HK1161320B

HK1161320B - Shock wave rapid dyeing machine of impulse type

Info

Publication number: HK1161320B
Application number: HK12101424.0A
Authority: HK
Inventors: 江兆城
Original assignee: 江兆城
Filing date: 2012-02-14
Publication date: 2013-09-06

Description

Impulse type detonation wave rapid dyeing machine

Technical Field

The invention relates to an impulse type detonation wave fast dyeing machine, which is an improved machine type of a spray type open-width pneumatic vibration acceleration dyeing machine and belongs to a dyeing and processing machine with high efficiency, multifunction, versatility and environment protection.

Background

In energy-saving and carbon-reducing calling, in order to reduce the impact of global warming and transition, a plurality of special processing technical fields are promoted to be applied to the processing of fiber fabrics, wherein the characteristics of cleaning, dyeing and finishing and processing technologies such as detonation wave, electrochemistry, low-temperature plasma technology, carbon dioxide supercritical fluid technology, biological enzyme processing technology, ultrasonic wave, radiation energy, microwave and the like are all actively developed all over the world at present due to the characteristics of convenience, rapidness, effectiveness, safety, wide applicability, dye saving, environmental pollution reduction, energy saving, convenience for realizing the automation of electronic computer control and the like. However, most of the technical development directions are mainly single and special models, and the efficient and environment-friendly models with multiple functions and one machine with multiple purposes are not smelled so far. Therefore, the former invention application of the spray open air vibration acceleration dyeing machine was more motivated (note: this case to obtain patent of invention of more than twenty countries including Taiwan (application date: 1997/2/25, application number: 86102237), mainland China (application date: 1997/04/29, application number: ZL97182145.3), United states (application date: 1997/03/31, application number: 828,884) Canada (application date: 1997/04/29, application number: 2,288,214), European Union (application date: 1997/4/29, application number: 97917988.4), India (application date: 1997/5/28, application number: 1126/MAS/97), Japan (application date: 1997/4/29, application number: 10546452), Korea (application date: 1999/10/28, application number: 997009996) and so on), further more clearly and more firmly improved direction and innovative power source, the energy-saving and carbon-reducing agent participates in energy saving and carbon reduction by more perfect new thinking and ideas, and assists the dyeing and finishing industry to successfully achieve the aim of clean production at an urgent moment.

As is known, the dyeing and finishing of textiles always uses water as a medium to perform various wet processing, which is one of pollution discharge users in industrial production, and under the pressure of increasing global warming warning, the international textile market is forced to start green whirlwind, which means that the environmental protection textiles will become the main appeal of future products. To ensure that the dyeing and finishing industry continues to evolve, the use of clean production techniques or facilities has been considered the only way in the long term.

In fact, the problem of warming and transition of climate has been the most gradual, and for the dye industry, it is necessary to speed up the steps from a new thinking and viewpoint, aiming at the replacement of new facilities or the establishment of new processes and new methods.

Therefore, in order to achieve better energy-saving, water-saving and clean production facilities, the fiber fabric and the dye or the treating agent are particularly oligomerized and concentrated in a high-energy fluctuation field to promote all the participating reactants to be processed more quickly and more efficiently in a very short time and in limited resources through the action of the high-energy fluctuation field, and meanwhile, the treatment technology of low-temperature plasma is also involved in the invention so as to promote the fiber fabric to obtain better and wider process invention space and obtain the best product treatment effect in certain processing procedures besides the aim of anhydrous processing.

At present, most of dyeing and finishing production facilities still use unidirectional (note: the wet processing cannot simultaneously process other working procedure operations within one time) wet processing as a mainstream, so that a large amount of water is consumed, a large amount of energy is wasted, the environment is seriously polluted, the processing cost is too high, unnecessary economic loss is caused, and the ecological great harm is brought.

The textile market is inclined to the appeal direction of small, various, multifunctional and delicate clean production, so that batch (batch) environment-friendly dyeing facilities become the main production flow, and for the common and conventional facilities, no matter an expanding type or a beaming type airflow dyeing machine or a more traditional jet type liquid flow dyeing machine, the problems of dyeing or other processing treatment of fabrics still cannot be effectively solved, for example: the problems of abnormal reproducibility, different colors on the left and the right, different colors in the front and the back, uneven dyeing of other line marks and the like, unsynchronized speed between a power cloth driving wheel and an actuating nozzle, insufficient moving speed of cloth, abrasion or collision and yarn hooking, and excessive jet force of the actuating nozzle, which cause yarn breakage of textile fibers, easily causing blockage of the nozzle and a filter in the treatment process, or lack of fullness of cloth body, poor efficiency in biological enzyme treatment, too slow treatment time, insufficient facility function, limited processing procedures, excessive energy use and excessive waste of water resources, cause a large amount of sewage treatment cost, also cause public safety problems or poor hand feeling due to the arrangement of the power cloth driving wheel, however, in the various problems mentioned above, except artificial careless, most of the problems are caused by poor facility design and manufacture, the main reason is that the work done by the fiber fabric and the dye liquor or the uneven heat transfer distribution between the treating liquor and the air flow, such as the tube difference color is generated in a multi-tube treating tank facility, because the common dyeing machines are all of multi-groove type, the method of distributing the dye liquor or the air flow also adopts the mode of dividing into two, dividing into four and dividing into eight to complete the branch type flow distribution operation, the biggest defect is that the T-shaped joints are too many due to the division, the fluid is difficult to be accurately divided into two equal halves according to the discussion of fluid dynamics, any uneven side deviation is generated on the leading pipeline, the error is larger, the originally set flow is changed, and the uneven dyeing problem caused by the divided flow is still unsolved. Therefore, in order to achieve the desired goal of clean dyeing and finishing, the above problems need to be solved at the same time, because the re-repairing and re-dyeing processes, which are caused each time a problem occurs, will cause a greater consumption of energy and water resources, and will also increase the load of production cost.

Tracing the development of dyeing theory to date, most dyeing theory is believed that the process of dyeing fibers with dyes can be divided into the following four stages:

1. the dye gradually approaches the fiber interface along with the dye liquid flowing in the dye liquid. The nature and state of the dye at this stage are basically independent of dyeing performance, and the dye molecules in a dissolved state or the dye particles in a suspended state flow with the dye liquor, and the migration speed of the dye particles is determined by the flow rate of the dye liquor.

2. Because a dynamic boundary layer (viscous flow layer) which is difficult to flow exists at the interface of the liquid and the fiber, the dye is close to the fiber mainly by self diffusion before entering the dynamic boundary layer and being close to the surface of the fiber to a certain distance. The migration speed of the dye at this stage is not only related to the flow rate of the dye liquor, but also related to the diffusion speed of the dye, and the dye molecules in a dissolved state can diffuse more quickly than the dyes in a suspended state and an aggregation state, so that the solubility and the dispersion state of the dye have great influence on the migration speed of the dye at this stage.

3. After the dye is diffused to a certain distance from the surface of the fiber, sufficient molecular acting force exists between the dye and the fiber, and the dye is rapidly adsorbed to 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, i.e. the force between the dye and the fiber, and also on the nature of the interfacial solution, where the solubility and dispersion state of the dye have a large influence. Therefore, the larger the force between the dye and the fiber at this stage, the better the dye is dissolved and the faster the adsorption speed is.

4. After the dye is adsorbed on the surface of the fiber, a difference in dye concentration or a difference in chemical level between the dye inside and outside the fiber is generated, and it is known from Fick's law that the dye diffuses and migrates from the surface of the fiber to the inside of the fiber. The migration speed is mainly determined by the chemical and physical microstructure of the fiber, and is also related to the molecular structure and concentration of the dye. The amorphous area of the fiber has large proportion, large pores or large free volume, the dye concentration on the surface of the fiber is high, and the dye can rapidly migrate into the fiber. The rate of dye migration at this stage is therefore directly related to the degree to which the fibre is swollen or plasticized and the concentration of dye at the surface of the fibre.

From the above, the dyeing speed depends on the solubility of the dye in the solution and the degree of swelling or plasticization of the fiber, in addition to the molecular structure of the dye and the fiber. In fact, the interaction relationship between the dye and the fiber does not need a large amount of working fluid to obtain dissolution or rapid dyeing, if the dye is dissolved in the excessive working fluid during dyeing, the contact opportunity between the dye or the treating agent and the fiber in a short distance is blocked by the excessive working fluid, the purpose of rapid dyeing or treatment is lost, most input energy is converted into the rotational kinetic energy of working fluid molecules and the energy from the vibration of each atom in the working fluid molecules, and various interaction forces irrelevant to dyeing or processing are formed among the working fluid molecules.

In order to make the dye have certain solubility during dyeing, a certain amount of polar groups are always introduced into the dye molecule during the synthesis production of the dye so as to increase the solubility of the dye. However, after the introduction of water-soluble ionic groups, in addition to improving the combination of dyes and fibers in a few cases, many problems are caused after the dyeing process is completed, such as the reduction of the wet fastness of the textile dyeing by hydration dissolution on the fibers, the difficulty in decoloring and purifying the water-soluble dyes remaining in the dye liquor, the difficulty in sewage treatment, and the like.

For insoluble disperse dyes, the molecules of the disperse dyes do not have ionic groups, and the disperse dyes are difficult to dye due to low solubility, low fiber swelling or plasticizing degree and low dyeing speed at the normal pressure of 100 ℃. The dye in the working solution can be dispersed in the working solution in a suspension state only by the aid of a large amount of dispersing agents, so that a large amount of dispersing agents are needed, the stability of the suspension is not easy to maintain, and the problems of dyeing and sewage treatment are caused. Therefore, the solubility of the disperse dye is properly improved, the dispersion stability of the dye can be maintained without reducing or using a dispersant, and the dye is beneficial to dyeing.

While hydrophobic synthetic fibers are difficult to swell in water and thus difficult to disperse in fibers, dyeing usually requires high temperatures, for example, polyester fibers must be dyed at high temperature and high pressure up to 130 ℃, if the degree of swelling or plasticization of these fibers can be increased, the dispersion rate of the dye in the fibers can be increased, or the dyeing temperature can be decreased.

In addition, as for the natural cellulose fiber, since the microstructure is complex, a very large number of cavities are easily formed and filled with air, and thus, when a solution is infiltrated, a relative motion is not easily generated, that is, a retention phenomenon occurs to cause dye to be not easily infiltrated, and thus, it usually takes a long time to obtain dye uptake; the surface of the wool fiber is provided with the scale layer, so that the wool fiber has a shielding effect on dye-uptake, the conventional dyeing is usually carried out in a boiling dyeing mode, and the dyeing time is long, so that the dyeing energy consumption is large, and the fiber damage is large. In addition, since the reactive dye generally reacts with water in a high-temperature and alkaline solution, the dyeing efficiency of the reactive dye is reduced, and after dyeing is finished, the dye in dyeing residual liquid is not absorbed completely, or the dyed fabric is washed off in post-treatment to generate loose color, which causes serious water pollution.

In short, one of the first conditions for dyeing fiber with dye is that the dye must be dissolved in the working solution, only the dye decomposed into monomolecular can be quickly adsorbed on the fiber and diffused into the fiber, and the dye crystal particles and the dye aggregate with larger volume can not be diffused into the fiber, so that if the physical mechanical mechanism generated by the high-energy fluctuation or high-energy particles can be utilized, the solubility of the insoluble dye can be improved in the working solution with extremely small liquid amount and high concentration, the adsorption speed of the fiber to the dye can be accelerated, the fiber can be solubilized or plasticized, the diffusion speed of the dye in the fiber can be accelerated, and the whole dyeing speed can be accelerated. As long as the selected dye has higher binding force with fiber molecules, the dye has good dyeing power and higher dyeing fastness.

Therefore, in order to increase the dyeing rate and shorten the dyeing time, besides reducing the water consumption, the suitable dyeing equipment is selected, the relative motion between the dye liquor and the fabric is enhanced, the suitable dye for the fiber, the matched dyeing auxiliary agent and the dyeing medium are selected, and the chemical structure and the physical microstructure of the fiber fabric are also key factors which need to be considered. If the fiber fabric is subjected to good pretreatment or modification pretreatment in advance or is subjected to modification and dyeing simultaneously, the adsorption speed of the dye to the surface of the fiber and the diffusion speed of the dye to the interior of the fiber are increased, the dyeing speed can be greatly increased, the dyeing time is shortened or the dyeing temperature is reduced, the production efficiency is improved, and the purposes of energy saving and carbon reduction in clean production are achieved.

Disclosure of Invention

The present invention relates to a detonation wave dyeing machine, which can utilize the expansion acceleration action of a co-constructed nozzle to make the dyeing liquor, treatment liquor or low-temperature plasma or other treatment medium, etc. be dispersed in high-speed air flow and concentrated in the field of a high-energy wave field with the mode of forming flush and congregate with fibre fabric so as to make all the participated reactants obtain required activation energy (activation energy) and further attain the goal of most economic cleaning production in shortest time.

During processing, when high-speed flowing air, steam, dye, treating agent and low-temperature plasma sprayed by the co-constructed nozzle are in contact collision with the fiber fabric, the fiber fabric falling downwards in a turning process can be utilized to form a bending end face effect, so that a large impact force and an impulsive force are obtained, and high-efficiency energy conversion is carried out; when the dyeing liquid and the treatment liquid are in fine particle shape or micro particle shape in a high momentum mode or are dispersed in a high speed air flow in a monomolecular mode in the process of proceeding, the dyeing liquid and the treatment liquid impact the fiber fabric which is turning in a direct close range mode, so that the surface of the moving fiber fabric continuously and repeatedly obtains strong elastic collision (note: air or common gas) and inelastic collision (note: working liquid or dye or treatment agent, and also comprises plasma), wherein, in the inelastic collision, the fabric can be promoted to obtain high-efficiency kinetic energy transfer, the fabric moving is accelerated, and simultaneously, enough liquid film quantity on the surface of the fiber fabric can be provided to generate cavitation (cavitation), and the elastic collision can promote a stream of high-speed pushing air flow between the lower side end face of the fiber fabric and the reflection actuating substrate, and can promote the air pressure difference between the upper end face and the lower end face of the fabric static pressure, the static pressure on the upper side end face of the fabric is larger than that of the lower side end face, so that the moving fiber fabric can continuously generate high-frequency strong fluctuation motion by utilizing the action of the pressure difference when passing through the reflection action plate, and can be freely spread.

When wet processing is performed, if the liquid film volume absorbed on the surface of the fiber fabric is thick enough and the velocity energy of the high-speed air flow is large enough, a large number of cavities can be generated in the boundary area of the surface of the fiber fabric in the wave process, and the shock wave (shock wave) effect is triggered. In the dry operation, a high-speed air stream may be ionized by corona discharge (corona discharge) or glow discharge (glow discharge) to generate a high-speed low-temperature plasma (low temperature plasma), which not only provides a high-energy particle treatment effect to the fabric, but also provides more ecological benefits from the dry processing.

During processing, the fiber fabric dropped in the cloth collecting tank can utilize the instantaneous blocking effect generated by the action force of momentum inertia and the air flow under the action of quick drive-off to cause air impact effect and further generate strong swinging phenomenon, so that the fiber fabric can utilize the swinging mechanism to forcibly remove and separate residual working liquid and peeled free fibers and other impure solid objects attached to the surface of the fiber fabric and simultaneously complete folding operation, so that the working liquid, the free fibers and other impure solid objects which are separated from the surface of the fabric can be directly led into the liquid collecting tank from a discharge port at the lower side of the cloth collecting tank and are filtered and collected by a precise screen filter, the fiber fabric in the cloth collecting tank can be promoted to obtain a cleaner state, and further, when the fiber fabric is contacted with dye liquor or treatment liquid in the next cycle, can not be blocked by the liquid film barrier of the residual working liquid. The filtered working solution can be supplied with the dye or the treating agent through the pump-free feeding device in the circulating conveying process, so that the high-concentration dissolved dye or the treating agent in the pump-free feeding device can be fed through the suction inlet of the pressurized circulating pump in a system of the circulating conveying pipe, and the high-concentration dissolved dye or the treating agent can be mixed in the limited amount of the circulating working solution, so that the extremely small bath ratio and the high uniformity can be obtained. Therefore, when the fiber fabric is contacted with the dye liquor or the treatment liquor again, higher potential energy and kinetic energy can be obtained, the concentration gradient, the temperature gradient and the chemical affinity gradient are improved, and the rapid permeation and diffusion effects of the dye liquor or the treatment liquor are promoted, so that the rapid processing is facilitated; besides, the acting force of mutual compression of the collected and folded fabrics in the collecting groove can be reduced to the minimum, and the generated tensile force can also be reduced to the minimum when the fiber fabrics move rapidly in the cloth guide pipe. During operation, the dye liquor or treating liquor pressurized by the pressurized circulating pump can spray atomized liquid drops with uniform pressure, uniform quantity, uniform temperature and uniform speed by each hydraulic atomizing nozzle under the action of the alternating-current liquid flow distributor on the conveying pipeline system.

The air flow pressurized by the blower can utilize the alternating-current type air flow distribution device on the conveying pipeline system to perform 90-degree steering to form rectangular distribution flow, and then the rectangular distribution flow is guided into respective distribution pipes, the kinetic energy of the moving air flow can be converted into static pressure energy through the action of the diffusion structure of the distribution pipes, so that the air flow can obtain larger expansion acceleration efficiency and distribution effects of pressure equalization, quantity equalization, temperature equalization and speed equalization when passing through each air floatation nozzle and each co-structure type nozzle, and therefore, the fiber fabric can be prevented from being dyed differently left and right and is not dyed uniformly to cause various color patterns, all other processing operations can be promoted, and various uniform hand feeling and appearances can be obtained. During operation, the return air in the treating tank may be distributed and returned via AC airflow returning device to avoid excessive disturbance of the airflow inside the treating tank and obtain stable and regular circular flow.

The invention particularly relates to an air flotation nozzle which is arranged on the horizontal tube wall end surface which is arranged on the lower side of a cloth guide tube and across the left and right side walls of a channel, along the channel direction, on the upstream and middle section, and on the cross section of the downstream section, a row of co-constructed nozzles which are arranged and combined in parallel and across the left and right side walls, and a U-shaped revolving plate which is arranged in the downstream direction of the co-constructed nozzle opening, is positioned at the lower side of the outlet of the cloth guide tube channel and the inner side space of the inlet of the upstream cloth falling section of a cloth collecting groove, and the upstream side end of the U-shaped revolving plate is overlapped and fixed on the lower side of the co-constructed nozzle opening in a stepped mode, so that the upstream side end surface of the U-shaped revolving plate forms a straight reflection actuating substrate, and a separation grid net which is arranged on the upstream and outer side of the cloth falling section of the cloth collecting groove on the downstream side, when dyeing or other processing treatment is carried out, the circulating air and working solution in the treatment tank and the dye liquor or treatment solution in the stock preparation barrel can be mutually communicated with the blower and the pressurizing circulating pump through respective pipeline systems to provide pressurized air and pressurized dye liquor or treatment solution, and the pressurized air and the pressurized dye liquor or treatment solution are sprayed out through the co-constructed nozzles, and simultaneously, partial pressurized air can also be respectively sprayed out through the air flotation nozzles. During operation, the fiber fabric can be floated by jetting a small amount of air flow through the air floating nozzle, most of the power energy can be concentrated in the co-constructed nozzles to be jetted, and the jetted high-speed air flow can be driven to change direction to form reverse discharge under the action of the U-shaped rotary plate, so that the fiber fabric can obtain strong driving force. Therefore, during operation, the co-constructed nozzle can be used as a main power source for the circular movement of the fabric, the traditional operation mode of a power cloth driving wheel can be abandoned, and the problem that the high-level processing treatment is difficult to achieve due to the excessive dispersion of the energy of working air flow of the multi-section type guide nozzle in the prior art can be solved. During operation, the hydraulic atomizing nozzle mechanism and the corona or glow discharge mechanism provided on the co-structural nozzle can be used for performing mutually alternating processes to obtain complementary treatment modes, so that various fiber fabrics can obtain wider and wider process invention space during processing.

The main object of the present invention is to provide an impulse type detonation wave fast dyeing machine, when dyeing or other processing processes are performed, the fiber fabric can utilize a co-constructed nozzle to spray high-speed damp or dry hot air flow, high-speed uniformly dispersed dye molecules, high-speed uniformly dispersed processing liquid molecules, high-speed flowing low-temperature plasma, or other high-speed uniformly dispersed micro-particles according to the processing process requirements, so that all the sprayed media can form oligomers and concentrate in a high-energy wave motion field to repeatedly and continuously collide with the fiber fabric, so that the participated reactants and the fiber fabric can perform high-efficiency energy transmission in a more ordered motion mode in a very short time, and besides that all the participated reactants can obtain required activation energy, the fiber fabric can also be promoted to perform in a shortest time, the aim of clean production is achieved by saving most energy, water, dye and treating agent.

The main purpose of the present invention is to provide an impulse type detonation wave fast dyeing machine, which can promote the dyeing liquid or the treatment liquid to form the wet processing purpose of small liquid amount, high concentration and high efficiency with the fiber fabric under the environment of low viscosity, low resistance, high potential energy, high penetration and high diffusivity by the high-frequency strong wave action or the detonation wave effect caused by the wave action when dyeing or other processing treatment is carried out. The detonation wave effect refers to that when the fiber fabric is processed, high-energy level fluctuation can be generated by the action of high-speed air flow, a compression area is formed in a wave crest area in the fluctuation process, and a sparse area is formed in a wave trough area. And further promoting any mass point on the surface area of the fiber fabric to continuously generate the fluctuation of the alternating compression area and sparse area, in the fluctuating compression area, promoting the average distance of air molecules at the periphery of the surface of the fiber fabric in the area to be shortened, and the density to be increased, and in the sparse area, the average distance of the air molecules to be increased and the density to be decreased, if the mass point fluctuation speed of the fiber fabric is fast enough, the generated fluctuation force is strong enough, so that the working solution molecules attached to the surface of the fiber fabric are also subjected to the alternating action of the compression area and the sparse area, and when the negative pressure in the sparse area is reduced to be below the critical value of the saturated vapor pressure, the average distance between the working solution molecules is increased to exceed the limit distance, thereby damaging the integrity of the working solution molecules or the attractive force structure between the working solution molecules and the fiber fabric, and consequently, causing the surface of the fiber fabric, the pores or the internal and external gap areas of the fiber tissue to generate cavities (which Once the cavity is formed, the negative pressure is increased to a maximum value, which results in a large number of cavitation bubbles (note: a vapor bubble or air bubble with very low density), and when a compression area is formed successively, most of the cavitation bubbles are crushed and destroyed by compression, so as to generate a shock wave effect, which is called herein as a shock wave effect, which is a process of crushing and destroying the cavitation bubbles, and concentrates a acting force synthesized by the wave energy of the fiber fabric and the compression wave energy generated by the surrounding pressure environment, and performs unobstructed jet flow movement in the cavitation environment. Therefore, when the cavitation bubbles collapse and break, the acting force can instantly generate a detonation wave towards the center of the cavitation bubbles from outside to inside, when the detonation wave passes through or impacts the surface or the inside and outside of the fiber fabric, the density pressure of all media and the vibration speed of particles on the surface of the fiber fabric or in the inside and outside boundary regions of the tissue can be changed sharply, and extremely high temperature and extremely high pressure can be generated on the extremely small space of the surface of the fiber or in the amorphous region of the fiber within extremely short time, so that during dyeing or other processing, the dyeing solution or the processing solution can generate strong impact force on the surface of the fiber or in the amorphous region of the fiber through the detonation wave generated by the breaking of the cavitation bubbles, thereby promoting the dyeing solution or the processing solution to obtain the solubility in the fiber, the energy for accelerating permeation and rapid diffusion, and also leading the molecular tissues of the fiber to generate the effect of accelerating swelling or plasticizing, can promote the non-activated molecules on the surface of the fiber fabric to obtain enough energy to be converted into activated molecules so as to achieve the aim of quick dyeing or other processing treatment.

The main object of the present invention is to provide an impulse type detonation wave fast dyeing machine, which can modify the fiber fabric or dye the fiber fabric while modifying the fiber fabric by utilizing the detonation wave effect caused by the high-energy fluctuation field during dyeing or other processing.

According to the microstructure of the fiber, no matter natural cellulose fiber or synthetic fiber is formed by aggregating long-chain molecules formed by decorating carbon atoms serving as a framework and hydrogen atoms or oxygen atoms and nitrogen atoms, the long-chain molecules belong to macromolecular compounds and comprise a crystallization area and an amorphous area, and in the crystallization area of the fiber, the molecules are regularly arranged, the acting force between the molecules is strong, the molecular structure is compact, so that dye molecules are difficult to enter; and in the amorphous area of the fiber, molecules are arranged in disorder, the acting force between the molecules is weak, the molecular structure is loose, and certain gaps exist. Thus, dye or treating agent molecules can only enter the amorphous regions of the fiber during dyeing or other processing, and dye molecules are difficult to enter if dry or at ambient temperatures.

In addition, according to the dyeing theory, no matter the dye is dyed according to a model of pore diffusion or a free volume diffusion model, the dyeing process can be smoothly carried out only by increasing the gaps of the amorphous area, namely increasing the specific surface area of the inner part and the outer part of the fiber, so that all the factors which are beneficial to the increase of the gaps of the amorphous area of the fiber and the increase of the specific surface area of the inner part and the outer part of the fiber are beneficial to the smooth operation of the dyeing or other processing processes. In terms of material mechanics, any material damage or failure results from excessive stress concentrations in the material and the origin of primary defects and cracks, which is provided by the voids in the amorphous regions of the fibrous polymer. Therefore, every time the fiber fabric is subjected to strong rapid fluctuation and cavitation bubble generation or destruction, the dislocation between the microcrystals or the breakage or recombination of partial fiber molecules are inevitably generated, the specific surface area inside the fiber is increased, and the void of the amorphous region is increased. Therefore, the fiber can be modified, and the dyeing can be simultaneously carried out while modifying.

The invention mainly aims to provide an impulse type detonation wave fast dyeing machine, which can perform anhydrous desizing or impurity removal or fiber fabric modification and modification by using the action of high-speed flowing low-temperature plasma during dyeing pretreatment. The high-speed flowing low-temperature plasma in the present invention is generated by corona discharge or sub-glow discharge between an electrode tip provided on a discharge pipe passage of a co-configured nozzle and a ring-shaped target, when the gas pressure is in the atmospheric pressure condition, using a large amount of air or other gas flowing at a high speed as a medium, and passing through the co-configured nozzle. During discharge, the electrode tip is applied with high voltage to make the electrode tip and the annular target produce unbalanced electric field, and the electric field lines concentrate at the place with great curvature of the electrode tip surface to make the voltage equipotential surface denser, so that under the action of high electric field and high voltage, the free electrons obtain high-level electrons in the electric field to force the high-energy electrons to be released from the electrode tip and accelerated toward the annular target, so that the high-energy electrons collide with partial high-speed airflow violently, and during collision, the high-energy electrons are dissociated to produce various high-energy active particles The high-energy active particles can generate mutual reaction and accompanied radiation energy, most of the high-energy active particles can generate violent impact with the surface of the fiber fabric to dissipate the energy, so that in the dissipation process, the high-energy active particles not only can generate equivalent free radicals but also can perform oxidation on the surface of the fiber fabric to further promote the surface of the nonpolar fiber fabric to increase a large amount of polar groups, and the natural impurities contained on the surface of the fiber fabric and the impurities such as sizing agent, oil stain and the like applied in textile processing can be removed by utilizing low-temperature plasma flowing at high speed, so that the fiber fabric has good moisture absorption and permeation effects to meet the subsequent processing procedures, because the conventional pretreatment procedures are long, the dosage of chemicals is large, and the water consumption is high, therefore, the production efficiency is lower, the energy consumption is high, and the discharge amount of waste water is large. Therefore, when the high-speed flowing low-temperature plasma is used for treatment, the high-speed flowing low-temperature plasma has good impurity removal and cleaning effects, can replace certain pretreatment chemical wet processing procedures, or can adopt milder pretreatment procedures to shorten the treatment time, reduce the dosage of chemical additives and reduce the treatment temperature after the surface treatment of the high-speed flowing low-temperature plasma, thereby improving the production efficiency, reducing the consumption and pollution of water resources and achieving the purposes of saving energy and reducing carbon. Therefore, if a high-speed flowing low-temperature plasma technology can be utilized in the pretreatment process, it has great environmental and economic benefits.

The invention mainly aims to provide an impulse type detonation wave fast dyeing machine which can be used for dyeing various fiber fabrics through a multifunctional technical field mechanism, and can also be used for carrying out processing treatments such as modification treatment, desizing treatment, refining treatment, bleaching treatment, biological enzyme treatment, dividing and weaving treatment, relaxation treatment, fading treatment, untwisting treatment, fluffing treatment, softening treatment, fibrillation treatment, stretching treatment, wrinkle eliminating treatment, color repairing treatment and the like on various fiber fabrics, so that the purposes of convenience, rapidness, effectiveness, safety, dye saving, medicament saving, energy saving, water resource saving, environmental pollution reduction in a clean production mode and convenience for realizing automatic control are achieved.

The invention mainly aims to provide an impulse type detonation wave fast dyeing machine, when dyeing or other processing treatments are carried out, wherein the circular moving power of a fabric is only driven by a row of co-constructed nozzles, the machine can abandon the transmission mode of a traditional mechanical power cloth carrying wheel, and meanwhile, the fabric can also automatically complete folding operation through high-speed air flow sprayed by the co-constructed nozzles, so that the traditional mechanical power cloth swinging mode can also be abandoned, therefore, the fabric is not damaged by the friction impact of the power cloth carrying wheel and a power cloth swinging device in the fast circular moving process, and is not subjected to the discontinuous phenomenon of the moving speed generated by a fiber fabric and the power cloth carrying wheel, and further, the purposes of simpler control and uniform moving can be obtained.

The main purpose of the present invention is to provide an impulse type detonation wave fast dyeing machine, which, when dyeing or other processing, wherein, before the fiber fabric enters the collecting groove, the folding operation can be finished through the swing of the boosting force, and the strong swing phenomenon can be generated through the air impact effect instantaneously caused by the fiber fabric, so that the residual working solution attached to the surface of the fiber fabric, the free fiber, the unreacted floating dye or other solid objects can be rapidly and forcibly driven away, the superposed fabric entering the collecting groove can comprehensively obtain the liquid removal and pollution reduction and the gravity for mutual extrusion reduction, the residual working solution attached to the fiber fabric is reduced to the minimum, and the operation of obtaining the minimum liquid volume is realized, therefore, in addition to facilitating the rapid treatment, the minimum amount of the working fluid and the treatment of high concentration can be created.

The main purpose of the present invention is to provide an impulse type detonation wave fast dyeing machine, wherein during dyeing or other processing, fiber fabric can be desized, refined, surface modified, polymerized and grafted by using low temperature plasma flowing at high speed in dry state environment, so that the purpose of obtaining wider invention process space during processing fiber fabric can be provided besides anhydrous processing.

The invention mainly aims to provide an impulse type detonation wave fast dyeing machine, which can be used for pre-pumping dye and treating agent into a container of a pump-free feeding device to correspond to variable pressure environments in a treatment tank during dyeing or other processing treatment, and highly-accurately supplying the dye and the treating agent by utilizing the potential energy, and aims to save pumping electric energy of high-lift micro-liquid quantity besides not influencing the flow value required by supplying due to the environmental change of temperature rise or pressure rise in the treatment tank.

The main object of the present invention is to provide an impulse type detonation wave fast dyeing machine, in which a power cloth driving wheel is not required to be arranged at the inlet of the front end of a cloth guide tube, and a mechanical cloth placing device is not required to be arranged at the outlet end of the cloth guide tube. Therefore, when in operation, the safe operation environment can be provided, the operators are not stressed or injured by the power cloth driving wheel, the sliding friction of the power cloth driving wheel and the winding phenomenon caused by asynchronism can be provided, and the moving speed of the fabric is not restricted when the fabric passes through the cloth guide pipe and is not influenced by the mechanical cloth swinging device.

Drawings

The following is a detailed description of the preferred embodiments of the invention and accompanying drawings that will help further understanding of the technical content and, objects and actions of the invention; the drawings relating to this embodiment are:

FIG. 1 is a side sectional view of the structure of an impulse type detonation wave fast dyeing machine;

FIG. 2 is a side cross-sectional view of a heightened type of structure of the impulse type detonation wave fast dyeing machine;

FIG. 3 is a side cross-sectional view of an elongated configuration of an impulse detonation wave fast dyeing machine;

FIG. 4A is a cross-sectional view of the structure of a co-constructed nozzle orifice;

FIG. 4B is a sectional view of the structure of the nozzle opening with the replaceable electric shock rod;

FIG. 5 is a perspective view of the AC type airflow distribution device;

FIG. 5A is a cross-sectional view of an alternative flow type air distribution device;

FIG. 5B is a sectional view of the structure of the double-tube AC type air flow distribution device;

fig. 6 is a sectional view of the structure of the ac type liquid flow distributor.

FIG. 7 is a perspective view of the AC type air flow reflux unit;

FIG. 7A is a cross-sectional view of an alternative flow air reflow apparatus;

fig. 7B is a sectional view of the structure of the double-tube ac type air flow reflux apparatus.

Description of the main reference numerals

Treatment tank 1

Cloth collecting groove 2

Fiber fabric 3

High-voltage power supply facility 5

Cloth guide tube 11

Working door opening 12

Reflection operation substrate 13

U-shaped rotary plate 14

Guide plate 15

Blower 16

Drip collector plate 18

Material preparing barrel 19

Pump-free feeding device 20

Inside separation grid 21

Outside separation grid 22

Slide bar 23

Mesh plate 24

Upstream doffing section 31

Diversion port 42

Road junction 43

Return port 46

Arc-shaped shunt pipe 61

Manifold 62

Gas flow delivery piping system 71

Pressurized circulation pump 72

Feed pump 73

Upstream inlet 111

Downstream outlet 112

Co-constructed nozzle 121

Air floatation nozzle 122

Wedge-shaped clearance passage 151

Airflow return pipe 160

Air heater 161

Airflow filter 162

Alternating current type airflow distribution device 163

Right entering oblique manifold 164

Left inlet oblique manifold 165

Manifold port 166

Co-constructed dispensing tube 167

Air flotation distribution pipe 168

Air flow regulating valve 169

Dye liquor return pipe 170

Dispensing port 172

Alternating current type liquid flow distributor 173

Right intake manifold 174

Left intake manifold 175

Pressure equalizing distribution tube 176

Shunting hole 178

Spout 179

Collecting flow guide groove 181

Flow guide tube 182

Working fluid collecting plate 184

Alternating current type airflow reflux device 190

Divergent tube 191

T-shaped confluence return pipe 192

Exhaust gas discharge and control valve 200

Fresh air inlet and control valve 201

Flow regulating valve 202

Fluid delivery tubing system 210

Vapor input and control valve 211

Other gas introduction port and control valve 212

Working fluid collecting tank 213

Working fluid recovery or drain valve 214

Working fluid screen filter 215

Working fluid heat exchanger 220

Circulation path 221

Annular electric target 12111

Jet pipe 12121

Replaceable electric shock rod 12122

High voltage power connection terminal 12123

Ground connection terminal 12124

Hydraulic atomizing nozzle 1216

Hydraulic atomizing nozzle opening 12161

Working fluid inlet 12162

Sliding valve stem 12164

Nozzle carrier 12165

Spring piston 12167

Actuating fluid inlet 12169

Best mode for carrying out the invention

Referring to fig. 1 to 7, the impulse type detonation wave fast dyeing machine of the present invention comprises a treatment tank 1, a cloth collecting tank 2, a fiber fabric 3, a cloth guide pipe 11, a working door hole 12, a reflection action base plate 13, a U-shaped revolving plate 14, a guide plate 15, a blower 16, a droplet collecting plate 18, a material preparation barrel 19, a pump-free feeding device 20, an inner separation grid 21, an outer separation grid 22, a slide bar 23, a mesh plate 24, an upstream falling cloth section 31, a diversion port 42, a passage port 43, a return port 46, an arc-shaped diversion pipe 61, a confluence passage pipe 62, an air flow conveying pipe system 71, a liquid flow pressurization circulating pump 72, a feeding pump 73, an upstream inlet 111, a downstream outlet 112, a co-constructed nozzle 121, an air flotation nozzle 122, a wedge-shaped gap passage 151, an air flow return pipe 160, an air heater 161, an air filter 162, an alternating-flow air flow distribution device 163, a right-entering inclined manifold 164, a, Left inlet oblique manifold 165, confluence port 166, common distribution pipe 167, air-float distribution pipe 168, air flow regulating valve 169, dye liquor return pipe 170, distribution port 172, alternating-current liquid flow distributor 173, right inlet manifold 174, left inlet manifold 175, pressure-equalizing distribution pipe 176, diversion hole 178, jet port 179, collecting diversion groove 181, diversion pipe 182, working liquid collecting plate 184, alternating-current air flow reflux device 190, divergent pipe 191, T-shaped confluence return pipe 192, exhaust gas discharge port and control valve 200, fresh air inlet port and control valve 201, flow regulating valve 203, liquid flow conveying piping system 210, vapor inlet port and control valve 211, other gas inlet port and control valve 212, working liquid recovery and discharge port valve 214, circulation passage 221, annular electric target 1211, injection pipe 12121, replaceable electric shock 12122, high-voltage power supply connection terminal 12123, ground connection terminal 12124, Hydraulic atomizing nozzle 1216, hydraulic atomizing nozzle orifice 12161, sliding valve stem 12164, nozzle seat 12165, spring piston 12167, actuating fluid inlet 12169.

Referring to fig. 1 to 3, the structure of the processing bath 1 is that the processing bath 1 can be formed into a multi-bath type by a single bath type or parallel arrangement, and is generally circular when used at high temperature and high pressure, and is not limited by a pressure-resistant structure when used at normal temperature and normal pressure, and the shape can be matched with the processing amount and special processing requirements, or the volume space of the processing bath 1 can be arbitrarily increased or lengthened according to the environmental field. For example: fig. 2 shows a heightened model, which can achieve a larger throughput. For example, as shown in fig. 3, the present invention is an extension type machine, which can correspond to a fiber web 3 that is particularly easy to crease, and which is suitable for a circular shape in practice to achieve an optimum use and a minimum floor space in consideration of the shape and structure of the fiber web 3 to correspond to a waterless processing environment, smooth movement of the fiber web 3, and material cost. As shown in FIG. 1, the cloth collecting groove 2 and the cloth guide tube 11 in the treating tank 1 are formed along the inner space of the tank wall to form a circular circulation path, because they are adapted to high and low temperatures or high and low pressures and are designed in the form of O-letter of English letters. Wherein the cloth guide pipe 11 is arranged right above the cloth collecting groove 2 and is arranged in the same axial direction. For convenience of explanation, the clockwise direction is taken as the circulating moving direction of the fiber fabric 3, the nine o ' clock direction is taken as the front end of the treating tank 1, the three o ' clock direction is taken as the rear end of the treating tank 1, the lowest part of the bottom of the treating tank 1 is provided with a dye liquid return pipe 170 in the six o ' clock direction, an air flow return pipe 160 is provided in the central space part in the treating tank 1, and the tank wall at the front end of the treating tank 1 is provided with a working door hole 12.

The upstream inlet 111 of the cloth guide tube 11 is arranged in the inner space of the front end groove wall of the processing groove 1, is adjacent to the working door hole 12, is communicated with the downstream outlet of the cloth collecting groove 2 and is positioned near the working door hole 12, the downstream outlet 112 of the cloth guide tube 11 is positioned at the rear end of the processing groove 1 and is communicated with the upstream of the cloth collecting groove 2, so that the front ends and the rear ends of the cloth guide tube 11 and the cloth collecting groove 2 are respectively communicated with each other to form a wide circulation passage. Which can provide for dyeing or other processing of the fabric 3 in a freely spreading or open manner over the path. On the horizontal tube wall end surfaces crossing the left and right sides of the passage below the cloth guide tube 11, a plurality of air flotation nozzles 122 are provided in both the upstream and midstream sections along the passage direction, and on the cross section of the downstream section, a row of co-constructed nozzles 121 crossing between the left and right side walls of the passage are provided in parallel and combined, and the structure of the co-constructed nozzles 121 is shown in fig. 4A, B. At a location upstream of the inlet 1213 on the path of the expansion accelerating injection pipe of the co-constructed nozzle 121, there is provided a hydraulic atomizing nozzle 1216 which is composed of a nozzle holder 12165 and a sliding valve stem 12164. In order to achieve a precise flow rate, the preset optimum opening is normally maintained, and the jet flow rate is determined by the gap cross-sectional area between the nozzle seat 12165 and the sliding valve stem 12164 and the magnitude of the liquid pressure. The sliding valve stem 12164 is provided with a spring piston 12167 mechanism, when the hydraulic atomizing nozzle orifice is blocked, it can be introduced into the air chamber of the spring piston 12167 mechanism through the actuating fluid inlet 12169 by using air pressure or hydraulic fluid, so that the cylinder pressure in the spring piston 12167 mechanism is greater than the spring force, the sliding valve stem 12164 can slide backward immediately, the gap cross-sectional area is enlarged, and the free fiber or other solid material staying in the hydraulic atomizing nozzle orifice 12161 can be removed. During operation, if the spray flow is increased, a balance point is obtained between the pressure exerted by the air cylinder and the elastic force of the spring, and the required spray flow can be obtained.

In operation, as shown in fig. 1 and 4A, the hydraulic atomizing nozzle 1216 is interconnected with the delivery pipe systems 210 and 170 and the pressurized circulating pump 72 via the ac type flow distributor 173, and the pressurized circulating pump 72 applies pressure to the dye liquor or treating liquor, which is generally pressurized to 5kg/c m, and then introduced into the hydraulic atomizing nozzle opening 12161 capable of generating strong shearing force for spraying and atomizing the dye liquor or treating liquor²The good atomization effect can be obtained, the atomization effect can be greatly improved under the condition that the pressure is higher and the temperature is higher, in order to ensure that the motion energy of the atomized dye liquor or treatment liquor is kept to improve the impact force, the atomization angle is controlled within the range of a small angle to carry out atomization, the dye liquor or treatment liquor which is broken and dissociated into particles can be fully dispersed in the injection pipe 12121 to be mixed with the high-speed air flow which is accelerating in expansion, and the atomized dye liquor or treatment liquor can be fully dispersed in the injection pipe 12121 and can pass through the co-constructed nozzle opening 1211The fiber fabric 3 is broken and dissociated again to form smaller particles, so that when the fiber fabric 3 is impacted, the uniform amount of the dye solution or the treatment solution and the uniform impact force can be obtained on the surface area of the fiber fabric 3. In order to achieve a more complete cleaning and production purpose, an exchangeable electric shock 12122 may be additionally provided at the center of the passage of the hydraulic atomizing nozzle opening 12161. as shown in fig. 4B, the electric shock 12122 is provided at the center of the sliding valve stem 12164 of the hydraulic atomizing nozzle 1216 integrally with the sliding valve stem 12164 of the insulator, and the other end thereof extends to the outside of the hydraulic atomizing nozzle 1216 to form a high voltage power connection terminal 12123 which is connected to the high voltage power supply 5 outside the treatment tank 1 via a cable. The wall of the nozzle 12121 in the path of the nozzle 121 is replaced by an insulator 12121, and the nozzle 1211 is arranged in the nozzle as an annular target 12111, which is integral with the nozzle 121, and a ground connection 12124 is provided on the annular target, which is connected to the ground surface via a cable.

An air-float distribution pipe 168 is provided in an outer space of the horizontal pipe wall crossing the left and right sides of the passage below the cloth guide pipe 11 at an inlet of the upstream and midstream sections with respect to the area of the air-float nozzles 122 in the passage direction, and an air flow rate adjustment valve 169 is provided at an upstream inlet of the air-float distribution pipe. At the inlet of the co-structural nozzle 121, in the space outside the air-float distribution pipe 168, there is a co-structural distribution pipe 167, at the inlet of the co-structural distribution pipe 167, on the path with the air flow conveying pipeline system 71, outside the co-structural distribution pipe, and near the central portion in the treatment tank 1, there is an alternating flow distribution device 163, as shown in fig. 1, 5A and 5B, which mainly includes two adjacent and symmetrical left-entering oblique manifold 165 and right-entering oblique manifold 164, with respect to the transverse direction of the treatment tank 1, the left-entering oblique manifold 165 is from left to right, the right-entering oblique manifold 164 is from right to left, the length is the same width as the width of the distribution guide pipe 11, if the width of the double-pipe distribution guide pipe 11 is the same width, if the double-pipe distribution guide pipe 11 is the same width as the width of the four-pipe distribution guide pipe 11, the length can be arbitrarily reduced or reduced according to the width of the distribution guide pipe 11, the oblique side wall of the oblique manifold is respectively provided with a row of shunt ports 42 which are arranged and combined in parallel along the passage direction, each shunt port 42 is respectively provided with an arc-shaped shunt pipe 61, the arc-shaped shunt pipes 61 can enable the shunt pipes which are staggered up and down to form a row of passage ports 43 in the same direction through the function of the arc-shaped shunt pipes 61 through geometric calculation, the downstream end outlet of each arc-shaped shunt pipe 61 forms a row of confluence ports 166 which are arranged in parallel in the same direction, the downstream side end at the confluence port 166 is provided with a confluence passage pipe 62, the upstream side end inlet of the confluence passage pipe is communicated with the confluence port 166, and the downstream side end outlet of the passage pipe is communicated with a common distribution pipe 167 and an air flotation distribution pipe 168.

Referring to fig. 6, an alternating current type fluid distributor 173 is disposed in a lower space of the hydraulic atomizing nozzle 1216 at the working fluid inlet 12162 and a passage of the fluid transport piping system 210, and the structure of the alternating current type fluid distributor 173 is shown in fig. 1 and 6. The device mainly comprises a left inlet manifold 175 and a right inlet manifold 174 which are arranged symmetrically and adjacently and a pressure equalizing distribution pipe 176, wherein the left inlet manifold 175 and the right inlet manifold 174 are arranged symmetrically and adjacently, the length of the pressure equalizing distribution pipe 176 is the same as the width of a cloth guide pipe 11 on the left side and the right side of the pressure equalizing distribution pipe 176, if the pressure equalizing distribution pipe 176 is used on a double-pipe cloth guide pipe 11, the width of the double-pipe cloth guide pipe 11 is the same as the width, if the pressure equalizing distribution pipe is used on a four-pipe cloth guide pipe 11, the width of the four-pipe cloth guide pipe 11 is the same as the width, the length of the four-pipe cloth guide pipe 11 can be arbitrarily widened or shortened according to the number of the cloth guide pipe 11, a row of shunting holes 178 are respectively arranged on the side walls of the left inlet manifold 175 and the right inlet manifold 174 along the downstream direction, a proper gap is kept between the shunting holes 178, between the two shunting holes 178, two rows of different-direction or staggered jet ports 179 are formed in, with respect to the inlet 12161 of the hydraulic atomizing nozzle, there are provided distribution ports 172 which can be connected to each other in a passage with the hydraulic atomizing nozzle 1216 by a communicating pipe.

Referring to FIGS. 1 to 3, an AC type air current reflux unit 190 is further provided at the center of the treatment tank 1 above the working fluid collecting plate 184, as shown in fig. 7, 7A and 7B, the ac type air flow reflux unit 190 is constructed, which is very close to the ac type air flow distribution device 163 in structure, mainly comprises two adjacent symmetrical divergent tubes 191 and a T-shaped confluence return tube 192, based on the transverse direction of the processing tank 1, the left collecting pipe is from left to right, the right collecting pipe is from right to left, the length is the same as the width of the cloth guide pipe 11, if the double-pipe cloth guide pipe 11, the width of the double-tube cloth guide tube 11 is the same, if the width of the four-tube cloth guide tube 11 is the same, the length of the guide tube 11 can be increased or decreased according to the number of the guide tube, and a row of parallel arranged and combined return openings 193 are respectively arranged on the lower side wall of the divergent tube 191 along the passage direction. The downstream outlet end of the divergent pipe is connected to the left and right ends of the T-shaped return pipe 192 through a 180-degree communicating rotary pipe 194, so that the return air flow can be communicated with the blower 16 through the return duct 160 at the central outlet of the T-shape.

Thus, in operation, the hydraulic atomizing nozzles 1216 may be operated by the alternating flow distributor 173 such that each hydraulic atomizing nozzle 1216 emits the same flow rate value. Therefore, in operation, the co-configured nozzles 121 can eject the same flow rate value from each of the co-configured nozzles 121 and each of the air flotation nozzles 122 by the action of the alternating current type airflow distribution device 163. Therefore, during operation, the co-constructed nozzle 121 can be used as a main power source for driving the fabric 3 to move circularly, during dyeing or other processing, the rotation period of the blades of the air blower 16 can be increased or decreased according to the characteristics and processing requirements of the fabric 3, so as to obtain the required working air flow rate, and the adjusting valve 169 at the inlet of the air-floating distribution pipe can be used for ejecting a proper amount of air flow from the air-floating nozzle 122 according to the unit area weight of the fabric 3, so as to float the fabric 3, so that the fabric 3 can obtain a relatively stable air flow to slide in an air cushion manner, and the friction contact and disturbance between the fabric 3 and the pipe wall are avoided, so as to reduce the resistance of the fabric 3 during rapid movement to the minimum. Therefore, the high speed air flow, or the high speed atomized dyeing liquid and treating agent, or the high speed low temperature plasma, or the high speed steam flow, or other gas or liquid, can be sprayed onto the lower surface of the fabric 3 in a direct close manner by the co-constructed nozzle 121, and the fabric 3 can be caused to generate a strong fluctuation by the reflection action substrate 13, and the high speed air flow is subjected to the end surface traction action of the reflection action substrate 13 and is propelled from the lower side of the fabric 3 toward the downstream direction by the reflection action substrate 13, so as to induce the pressure difference action, and further cause the fabric 3 to generate an accelerated movement and a fluctuation movement, and the fabric 3 in the upstream and midstream sections along the passage direction on the horizontal tube wall end surface crossing between the left and right side walls of the passage through the lower side of the fabric guide tube 11, due to the acceleration of the movement of the fabric 3, the air at the boundary of the upper surface of the fabric 3 is pulled, and a fast flowing low-pressure area is formed, so that when the fabric 3 passes through the fabric guide tube 11, a vertical downward pressure is continuously generated on the upper end surface of the fabric 3, and when the fabric 3 is continuously driven by the push-pull of the co-configured nozzle 121, in addition to causing the fabric 3 to generate a fabric spreading effect in the downstream section of the co-configured nozzle 121, the fabric 3 is also pulled to move in an open-width air-floating manner in the upstream and midstream sections of the fabric guide tube 11, and moves along the passage toward the co-configured nozzle 121 along the passage immediately on the tube wall end surface below the passage.

Referring to fig. 1 to 3, a U-shaped rotary plate 14 is provided between the lower side of the outlet of the passage of the cloth guide tube 11 and the inner side of the inlet of the upstream distribution section 31 of the cloth collection tank 2 in the downstream section of the discharge direction of the co-constructed nozzle 121, the upstream side end of the U-shaped rotary plate 14 is fixed in a stepwise manner in a manner overlapping with the lower side of the opening of the co-constructed nozzle 121 so that the upstream side end face of the U-shaped rotary plate 14 forms a straight reflection operation base plate 13, an inner separation grid 21 and an outer separation grid 22 are provided in the distribution section 31 on the downstream outer side end face of the U-shaped rotary plate 14, a guide plate 15 is provided directly above the co-constructed nozzle 121 in the downstream section of the passage of the cloth guide tube 11, the upstream side end of the guide plate 15 overlaps with the tube wall of the cloth guide tube 11, and the downstream side end thereof is connected to the outer separation grid 22 of the distribution section 31 of the cloth collection tank 2 by the action of the guide plate 15, the downstream section space of the passage of the cloth guide tube 11 forms a tapered wedge-shaped gap 151, when the fiber fabric 3 passes through the wedge-shaped gap 151, it can be caused by the relative movement between the lower end surface of the guide plate 15 and the upper end surface of the fiber fabric 3, so as to cause the air above the fiber fabric 3 to be squeezed into the wedge-shaped gap to generate pressure in the cloth guide tube 11, thereby, the fiber fabric 3 passing through the co-constructed nozzle 121 can obtain downward pressure again, and the co-constructed nozzle 121 can be caused to obtain larger reaction force when the high-speed air flow is jetted to impact with the fiber fabric 3, and also can cause the air flow on the upper end surface of the fiber fabric 3 to continuously provide larger static pressure air flow when the fiber fabric 3 passes through the U-shaped revolving plate 14, which can provide the reflection energy generated by the fiber fabric 3 between the reflection action substrate 13 and the guide plate 15, all can be transmitted to the fiber fabric 3, thereby increasing the wave energy and wave frequency.

The downstream outlet of the cloth guide pipe 11 and the upstream cloth falling section 31 of the cloth collecting groove 2 are provided with a cloth swinging and liquid removing mechanism. The cloth swinging and liquid removing mechanism consists of the U-shaped rotary plate 14, the guide plate 15, the inner separation grid 21, the outer separation grid 22, the liquid drop collecting plate 18 and the working liquid collecting plate 184 which are explained above, wherein, an inner separation grid 21 and an outer separation grid 22 are respectively arranged on the inner and outer side walls of the cropping zone 31 at the upstream side end of the passage of the collecting and distributing groove 2, the upstream side end of the inner separation grid 21 is arranged at the interconnecting part of the U-shaped revolving plate 14 and the droplet collecting plate 18, and is arranged at the upstream side end of the collecting and distributing groove 2 in a relatively upright way and is positioned at the inner side of the cropping zone 31, the downstream end of the liquid collecting plate is connected to the upstream end of the working liquid collecting plate 184, the downstream end of the liquid collecting plate 18 is provided with a collecting guide groove 181, a guide pipe 182 is provided on the lower side wall of the collecting guide groove 181 and at the lowest portion of the working fluid collecting plate 184, and guides the collected working fluid to the discharge port 170 below the collecting and distributing tank 2 for discharge. The upstream side end of the outer separation grid 22 is engaged with the downstream side end of the guide plate 15, and the downstream side end thereof is engaged with the slide bar 23 and the mesh plate 24 on the lower side of the passage of the collecting and distributing tank 2, so that a circulation passage 221 for an air flow is formed between the outer side of the collecting and distributing tank 2 and the inner wall of the treatment tank 1, and the air flow discharged from the outer separation grid 22 can be guided to the passage of the cloth guide duct 11 at the front end of the treatment tank 1 through the circulation passage 221. The droplets, the free fibers and other impure solid matter discharged from the outer separation grid 22 are collected by the inner wall of the treatment tank 1, discharged to the lower discharge port 170 along the wall surface, and introduced into the working fluid collection tank 213. During operation, the high-speed air flow ejected from the co-structural nozzle 121 will be discharged through the upper side of the inner separation grid 21 along the end surface of the reflective actuation substrate 13 and the end surface of the U-shaped rotary plate 14 under the action of the lower end surface of the fiber fabric and the end surface of the reflective actuation substrate 13 and the U-shaped rotary plate 14, and at the same time, the fiber fabric 3 falling toward the collecting and distributing groove 2 will be pulled to move toward the inner separation grid 21, when the fiber fabric is blocked by the inner separation grid 21, the air flow will be instantly blocked to the passage from the inner separation grid 21, so that the high-speed air flow will instantly generate air-shock effect to develop expansion potential energy, and the fiber fabric 3 will be rapidly moved toward the outer separation grid 22 and continuously developed toward the lower side of the distributing section 31, therefore, the fiber fabric 3 of the inner separation grid 21 will be acted by the downward expanding air flow, the fiber fabric 3 is forced to move from the upper side to the lower side of the inner separation grid 21, when the fiber fabric 3 leaves the upper side of the inner separation grid 21, namely the passage of the inner separation grid 21 is opened again, so that the high-speed air flow acted by the U-shaped rotary plate 14 returns to the passage of the inner separation grid 21 again to be discharged, and the actions can be continuously and repeatedly generated during the operation, therefore, the fiber fabric 3 can generate a strong swinging phenomenon due to the change of the direction of the high-speed air flow when passing through the U-shaped rotary plate 14, and in the swinging process, every time when the fiber fabric 3 carries out reverse swinging, the fiber fabric 3 can promote the residual working solution attached to the surface of the fiber fabric 3 to cause strong tensile force to be separated from the fiber fabric 3 which moves reversely. Therefore, in addition to causing a large amount of residual working fluid to be separated from the surface of the fabric 3 in a manner of instantaneously generating droplets and accompanying the passage of the air flow from the inner separation wire 21 and the outer separation wire 22 to leave the doffing section 31 of the collecting chute 2, the fiber fabric dropped into the collecting chute 2 can be also made to smoothly perform the folding work by the swinging action.

Referring to fig. 1 to 3, an air filter 162, an exhaust gas outlet and control valve 200, a fresh air inlet and control valve 201, a flow control valve 202 disposed between the exhaust gas outlet and control valve 200 and the fresh air inlet and control valve 201 are disposed on the return duct 160, a steam inlet and control valve 211 and other gas inlets and control valves 212 are disposed on the liquid flow duct system 210, a working fluid collecting tank 213 and a recycling or discharging port 214 are disposed at the bottom of the treatment tank 1, and the valves for introducing or discharging can be arbitrarily controlled according to the process requirements.

It also includes an air heater 161 and an air filter 162 connected to the air delivery 71 and the return path 160, respectively, and forming a path with the blower 16.

Therefore, when dyeing or other processing is performed, the circulating air and working fluid in the treatment tank 1 and the dye solution or treatment fluid in the pumpless feeding device 20 or the stock tank 19 can be communicated with each other through the respective pipe systems and the blower 16 and the feeding pump 73, and pressurized air and pressurized dye solution or treatment agent can be ejected by the co-constructed nozzles 121, and part of the pressurized air can be ejected through the air flotation nozzles 122.

The above detailed description is specific to possible embodiments of the present invention, which are not intended to limit the scope of the invention, and equivalent implementations or variations may be made without departing from the spirit of the present invention, such as: equivalent embodiments of these variations are intended to be encompassed by the claims of this application.

Claims

1. An impulse type detonation wave fast dyeing machine, which has at least one processing tank (1) combined side by side and is connected and communicated with a conveying pipeline system (71, 160, 210, 170), each processing tank (1) is internally provided with a cloth collecting tank (2) capable of providing textile collection and folding and a cloth guide pipe (11) capable of providing textile accelerated movement, the front end and the rear end of the two are respectively communicated with each other and form a wide circulation passage, and the textile can be fast dyed and processed in a widening mode on the passage, and the machine is characterized by comprising:

the air floatation nozzle (122) consists of a plurality of small hole passages, is arranged on the lower pipe wall of the upstream and midstream sections along the passage of the cloth guide pipe (11), and is communicated with the blower (16) through an air floatation distribution pipe (168) and air flow conveying pipeline systems (71, 160);

a co-constructed nozzle (121), the co-constructed nozzle (121) is composed of a gas injection pipe (12121) and a hydraulic atomization nozzle (1216), which is installed on a section of the downstream section of the cloth guide pipe (11) near the outlet of the cloth guide pipe (11), and a row of co-constructed nozzles (121) combined side by side are connected and communicated with the blower (16) and the pressurized circulation pump (72) through a co-constructed distribution pipe (167) and gas flow delivery pipe systems (71, 160) and liquid flow delivery pipe systems (210, 170).

2. An impulse type detonation wave fast dyeing machine according to claim 1, characterized by further comprising a reflection action base plate (13) mounted in a downstream direction of the co-constructed nozzle (121) in a stepwise manner lap-jointed to a lower side of the co-constructed nozzle (121).

3. An impulse type detonation wave fast dyeing machine according to claim 1, characterized by further comprising a U-shaped revolving plate (14) installed downstream of the co-constructed nozzle (121) between the lower side of the outlet of the passage of the cloth guide tube (11) and the inner side of the upstream inlet of the cloth collection chute (2).

4. An impulse type detonation wave fast dyeing machine as claimed in claim 1, additionally comprising:

a U-shaped rotary plate (14) which is arranged at the downstream side of the reflection actuating substrate (13), is formed by extending the reflection actuating substrate (13) and forms an arc-shaped loop in a progressive mode;

a droplet collecting plate (18) provided at the downstream end of the U-shaped rotating plate (14);

a collection guide groove (181) provided at a downstream side end of the droplet collection plate (18);

a flow guide pipe (182) arranged on the lower side wall of the collecting flow guide groove (181);

an inner separation grid (21) which is arranged at a position where the upstream side end is connected with the U-shaped rotary plate (14) and the liquid drop collecting plate (18) and is arranged at the inner side of a cropping section (31) at the upstream side end of the cropping slot (2) in a vertical or near vertical mode;

the upstream end of the outside separation grid net (22) is arranged at the downstream end of the guide plate (15), and the downstream end thereof is mutually connected with a slide bar (23) and a mesh plate (24) at the lower side of the collecting and distributing groove passage;

and a working fluid collecting plate (184) which is provided at the downstream end of the inner separation grid (21) and is positioned on the upper side of the passage of the collecting groove (2).

5. An impulse type detonation wave fast dyeing machine, which has at least one processing tank (1) combined side by side, and the conveying pipeline systems (71, 160, 210, 170) are connected and communicated with each other, each processing tank (1) is provided with a cloth collecting tank (2) for collecting and folding textiles and a cloth guide pipe (11) for accelerating the movement of the textiles, the front end and the rear end of the two are respectively communicated with each other and form a wide circulation passage, and the textiles can be fast dyed and processed in a widening mode on the passage, the impulse type detonation wave fast dyeing machine is characterized by comprising:

a co-structural nozzle (121), the co-structural nozzle (121) is composed of a gas injection pipe (12121) and a hydraulic atomizing nozzle (1216), wherein the co-structural nozzle (121) has a central passage of the injection pipe (12121), a hydraulic atomizing nozzle (1216) is provided at an upstream side end of an inlet (1213), a replaceable electric shock rod (12122) is provided at a central portion of a passage of a hydraulic atomizing nozzle opening (12161), wherein a discharge tip is provided at a central portion of the hydraulic atomizing nozzle opening (12161), and the other end thereof extends to an outer side of the hydraulic atomizing nozzle body (1216) which is connected to a high voltage power supply (5) via a cable, a ring-shaped electric target (12111) is provided at the co-structural nozzle opening (1211) which forms a co-structural body with the ground surface via a cable, the co-structural nozzle (121) is installed at a cross-sectional surface of a downstream section of the cloth guide pipe (11), near the exit of the cloth guide (11), a row of nozzles (121) is arranged in a plurality of side-by-side combinations, which can be connected and communicated with the blower (16) and the pressure circulating pump (72) through a distribution pipe (167) and air flow conveying pipe systems (71, 160) and liquid flow conveying pipe systems (210, 170).

6. An impulse type detonation wave fast dyeing machine according to claim 5, characterized by further comprising a U-shaped revolving plate (14) installed downstream of the co-constructed nozzle (121) between the lower side of the outlet of the passage of the cloth guide tube (11) and the inner side of the upstream inlet of the cloth collection chute (2).

7. An impulse type detonation wave fast dyeing machine according to claim 5, characterized by further comprising a reflection action base plate (13) mounted on the lower side of the co-constructed nozzle (121) in a stepwise manner overlapping-fixed in the downstream direction of the co-constructed nozzle (121).

8. An impulse type detonation wave fast dyeing machine as claimed in claim 5, additionally comprising:

the upstream end of the outside separation grid (22) is arranged at the downstream end of the guide plate (15), and the downstream end thereof is mutually connected with the slide bar (23) and the mesh plate (24) at the lower side of the passage of the collecting and distributing groove (2);

and a working fluid collecting plate (184) which is arranged at the downstream side end of the inner separation grid (21).

9. An impulse type detonation wave fast dyeing machine according to claim 5, characterized in that an alternating current type liquid flow distributor (173) is arranged between the hydraulic atomizing nozzle (1216) and the conveying pipeline system (210), the alternating current type liquid flow distributor (173) comprises two symmetrical left inlet manifold pipes (175) and right inlet manifold pipes (174) which are arranged adjacently, and a pressure equalizing distribution pipe (63), based on the transverse direction of the treating tank (1), on the left and right sides of the pressure equalizing distribution pipe (63), the left inlet manifold pipes (175) are from left to right, the right inlet manifold pipes (174) are from right to left, the length is the same as the width of the cloth guiding pipes (11), if used for the double-pipe cloth guiding pipes (11), the width of the double-pipe cloth guiding pipes (11) is the same as the width, if used for the four-pipe cloth guiding pipes (11), the length can be arbitrarily widened or shortened according to the width of the cloth guiding pipes (11), a row of branch flow holes (81) are respectively arranged on the side walls of the left inlet manifold (175) and the right inlet manifold (174) along the downstream direction, a proper gap is kept between the branch flow holes (81) and the branch flow holes (81), two rows of jet flow ports (44) which are arranged in a relative staggered mode and are different in direction or staggered are formed between the branch flow holes (81), and outlets which can be mutually connected with the hydraulic atomizing nozzles (12163) through communicating pipes are respectively arranged on the side wall above the pressure equalizing distribution pipe (63) and opposite to the inlets of the hydraulic atomizing nozzles (12163).

10. An impulse type detonation wave fast dyeing machine as claimed in claim 5, characterized in that its air flow conveying piping system further comprises an alternating flow air flow return device (190), said alternating flow air flow return device (190) and return piping system (160) being interconnected in communication with the blower (16).

11. An impulse type detonation wave fast dyeing machine, which has at least one processing tank (1) combined side by side, and the conveying pipeline systems (71, 160, 210, 170) are connected and communicated with each other, each processing tank (1) is provided with a cloth collecting tank (2) for collecting and folding textiles and a cloth guide pipe (11) for accelerating the movement of the textiles, the front end and the rear end of the two are respectively communicated with each other and form a wide circulation passage, and the textiles can be fast dyed and processed in a widening mode on the passage, the impulse type detonation wave fast dyeing machine is characterized by comprising:

a co-constructed nozzle (121), the co-constructed nozzle (121) is composed of a gas injection pipe (12121) and a hydraulic atomization nozzle (1216), and is arranged on the section surface of the downstream section of the cloth guide pipe (11), close to the outlet of the cloth guide pipe (11), and a row of co-constructed nozzles (121) which are combined side by side are connected and communicated with the blower (16) and the pressurizing circulation pump (72) through a co-constructed distribution pipe (167), a gas flow conveying pipeline system (71, 160) and a liquid flow conveying pipeline system (210, 170);

an alternating-current airflow distribution device (163) which is provided between the air-floating nozzle (122), the co-constructed nozzle (121), and the conveying pipeline system (71);

an alternating flow distributor (173) disposed between the hydraulic atomizing nozzle (1216) and the delivery line system (210).

12. An impulse type detonation wave fast dyeing machine according to claim 11, characterized by further comprising a U-shaped revolving plate (14) installed downstream of the co-constructed nozzle (121) between the lower side of the outlet of the passage of the cloth guide tube (11) and the inner side of the upstream inlet of the cloth collection chute (2).

13. An impulse type detonation wave fast dyeing machine according to claim 11, characterized by further comprising a reflection action base plate (13) mounted downstream of the co-constructed nozzle (121) and lap-fixed in a stepwise manner on the lower side of the co-constructed nozzle (121).

14. An impulse type detonation wave fast dyeing machine as claimed in claim 11, additionally comprising:

a U-shaped rotary plate (14) which is arranged at the downstream side of the reflection actuating substrate (13), is formed by extending the reflection actuating substrate (13) and forms an arc-shaped loop in a progressive mode; a droplet collecting plate (18) provided at the downstream end of the U-shaped rotating plate (14); a collection guide groove (181) provided at a downstream side end of the droplet collection plate (18); a flow guide pipe (182) arranged on the lower side wall of the collecting flow guide groove (181); an inner separation grid (21) which is arranged at a position where the upstream side end is connected with the U-shaped rotary plate (14) and the liquid drop collecting plate (18) and is arranged at the inner side of a cropping section (31) at the upstream side end of the cropping slot (2) in a vertical or near vertical mode;

the upstream end of the outside separation grid net (22) is arranged at the downstream end of the U-shaped rotary plate (14), and the downstream end thereof is mutually connected with a slide bar (23) and a mesh plate (24) at the lower side of the collecting and distributing groove passage;

15. An impulse type detonation wave fast dyeing machine as claimed in claim 11, characterized in that said alternating current type air flow distribution device (163) comprises two adjacent symmetrical left-entering oblique manifold (165) and right-entering oblique manifold (164), with respect to the transverse direction of the treatment tank (1), the left-entering oblique manifold (165) is from left to right, the right-entering oblique manifold (164) is from right to left, the length is the same as the width of the fabric guide tube (11), if the double tube fabric guide tube (11) is the same as the width of the double tube fabric guide tube (11), if the four tube fabric guide tube (11) is the same as the width of the four tube fabric guide tube (11), the length can be arbitrarily widened or narrowed according to the number of the fabric guide tube (11), a row of parallel arranged and combined branch ports (42) are provided on the oblique side wall of the oblique manifold along the passage direction, each branch port (42) is provided with an arc-shaped branch pipe (61), the arc-shaped shunt tubes (61) can enable the shunt tubes which are staggered up and down to form a row of same-direction access openings (43) through the action of the arc-shaped shunt tubes (61) through geometric calculation, so that the outlets of the downstream ends of the arc-shaped shunt tubes (61) form a row of confluence openings (166) which are arranged in parallel and in the same direction, a gradually expanded confluence passage pipe (62) is arranged at the downstream side end of the confluence opening (166), the inlets of the upstream side ends of the confluence passages are communicated with the confluence openings (166), and the outlets of the downstream side ends are communicated with a common distribution pipe (167) and an air flotation distribution pipe (168).

16. An impulse type detonation wave fast dyeing machine as claimed in claim 11, characterized in that the inlet upstream passage of the blower (16) is provided with a fresh air inlet (201) and an exhaust gas outlet (200), and a treatment liquid recovery or discharge port at the bottom of the lower side of the treatment tank (1), each inlet and discharge port being provided with a control valve which can be arbitrarily controlled according to the process requirements.

17. An impulse type detonation wave fast dyeing machine as claimed in claim 11, characterized in that it additionally comprises an air heat exchanger (161) and an air filter (162), and a working fluid heat exchanger (220) and a working fluid screen filter (215), connected to the gas delivery pipe system (71, 160) and the liquid delivery pipe system (210, 170), respectively.

18. An impulse type detonation wave fast dyeing machine, which has at least one processing tank (1) combined side by side, and the conveying pipeline systems (71, 160, 210, 170) are connected and communicated with each other, each processing tank (1) is provided with a cloth collecting tank (2) for collecting and folding textiles and a cloth guide pipe (11) for accelerating the movement of the textiles, the front end and the rear end of the two are respectively communicated with each other and form a wide circulation passage, and the textiles can be fast dyed and processed in a widening mode on the passage, the impulse type detonation wave fast dyeing machine is characterized by comprising:

the air floatation nozzle (122) consists of a plurality of small hole passages, is arranged on the pipe wall of the upper stream and the lower stream sections of the passages of the cloth guide pipe (11), and is communicated with the blower (16) through an air floatation distribution pipe (168) and air flow conveying pipeline systems (71, 160);

a co-structural nozzle (121), the co-structural nozzle (121) is composed of a gas injection pipe (12121) and a hydraulic atomizing nozzle (1216), wherein the co-structural nozzle (121) has a central passage of the injection pipe (12121), a hydraulic atomizing nozzle (1216) is provided at an upstream side end of an inlet (1213), a replaceable electric shock rod (12122) is provided at a central portion of a passage of the hydraulic atomizing nozzle opening (1216), wherein a discharge tip is located at a central portion of the hydraulic atomizing nozzle opening (12161), and the other end extends to an outer side of the hydraulic atomizing nozzle body (1216) which is connected to a high voltage power source via an electric cable, an annular electric target (12111) is provided at the co-structural nozzle opening (1211) which forms a co-structural body with the co-structural body (1211) which is connected to the ground surface via an electric cable, the co-structural nozzle (121) is installed on a cross section of a downstream section of the cloth guide pipe (11), near the exit of the cloth guide tube (11), a row of nozzles (121) combined side by side, which can be connected and communicated with the blower (16) and the pressurized circulating pump (72) through a distribution tube (167), a gas flow conveying pipeline system (71160) and liquid flow conveying pipeline systems (210, 170);

an alternating-current airflow distribution device (163) which is arranged between the air flotation nozzle (122), the co-constructed nozzle (121) and the airflow conveying pipeline system (71);

an alternating flow distributor (173) disposed between the hydraulic atomizing nozzle (1216) and the fluid delivery piping system (210).

19. An impulse type detonation wave fast dyeing machine according to claim 18, characterized in that it further comprises a U-shaped revolving plate (14) arranged downstream of the co-constructed nozzle (121) between the lower side of the outlet of the passage of the cloth guide tube (11) and the inner side of the upstream inlet of the cloth collection chute (2).

20. An impulse type detonation wave fast dyeing machine according to claim 18, characterized by further comprising a reflection action base plate (13) mounted in a downstream direction of the co-constructed nozzle (121) in a stepwise overlapping manner on a lower side of the co-constructed nozzle (121).

21. An impulse type detonation wave fast dyeing machine as claimed in claim 18, additionally comprising:

an inner separation grid (21) which is arranged at the upstream side end, is arranged at the position where the U-shaped rotary plate (14) and the liquid drop collecting plate (18) are connected with each other, and is vertically or nearly vertically arranged at the inner side of a cropping section (31) at the upstream side end of the cropping slot (2);

22. An impulse type detonation wave fast dyeing machine according to claim 18, characterized in that the alternating flow distributor (173) comprises two symmetrically arranged left inlet manifold (175) and right inlet manifold (174) and a pressure equalizing distribution pipe (63), in which the left inlet manifold (175) is arranged from left to right, the right inlet manifold (174) is arranged from right to left, the length is the same as the width of the fabric guide tube (11), in the case of a double tube fabric guide tube (11), the width of the double tube fabric guide tube (11) is the same as the width, in the case of a four tube fabric guide tube (11), the length is arbitrarily widened or shortened depending on the number of the fabric guide tube (11), and a row of branch holes (178) are respectively arranged in the downstream direction on the side walls of the left inlet manifold (175) and the right inlet manifold (174), in the lateral direction of the treatment tank (1), proper gaps are kept between the branch flow holes (178) and the branch flow holes (178), two rows of jet flow ports (179) in different directions or staggered are formed between the branch flow holes (178) of the two branches in a relative staggered arrangement mode, and outlets (172) are respectively arranged on the side wall above the pressure equalizing distribution pipe (176) and opposite to a working fluid inlet (12161) of the hydraulic atomizing nozzle (1216), and can be mutually connected with the hydraulic atomizing nozzle (1216) through communicating pipes to form a passage.

23. An impulse type detonation wave fast dyeing machine as claimed in claim 18, characterized in that said alternating current type air flow distribution device (163) comprises two adjacent symmetrical left-entering oblique manifold (165) and right-entering oblique manifold (164), with respect to the transverse direction of the treatment tank (1), the left-entering oblique manifold (165) is from left to right, the right-entering oblique manifold (164) is from right to left, the length is the same as the width of the fabric guide tube (11), if the double tube fabric guide tube (11) is the same as the width of the double tube fabric guide tube (11), if the four tube fabric guide tube (11) is the same as the width of the four tube fabric guide tube (11), the length can be arbitrarily widened or narrowed depending on the number of the fabric guide tube (11), a row of parallel arranged and combined branch ports (42) are provided on the oblique side wall of the oblique manifold along the passage direction, each branch port (42) is provided with an arc-shaped branch pipe (61), the arc-shaped shunt pipes (61) can enable the shunt pipes which are staggered up and down to form a row of same-direction access openings (43) through geometric calculation, and enable the outlets of the downstream ends of the arc-shaped shunt pipes (61) to form a row of parallel-arranged same-direction confluence openings (166) under the action of the arc-shaped shunt pipes (61), the outlets of the downstream ends at the confluence openings (166) are respectively connected and communicated with a co-constructed distribution pipe (167) and an air-flotation distribution pipe (168), and air flow regulating valves (169) are arranged at the inlets of the air-flotation distribution pipe (168).

24. An impulse type detonation wave fast dyeing machine as claimed in claim 18, characterized in that its delivery piping system further comprises an alternating current type air current reflux device (190), the alternating current type air current reflux device (190) mainly comprises two adjacent symmetrical divergent tubes (191) and a T-shaped confluence reflux tube (192), based on the transverse direction of the treatment tank (1), the left side confluence tube is from left to right, the right side confluence tube is from right to left, the length is the same width as the width of the cloth guide tube (11), if the double tube cloth guide tube (11), the width of the double tube cloth guide tube (11) is the same width, if the four tube cloth guide tube (11), the width of the four tube cloth guide tube (11) is the same width, the length can be arbitrarily widened or reduced according to the number of the cloth guide tube (11), along the passage direction on the lower side wall of the divergent tube (191), each is provided with a row of reflux ports (193) arranged and combined in parallel, the downstream outlet end of the divergent pipe is communicated with the left and right side ends of a T-shaped return pipe (192) through a 180-degree communicating rotary pipe (194), so that the return air flow can be communicated with a blower (16) through a return conveying pipe (160) at the central outlet of the T shape.

25. An impulse type detonation wave fast dyeing machine as claimed in claim 18, characterized in that the inlet upstream passage of said blower (16) is provided with a fresh air inlet (201) and an exhaust gas outlet (200), and a treatment liquid recovery or discharge outlet at the bottom of the lower side of the treatment tank (1), each inlet and discharge outlet being provided with a control valve which can be arbitrarily controlled according to the process requirements.

26. An impulse type detonation wave fast dyeing machine according to claim 18, characterized in that it additionally comprises an air heat exchanger (161) and an air filter (162), and a working fluid heat exchanger (220) and a working fluid screen filter (215), which are connected to the gas conveying piping system (71, 160) and the liquid conveying piping system (210, 170), respectively.