped shunt tubes (61). The downstream side end outlets at 166) are interconnected with the co-distribution distribution tube (167) and the air flotation distribution tube (168), respectively. An air flow regulating valve (169) is provided at the inlet of the air flotation distribution tube (168). 46 201142104 26. The impulsive detonation wave fast dyeing machine according to claim 20, wherein the conveying pipeline system further comprises an alternating current airflow recirculating device (19〇), the alternating current airflow recirculating device (190), It mainly consists of two adjacent symmetric single oblique manifolds (191) and a τ-shaped manifold returning tube (192), which is oriented transversely to the processing tank (1), and the left side of the manifold is from left to right and right. The busbars are from right to left, and the length is the same width as the width of the guide tube (11). If it is in the double-tube guide tube (11), the width of the double-tube guide tube (11) is the same width, if it is at four The tube guide tube (11, the width of the four tube guide tube (11) is the same width, and the length can be arbitrarily widened or reduced according to the number of the guide tube (11), in the single oblique manifold (191) The lower side wall is provided with a row of parallel return ports (193) arranged in parallel along the path of the passage, and a 180 degree connecting rotary pipe (194) and a U-shaped return pipe are arranged at the downstream outlet end of the single oblique collecting pipe. (192) The left and right sides are connected to each other so that the return airflow can be at the center exit of the U-shape, and then the return duct (160) An impulsive detonation wave fast dyeing machine as described in claim 2, wherein a new air inlet port is provided in the upstream passage of the suction port of the blower (16) (2〇 1) and the exhaust gas discharge port (200), and the treatment liquid recovery or discharge port at the bottom of the lower side of the treatment tank (1) are provided with a control valve on each of the introduction and discharge ports, which can be arbitrarily controlled according to the process. 28. The impulse detonation wave fast dyeing machine of claim 2, further comprising an air heat master (161) and an air transition (162), and a working fluid heat exchanger (220) And a working fluid sifter (215) connected to the gas delivery line system (71) (16 〇) and the liquid delivery line system (210) (170), respectively. 4747
TW99116240A 2010-05-21 2010-05-21 Impulsive Detonation Wave Fast Dyeing Machine TWI439595B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114000293A (en) * 2021-11-22 2022-02-01 浙江嘉欣兴昌印染有限公司 Uniform dyeing process for heavy fabric

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114000293A (en) * 2021-11-22 2022-02-01 浙江嘉欣兴昌印染有限公司 Uniform dyeing process for heavy fabric
CN114000293B (en) * 2021-11-22 2024-05-03 浙江嘉欣兴昌印染有限公司 Uniform dyeing process for heavy fabric

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