CN110760327B - Coal liquefaction plant and process - Google Patents
Coal liquefaction plant and process Download PDFInfo
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- CN110760327B CN110760327B CN201911032841.XA CN201911032841A CN110760327B CN 110760327 B CN110760327 B CN 110760327B CN 201911032841 A CN201911032841 A CN 201911032841A CN 110760327 B CN110760327 B CN 110760327B
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- 239000003245 coal Substances 0.000 title claims abstract description 243
- 238000000034 method Methods 0.000 title abstract description 10
- 239000007789 gas Substances 0.000 claims abstract description 69
- 238000005086 pumping Methods 0.000 claims abstract description 26
- 239000011261 inert gas Substances 0.000 claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 claims abstract description 6
- 238000009434 installation Methods 0.000 claims description 34
- 238000007789 sealing Methods 0.000 claims description 6
- 230000000903 blocking effect Effects 0.000 claims description 3
- 238000002309 gasification Methods 0.000 abstract 4
- 238000010586 diagram Methods 0.000 description 6
- 238000003912 environmental pollution Methods 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000012993 chemical processing Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/50—Fuel charging devices
- C10J3/506—Fuel charging devices for entrained flow gasifiers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/008—Controlling or regulating of liquefaction processes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16K—VALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
- F16K17/00—Safety valves; Equalising valves, e.g. pressure relief valves
- F16K17/20—Excess-flow valves
- F16K17/22—Excess-flow valves actuated by the difference of pressure between two places in the flow line
- F16K17/24—Excess-flow valves actuated by the difference of pressure between two places in the flow line acting directly on the cutting-off member
- F16K17/26—Excess-flow valves actuated by the difference of pressure between two places in the flow line acting directly on the cutting-off member operating in either direction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16K—VALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
- F16K17/00—Safety valves; Equalising valves, e.g. pressure relief valves
- F16K17/20—Excess-flow valves
- F16K17/22—Excess-flow valves actuated by the difference of pressure between two places in the flow line
- F16K17/24—Excess-flow valves actuated by the difference of pressure between two places in the flow line acting directly on the cutting-off member
- F16K17/28—Excess-flow valves actuated by the difference of pressure between two places in the flow line acting directly on the cutting-off member operating in one direction only
- F16K17/30—Excess-flow valves actuated by the difference of pressure between two places in the flow line acting directly on the cutting-off member operating in one direction only spring-loaded
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16K—VALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
- F16K17/00—Safety valves; Equalising valves, e.g. pressure relief valves
- F16K17/20—Excess-flow valves
- F16K17/34—Excess-flow valves in which the flow-energy of the flowing medium actuates the closing mechanism
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0903—Feed preparation
- C10J2300/0906—Physical processes, e.g. shredding, comminuting, chopping, sorting
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/093—Coal
- C10J2300/0933—Coal fines for producing water gas
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/093—Coal
- C10J2300/0936—Coal fines for producing producer gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1693—Integration of gasification processes with another plant or parts within the plant with storage facilities for intermediate, feed and/or product
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- Engineering & Computer Science (AREA)
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- Oil, Petroleum & Natural Gas (AREA)
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- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
技术领域technical field
本发明涉及煤炭液化技术领域,具体地说,涉及一种煤炭液化装置及工艺。The invention relates to the technical field of coal liquefaction, in particular to a coal liquefaction device and a process.
背景技术Background technique
煤炭液化是把固态状态的煤炭通过化学加工,使其转化为液体产品(液态烃类燃料,如汽油、柴油等产品或化工原料)的技术。煤炭通过液化可将硫等有害元素以及灰分脱除,得到洁净的二次能源,对优化终端能源结构、解决石油短缺、减少环境污染具有重要的战略意义。Coal liquefaction is a technology that converts solid coal into liquid products (liquid hydrocarbon fuels, such as gasoline, diesel and other products or chemical raw materials) through chemical processing. Coal liquefaction can remove harmful elements such as sulfur and ash to obtain clean secondary energy, which is of great strategic significance for optimizing the terminal energy structure, solving oil shortages and reducing environmental pollution.
煤炭液化加料时通常在锁斗中进行,先将煤炭加入锁斗,之后封闭锁斗并向锁斗中充入惰性气体使得锁斗中的气压与气化炉的压强相同,之后将煤炭输送进气化炉中,之后关闭锁斗与气化炉之间的阀门,并将惰性气体排出锁斗中进行下一次的上料。这样的上料方式不仅效率较低,并且会向空气中排放大量的氮气以及二氧化碳,十分的不环保。Coal liquefaction and feeding are usually carried out in the lock hopper. First, the coal is added to the lock hopper, then the lock hopper is closed and the inert gas is filled into the lock hopper so that the air pressure in the lock hopper is the same as the pressure of the gasifier, and then the coal is transported into the lock hopper. In the gasifier, then close the valve between the lock hopper and the gasifier, and discharge the inert gas from the lock hopper for the next feeding. Such a feeding method is not only inefficient, but also emits a large amount of nitrogen and carbon dioxide into the air, which is not environmentally friendly.
发明内容SUMMARY OF THE INVENTION
针对现有技术中存在的煤炭的液化过程中加料效率较低且会污染环境缺陷,本发明提供了一种煤炭液化装置及工艺。其能够达到提升粉煤的加料效率以及避免污染环境的效果。Aiming at the defects of low feeding efficiency and environmental pollution in the coal liquefaction process existing in the prior art, the present invention provides a coal liquefaction device and a process. It can achieve the effect of improving the feeding efficiency of pulverized coal and avoiding environmental pollution.
为了解决上述技术问题,本发明通过下述技术方案得以解决:In order to solve the above-mentioned technical problems, the present invention is solved by the following technical solutions:
一种煤炭液化装置,其包括用于储存惰性气体用的气体储存罐,气体储存罐的两端均设有粉煤储存罐,粉煤储存罐上端连接有破碎机构,破碎机构包括破碎釜,破碎釜与粉煤储存罐之间连接有进料管道,破碎釜中设有破碎腔,破碎腔中设有若干个沿破碎腔高度方向间隔设置的支撑板,破碎腔的中心处设有可转动的转轴,转轴上设有若干个用于与支撑板进行配合的转动板,支撑板与转动板上均设有用于供粉煤穿过的过料通孔;粉煤储存罐与气体储存罐之间设有用于连接气体储存罐与粉煤储存罐的第一连接管,第一连接管上设有用于输送气体储存罐与粉煤储存罐中气体的泵送机构;气体储存罐的下方设有气化炉,粉煤储存罐与气化炉之间设有用于连接粉煤储存罐与气化炉的第二连接管,第二连接管上设有第一阀门。A coal liquefaction device includes a gas storage tank for storing inert gas, both ends of the gas storage tank are provided with pulverized coal storage tanks, the upper end of the pulverized coal storage tank is connected with a crushing mechanism, and the crushing mechanism includes a crushing kettle, and the crushing mechanism includes a crushing kettle. A feeding pipeline is connected between the kettle and the pulverized coal storage tank. The crushing kettle is provided with a crushing cavity. The crushing cavity is provided with a number of supporting plates arranged at intervals along the height direction of the crushing cavity. The center of the crushing cavity is provided with a rotatable A rotating shaft, there are several rotating plates on the rotating shaft for cooperating with the supporting plate, and the supporting plate and the rotating plate are both provided with through holes for passing through the pulverized coal; between the pulverized coal storage tank and the gas storage tank There is a first connecting pipe for connecting the gas storage tank and the pulverized coal storage tank, and a pumping mechanism for transporting the gas in the gas storage tank and the pulverized coal storage tank is arranged on the first connecting pipe; A second connecting pipe for connecting the pulverized coal storage tank and the gasifier is arranged between the pulverized coal storage tank and the gasifier, and the second connecting pipe is provided with a first valve.
通过本发明的气体储存罐以及两端的粉煤储存罐的设置,能够使得该煤炭液化装置可以连续的向气化炉中添加粉煤,从而较佳的提升了煤炭液化的效率。同时,也避免了向空气中排放惰性气体,从而既节省了生产成本,又避免了对环境造成污染。The arrangement of the gas storage tank and the pulverized coal storage tanks at both ends of the present invention enables the coal liquefaction device to continuously add pulverized coal to the gasifier, thereby better improving the efficiency of coal liquefaction. At the same time, the emission of inert gas into the air is also avoided, thereby saving production costs and avoiding environmental pollution.
其中,破碎机构的设置,使得破碎釜可以连续进行粉煤的生产,也使得破碎机构生产的粉煤可以较为方便的输送至粉煤储存罐中,从而较佳的提升了该煤炭液化装置的生产效率。Among them, the setting of the crushing mechanism enables the crushing kettle to continuously produce pulverized coal, and also enables the pulverized coal produced by the crushing mechanism to be conveniently transported to the pulverized coal storage tank, thereby better improving the production of the coal liquefaction device. efficiency.
作为优选,泵送机构包括设置于第一连接管上且两端部与第一连接管相连接的U型连接管,第一连接管上位于U型连接管与第一连接管的连接处之间设有与U型连接管相连接的第三连接管,第三连接管上设有第一气泵;U型连接管上位于U型连接管与第三连接管的连接处的两端分别设有第二阀门以及第三阀门,第二阀门设置在靠近粉煤储存罐处,第三阀门设置在靠近气体储存罐处;第一连接管上设有位于第三连接管与第一连接管的连接处两端的第四阀门以及第五阀门,第四阀门设置在第三连接管与第一连接管的连接处与U型连接管与第一连接管的连接处之间且靠近粉煤储存罐端;第五阀门设置在第三连接管与第一连接管连接处与U型连接管与第一连接管的连接处之间且靠近气体储存罐处。Preferably, the pumping mechanism includes a U-shaped connecting pipe arranged on the first connecting pipe and two ends of which are connected with the first connecting pipe, and the first connecting pipe is located at the connection between the U-shaped connecting pipe and the first connecting pipe. There is a third connecting pipe connected with the U-shaped connecting pipe, and a first air pump is arranged on the third connecting pipe; There are a second valve and a third valve, the second valve is arranged near the pulverized coal storage tank, and the third valve is arranged near the gas storage tank; the first connecting pipe is provided with a valve between the third connecting pipe and the first connecting pipe. The fourth valve and the fifth valve at both ends of the connection, the fourth valve is arranged between the connection between the third connection pipe and the first connection pipe and the connection between the U-shaped connection pipe and the first connection pipe and is close to the pulverized coal storage tank The fifth valve is arranged between the connection between the third connection pipe and the first connection pipe and the connection between the U-shaped connection pipe and the first connection pipe and is close to the gas storage tank.
本发明中,通过泵送机构的设置,可以使得在气体储存罐以及粉煤储存罐进行冲放气压时,可以先通过管道的连通使得粉煤储存罐与气体储存罐中的气压相同,避免了直接利用第一气泵进行粉煤储存罐以及气体储存罐气压的交换,从而避免了由于气体压力过高而导致第一气泵的损坏,从而较佳的提升了该煤炭液化装置的稳定性。In the present invention, through the setting of the pumping mechanism, when the gas storage tank and the pulverized coal storage tank are flushed and released, the air pressure in the pulverized coal storage tank and the gas storage tank can be made the same through the communication of the pipeline first, avoiding the need for The first air pump is directly used to exchange the air pressure of the pulverized coal storage tank and the gas storage tank, thereby avoiding the damage of the first air pump due to excessive gas pressure, thereby better improving the stability of the coal liquefaction device.
作为优选,第一连接管上设有位于泵送机构与粉煤储存罐之间的过滤装置,过滤装置包括滤网安装座,滤网安装座中设有滤网安装腔,滤网安装腔中设有若干组卡槽,卡槽中卡接有第一滤网,滤网安装座的上端部设有用于对滤网安装腔进行密封的滤网安装腔盖板。Preferably, the first connecting pipe is provided with a filter device located between the pumping mechanism and the pulverized coal storage tank, the filter device includes a filter screen mounting seat, and a filter screen mounting cavity is provided in the filter screen mounting seat, and the filter screen mounting cavity is There are several groups of card slots, the first filter screen is clipped in the card slots, and the upper end of the filter screen installation seat is provided with a filter screen installation cavity cover plate for sealing the filter screen installation cavity.
本发明中,通过过滤机构的设置,能够对第一连接管中的粉煤进行过滤,避免了粉煤进入第一气泵中造成第一气泵的损坏,从而较佳的提升了本实施例中煤炭液化装置的稳定性。In the present invention, through the arrangement of the filtering mechanism, the pulverized coal in the first connecting pipe can be filtered, so as to avoid the pulverized coal entering the first air pump and causing damage to the first air pump, thereby better improving the coal in this embodiment. Stability of liquefaction plants.
作为优选,滤网安装腔底面向下凹陷形成滤网安装台阶,滤网安装台阶上设有垂直于第一滤网设置且用于对第一滤网进行支撑的第二滤网,第二滤网的底端设有整体呈倒圆台型的粉煤储存腔。Preferably, the bottom surface of the filter screen installation cavity is recessed downward to form a filter screen installation step, and the filter screen installation step is provided with a second filter screen arranged perpendicular to the first filter screen and used for supporting the first screen The bottom end of the net is provided with a pulverized coal storage cavity which is in the shape of a rounded table as a whole.
本发明中,通过第二滤网以及粉煤储存的设置,能够使得滤网安装腔中的粉煤可以落至粉煤储存腔中,从而方便了对于过滤装置中的粉煤进行收集。In the present invention, through the arrangement of the second filter screen and the pulverized coal storage, the pulverized coal in the filter screen installation cavity can be dropped into the pulverized coal storage cavity, thereby facilitating the collection of the pulverized coal in the filter device.
作为优选,粉煤储存罐与滤网安装座之间设有用于连接粉煤储存罐与滤网安装座的第四连接管,第四连接管的端部与粉煤储存腔相连接,第四连接管上设有第六阀门。Preferably, a fourth connecting pipe for connecting the pulverized coal storage tank and the screen mounting seat is provided between the pulverized coal storage tank and the filter screen mounting seat, and the end of the fourth connecting pipe is connected with the pulverized coal storage cavity, and the fourth connecting pipe is A sixth valve is arranged on the connecting pipe.
本发明中,通过第四连接管以及第六阀门的设置,能够使得在向粉煤储存罐中加压时,可以打开第六阀门,使得粉煤储存腔中的粉煤可以通过第四连接管输送至粉煤储存罐中,从而方便了对于粉煤储存腔中粉煤的回收利用。In the present invention, through the arrangement of the fourth connecting pipe and the sixth valve, the sixth valve can be opened when the pulverized coal storage tank is pressurized, so that the pulverized coal in the pulverized coal storage cavity can pass through the fourth connecting pipe It is transported to the pulverized coal storage tank, thereby facilitating the recycling of pulverized coal in the pulverized coal storage cavity.
作为优选,第一连接管上位于过滤装置以及U型连接管之间设有泄压装置,泄压装置包括呈管状的泄压管,泄压管中设有内管,泄压管内壁与内管外壁形成泄压腔,内管中心处的外侧壁上设有与泄压管内部侧壁固定连接的第一环形安装板,第一环形安装板将泄压腔分隔成为两个相对独立的空间;内管的中心处设有第二环形安装板,内管的外侧壁上靠近第二环形安装板端设有若干个均匀且沿内管轴线方向间隔分布的导气孔,内管中可滑动的设有滑动柱,滑动柱上靠近第二环形安装板的端部设有盲孔,内管中设有弹簧,弹簧的一端抵靠在盲孔中,弹簧的另一端抵靠在第二环形安装板上;内管的两端开口处设有用于对滑动柱进行阻挡的挡板,挡板的中心处设有挡板通孔。Preferably, a pressure relief device is provided on the first connecting pipe between the filter device and the U-shaped connecting pipe. The pressure relief device includes a tubular pressure relief pipe, and an inner pipe is arranged in the pressure relief pipe. The outer wall of the pipe forms a pressure relief cavity, and the outer side wall at the center of the inner pipe is provided with a first annular mounting plate fixedly connected to the inner side wall of the pressure relief pipe, and the first annular mounting plate divides the pressure relief cavity into two relatively independent spaces The center of the inner pipe is provided with a second annular mounting plate, and the outer side wall of the inner pipe is provided with a number of air guide holes evenly distributed along the axis of the inner pipe near the end of the second annular mounting plate. There is a sliding column, the end of the sliding column close to the second annular mounting plate is provided with a blind hole, the inner tube is provided with a spring, one end of the spring abuts against the blind hole, and the other end of the spring abuts against the second annular mounting plate The openings at both ends of the inner tube are provided with baffles for blocking the sliding column, and the center of the baffles is provided with a baffle through hole.
本发明中,通过泄压装置的设置,能够避免了在进行粉煤储存罐以及气体储存管间惰性气体的交换时由于压力的快速变化而造成管道的抖动,从而提升了该煤炭液化装置在使用时的稳定性。In the present invention, the setting of the pressure relief device can avoid the vibration of the pipeline caused by the rapid change of pressure during the exchange of the inert gas between the pulverized coal storage tank and the gas storage pipe, thereby improving the use of the coal liquefaction device. time stability.
作为优选,破碎腔的侧壁上设有若干个沿破碎腔高度方向设置的条形凹槽,破碎腔的侧壁上设有若干沿破碎腔高度方向设置的环形槽,支撑板上设有与条形凹槽以及环形槽相配合的凸块。Preferably, the side wall of the crushing cavity is provided with a number of strip-shaped grooves arranged along the height direction of the crushing cavity, the side wall of the crushing cavity is provided with a number of annular grooves arranged along the height direction of the crushing cavity, and the support plate is provided with The strip grooves and the annular grooves are matched with the protrusions.
本发明中,通过条形凹槽、环形槽以及凸块的设置,能够在进支撑板的安装时,将支撑板上的凸块放置在条形凹槽中,之后移动支撑板,当支撑板移动至环形槽处时,旋转支撑板,使得凸块旋入环形槽中,从而较为方便的实现了对于支撑板的安装。In the present invention, through the arrangement of the strip-shaped groove, the annular groove and the convex block, the convex block on the supporting plate can be placed in the strip-shaped groove during the installation of the supporting plate, and then the supporting plate can be moved. When moving to the annular groove, the support plate is rotated, so that the protrusions are screwed into the annular groove, so that the installation of the support plate is more convenient.
作为优选,转轴的侧壁上设有若干个沿其高度方向设置的转动板卡槽,转动板上中心处设有与转轴间隙配合的转动板通孔,转动板通孔的内壁上设有与转动板卡槽相配合的卡块;破碎釜的侧壁上设有穿过环形槽的限位孔,凸块上设有与限位孔相配合的凸块通孔,限位孔中设有穿过凸块通孔的限位杆。Preferably, the side wall of the rotating shaft is provided with a number of rotating plate clamping slots arranged along the height direction, the center of the rotating plate is provided with a rotating plate through hole that fits with the rotating shaft, and the inner wall of the rotating plate through hole is provided with The clamping block matched with the clamping groove of the rotating plate; the side wall of the crushing kettle is provided with a limit hole passing through the annular groove, the convex block is provided with a convex block through hole matched with the limit hole, and the limit hole is provided with a limit hole. Limit levers that pass through the through holes of the bumps.
本发明中,通过限位孔、凸块通孔以及限位杆的设置,能够通过限位杆与凸块通孔的配合对支撑板进行限位,避免了支撑板在使用时发生转动,从而提升了该煤炭液化装置在使用时的稳定性。In the present invention, through the arrangement of the limit hole, the through hole of the bump, and the limit rod, the support plate can be limited by the cooperation of the limit rod and the through hole of the bump, so as to avoid the rotation of the support plate during use, thereby preventing the support plate from rotating during use. The stability of the coal liquefaction device in use is improved.
作为优选,破碎釜的上端部设有用于对破碎腔进行密封的破碎釜盖板,破碎釜盖板上设有用于驱动转轴的电机;破碎釜盖板设有若干个均匀的进料口。Preferably, the upper end of the crushing kettle is provided with a crushing kettle cover for sealing the crushing cavity, the crushing kettle cover is provided with a motor for driving the rotating shaft; the crushing kettle cover is provided with several uniform feeding ports.
本发明中,通过进料口以及破碎釜盖板的设置,能够使得在进行煤炭的破碎时,可以通过进料口连续地向破碎腔中添加煤炭,从而使得破碎釜可以连续的进行对于煤炭的破碎。In the present invention, through the setting of the feeding port and the crushing kettle cover, when the coal is crushed, coal can be continuously added to the crushing cavity through the feeding port, so that the crushing kettle can continuously carry out the coal crushing process. broken.
本发明还提供了基于上述任一煤炭液化装置的液化工艺,其包括以下步骤:The present invention also provides a liquefaction process based on any of the above-mentioned coal liquefaction devices, which comprises the following steps:
步骤一、打开其中一个粉煤储存罐上破碎釜的排料口,使得破碎釜中的粉煤通过进料管道进入与其相连接的粉煤储存罐中;Step 1, open the discharge port of the crushing kettle on one of the pulverized coal storage tanks, so that the pulverized coal in the crushing kettle enters the pulverized coal storage tank connected with it through the feeding pipeline;
步骤二、当粉煤储存罐中的粉煤堆积到一定量后,接通泵送机构的电源将气体储存罐中的惰性气体充入粉煤储存罐中,当粉煤储存罐中的压力与气化炉的压力相同时,打开第一阀门,使得粉煤储存罐中的粉煤落入气化炉中并在气化炉中液化;Step 2: When the pulverized coal in the pulverized coal storage tank is accumulated to a certain amount, the power supply of the pumping mechanism is turned on to fill the inert gas in the gas storage tank into the pulverized coal storage tank. When the pressure in the pulverized coal storage tank is equal to When the pressure of the gasifier is the same, the first valve is opened, so that the pulverized coal in the pulverized coal storage tank falls into the gasifier and liquefies in the gasifier;
步骤三、在将粉煤储存罐中的粉煤输送至气化炉时,将之前为添加粉煤的粉煤储存罐中上破碎釜的进料口打开,使得破碎釜中的粉煤进入粉煤储存罐中,在粉煤储存罐中的粉煤完全排入气化炉时,另一个粉煤储存罐中的粉煤添加完成,此时打开泵送机构上的相关阀门使得气体储存罐中的压力与其相邻的两个粉煤储存罐中的压力相等;Step 3: When the pulverized coal in the pulverized coal storage tank is transported to the gasifier, open the feeding port of the upper crushing kettle in the pulverized coal storage tank previously added with pulverized coal, so that the pulverized coal in the crushing kettle enters the pulverized coal. In the coal storage tank, when the pulverized coal in the pulverized coal storage tank is completely discharged into the gasifier, the addition of the pulverized coal in the other pulverized coal storage tank is completed. The pressure is equal to the pressure in the two adjacent pf storage tanks;
步骤四、调节泵送机构上阀门的关闭,之后通过泵送机构的作用使得排空粉煤的粉煤储存罐的中压力降至大气压,使得填充完成粉煤的粉煤储存罐的压力与气化炉相等;Step 4: Adjust the closing of the valve on the pumping mechanism, and then reduce the medium pressure of the pulverized coal storage tank for emptying pulverized coal to atmospheric pressure through the action of the pumping mechanism, so that the pressure of the pulverized coal storage tank filled with pulverized coal is the same as the gas pressure. The furnace is equal;
步骤五、依次重复进行步骤一至步骤四的操作。Step 5: Repeat the operations from Step 1 to Step 4 in sequence.
附图说明Description of drawings
图1为实施例1中的煤炭液化装置的结构示意图。FIG. 1 is a schematic structural diagram of the coal liquefaction device in Example 1. FIG.
图2为实施例1中A部分的放大图。FIG. 2 is an enlarged view of part A in Example 1. FIG.
图3为图1中过滤装置的剖视图。FIG. 3 is a cross-sectional view of the filter device of FIG. 1 .
图4为图1中泄压装置的结构示意图。FIG. 4 is a schematic structural diagram of the pressure relief device in FIG. 1 .
图5为图4中泄压装置的剖视图。FIG. 5 is a cross-sectional view of the pressure relief device of FIG. 4 .
图6为图1中破碎釜的剖视图。FIG. 6 is a cross-sectional view of the crushing kettle in FIG. 1 .
图7为图6中支撑板的结构示意图。FIG. 7 is a schematic structural diagram of the support plate in FIG. 6 .
图8为图6中破碎腔的结构示意图。FIG. 8 is a schematic structural diagram of the crushing chamber in FIG. 6 .
图9为图6中转轴的结构示意图。FIG. 9 is a schematic structural diagram of the rotating shaft in FIG. 6 .
图10为图6中转动板的结构示意图。FIG. 10 is a schematic structural diagram of the rotating plate in FIG. 6 .
附图中各数字标号所指代的部位名称如下:The names of the parts referred to by the numerals in the accompanying drawings are as follows:
110、气体储存罐;111、第二气泵;120、粉煤储存罐;121、破碎釜;122、进料管道;130、第一连接管;140、气化炉;150、第二连接管;151、第一阀门;160、U型连接管;170、滤网安装座;180、第四连接管;181、第六阀门;190、泄压管;210、第三连接管;220、第一气泵;230、第二阀门;240、第三阀门;250、第四阀门;260、第五阀门;310、滤网安装腔;320、卡槽;330、第一滤网;340、滤网安装腔盖板;350、滤网安装台阶;360、第二滤网;370、粉煤储存腔;410、内管;420、连接座;421、连接座通孔;510、泄压腔;520、第一环形安装板;530、第二环形安装板;540、导气孔;550、滑动柱;551、盲孔;560、弹簧;570、挡板;571、挡板通孔;610、破碎腔;620、支撑板;630、转轴;640、转动板;650、破碎釜盖板;651、进料口;660、电机;710、过料通孔;720、凸块;721、凸块通孔;810、条形凹槽;820、环形槽;830、限位孔;840、限位杆;910、转动板卡槽;1010、转动板通孔;1020、卡块。110, gas storage tank; 111, second gas pump; 120, pulverized coal storage tank; 121, crushing kettle; 122, feed pipeline; 130, first connecting pipe; 140, gasifier; 150, second connecting pipe; 151, the first valve; 160, the U-shaped connecting pipe; 170, the filter screen mounting seat; 180, the fourth connecting pipe; 181, the sixth valve; 190, the pressure relief pipe; 210, the third connecting pipe; 220, the first Air pump; 230, second valve; 240, third valve; 250, fourth valve; 260, fifth valve; 310, filter installation cavity; 320, card slot; 330, first filter; 340, filter installation Cavity cover; 350, filter screen installation step; 360, second filter screen; 370, pulverized coal storage cavity; 410, inner pipe; 420, connecting seat; 421, connecting seat through hole; 510, pressure relief chamber; 520, 530, second annular mounting plate; 540, air guide hole; 550, sliding column; 551, blind hole; 560, spring; 570, baffle; 571, baffle through hole; 610, crushing cavity; 620, supporting plate; 630, rotating shaft; 640, rotating plate; 650, crushing kettle cover plate; 651, feeding port; 660, motor; 710, material passing hole; 720, bump; 721, bump through hole; 810, strip groove; 820, annular groove; 830, limit hole; 840, limit rod; 910, rotating plate slot; 1010, rotating plate through hole;
具体实施方式Detailed ways
为进一步了解本发明的内容,结合附图和实施例对本发明作详细描述。应当理解的是,实施例仅仅是对本发明进行解释而并非限定。In order to further understand the content of the present invention, the present invention will be described in detail with reference to the accompanying drawings and embodiments. It should be understood that the embodiments are only for explaining the present invention and not for limiting.
实施例1Example 1
如图1-10所示,本实施例提供了一种煤炭液化装置,其包括用于储存惰性气体用的气体储存罐110,气体储存罐110的两端均设有粉煤储存罐120,粉煤储存罐120上端连接有破碎机构,破碎机构包括破碎釜121,破碎釜121与粉煤储存罐120之间连接有进料管道122,破碎釜121中设有破碎腔610,破碎腔610中设有若干个沿破碎腔610高度方向间隔设置的支撑板620,破碎腔610的中心处设有可转动的转轴630,转轴630上设有若干个用于与支撑板620进行配合的转动板640,支撑板620与转动板640上均设有用于供粉煤穿过的过料通孔710;粉煤储存罐120与气体储存罐110之间设有用于连接气体储存罐110与粉煤储存罐120的第一连接管130,第一连接管130上设有用于输送气体储存罐110与粉煤储存罐120中气体的泵送机构;气体储存罐110的下方设有气化炉140,粉煤储存罐120与气化炉140之间设有用于连接粉煤储存罐120与气化炉140的第二连接管150,第二连接管150上设有第一阀门151。As shown in FIGS. 1-10 , this embodiment provides a coal liquefaction device, which includes a
通过本实施例中的气体储存罐110以及两端的粉煤储存罐120的设置,能够使得在添加粉煤时,工作人员可通过控制泵送机构使得两个粉煤储存罐120处于不同的工作状态,即在一个粉煤储存罐120处于向气化炉中添加粉煤的状态时,另一个粉煤储存罐120处于填充粉煤的状态;从而使得该煤炭液化装置可以连续的向气化炉140中添加粉煤,从而较佳的提升了煤炭液化的效率。同时,当粉煤储存罐120中的粉煤填充完成后,工作人员可以通过泵送机构将粉煤储存罐120中的惰性气体泵送至气体储存罐110中,避免了向空气中排放惰性气体,从而既节省了生产成本,又避免了对环境造成污染。破碎机构的设置,使得破碎釜121可以连续进行粉煤的生产,也使得破碎机构生产的粉煤可以较为方便的输送至粉煤储存罐120中,从而较佳的提升了该煤炭液化装置的生产效率。Through the arrangement of the
本实施例中,泵送机构包括设置于第一连接管130上且两端部与第一连接管130相连接的U型连接管160,第一连接管130上位于U型连接管160与第一连接管130的连接处之间设有与U型连接管160相连接的第三连接管210,第三连接管210上设有第一气泵220;U型连接管160上位于U型连接管160与第三连接管210的连接处的两端分别设有第二阀门230以及第三阀门240,第二阀门230设置在靠近粉煤储存罐120处,第三阀门240设置在靠近气体储存罐110处;第一连接管130上设有位于第三连接管210与第一连接管130的连接处两端的第四阀门250以及第五阀门260,第四阀门250设置在第三连接管210与第一连接管130的连接处与U型连接管160与第一连接管130的连接处之间且靠近粉煤储存罐120端;第五阀门260设置在第三连接管210与第一连接管130连接处与U型连接管160与第一连接管130的连接处之间且靠近气体储存罐110处。In this embodiment, the pumping mechanism includes a U-shaped connecting
通过本实施例中的泵送机构结构的设置,能够在进行对于粉煤储存罐120加压时,先打开第四阀门250以及第五阀门260,使得第二阀门230以及第三阀门240处于关闭状态,气体储存罐110中的惰性气体将会向着粉煤储存罐120中流动,当气体储存罐110中的压力与粉煤储存罐120中的压力相等时,打开第三阀门240,关闭第四阀门250,接通第一气泵220的电源,继续将气体储存罐110中的惰性气体充入粉煤储存罐120中直至粉煤储存罐120中的压力与气化炉140中的压力相同;当完成粉煤储存罐120中粉煤的输送后,打开第二阀门230以第三阀门240,使得第四阀门250以及第五阀门260处于关闭状态,此时粉煤储存罐120中的惰性气体将会流动至气体储存罐110中,当粉煤储存罐120中的压力与气体储存罐110中的压力相同时,打开第四阀门250,关闭第五阀门260,接通第一气泵220的电源,使得粉煤储存罐120中的惰性气体可以被抽送至气体储存罐110中,直至粉煤储存罐120中的气压与大气压相同。通过泵送机构的设置,可以使得在气体储存罐110以及粉煤储存罐120进行冲放气压时,可以先通过管道的连通使得粉煤储存罐120与气体储存罐110中的气压相同,避免了直接利用第一气泵220进行粉煤储存罐120以及气体储存罐110气压的交换,从而避免了由于气体压力过高而导致第一气泵220的损坏,从而较佳的提升了该煤炭液化装置的稳定性。Through the configuration of the pumping mechanism in this embodiment, when pressurizing the pulverized
本实施例中,第一连接管130上设有位于泵送机构与粉煤储存罐120之间的过滤装置,过滤装置包括滤网安装座170,滤网安装座170中设有滤网安装腔310,滤网安装腔310中设有若干组卡槽320,卡槽320中卡接有第一滤网330,滤网安装座170的上端部设有用于对滤网安装腔310进行密封的滤网安装腔盖板340。In this embodiment, the first connecting
通过本实施例中的过滤机构的设置,能够对第一连接管130中的粉煤进行过滤,避免了粉煤进入第一气泵220中造成第一气泵220的损坏,从而较佳的提升了本实施例中煤炭液化装置的稳定性。Through the arrangement of the filtering mechanism in this embodiment, the pulverized coal in the first connecting
本实施例中,滤网安装腔310底面向下凹陷形成滤网安装台阶350,滤网安装台阶350上设有垂直于第一滤网330设置且用于对第一滤网330进行支撑的第二滤网360,第二滤网360的底端设有整体呈倒圆台型的粉煤储存腔370。In this embodiment, the bottom surface of the filter
通过本实施例中的第二滤网360以及粉煤储存腔370的设置,能够使得滤网安装腔310中的粉煤可以落至粉煤储存腔370中,从而方便了对于过滤装置中的粉煤进行收集。Through the arrangement of the
本实施例中,粉煤储存罐120与滤网安装座170之间设有用于连接粉煤储存罐120与滤网安装座170的第四连接管180,第四连接管180的端部与粉煤储存腔370相连接,第四连接管180上设有第六阀门181。In this embodiment, a fourth connecting
通过本实施例中的第四连接管180以及第六阀门181的设置,能够使得在向粉煤储存罐120中加压时,可以打开第六阀门181,使得粉煤储存腔370中的粉煤可以通过第四连接管180输送至粉煤储存罐120中,从而方便了对于粉煤储存腔370中粉煤的回收利用。Through the arrangement of the fourth connecting
本实施例中,第一连接管130上位于过滤装置以及U型连接管160之间设有泄压装置,泄压装置包括呈管状的泄压管190,泄压管190中设有内管410,泄压管190内壁与内管410外壁形成泄压腔510,内管410中心处的外侧壁上设有与泄压管190内部侧壁固定连接的第一环形安装板520,第一环形安装板520将泄压腔510分隔成为两个相对独立的空间;内管410的中心处设有第二环形安装板530,内管410的外侧壁上靠近第二环形安装板530端设有若干个均匀且沿内管410轴线方向间隔分布的导气孔540,内管410中可滑动的设有滑动柱550,滑动柱550上靠近第二环形安装板530的端部设有盲孔551,内管410中设有弹簧560,弹簧560的一端抵靠在盲孔551中,弹簧560的另一端抵靠在第二环形安装板530上;内管410的两端开口处设有用于对滑动柱550进行阻挡的挡板570,挡板570的中心处设有挡板通孔571。In this embodiment, a pressure relief device is provided on the first connecting
通过本实施例中的泄压装置的设置,能够在进行粉煤储存罐120以及气体储存罐110的气体交换时,惰性气体从内管410与泄压管190之间一侧的空腔进入,通过第二环形安装板530一侧导气孔540流入内管410中,之后通过内管410的第二环形安装板530经由第二环形安装板530另一侧的导气孔540流出。当滑动柱550受到压力时,滑动柱550将向着第二环形安装板530的一侧移动,对导气孔540进行阻挡,使得气体的流量的降低,从而避免了在进行粉煤储存罐120以及气体储存管110间惰性气体的交换时由于压力的快速变化而造成管道的抖动,从而提升了该煤炭液化装置在使用时的稳定性。Through the setting of the pressure relief device in this embodiment, when the gas exchange between the pulverized
本实施例中,挡板570与内管410的内壁螺纹连接。In this embodiment, the
通过本实施例中的挡板570与内管410的螺纹连接,既方便了对于挡板570的安装,又方便了对于滑动柱550以及弹簧560的更换,从而方便了日常的维护。The threaded connection between the
本实施例中,泄压管190的两端部沿其周向外扩形成连接座420,连接座420上设有若干个均匀分布的连接座通孔421。In this embodiment, both ends of the
通过本实施例中的连接座通孔421的设置,能够使得在进行对于该泄压装置的安装时,可以通过穿过连接座通孔421的螺栓将泄压装置安装在第一连接管130上,从而较为方便的实现了对于泄压装置的安装。Through the arrangement of the connecting seat through
本实施例中,气体储存罐110上连接有用于将惰性气体泵入气体储存罐的第二气泵111。In this embodiment, the
通过本实施例中的第二气泵111的设置,能够在少量惰性气体通过粉煤储存罐120以及第二连接管150进入气化炉140并通过气化炉140排出后,可以通过第二气泵111向气体储存罐111中泵入惰性气体,从而提升了煤炭液化装置在使用时的稳定性。With the arrangement of the second air pump 111 in this embodiment, after a small amount of inert gas enters the
本实施例中,破碎腔610的侧壁上设有若干个沿破碎腔610高度方向设置的条形凹槽810,破碎腔610的侧壁上设有若干沿破碎腔610高度方向设置的环形槽820,支撑板620上设有与条形凹槽810以及环形槽820相配合的凸块720。In this embodiment, the side wall of the crushing
通过本实施例中的条形凹槽810、环形槽820以及凸块720的设置,能够在进支撑板620的安装时,将支撑板620上的凸块720放置在条形凹槽810中,之后移动支撑板620,当支撑板620移动至环形槽820处时,旋转支撑板620,使得凸块720旋入环形槽820中,从而较为方便的实现了对于支撑板620的安装。Through the arrangement of the
本实施例中,转轴630的侧壁上设有若干个沿其高度方向设置的转动板卡槽910,转动板640上中心处设有与转轴630间隙配合的转动板通孔1010,转动板通孔1010的内壁上设有与转动板卡槽910相配合的卡块1020;破碎釜121的侧壁上设有穿过环形槽820的限位孔830,凸块720上设有与限位孔830相配合的凸块通孔721,限位孔830中设有穿过凸块通孔721的限位杆840。In this embodiment, the side wall of the
通过本实施例中的限位孔830、凸块通孔721以及限位杆840的设置,能够通过限位杆840与凸块通孔721的配合对支撑板620进行限位,避免了支撑板620在使用时发生转动,从而提升了该煤炭液化装置在使用时的稳定性。Through the arrangement of the
本实施例中,破碎釜121的上端部设有用于对破碎腔610进行密封的破碎釜盖板650,破碎釜盖板650上设有用于驱动转轴630的电机660;破碎釜盖板650设有若干个均匀的进料口651。In this embodiment, the crushing
通过本实施例中的进料口651以及破碎釜盖板650的设置,能够使得在进行煤炭的破碎时,可以通过进料口651连续地向破碎腔610中添加煤炭,从而使得破碎釜121可以连续的进行对于煤炭的破碎。Through the setting of the feeding
本实施例还提供基于上述煤炭液化装置的液化工艺,其包括以下步骤:This embodiment also provides a liquefaction process based on the above-mentioned coal liquefaction device, which includes the following steps:
步骤一、打开其中一个粉煤储存罐120上破碎釜121的排料口,使得破碎釜121中的粉煤通过进料管道122进入与其相连接的粉煤储存罐120中;Step 1, open the discharge port of the crushing
步骤二、当粉煤储存罐120中的粉煤堆积到一定量后,接通泵送机构的电源将气体储存罐110中的惰性气体充入粉煤储存罐120中,当粉煤储存罐120中的压力与气化炉140的压力相同时,打开第一阀门151,使得粉煤储存罐120中的粉煤落入气化炉140中并在气化炉140中液化;Step 2: When the pulverized coal in the pulverized
步骤三、在将粉煤储存罐120中的粉煤输送至气化炉140时,将之前为添加粉煤的粉煤储存罐120中上破碎釜121的进料口打开,使得破碎釜121中的粉煤进入粉煤储存罐120中,在粉煤储存罐120中的粉煤完全排入气化炉140时,另一个粉煤储存罐120中的粉煤添加完成,此时打开泵送机构上的相关阀门使得气体储存罐110中的压力与其相邻的两个粉煤储存罐120中的压力相等;Step 3: When the pulverized coal in the pulverized
步骤四、调节泵送机构上阀门的关闭,之后通过泵送机构的作用使得排空粉煤的粉煤储存罐120的中压力降至大气压,使得填充完成粉煤的粉煤储存罐120的压力与气化炉140相等;Step 4: Adjust the closing of the valve on the pumping mechanism, and then reduce the pressure of the pulverized
步骤五、依次重复进行步骤一至步骤四的操作。Step 5: Repeat the operations from Step 1 to Step 4 in sequence.
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