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CN2498158Y - Pyrolyzer for producing moderate gas from biological materials - Google Patents

Pyrolyzer for producing moderate gas from biological materials Download PDF

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Publication number
CN2498158Y
CN2498158Y CN01262443.8U CN01262443U CN2498158Y CN 2498158 Y CN2498158 Y CN 2498158Y CN 01262443 U CN01262443 U CN 01262443U CN 2498158 Y CN2498158 Y CN 2498158Y
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gas
heater
inner cylinder
furnace body
pyrolysis oven
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顾念祖
王景南
范宝根
张子馨
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Southeast University
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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Abstract

由生物质制取中热值煤气的热解炉是一种生产生物质煤气的设备,该热解炉的炉体中,内筒的外侧设有括板搅拌器,外筒的外侧是保温层,在炉体的上端设有加料斗,在加料斗与炉体之间设有锁气器,驱动装置与内筒相连,在炉体的下部设有炉箅和水封、出渣口、煤气出气口,燃烧器位于炉体的下部与内筒相接。燃烧器位于炉体的下部与内筒和外筒之间的空隙相连通,组成外热式的热解炉。将炉体横向倾斜放置,加料斗和锁气器位于炉体一端的上部,出渣口、煤气出口位于炉体另一端的下部,组成倾料式热解炉。

The pyrolysis furnace for producing medium calorific value gas from biomass is a kind of equipment for producing biomass gas. In the furnace body of the pyrolysis furnace, the outer side of the inner cylinder is equipped with a plate stirrer, and the outer side of the outer cylinder is an insulation layer. , There is a feeding hopper on the upper end of the furnace body, a gas locker is provided between the feeding hopper and the furnace body, the driving device is connected with the inner cylinder, and a grate, water seal, slag outlet, gas The gas outlet and the burner are located at the lower part of the furnace body and connected with the inner cylinder. The burner is located at the lower part of the furnace body and communicates with the gap between the inner cylinder and the outer cylinder to form an external heating type pyrolysis furnace. The furnace body is placed horizontally and obliquely, the feeding hopper and the gas locker are located at the upper part of one end of the furnace body, and the slag outlet and the gas outlet are located at the lower part of the other end of the furnace body, forming a charging-type pyrolysis furnace.

Description

由生物质制取中热值煤气的热解炉Pyrolysis furnace for producing medium calorific value gas from biomass

一、技术领域1. Technical field

本实用新型是一种制取中热值煤气的热解炉,属于生物质煤气生产设备的技术领域。The utility model relates to a pyrolysis furnace for preparing medium calorific value gas, which belongs to the technical field of biomass gas production equipment.

二、背景技术2. Background technology

生物质能(秸秆、城镇生活垃圾中的有机质、林木废弃物等)面广量大,是取之不尽,用之不竭的可再生能源,它含S、N等元素极少,燃用时放出的CO2通过光合作用又被植物吸收,总的来说是CO2净释放量为零,不会造成温室效应。随着石油等常规能源价格的不断上升,可再生能源在新的世纪中将占有日益突出的地位,得到世界上大多数国家的重视。生物质能现占世界总能耗的14%左右,并稳步增长。美国将在2001年,生物质能利用量超过核能,成为仅次于煤的第二大能源。到2050年,生物质能将占全球燃烧直接用量的40%,全球电力的20%。Biomass energy (straw, organic matter in urban domestic waste, forest waste, etc.) The released CO 2 is absorbed by plants through photosynthesis. Generally speaking, the net release of CO 2 is zero and will not cause the greenhouse effect. With the rising price of conventional energy such as oil, renewable energy will occupy an increasingly prominent position in the new century and will be valued by most countries in the world. Biomass energy now accounts for about 14% of the world's total energy consumption and is growing steadily. In 2001, the United States will use biomass energy to surpass nuclear energy and become the second largest energy source next to coal. By 2050, biomass energy will account for 40% of global direct consumption of combustion and 20% of global electricity.

由生物质热解制取中热值煤气的设备目前有流态化和循环流化床,该设备由于采用空气作为介质,空气中有79%的氮,所制得的煤气热值一般为5MJ/NM3。另一种是采用氧气气化,可以使热能值达到11-17MJ/NM3,但由于氧气的生产成本较高,因此总体算来不经济,成本较高,还有一种是间壁式生物热解炉,采用煤和秸秆两种物质。Currently, there are fluidized and circulating fluidized bed equipment for producing medium calorific value gas by pyrolysis of biomass. Since the equipment uses air as the medium and there are 79% nitrogen in the air, the calorific value of the gas produced is generally 5MJ. /NM 3 . The other is to use oxygen gasification, which can make the thermal energy value reach 11-17MJ/NM 3 , but due to the high production cost of oxygen, it is generally uneconomical and costly. There is also a partition type biopyrolysis Furnace, using coal and straw two materials.

三、发明内容3. Contents of the invention

本实用新型的发明目的是提供一种结构简单,煤气的生产成本低,能充分利用秸秆和生活垃圾的由生物质制取中热值煤气的热解炉。The purpose of the invention of the utility model is to provide a pyrolysis furnace for producing medium calorific value gas from biomass with simple structure, low gas production cost and full utilization of straw and domestic garbage.

本实用新型的由生物质制取中热值煤气的热解炉,由炉体和进料装置,出料装置所组成,该热解炉的炉体中,内筒的外侧设有括板搅拌器,外筒的外侧是保温层,在炉体的上端设有加料斗,在加料斗与炉体之间设有锁气器,驱动装置与内筒相连,在炉体的下部设有炉篦和水封、出渣口、煤气出气口,燃烧器位于炉体的下部与内筒相接。燃烧器位于炉体的下部与内筒和外筒之间的空隙相连通,组成外热式的热解炉。将炉体横向倾斜放置,加料斗和锁气器位于炉体一端的上部,出渣口、煤气出口位于炉体另一端的下部,组成倾料式热解炉。The pyrolysis furnace of the utility model for producing medium calorific value gas from biomass is composed of a furnace body, a feeding device, and a discharge device. The outside of the outer cylinder is an insulation layer, a hopper is provided at the upper end of the furnace body, an air lock is provided between the hopper and the furnace body, the driving device is connected with the inner cylinder, and a grate is provided at the lower part of the furnace body And water seal, slag outlet, gas outlet, the burner is located at the lower part of the furnace body and connected with the inner cylinder. The burner is located at the lower part of the furnace body and communicates with the gap between the inner cylinder and the outer cylinder to form an external heating type pyrolysis furnace. The furnace body is placed horizontally and obliquely, the feeding hopper and gas locker are located at the upper part of one end of the furnace body, and the slag outlet and gas outlet are located at the lower part of the other end of the furnace body, forming a tilting type pyrolysis furnace.

本实用新型的优点在于:The utility model has the advantages of:

热解炉整体的结构简单,气化的效率高,不仅能产生中热值煤气,而且可明显减少环境污染,利废为宝。The overall structure of the pyrolysis furnace is simple, and the efficiency of gasification is high. It can not only produce gas with medium calorific value, but also significantly reduce environmental pollution and turn waste into treasure.

目前全国有75万多个村,6亿多吨秸杆。随着人民生活水平的提高,我国秸杆资源大量浪费和农村商品能源紧张,以及带来大气和水污染等问题。若将1/3的秸秆用于产生中热值煤气,即可节约1亿t标准煤,减排CO2约1.4亿t,SO2 140万t,烟尘100万t。并可促使小城镇的建设遵循可持续发展的道路,具有显著的节能、环保和社会效益。At present, there are more than 750,000 villages and more than 600 million tons of straw in the country. With the improvement of people's living standards, my country's straw resources are wasted in large quantities and rural commodity energy shortages, as well as problems such as air and water pollution. If 1/3 of the straw is used to produce medium calorific value gas, 100 million tons of standard coal can be saved, CO 2 emissions can be reduced by about 140 million tons, SO 2 by 1.4 million tons, and soot by 1 million tons. And it can promote the construction of small towns to follow the road of sustainable development, which has remarkable energy saving, environmental protection and social benefits.

城镇生活垃圾的处理原则是无害化、减量化和资源化。目前世界上垃圾的处理方法有四种:焚烧发电、填埋、堆肥和热解。焚烧发电能实现上述的三化,其唯一的缺点是投资太高,平均每天处理1t垃圾,若采用进口设备为40~70万元,国产设备也需10~20万元;采用填埋法时,占地面积太多,1t垃圾占地2.5~3.2m2,且填埋后因厌氧产生的沼气会造成垃圾场的爆炸,造成很大的经济损失,全球每年因垃圾填埋爆炸造成的经济损失达12亿美元。我国已填埋垃圾60多亿t,占地5万多m2,许多城市已被垃圾填埋场所包围;堆肥占地也较多,且投资也较高,所生产的堆肥只能用于林地等旱作物,销路成问题;热解是一种处理垃圾的新方法,其特点是需要的投资少,可达到垃圾处理三化的目的,可设在任何地点,分选后,每天处理1t垃圾的初投资为3~4万元,运行成本与焚烧发电大致相同,但所产可燃气体(煤气)的成本仅为工业煤气的一半左右,是一种很有发展前景的垃圾处理方法,适合于资金短缺的中小城镇处理垃圾。The principles of urban domestic waste disposal are harmless, volume reduction and recycling. There are currently four ways to deal with waste in the world: incineration for power generation, landfill, composting and pyrolysis. Incineration power generation can achieve the above-mentioned three modernizations, but its only disadvantage is that the investment is too high. On average, 1 ton of garbage is processed every day. If imported equipment is used, it costs 400,000 to 700,000 yuan, and domestic equipment also needs 100,000 to 200,000 yuan; , covers too much area, 1 ton of garbage occupies an area of 2.5-3.2m 2 , and the methane generated by anaerobic gas after landfill will cause the explosion of the garbage dump, causing great economic losses. Economic losses amounted to $1.2 billion. China has landfilled more than 6 billion tons of garbage, covering an area of more than 50,000 m 2 , many cities have been surrounded by landfill sites; compost also occupies a lot of land, and the investment is also high, and the compost produced can only be used in forest land Such as dry crops, sales are a problem; pyrolysis is a new method of waste treatment, which is characterized by the need for less investment, can achieve the purpose of three waste treatment, can be located in any place, after sorting, 1t per day The initial investment of garbage is 30,000 to 40,000 yuan, and the operating cost is roughly the same as that of incineration power generation, but the cost of combustible gas (coal gas) produced is only about half of that of industrial gas. Dispose of garbage in small and medium-sized cities and towns that are short of funds.

四、附图说明4. Description of drawings

图1是本实用新型的总体结构示意图。其中有加料斗1、锁气器2、内筒3、刮板搅拌器4、燃烧器5、外筒6、传动机构7、出渣口8、煤气出口9、炉篦10、水封11、保温层12。Fig. 1 is the overall structural representation of the utility model. Among them, there are hopper 1, gas locker 2, inner cylinder 3, scraper agitator 4, burner 5, outer cylinder 6, transmission mechanism 7, slag outlet 8, gas outlet 9, grate 10, water seal 11, Insulation layer 12.

图2是本实用新型外热式的结构示意图。Fig. 2 is a structural schematic diagram of the external heating type of the utility model.

图3是本实用新型内热倾斜式的结构示意图。Fig. 3 is a schematic structural diagram of the internal heating inclined type of the utility model.

图4是外热倾斜式的结构示意图。Fig. 4 is a schematic structural diagram of an external heating inclined type.

五、具体实施方式5. Specific implementation

实施例1:直立外热式热解炉的实施方案:Embodiment 1: the embodiment of vertical external heating type pyrolysis furnace:

该热解炉体由旋转的内筒3和固定的高温烟气外筒6组成,内、外筒均由耐热的钢材制成,内筒3的上部设有加料斗1和锁气器2,内筒的下部设有出渣口8,煤气出口9,炉篦10、水封11,内筒由传动机构7带动旋转,在内筒3内设有括板4,它随内筒旋转,将物料搅动,并使物料紧靠高温烟气的内筒外壁,热量由外传给内筒里的物料。水封11和锁气器2的作用是防止外界的空气漏入,达到隔绝空气的热解条件,生物质物料由内筒的上部进入热解炉,经由预热到下部的高温热解,烟气与物料的流动方向为逆流。生物质在热解炉内产生的渣和煤气都是由上向下流动,煤气在出口前都要经过热解炉中的最高温度段,使煤气中的焦油产生二次裂解。The pyrolysis furnace body is composed of a rotating inner cylinder 3 and a fixed high-temperature flue gas outer cylinder 6. Both the inner and outer cylinders are made of heat-resistant steel. The upper part of the inner cylinder 3 is equipped with a feeding hopper 1 and an air locker 2. , the bottom of the inner cylinder is provided with a slag outlet 8, a gas outlet 9, a grate 10, a water seal 11, the inner cylinder is driven to rotate by the transmission mechanism 7, and the inner cylinder 3 is provided with a bracket 4, which rotates with the inner cylinder, Agitate the material and make the material close to the outer wall of the inner cylinder of the high-temperature flue gas, and the heat is transferred from the outside to the material in the inner cylinder. The function of the water seal 11 and the air lock 2 is to prevent the outside air from leaking in and achieve the pyrolysis conditions of air isolation. The biomass material enters the pyrolysis furnace from the upper part of the inner cylinder, and is preheated to the lower part for high-temperature pyrolysis, and the smoke The flow direction of gas and material is countercurrent. The slag and coal gas produced by biomass in the pyrolysis furnace flow from top to bottom, and the coal gas must pass through the highest temperature section in the pyrolysis furnace before being exported, so that the tar in the gas will undergo secondary cracking.

实施例2:直立内热式热解炉的实施方案:Embodiment 2: the embodiment of vertical internal heating type pyrolysis furnace:

该热解炉的炉体由固定的外筒6和内筒3,内外筒均由耐热钢材制成,外筒上端设有加料斗1和锁气器2,外筒的下端设有出渣口8、煤气出口9、炉篦10、水封11,内筒的外侧设有括板搅拌器4,内外筒之间的下部装有燃烧器5,高温烟气在内筒的圆形通道内从下到上流动,通过内筒外壁将热量传给外筒内的物料。水封11和锁气器2的作用是防止外界空气的漏入,达到隔绝空气的热解条件,生物质物料由内筒的上部进入热解炉,经由预热到下部的高温热解,烟气与物料的流动方向为逆流。生物质在热解炉内产生的渣和煤气都是由上向下流动,煤气在出口前都要经过热解炉中的最高温度段,使煤气中的焦油产生二次裂解。The furnace body of the pyrolysis furnace is composed of a fixed outer cylinder 6 and an inner cylinder 3, both of which are made of heat-resistant steel, the upper end of the outer cylinder is provided with a feeding hopper 1 and an air locker 2, and the lower end of the outer cylinder is provided with a slag outlet Port 8, gas outlet 9, grate 10, water seal 11, the outer side of the inner cylinder is equipped with a bracket stirrer 4, the lower part between the inner and outer cylinders is equipped with a burner 5, and the high-temperature flue gas is in the circular passage of the inner cylinder It flows from bottom to top, and transfers heat to the material in the outer cylinder through the outer wall of the inner cylinder. The function of the water seal 11 and the air locker 2 is to prevent the leakage of outside air and achieve the pyrolysis conditions of air isolation. The biomass material enters the pyrolysis furnace from the upper part of the inner cylinder, and is preheated to the lower part for high-temperature pyrolysis. The flow direction of gas and material is countercurrent. The slag and coal gas produced by biomass in the pyrolysis furnace flow from top to bottom, and the coal gas must pass through the highest temperature section in the pyrolysis furnace before being exported, so that the tar in the gas will undergo secondary cracking.

实施例3:倾斜式内热热解炉实施方案:Embodiment 3: Inclined internal thermal pyrolysis furnace implementation:

由传动机构7带动内筒3旋转,外筒包裹内筒,内外筒均由耐热钢材制成,外筒的一端为料斗1和锁气器2,另一端为出渣口8、煤气出口9,括板搅拌器4装在内筒3外侧,跟随内筒一起旋转,燃烧器5装在内筒中,靠近出渣口处,高温烟气在内筒中由出料口处向加料斗方向流动,烟气与物料流动方向为逆流。热量经由内筒壁传给内外筒间的物料。水封10和锁气器2的作用是防止外界空气的漏入,达到隔绝空气的热解条件。煤气在出口前都要经过热解炉中的最高温度段,使煤气中的焦油产生二次裂解。The transmission mechanism 7 drives the inner cylinder 3 to rotate, and the outer cylinder wraps the inner cylinder. Both the inner and outer cylinders are made of heat-resistant steel. One end of the outer cylinder is the hopper 1 and the gas locker 2, and the other end is the slag outlet 8 and the gas outlet 9. , the bracket stirrer 4 is installed outside the inner cylinder 3, and rotates with the inner cylinder, the burner 5 is installed in the inner cylinder, close to the slag outlet, and the high-temperature flue gas flows in the inner cylinder from the outlet to the direction of the hopper. The flow direction of flue gas and material is countercurrent. The heat is transferred to the material between the inner and outer cylinders through the inner cylinder wall. The effect of water seal 10 and air locker 2 is to prevent outside air from leaking in, reaching the pyrolysis condition of isolating air. Before the gas is exported, it must pass through the highest temperature section in the pyrolysis furnace, so that the tar in the gas will undergo secondary cracking.

实施例4:倾斜式外热热解炉实施方案:Embodiment 4: Inclined external thermal pyrolysis furnace implementation:

由传动机构7带动内筒上的括板搅拌器4,外筒包裹内筒,内外筒均由耐热钢板制成,内筒的一端为料斗1和锁气器2,另一端为出渣口8,煤气出口9,燃烧器5装在内外筒间,靠近出渣口一端,高温烟气在内外筒间由出料口处向加料斗方向流动,烟气与物料流动方向为逆流。热量径由内筒壁传给筒内的物料。水封10和锁气器2的作用是防止外界空气的漏入,达到隔绝空气的热解条件。煤气在出口前都要经过热解炉中的最高温度段,使煤气中的焦油达到二次裂解。The transmission mechanism 7 drives the plate agitator 4 on the inner cylinder, and the outer cylinder wraps the inner cylinder. Both the inner and outer cylinders are made of heat-resistant steel plates. One end of the inner cylinder is the hopper 1 and the air locker 2, and the other end is the slag outlet. 8. The gas outlet 9 and the burner 5 are installed between the inner and outer cylinders, close to the slag outlet. The high-temperature flue gas flows between the inner and outer cylinders from the outlet to the direction of the hopper, and the flow direction of the flue gas and the material is countercurrent. The heat is transferred from the inner cylinder wall to the material in the cylinder. The effect of water seal 10 and air locker 2 is to prevent outside air from leaking in, reaching the pyrolysis condition of isolating air. Before the gas is exported, it must pass through the highest temperature section in the pyrolysis furnace, so that the tar in the gas can achieve secondary cracking.

Claims (3)

  1. One kind produce by biomass in the pyrolysis oven of calorific value of gas, by body of heater, feeding unit and drawing mechanism are formed, it is characterized in that in the body of heater of this pyrolysis oven, the outside of inner core (3) is provided with rubbing board agitator (4), the outside of urceolus is thermal insulation layer (12), be provided with loading hopper (1) in the upper end of body of heater, between loading hopper (1) and body of heater, be provided with air locking device (2), drive unit (7) links to each other with inner core (3), be provided with fire grate (10) and water seal (11) in the bottom of body of heater, slag notch (8), coal gas air outlet (9), bottom and inner core (3) that burner (5) is positioned at body of heater join, and form the pyrolysis oven of internal heat type.
  2. 2. according to claim 1 produce by biomass in the pyrolysis oven of calorific value of gas, it is characterized in that burner (5) is positioned at the bottom of body of heater and is connected the pyrolysis oven of composition external-heat with space between inner core (3) and the urceolus (6).
  3. 3. the pyrolysis oven of producing middle calorific value of gas by biomass according to claim 1, it is characterized in that the body of heater transverse inclination is placed, loading hopper (1) and air locking device (2) are positioned at the top of body of heater one end, slag notch (8), gas exit (9) are positioned at the bottom of the body of heater the other end, form the material formula pyrolysis oven that inclines.
CN01262443.8U 2001-08-29 2001-08-29 Pyrolyzer for producing moderate gas from biological materials Expired - Fee Related CN2498158Y (en)

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* Cited by examiner, † Cited by third party
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CN101007955B (en) * 2006-01-26 2010-05-12 张兴权 Carbonized city garbage fuel block preparation method and its dedicated apparatus
CN101220282B (en) * 2007-12-04 2011-01-12 上海四方锅炉厂 Propulsion type feeding biomass gasification stoves thermal decomposition device
CN101984020A (en) * 2010-10-26 2011-03-09 西峡龙成特种材料有限公司 External heating coal decomposing equipment with fold pipes
CN101985562A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Horizontal coal separating equipment with multiple combustors
CN101985559A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Electrothermal coal decomposing equipment
CN101985565A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Coal separating equipment with multiple combustors and parent-son pipes
CN101985560A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Vertical coal decomposition equipment with transversely-inserted gas tubes
CN101985557A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Decomposition device of single coal-material burner
CN101985558A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Coal decomposing equipment
CN101985563A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Vertical decomposing device with horizontal intubation tube for coal materials
CN101985561A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Vertical umbrella supporting coal decomposing equipment
CN101985566A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Horizontal rotating device for coal material decomposition
CN102260536A (en) * 2011-06-24 2011-11-30 华中科技大学 Internal circulation external heating type gasification device
CN102329631A (en) * 2011-09-01 2012-01-25 南京大学 Revolving-scraper type biomass pyrolysis reactor
WO2012055122A1 (en) * 2010-10-26 2012-05-03 西峡龙成特种材料有限公司 Method for decomposing coal material with circulating heating gas and equipment thereof
CN103074111A (en) * 2013-01-28 2013-05-01 秦恒飞 Equipment and technology for producing synthesis gas through cooperating outer cylinder air gasification with inner cylinder steam gasification
CN103788973A (en) * 2014-02-26 2014-05-14 中国科学院地球化学研究所 Cracking box of continuous charcoal production equipment
EP2607453A4 (en) * 2010-08-19 2014-10-22 Xixia Dragon Into Special Mat Vertical pyrolysis equipment for coal substance
CN105546558A (en) * 2016-02-04 2016-05-04 赵海舜 Biomass combustion machine capable of discharging slag without furnace shutdown
CN105925285A (en) * 2016-06-16 2016-09-07 北京神雾环境能源科技集团股份有限公司 Quick powdered coal pyrolysis device
CN109647341A (en) * 2019-01-29 2019-04-19 北京云水浩瑞环境科技有限公司 The system and method for preparing adsorbent material using sludge

Cited By (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101007955B (en) * 2006-01-26 2010-05-12 张兴权 Carbonized city garbage fuel block preparation method and its dedicated apparatus
CN101220282B (en) * 2007-12-04 2011-01-12 上海四方锅炉厂 Propulsion type feeding biomass gasification stoves thermal decomposition device
WO2012022057A1 (en) * 2010-08-16 2012-02-23 西峡龙成特种材料有限公司 Electrical-heating coal material decomposition device
AU2010359252B2 (en) * 2010-08-16 2014-06-12 Xixia Dragon Into Special Material Co., Ltd Electrical-heating coal material decomposition device
CN101985559B (en) * 2010-08-19 2011-08-17 西峡龙成特种材料有限公司 Electrothermal coal decomposing equipment
US8945349B2 (en) 2010-08-19 2015-02-03 Xixia Dragon Into Special Material Co., Ltd. Electrical heating coal material decomposition apparatus
CN101985560A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Vertical coal decomposition equipment with transversely-inserted gas tubes
CN101985557A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Decomposition device of single coal-material burner
CN101985558A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Coal decomposing equipment
CN101985563A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Vertical decomposing device with horizontal intubation tube for coal materials
CN101985561A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Vertical umbrella supporting coal decomposing equipment
CN101985566A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Horizontal rotating device for coal material decomposition
CN101985566B (en) * 2010-08-19 2013-06-12 西峡龙成特种材料有限公司 Horizontal rotating device for coal material decomposition
CN101985557B (en) * 2010-08-19 2011-09-14 西峡龙成特种材料有限公司 Decomposition device of single coal-material burner
CN101985562B (en) * 2010-08-19 2011-09-14 西峡龙成特种材料有限公司 Horizontal coal separating equipment with multiple combustors
CN101985565A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Coal separating equipment with multiple combustors and parent-son pipes
CN101985558B (en) * 2010-08-19 2012-01-04 西峡龙成特种材料有限公司 Coal decomposing equipment
EP2607453A4 (en) * 2010-08-19 2014-10-22 Xixia Dragon Into Special Mat Vertical pyrolysis equipment for coal substance
WO2012022060A1 (en) * 2010-08-19 2012-02-23 西峡龙成特种材料有限公司 Horizontal coal decomposition device with multiple burners
CN101985559A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Electrothermal coal decomposing equipment
CN101985562A (en) * 2010-08-19 2011-03-16 西峡龙成特种材料有限公司 Horizontal coal separating equipment with multiple combustors
EA027620B1 (en) * 2010-08-19 2017-08-31 Сися Дрегон Инту Спешиал Матириал Ко., Лтд. Electrical-heating coal material decomposition device
CN101985561B (en) * 2010-08-19 2013-04-24 西峡龙成特种材料有限公司 Umbrella supporting vertical decomposing equipment for coal
CN101985560B (en) * 2010-08-19 2013-06-12 西峡龙成特种材料有限公司 Vertical coal decomposition equipment with transversely-inserted gas tubes
CN101985563B (en) * 2010-08-19 2013-06-12 西峡龙成特种材料有限公司 Vertical decomposing device with horizontal intubation tube for coal materials
CN101985565B (en) * 2010-08-19 2013-06-12 西峡龙成特种材料有限公司 Coal separating equipment with multiple combustors and parent-son pipes
WO2012055122A1 (en) * 2010-10-26 2012-05-03 西峡龙成特种材料有限公司 Method for decomposing coal material with circulating heating gas and equipment thereof
EA024446B1 (en) * 2010-10-26 2016-09-30 Сися Дрегон Инту Спешиал Матириал Ко., Лтд. Coal decomposition method and equipment in cycle heating gas style
CN101984020B (en) * 2010-10-26 2015-12-09 西峡龙成特种材料有限公司 Broken pipe external heating type coal substance decomposition equipment
CN101984020A (en) * 2010-10-26 2011-03-09 西峡龙成特种材料有限公司 External heating coal decomposing equipment with fold pipes
CN102260536B (en) * 2011-06-24 2013-03-20 华中科技大学 Internal circulation external heating type gasification device
CN102260536A (en) * 2011-06-24 2011-11-30 华中科技大学 Internal circulation external heating type gasification device
CN102329631B (en) * 2011-09-01 2013-09-25 南京大学 Revolving-scraper type biomass pyrolysis reactor
CN102329631A (en) * 2011-09-01 2012-01-25 南京大学 Revolving-scraper type biomass pyrolysis reactor
CN103074111B (en) * 2013-01-28 2014-01-29 秦恒飞 Equipment and process for syngas production from outer cylinder air gasification combined with inner cylinder water vapor gasification
CN103074111A (en) * 2013-01-28 2013-05-01 秦恒飞 Equipment and technology for producing synthesis gas through cooperating outer cylinder air gasification with inner cylinder steam gasification
CN103788973A (en) * 2014-02-26 2014-05-14 中国科学院地球化学研究所 Cracking box of continuous charcoal production equipment
CN105546558A (en) * 2016-02-04 2016-05-04 赵海舜 Biomass combustion machine capable of discharging slag without furnace shutdown
CN105925285A (en) * 2016-06-16 2016-09-07 北京神雾环境能源科技集团股份有限公司 Quick powdered coal pyrolysis device
CN109647341A (en) * 2019-01-29 2019-04-19 北京云水浩瑞环境科技有限公司 The system and method for preparing adsorbent material using sludge

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