TWI769887B - Coal water removal equipment - Google Patents
Coal water removal equipment Download PDFInfo
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- TWI769887B TWI769887B TW110125237A TW110125237A TWI769887B TW I769887 B TWI769887 B TW I769887B TW 110125237 A TW110125237 A TW 110125237A TW 110125237 A TW110125237 A TW 110125237A TW I769887 B TWI769887 B TW I769887B
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- dewatering equipment
- microwave heating
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- 239000003245 coal Substances 0.000 title claims abstract description 126
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 41
- 238000010438 heat treatment Methods 0.000 claims abstract description 73
- 239000000428 dust Substances 0.000 claims description 11
- 238000007599 discharging Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 description 19
- 239000002184 metal Substances 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 4
- 238000010248 power generation Methods 0.000 description 4
- 239000013078 crystal Substances 0.000 description 3
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 2
- 239000003830 anthracite Substances 0.000 description 2
- 239000002802 bituminous coal Substances 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003077 lignite Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003415 peat Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 239000003476 subbituminous coal Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
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- Solid Fuels And Fuel-Associated Substances (AREA)
- Water Treatment By Sorption (AREA)
- Drying Of Solid Materials (AREA)
Abstract
本發明係有關於一種煤炭除水設備,用於降低一煤炭的含水量,該煤炭除水設備包括一微波加熱裝置,該微波加熱裝置包括一微波腔體、一輸送件以及複數個微波產生件,該等微波產生件產生微波並發射至該微波腔體內,該輸送件設置於該微波腔體中,並將該煤炭從該微波腔體的進料口傳送至出料口;其中,該煤炭經過該微波加熱裝置微波加熱後,該煤炭的含水量從25%至35%的範圍降低至10%至20%的範圍,且該煤炭產生複數個裂縫。 The invention relates to a coal dewatering device for reducing the moisture content of coal. The coal dewatering device includes a microwave heating device, and the microwave heating device includes a microwave cavity, a conveying part and a plurality of microwave generating parts , the microwave generating parts generate microwaves and transmit them into the microwave cavity, the conveying part is arranged in the microwave cavity, and transmits the coal from the inlet to the outlet of the microwave cavity; wherein, the coal After microwave heating by the microwave heating device, the moisture content of the coal is reduced from a range of 25% to 35% to a range of 10% to 20%, and the coal produces a plurality of cracks.
Description
本發明係有關於一種煤炭處理的技術領域,特別是有關於一種可大幅地降低煤炭含水量之煤炭除水設備。 The present invention relates to the technical field of coal treatment, in particular to a coal dewatering device that can greatly reduce the moisture content of coal.
煤炭係為目前生活中不可或缺的礦產,依含炭量及熱值區分,煤炭的種類主要可分為無煙煤、煙煤亞煙煤、褐煤及泥煤等,而不同種類的煤炭會具有不同的用途,例如,褐煤可用於發電,亞煙煤可用於發電及產熱,煙煤可用於發電及冶金,無煙煤普遍用於家庭產熱也可用於發電。 Coal is an indispensable mineral in current life. According to the carbon content and calorific value, the types of coal can be mainly divided into anthracite, bituminous coal, lignite and peat, etc., and different types of coal will have different uses. For example, lignite can be used for power generation, sub-bituminous coal can be used for power generation and heat production, bituminous coal can be used for power generation and metallurgy, and anthracite coal is commonly used for household heat production and can also be used for power generation.
煤的水分含量是評價煤炭的經濟價值的基本指標。煤炭在開採出來之後,其本身會有含水量,外水與內水,統稱為全水;外水為吸附於煤表面與毛細孔中的水分,內水即其內部之結晶水,而此結晶水也具有一定之重量。如此,當要運送煤炭至提煉的單位或工廠時,具有含水量之煤炭會增加運送的重量,對於具有一定容積的貨船或貨車而言,每次所能運送的煤炭量即相對減少,進而造成運送的成本增加。 The moisture content of coal is the basic index to evaluate the economic value of coal. After coal is mined, it will have water content. External water and internal water are collectively referred to as total water; external water is the water adsorbed on the surface of the coal and in the capillary pores, and the internal water is the crystal water inside. Water also has a certain weight. In this way, when the coal is to be transported to the refining unit or factory, the coal with water content will increase the transport weight. For a cargo ship or truck with a certain volume, the amount of coal that can be transported each time is relatively reduced, resulting in The cost of shipping increases.
為解決上述問題,必須先對開採出的煤炭進行除水。現有的煤炭除水設備是以旋窯爐加熱的方式對煤炭加熱除水使之乾燥,然而,此方式因加熱所產生的熱能係由外向內,且因為煤炭為燃料,需使用間接加 熱式的旋窯爐,以免煤炭燃燒。但結晶水不易被破壞,相對地拉長除水至完全乾燥的時間,進而影響後續的製程,例如研磨製程。 In order to solve the above problems, it is necessary to remove water from the mined coal. Existing coal dewatering equipment uses rotary kiln heating to heat and dewater coal to dry it. However, the heat energy generated by heating in this method is from outside to inside, and because coal is used as fuel, indirect heating is required. Hot rotary kiln to avoid coal burning. However, the crystal water is not easily destroyed, and the time for removing the water to be completely dry is relatively prolonged, which in turn affects the subsequent process, such as the grinding process.
有鑑於此,本發明的目的在於提供一種煤炭除水設備。煤炭係可利用微波加熱裝置之微波加熱而大幅地降低含水量,且經過微波加熱後之煤炭會產生裂縫而有利於後續之破碎製程、研磨製程等。前述之目的及功效係可藉由下述技術手段達成。 In view of this, the purpose of the present invention is to provide a coal dewatering equipment. The water content of coal can be greatly reduced by microwave heating of the microwave heating device, and the coal after microwave heating will produce cracks, which is beneficial to the subsequent crushing process, grinding process, etc. The aforementioned purposes and effects can be achieved by the following technical means.
本發明之煤炭除水設備係用於降低一煤炭的含水量,該煤炭除水設備包括一微波加熱裝置,該微波加熱裝置包括一微波腔體、一輸送件以及複數個微波產生件,該等微波產生件產生微波並發射至該微波腔體內,該輸送件設置於該微波腔體中,並將該煤炭從該微波腔體的進料口傳送至出料口;其中,該煤炭經過該微波加熱裝置微波加熱後,該煤炭的含水量從25%至35%的範圍降低至10%至20%的範圍,且該煤炭產生複數個裂縫。 The coal dewatering equipment of the present invention is used to reduce the moisture content of a coal. The coal dewatering equipment includes a microwave heating device, and the microwave heating device includes a microwave cavity, a conveying element and a plurality of microwave generating elements. The microwave generating part generates microwaves and transmits them into the microwave cavity; the conveying part is arranged in the microwave cavity, and transmits the coal from the feeding port of the microwave cavity to the discharging port; wherein, the coal passes through the microwave After microwave heating by the heating device, the moisture content of the coal is reduced from a range of 25% to 35% to a range of 10% to 20%, and a plurality of cracks are formed in the coal.
可選擇地,於一非限制性的例示實施態樣中,該微波加熱裝置的輸出功率為120瓩。 Optionally, in a non-limiting exemplary embodiment, the output power of the microwave heating device is 120 watts.
可選擇地,於一非限制性的例示實施態樣中,該微波加熱裝置的該輸送件為一螺旋件,該螺旋件沿該微波腔體的軸向延伸。 Optionally, in a non-limiting exemplary embodiment, the conveying member of the microwave heating device is a helical member, and the helical member extends along the axial direction of the microwave cavity.
可選擇地,於一非限制性的例示實施態樣中,該輸送件包括一軸體以及一螺旋板,該螺旋板沿著該軸體的軸向設置。 Optionally, in a non-limiting exemplary embodiment, the conveying member includes a shaft body and a spiral plate, and the spiral plate is disposed along the axial direction of the shaft body.
可選擇地,於一非限制性的例示實施態樣中,該軸體的一端連接於一驅動裝置,該驅動裝置驅動該軸體旋轉而使該螺旋板旋轉。 Optionally, in a non-limiting exemplary embodiment, one end of the shaft body is connected to a driving device, and the driving device drives the shaft body to rotate to rotate the spiral plate.
可選擇地,於一非限制性的例示實施態樣中,其中更包括一輸送帶,該煤炭經由該輸送帶輸送至該微波加熱裝置。 Optionally, in a non-limiting exemplary embodiment, a conveyor belt is further included, and the coal is conveyed to the microwave heating device via the conveyor belt.
可選擇地,於一非限制性的例示實施態樣中,該微波加熱裝置更附接有一集塵器。 Optionally, in a non-limiting exemplary embodiment, the microwave heating device is further attached with a dust collector.
可選擇地,於一非限制性的例示實施態樣中,該微波加熱裝置更附接有一冷凝器。 Optionally, in a non-limiting exemplary embodiment, the microwave heating device is further attached with a condenser.
可選擇地,於一非限制性的例示實施態樣中,其中更包括一破碎裝置,其係接收並破碎經過該微波加熱裝置微波加熱後之該煤炭。 Optionally, in a non-limiting exemplary embodiment, it further includes a crushing device, which receives and crushes the coal after microwave heating by the microwave heating device.
可選擇地,於一非限制性的例示實施態樣中,該破碎裝置更附接有一另一集塵器。 Optionally, in a non-limiting exemplary embodiment, the crushing device is further attached with another dust collector.
可選擇地,於一非限制性的例示實施態樣中,該微波腔體係為一空心腔體,且該進料口與該出料口分別設置在該微波腔體的相對兩端。 Optionally, in a non-limiting exemplary embodiment, the microwave cavity system is a hollow cavity, and the feeding port and the discharging port are respectively disposed at opposite ends of the microwave cavity.
可選擇地,於一非限制性的例示實施態樣中,該微波產生件為磁控管。 Optionally, in a non-limiting exemplary embodiment, the microwave generating element is a magnetron.
可選擇地,於一非限制性的例示實施態樣中,該進料口具有一進料斗。 Optionally, in a non-limiting exemplary embodiment, the feed port has a feed hopper.
可選擇地,於一非限制性的例示實施態樣中,該微波腔體靠近該出料口的一端設有多個進氣口,該微波腔體靠近該進料斗的一端設有一排氣口,該進氣口設有多個氣流產生件。 Optionally, in a non-limiting exemplary embodiment, an end of the microwave cavity close to the discharge port is provided with a plurality of air inlets, and an end of the microwave cavity close to the feed hopper is provided with an exhaust port , the air inlet is provided with a plurality of airflow generating parts.
可選擇地,於一非限制性的例示實施態樣中,更包括一基座上,該基座包括一支撐架、多個承載板以及一工作梯。 Optionally, in a non-limiting exemplary embodiment, it further includes a base, and the base includes a support frame, a plurality of carrying plates and a working ladder.
可選擇地,於一非限制性的例示實施態樣中,該支撐架設置成與地面具有一傾斜角,該進料口至該出料口朝下方傾斜。 Optionally, in a non-limiting exemplary embodiment, the support frame is arranged to have an inclined angle with the ground, and the inlet to the outlet is inclined downward.
可選擇地,於一非限制性的例示實施態樣中,更包括一水冷式系統包括一進水管以及一排水管,該進水管以及該排水管分別設置多個副管,每個副管設置一閥體、並經由一軟管連接於該微波產生件。 Optionally, in a non-limiting exemplary embodiment, a water-cooled system further includes a water inlet pipe and a drain pipe, the water inlet pipe and the drain pipe are respectively provided with a plurality of auxiliary pipes, and each auxiliary pipe is provided with A valve body is connected to the microwave generating element via a hose.
可選擇地,於一非限制性的例示實施態樣中,該微波產生件在微波腔體上係彼此交錯排列。 Optionally, in a non-limiting exemplary embodiment, the microwave generating elements are arranged in a staggered arrangement on the microwave cavity.
本發明亦有關一種煤炭除水製程,包括下列步驟:提供一煤炭原礦,該煤炭原礦具有一第一含水量;輸送該煤炭原礦至一微波加熱裝置;以及以該微波加熱裝置微波加熱該煤炭原礦並得到一煤炭,且該煤炭具有一第二含水量並產生複數個裂縫;其中,該第一含水量為25%至35%的範圍,且該第二含水量為10%至20%的範圍。 The present invention also relates to a process for removing water from coal, comprising the following steps: providing a raw coal ore with a first water content; transporting the raw coal ore to a microwave heating device; and microwave heating the raw coal ore with the microwave heating device and obtain a coal, and the coal has a second water content and produces a plurality of cracks; wherein, the first water content is in the range of 25% to 35%, and the second water content is in the range of 10% to 20% .
可選擇地,於一非限制性的例示實施態樣中,於微波加熱之步驟之後,更包括下列步驟:以一破碎裝置破碎該煤炭。 Optionally, in a non-limiting exemplary embodiment, after the step of microwave heating, the following step is further included: crushing the coal with a crushing device.
本發明的煤炭除水設備及製程係利用微波加熱裝置產生微波後照射至煤炭,使煤炭快速加熱,利用熱漲冷縮之原理而產生裂縫,進而有利於後續之破碎製程、研磨製程等。另外,在微波加熱下,熱能由外向內直接破壞煤炭內部的結晶水並使其向外蒸散,大幅地降低煤炭的含水量。 The coal dewatering equipment and process of the present invention utilizes the microwave heating device to generate microwaves and then irradiates the coal to heat the coal rapidly, and utilizes the principle of thermal expansion and contraction to generate cracks, which is beneficial to the subsequent crushing process, grinding process, etc. In addition, under microwave heating, the heat energy directly destroys the crystal water inside the coal from the outside to the inside and makes it evaporate to the outside, which greatly reduces the moisture content of the coal.
10:煤炭除水設備 10: Coal water removal equipment
11:微波腔體 11: Microwave cavity
12:微波產生件 12: Microwave generator
13:輸送件 13: Conveyor
16:變壓裝置 16: Transformer device
17:驅動裝置 17: Drive unit
18:基座 18: Pedestal
19:水冷式系統 19: Water-cooled system
20:輸送帶 20: Conveyor belt
30:微波加熱裝置 30: Microwave heating device
31:集塵器 31: Dust collector
32:冷凝器 32: Condenser
40:破碎裝置 40: Crushing device
41:集塵器 41: Dust collector
111:進料口 111: Feed port
112:出料口 112: discharge port
113:進料斗 113: Feed Hopper
115:進氣口 115: Air intake
116:排氣口 116: exhaust port
117:氣流產生件 117: Airflow generating parts
131:軸體 131: Shaft
132:螺旋板 132: Spiral Plate
181:支撐架 181: Support frame
182:承載板 182: Carrier plate
183:工作梯 183: Working Ladder
191:進水管 191: water inlet pipe
192:排水管 192: Drainpipe
193:副管 193: Deputy
194:閥體 194: valve body
195:軟管 195: Hose
B:軸承 B: Bearing
第1圖為本發明的微波加熱裝置的一實施例的立體圖。 FIG. 1 is a perspective view of an embodiment of the microwave heating apparatus of the present invention.
第2圖為第1圖的微波加熱裝置的俯視圖。 FIG. 2 is a plan view of the microwave heating apparatus of FIG. 1 .
第3圖為第1圖的微波加熱裝置的前視圖。 Fig. 3 is a front view of the microwave heating device of Fig. 1 .
第4圖為第1圖的微波加熱裝置的剖視圖。 FIG. 4 is a cross-sectional view of the microwave heating device of FIG. 1 .
第5圖為第1圖的微波加熱裝置對煤炭進行微波加熱的示意圖。 FIG. 5 is a schematic view of the microwave heating apparatus of FIG. 1 for microwave heating of coal.
第6圖為第1圖的微波加熱裝置的後視圖。 FIG. 6 is a rear view of the microwave heating device of FIG. 1 .
第7圖為第1圖的微波加熱裝置的微波產生件的放大圖。 FIG. 7 is an enlarged view of the microwave generating member of the microwave heating apparatus of FIG. 1 .
第8圖為微波加熱裝置的另一實施例的剖視圖。 Fig. 8 is a cross-sectional view of another embodiment of the microwave heating device.
第9圖為微波加熱裝置的又另一實施例的剖視圖。 FIG. 9 is a cross-sectional view of yet another embodiment of a microwave heating device.
第10圖為本發明的處理流程圖。 Fig. 10 is a process flow chart of the present invention.
第11圖為煤炭微波加熱之工作效率曲線圖。 Figure 11 is a graph of the working efficiency of coal microwave heating.
第12圖為煤炭經過微波加熱後之其中一個實驗結果範例。 Figure 12 shows an example of one of the experimental results after the coal was heated by microwave.
第13圖為煤炭經過微波加熱後之另外一個實驗結果範例。 Figure 13 shows another example of experimental results after the coal was heated by microwave.
請同時參閱第1圖至第4圖,其中顯示有一煤炭除水設備10,其係用於降低一煤炭的含水量,且此煤炭除水設備10包括一微波加熱裝置30,並且微波加熱裝置30包括一微波腔體11、複數個微波產生件12以及一輸送件13。
Please refer to FIG. 1 to FIG. 4 at the same time, there is shown a
微波腔體11係為一空心腔體,其具有一進料口111以及一出料口112,且進料口111與出料口112分別設置在微波腔體11的相對兩端。此外,進料口111具有一進料斗113,進料斗113朝向上方直立,煤炭例如藉由一輸送帶20(請參閱第10圖)輸送至進料斗113、並藉由進料斗113的導引通過進料口111進入微波腔體11中;出料口112朝向微波腔體11的下方,經過微波加熱後的煤炭從出料口112離開微波腔體11。此處所稱的「上方」係指離開地面的方向,而「下方」係指朝向地面的方向。
The
如第1圖及第2圖所示,複數個微波產生件12分別插置於微波腔體11的外殼,每個微波產生件12具有一微波發射端,微波發射端位於微波腔體11內,微波發射端發出微波,微波照射至輸送至微波腔體11中的煤炭,而且由於本實施例的微波腔體11係為金屬製成,因此微波可由微波腔體11不斷地反射而反覆地照射至煤炭。
As shown in FIG. 1 and FIG. 2, a plurality of
在本實施例中,微波腔體11為多邊形的腔體,例如微波腔體11由十二個矩形的金屬板件沿一外接的圓柱面兩兩相接排列而形成筒狀的結構,上半部(180度)的六個矩形金屬板中,每個矩形的金屬板件上設有兩列孔位,因此總共有12列的孔位,每個孔位設置一個微波產生件12。
In this embodiment, the
另在本實施例中,微波產生件12為磁控管(magnetron)。磁控管具有中心陰極、環繞中心陰極的陽極以及設置在陰極與陽極軸向兩端的磁鐵,在陰極及陽極之間施加高電壓,而且對陰極加熱,使熱電子游離並在陰極與陽極之間的電場空間中移動,再搭配兩端的磁鐵所產生的磁場,在陰極與陽極之間的共振腔中產生微波,產生的微波經由微波發射端的天線發射至微波腔體11中。由於磁控管需要高電壓,因此在微波腔體11的外
部兩側設置多個變壓裝置16,將市電的電壓(110V或220V)轉換成磁控管所需要的高電壓(例如4000V)。
In addition, in this embodiment, the
再如第4圖所示,輸送件13設置在微波腔體11中,本實施例的輸送件13為一螺旋件,其沿微波腔體11的軸向延伸,且其包括一軸體131以及一螺旋板132,螺旋板132沿著軸體131的軸向設置。此外,軸體131的兩端分別由軸承B可旋轉地支持。
As shown in FIG. 4, the conveying
再請同時參閱第1圖至第3圖,軸體131的一端連接於一驅動裝置17,驅動裝置17驅動軸體131旋轉而使螺旋板132旋轉。在本實施例中,驅動裝置17為電動馬達。驅動裝置17的輸出軸經由聯軸器連接於軸體131,藉此使驅動裝置17得以驅動軸體131旋轉。
Please refer to FIGS. 1 to 3 at the same time. One end of the
請同時參閱第4圖及第6圖,在微波腔體11靠近出料口112的一端設有多個進氣口115,而在微波腔體11靠近進料斗113的一端設有排氣口116,在進氣口115設有多個氣流產生件117,在本實施例中,氣流產生件117為風扇,風扇轉動,藉以驅動空氣進入微波腔體11而在微波腔體11中產生氣流,氣流從排氣口116排出。
Please refer to FIG. 4 and FIG. 6 at the same time, a plurality of
再如第1圖至第3圖所示,微波腔體11、微波產生件12、輸送件13、變壓裝置16及驅動裝置17分別設置在一基座18上,基座18包括一支撐架181、多個承載板182以及一工作梯183。如第3圖所示,為了使煤炭在微波腔體11中的輸送更為順暢,支撐架181設置成與地面具有一傾斜角,亦即從進料口111至出料口112朝下方傾斜。如此,除了輸送件13推送煤炭從進料口111朝出料口112前進之外,煤炭也可利用傾斜的支撐架181藉由重力作用而從進料口111朝出料口112輸送。此外,如第1圖及第2圖所示,承
載板182設置在微波腔體11與變壓裝置16之間、以及驅動裝置17的兩側,工作梯183架設在支撐架181的一側,操作人員可經由工作梯183攀爬至承載板182,以方便進行維修或操作。
As shown in Figures 1 to 3, the
請參閱第5圖,煤炭輸送進入進料斗113之後,藉由進料斗113的導引而經由進料口111進入微波腔體11,且設置在微波腔體11中的輸送件13推送煤炭沿軸向前進,此時,微波產生件12產生微波並且使微波發射至微波腔體11中而照射在煤炭。如此,藉由微波可使煤炭中的水分子旋轉而使煤炭分子產生振盪,藉此升高煤炭的溫度,且隨著溫度升高,部分的水以及煤炭的粉塵等上升而懸浮在微波腔體11中,氣流產生件117在微波腔體11中產生的氣流將水氣及粉塵等經由排氣口116排出。
Please refer to FIG. 5 , after the coal is conveyed into the
如上所述,煤炭經由微波照射後,煤炭會因為此微波加熱而降低含水量,經實驗結果,含水量可從25%至35%的範圍降低至10%至20%的範圍。再者,煤炭的結構經過微波照射後會變得更為鬆散而產生裂縫,進而有利於後續之破碎製程、研磨製程等。 As mentioned above, after the coal is irradiated with microwaves, the coal will reduce the moisture content due to the microwave heating. According to the experimental results, the moisture content can be reduced from the range of 25% to 35% to the range of 10% to 20%. Furthermore, the structure of the coal will become more loose after microwave irradiation, resulting in cracks, which is beneficial to the subsequent crushing process, grinding process and the like.
於上述微波加熱之過程中,微波加熱裝置30的輸出功率為120瓩,當然並不以此為限,其可例如介於100瓩至400瓩之間,諸如150瓩、210瓩、240瓩、270瓩、300瓩、330瓩、360瓩等,實際實施時,微波加熱裝置30可依照所欲加熱的煤炭種類調整輸出功率以及加熱溫度。在本實施例中,微波加熱裝置30可使煤炭加熱於75℃至85℃間,較佳地,微波加熱裝置30可使煤炭加熱於80℃左右,使煤炭含水量經過微波加熱後大幅地減少外,也可避免煤炭於加熱過程中燃燒。
In the above-mentioned microwave heating process, the output power of the
請參閱第7圖,本實施例的微波產生件12為磁控管之形式,其係使用水冷式系統19(請同時參閱第3圖)對磁控管的陽極進行冷卻。水冷式系統19包括一進水管191以及一排水管192,進水管191以及排水管192分別設置多個副管193,每個副管193設置一閥體194、並經由一軟管195連接於微波產生件12,微波產生件12的陽極上環繞一水套,冷卻水從進水管191經由副管193、閥體194及軟管195通過水套,並吸收陽極產生的熱後,溫度升高的冷卻水經由軟管195、閥體194以及副管193進入排水管192,藉以達成水冷卻效果。
Referring to FIG. 7 , the
請參閱第8圖,其表示本發明的微波加熱裝置的另一實施例。在本實施例中,微波產生件12在微波腔體11上係彼此交錯排列。
Please refer to FIG. 8, which shows another embodiment of the microwave heating device of the present invention. In this embodiment, the
請參閱第9圖,其表示本發明的微波加熱裝置的又另一實施例。在本實施例中,一部分的微波產生件12在靠近微波腔體11頂部的矩形金屬板件上排列得較為緊密(間距較小),且另一部分的微波產生件12在靠近微波腔體11底部的矩形金屬板件上排列得較為疏散(間距較大),
Please refer to FIG. 9, which shows yet another embodiment of the microwave heating device of the present invention. In the present embodiment, a part of the
請參閱第10圖,其係為本發明的處理流程圖。如圖所示,要進行煤炭除水製程時,先提供一煤炭原礦,例如剛開採之煤炭原礦,且此煤炭原礦具有一第一含水量;之後,利用一輸送帶20輸送煤炭原礦至微波加熱裝置30,並以微波加熱裝置30微波加熱煤炭原礦並得到一煤炭,而且此煤炭具有一第二含水量並產生複數個裂縫;其中,如同上述,第一含水量為25%至35%的範圍,且第二含水量為10%至20%的範圍,亦即經微波加熱後,煤炭的含水量會從25%至35%的範圍降低至10%至20%的範圍。
Please refer to FIG. 10, which is a process flow chart of the present invention. As shown in the figure, when the coal water removal process is to be carried out, a raw coal ore, such as a newly mined coal ore, is provided first, and the coal raw ore has a first water content; then, a
於本實施例中,經由微波加熱後所得到之煤炭可再以一破碎裝置40進行破碎以利後續之使用,例如研磨製程,且如上所述,經由微波加熱後所得到之煤炭會產生複數個裂縫,因此在破碎製程、研磨製程上可很方便地進行。
In this embodiment, the coal obtained by microwave heating can be further crushed by a crushing
再如第10圖所示,於本實施例中,微波加熱裝置30可更附接有一集塵器31及一冷凝器32,破碎裝置40可更附接有一另一集塵器41。前述之集塵器31及另一集塵器41可於製程期間收集所產生之煙塵(飛灰),冷凝器32則可用於冷凝經微波加熱後所得到之氣體,並加以回收以供後續需要時使用。
As shown in FIG. 10 , in this embodiment, a
請參閱第11圖,其係顯示煤炭微波加熱之工作效率曲線圖。於第11圖中,橫軸之暴露時間代表煤炭暴露於微波加熱之時間(分鐘),縱軸之比較工作指數代表可以節省之煤炭研磨工作的時間百分比,例如,微波5分鐘,可以減少研磨工作時間約50%。換言之,利用微波加熱可大幅節省煤炭除水時間,並因此有利於後續破碎製程、研磨製程所需耗費的工作時間。 Please refer to Figure 11, which is a graph showing the working efficiency of coal microwave heating. In Figure 11, the exposure time on the horizontal axis represents the time (minutes) that the coal is exposed to microwave heating, and the comparative work index on the vertical axis represents the percentage of coal grinding work that can be saved. For example, microwaves for 5 minutes can reduce grinding work. about 50% of the time. In other words, the use of microwave heating can greatly save the time for dewatering the coal, which is beneficial to the working time required for the subsequent crushing and grinding processes.
請參閱第12圖,其顯示煤炭經過微波加熱後之其中一個實驗結果範例,如第12圖所示,水分的數據值皆顯著下降,即煤炭含水量經過微波加熱後係大幅地減少,而AR熱值則提升37.2%,同時煤炭的特性之一之總硫幾乎不變。(註:AR熱值係指每一公斤可以提共多少千卡的熱量(還有其他單位,如MJ/Kg(百萬焦耳/公斤);AR(As Received Base)意指用風乾試樣或恆濕試樣分析所得結果(%)或測定之發熱量(熱值),換算能成為當時分批交貨狀態之基準之表示法,即含有總水分之狀態。) Please refer to Figure 12, which shows an example of experimental results after the coal is heated by microwave. As shown in Figure 12, the data values of moisture are all significantly reduced, that is, the moisture content of coal is greatly reduced after microwave heating, while AR The calorific value is increased by 37.2%, while the total sulfur, one of the characteristics of coal, is almost unchanged. (Note: AR calorific value refers to the total number of kilocalories that can be lifted per kilogram (there are other units, such as MJ/Kg (million joules/kg); AR (As Received Base) means using air-dried samples or The result (%) or the measured calorific value (calorific value) obtained from the analysis of the constant-humidity sample can be converted into a representation of the current batch delivery status, that is, the status of total moisture content.)
請參閱第13圖,其顯示煤炭經過微波加熱後之另外一個實驗結果範例,如第13圖所示,對兩種不同規格之煤炭進行實驗,同樣的,水分的數據值皆顯著下降。 Please refer to Figure 13, which shows another example of the experimental results after the coal is heated by microwave. As shown in Figure 13, two different specifications of coal are tested. Similarly, the data values of moisture are significantly reduced.
惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍,即大凡依本發明申請專利範圍及發明說明內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。另外,本發明的任一實施例或申請專利範圍不須達成本發明所揭露之全部目的或優點或特點。此外,摘要部分和標題僅是用來輔助專利文件搜尋之用,並非用來限制本發明之權利範圍。 However, the above are only preferred embodiments of the present invention, and should not limit the scope of the present invention, that is, any simple equivalent changes and modifications made according to the scope of the patent application of the present invention and the contents of the description of the invention, All still fall within the scope of the patent of the present invention. In addition, it is not necessary for any embodiment of the present invention or the claimed scope of the present invention to achieve all of the objects or advantages or features disclosed herein. In addition, the abstract section and the title are only used to assist the search of patent documents and are not intended to limit the scope of the present invention.
10:煤炭除水設備 10: Coal water removal equipment
11:微波腔體 11: Microwave cavity
12:微波產生件 12: Microwave generator
16:變壓裝置 16: Transformer device
17:驅動裝置 17: Drive unit
18:基座 18: Pedestal
113:進料斗 113: Feed Hopper
116:排氣口 116: exhaust port
181:支撐架 181: Support frame
182:承載板 182: Carrier plate
183:工作梯 183: Working Ladder
30:微波加熱裝置 30: Microwave heating device
B:軸承 B: Bearing
Claims (16)
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| CN103013614A (en) * | 2012-12-28 | 2013-04-03 | 山东博润工业技术股份有限公司 | Coal drying and upgrading method |
| CN103074140A (en) * | 2012-12-28 | 2013-05-01 | 神华集团有限责任公司 | Coal impurity removing system |
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| CN106675661A (en) * | 2015-11-05 | 2017-05-17 | 中国石油化工股份有限公司大连石油化工研究院 | Method for continuous pyrolysis and gasification of material |
| CN107150998A (en) * | 2017-06-07 | 2017-09-12 | 中国科学院过程工程研究所 | A kind of coal desulfurization and the system and method for reclaiming elemental sulfur |
| TWM618338U (en) * | 2021-07-09 | 2021-10-11 | 永虹先進材料股份有限公司 | Coal dewatering equipment |
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| CN103013614A (en) * | 2012-12-28 | 2013-04-03 | 山东博润工业技术股份有限公司 | Coal drying and upgrading method |
| CN103074140A (en) * | 2012-12-28 | 2013-05-01 | 神华集团有限责任公司 | Coal impurity removing system |
| CN104962300A (en) * | 2015-06-24 | 2015-10-07 | 南京三乐微波技术发展有限公司 | Coal microwave dry distillation equipment and coal microwave dry distillation treatment method thereof |
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| TWM618338U (en) * | 2021-07-09 | 2021-10-11 | 永虹先進材料股份有限公司 | Coal dewatering equipment |
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