CN107033973A - A kind of inside and outside hot integral biomass revolution pyrolytic gasification equipment and application - Google Patents
A kind of inside and outside hot integral biomass revolution pyrolytic gasification equipment and application Download PDFInfo
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- 238000002309 gasification Methods 0.000 title claims abstract description 61
- 239000002028 Biomass Substances 0.000 title claims abstract description 32
- 238000000197 pyrolysis Methods 0.000 claims abstract description 71
- 238000010438 heat treatment Methods 0.000 claims abstract description 38
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000000463 material Substances 0.000 claims abstract description 20
- 238000007789 sealing Methods 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 230000004913 activation Effects 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 42
- 239000007787 solid Substances 0.000 claims description 22
- 238000000926 separation method Methods 0.000 claims description 18
- 238000002485 combustion reaction Methods 0.000 claims description 16
- 239000003610 charcoal Substances 0.000 claims description 10
- 238000004321 preservation Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 5
- 239000000428 dust Substances 0.000 claims description 4
- 238000004064 recycling Methods 0.000 claims description 4
- 239000011810 insulating material Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000003345 natural gas Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 2
- 230000010354 integration Effects 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract 1
- 239000002023 wood Substances 0.000 description 6
- 241000251468 Actinopterygii Species 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 238000001754 furnace pyrolysis Methods 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Classifications
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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
- C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
- C10J3/60—Processes
-
- 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
- C10J3/72—Other features
-
- 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
- C10J2200/00—Details of gasification apparatus
- C10J2200/09—Mechanical details of gasifiers not otherwise provided for, e.g. sealing means
-
- 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
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明公开了一种内外热一体生物质回转热解气化设备及应用,该设备主要由进料装置、外热式热解装置、内热式气化装置、密封装置、出料装置、燃烧器等组成。进出料装置和密封装置保证了热解气化设备的密封性和热解气化反应的连续运行。采用高温燃气回用为外热热解提供热量,降低能耗。将水蒸气和空气混合气作为气化介质在内热式转炉内与物料发生气活化反应,生成燃气和活性炭。
The invention discloses a biomass rotary pyrolysis gasification equipment with internal and external heat integration and its application. The equipment mainly consists of a feeding device, an external heat type pyrolysis device, an internal heat type gasification device, a sealing device, a discharge device, and a burner and so on. The feeding and discharging device and the sealing device ensure the sealing of the pyrolysis and gasification equipment and the continuous operation of the pyrolysis and gasification reaction. High-temperature gas reuse is used to provide heat for external heat pyrolysis to reduce energy consumption. The mixed gas of water vapor and air is used as the gasification medium to undergo a gas activation reaction with the material in the internal heating converter to generate gas and activated carbon.
Description
技术领域technical field
本发明涉及回转热解气化设备和方法,尤其涉及一种内外热一体生物质回转热解气化设备及应用。The invention relates to a rotary pyrolysis gasification device and method, in particular to a biomass rotary pyrolysis gasification device with integrated internal and external heat and its application.
背景技术Background technique
生物质是一种清洁的可再生能源。生物质热解气化是生物质利用的重要途径。生物质热解是指生物质原料在隔绝空气或者添加少量空气条件下受热分解产生可凝和不可凝气体以及固体炭等不同形态的物质,热解得到的气体热值一般在12000kJ/Nm3以上;生物质气化是指生物质原料与气化剂,如水蒸气、氧气或者空气等,在一定的温度条件下,发生气固反应的过程。Biomass is a clean and renewable energy source. Biomass pyrolysis gasification is an important way of biomass utilization. Biomass pyrolysis refers to the thermal decomposition of biomass raw materials under the condition of isolation of air or adding a small amount of air to produce condensable and non-condensable gases and solid carbon and other substances in different forms. The calorific value of the gas obtained by pyrolysis is generally above 12000kJ/Nm 3 ; Biomass gasification refers to the process of gas-solid reaction between biomass raw materials and gasification agents, such as water vapor, oxygen or air, under certain temperature conditions.
国内生物质热解工业化应用中,基本都是热解气化的反应过程,以得到固体和气体产物为主要目标。目前应用比较多的热解气化设备有固定床气化炉、流化床气化炉和回转炉等。固定床与流化床炉热解气化主要以得到的燃气为主,得到的炭品质较低。回转炉热解主要以得到木炭产品为主,得到的燃气量较少。In the domestic industrial application of biomass pyrolysis, it is basically a reaction process of pyrolysis and gasification, with the main goal of obtaining solid and gas products. At present, the pyrolysis gasification equipment widely used includes fixed bed gasifier, fluidized bed gasifier and rotary furnace. Pyrolysis gasification in fixed bed and fluidized bed furnaces is mainly based on the gas obtained, and the charcoal quality obtained is low. Rotary furnace pyrolysis is mainly to obtain charcoal products, and the amount of gas obtained is small.
发明内容Contents of the invention
本发明的目的是提供一种生物质回转热解气化设备及应用,将固体生物质尤其是木块、木屑、果壳等颗粒状生物质原料连续、高效、高质的生产生物质燃气并联产具有吸附能力的生物质炭产品。The purpose of the present invention is to provide a biomass rotary pyrolysis gasification equipment and its application, which can continuously, efficiently and high-quality produce biomass gas from solid biomass, especially granular biomass raw materials such as wood blocks, wood chips, and fruit shells. Co-production of biochar products with adsorption capacity.
本发明采用以下技术方案:一种生物质回转热解气化设备,包括进料装置、热解装置、气化装置和出料装置,沿物料运行方向依次由进料装置、外热式热解装置、密封装置、内热式气化装置、气固分离装置组成;内热式气化装置还连接出料装置,气固分离装置连接气体回用装置,气体回用装置与外热式热解装置连接。The present invention adopts the following technical solutions: a biomass rotary pyrolysis gasification equipment, including a feed device, a pyrolysis device, a gasification device and a discharge device. device, sealing device, internal thermal gasification device, and gas-solid separation device; the internal thermal gasification device is also connected to the discharge device, the gas-solid separation device is connected to the gas recycling device, and the gas recycling device is connected to the external thermal pyrolysis device .
所述的进料装置和出料装置均为螺旋状导料管,沿正螺旋方向在装置外盘绕。The feeding device and the discharging device are both helical feeding tubes, which are coiled outside the device along the normal helical direction.
所述的外热式热解装置为外加热回转炉结构,回转炉炉壁外部套有保温炉壁,回转炉炉壁与保温炉壁之间的中空部分为燃烧室,The external heating type pyrolysis device is an external heating rotary furnace structure, the outer wall of the rotary furnace is covered with a heat preservation furnace wall, and the hollow part between the furnace wall of the rotary furnace and the heat preservation furnace wall is a combustion chamber.
所述的燃烧室底部设有热解气燃烧喷嘴和燃烧器,燃烧室保温炉壁设有螺旋型烟道。The bottom of the combustion chamber is provided with a pyrolysis gas combustion nozzle and a burner, and the wall of the combustion chamber is provided with a spiral flue.
所述的保温炉壁上设有螺旋型烟道,使燃烧室内的高温烟气沿回转炉炉壁做螺旋型运动,提高传热效率。The wall of the holding furnace is provided with a spiral flue, so that the high-temperature flue gas in the combustion chamber makes a spiral movement along the wall of the rotary furnace, thereby improving the heat transfer efficiency.
所述的燃烧器包括柴油燃烧器、液化气燃烧器、天然气燃烧器或颗粒燃烧器等,用于冷炉启动。The burners include diesel burners, liquefied gas burners, natural gas burners or particle burners, etc., which are used for cold furnace start-up.
所述的密封装置与转炉连接处采用鱼鳞密封结构,内部空腔通入水蒸气,底部有排水口。The connection between the sealing device and the converter adopts a fish scale sealing structure, the inner cavity is filled with water vapor, and there is a drain at the bottom.
所述的内热式气化装置为内热式回转炉结构,回转炉内壁衬有耐火保温材料,回转炉炉壁上设有水蒸气空气混合进气管。The internal heating type gasification device is an internal heating type rotary furnace structure, the inner wall of the rotary furnace is lined with refractory and heat-insulating materials, and a water vapor air mixing inlet pipe is arranged on the rotary furnace wall.
所述的水蒸气空气混合进气管设有定向开关阀和电磁流量阀,当进气管转至上方时定向开关阀自动关闭,当进气管转至下方时开关阀开启;通过电磁流量阀调节进气量大小。The water vapor air mixed intake pipe is provided with a directional on-off valve and an electromagnetic flow valve, the directional on-off valve is automatically closed when the intake pipe is turned to the top, and the on-off valve is opened when the intake pipe is turned to the bottom; the air intake is adjusted by the electromagnetic flow valve volume size.
所述的气固分离装置包括气固分离室、旋风分离器和关风机。The gas-solid separation device includes a gas-solid separation chamber, a cyclone separator and a shut-off fan.
所述的外热式热解装置的炉壁的外直径小于内热式气化装置内壁的直径,且外热式热解装置的筒体伸入内热式气化装置的筒体内100~500mm。The outer diameter of the furnace wall of the external heating type pyrolysis device is smaller than the inner wall diameter of the internal heating type gasification device, and the cylinder of the external heating type pyrolysis device extends into the cylinder of the internal heating type gasification device by 100-500 mm.
应用所述的生物质回转热解气化设备的方法,物料由进料装置进入,随着装置的转动前移进入外热式热解装置的热解室,在外热式热解装置内物料发烧热解反应产生热解气和炭,随着装置的转动炭向前移动再进入内热式气化装置内,在内热式气化装置内与进入的水蒸气和空气混合气发生气化活化反应,生产燃气和活性炭,生成的活性炭由出料装置送出,燃气则进入气固分离装置分离除尘后,部分燃气返回外热式热解装置作为外加热能源使用,剩余部分送入用气系统。Applying the method of biomass rotary pyrolysis gasification equipment, the material enters from the feeding device, and moves forward with the rotation of the device into the pyrolysis chamber of the external thermal pyrolysis device, and the material is heated in the external thermal pyrolysis device The pyrolysis reaction produces pyrolysis gas and charcoal. With the rotation of the device, the charcoal moves forward and then enters the internal heat gasification device, and the gasification activation reaction occurs with the incoming water vapor and air mixture in the internal heat gasification device. To produce gas and activated carbon, the generated activated carbon is sent out from the discharge device, and the gas enters the gas-solid separation device for separation and dust removal, part of the gas returns to the external thermal pyrolysis device for use as external heating energy, and the remaining part is sent to the gas consumption system.
有益效果:Beneficial effect:
1、本发明中,通过螺旋状导料管进行物料输送,利用物料自身密封,相对于传统的螺旋输送器具有结构简单,密封性好,无动力消耗,造价低廉等优点。1. In the present invention, the material is transported through the spiral material guide tube and sealed by the material itself. Compared with the traditional screw conveyor, it has the advantages of simple structure, good sealing performance, no power consumption, and low cost.
2、本发明的燃烧室设有螺旋型烟道,可以提高传热效率,降低排烟温度。2. The combustion chamber of the present invention is provided with a spiral flue, which can improve heat transfer efficiency and reduce exhaust gas temperature.
3、本发明的密封结构与转筒连接处采用鱼鳞式密封,密封结构内通入水蒸气,使密封器内始终处于正压状态,阻止空气进入转炉内部。采用水蒸气正压密封结构避免了的现有机械密封结构复杂、造价高且密封效果不好的问题。3. The connection between the sealing structure and the rotating drum of the present invention adopts a fish scale seal, and water vapor is introduced into the sealing structure, so that the inside of the sealer is always in a positive pressure state, preventing air from entering the inside of the converter. The adoption of the water vapor positive pressure sealing structure avoids the existing problems of complex structure, high cost and poor sealing effect of the existing mechanical seal.
4、本发明利用生物质炭化活化产生的可燃气燃烧提供能量,正常运行后,无需外部加热,相对于传统工艺节约了能源。4. The present invention uses the combustion of combustible gas produced by biomass carbonization and activation to provide energy. After normal operation, no external heating is required, which saves energy compared with traditional processes.
5、本发明的内外热一体热解回转炉,物料先经外加热发生热解反应,生成热解气和炭,再进入内热式气化装置,送入水蒸气与空气混合气体进行气化活化反应。与传统先炭化后活化的物理法活性炭生产工艺相比,本发明具有设备投资低,能源利用效率高,生产成本低的优点。5. In the pyrolysis rotary furnace with internal and external heat integration of the present invention, the material is first heated externally to undergo a pyrolysis reaction to generate pyrolysis gas and charcoal, and then enters the internal heat type gasification device, and is fed into a mixed gas of water vapor and air for gasification activation reaction. Compared with the traditional physical activated carbon production process of first carbonizing and then activating, the invention has the advantages of low equipment investment, high energy utilization efficiency and low production cost.
附图说明Description of drawings
图1是本发明装置的结构示意图。Fig. 1 is a structural schematic diagram of the device of the present invention.
其中,进料装置1、外热式热解装置2、保温炉壁3,密封装置4、内热式气化装置5、水蒸气空气混合进气管6、耐火保温材料7、出料装置8、气固分离室9、旋风分离器10、关风机11、螺旋风道12、热解气燃烧喷嘴13、燃烧器14。Among them, feeding device 1, external thermal pyrolysis device 2, heat preservation furnace wall 3, sealing device 4, internal thermal gasification device 5, water vapor and air mixing inlet pipe 6, refractory insulation material 7, discharge device 8, gas Solid separation chamber 9, cyclone separator 10, shut-off fan 11, spiral air duct 12, pyrolysis gas combustion nozzle 13, burner 14.
图2是本发明的进料装置结构示意图。Fig. 2 is a schematic structural view of the feeding device of the present invention.
图3是本发明密封装置结构示意图。Fig. 3 is a structural schematic diagram of the sealing device of the present invention.
其中,外热式回转炉鱼鳞密封15、密封仓体16、水蒸气进口17、内热式回转炉鱼鳞密封18、排水口19。Among them, external heating type rotary furnace fish scale seal 15, sealed bin body 16, water vapor inlet 17, internal heating type rotary furnace fish scale seal 18, and water outlet 19.
具体实施方式detailed description
以下结合附图对本发明进行详细说明。The present invention will be described in detail below in conjunction with the accompanying drawings.
一种生物质回转热解气化设备,主要由进料装置1、外热式热解装置2、内热式气化装置5、密封装置4、出料装置8、气固分离室9、燃烧器14等组成。进料装置连接外热式热解装置,外热式热解装置与内热式气化装置通过密封装置相连,出料装置、气固分离室与外热式热解装置连接,气固分离室将燃气中的固体分离,部分高温燃气送入燃烧器为外热式热解装置提供热量。A biomass rotary pyrolysis gasification equipment, mainly composed of a feed device 1, an external thermal pyrolysis device 2, an internal thermal gasification device 5, a sealing device 4, a discharge device 8, a gas-solid separation chamber 9, and a burner 14 and so on. The feeding device is connected to the external thermal pyrolysis device, the external thermal pyrolysis device is connected to the internal thermal gasification device through a sealing device, the discharge device, the gas-solid separation chamber are connected to the external thermal pyrolysis device, and the gas-solid separation chamber will The solids in the gas are separated, and part of the high-temperature gas is sent to the burner to provide heat for the external thermal pyrolysis device.
所述的进料装置为螺旋状导料管,沿正螺旋方向在炉壁外盘绕,随回转炉转动。物料随着转动在导料管内向前移动并进入炉内。The feeding device is a spiral feeding pipe, which is coiled outside the furnace wall along the positive spiral direction and rotates with the rotary furnace. With the rotation, the material moves forward in the material guide tube and enters the furnace.
所述的外热式热解装置为外加热回转炉,回转炉外部套有保温炉壁,回转炉炉壁与保温炉壁之间的中空部分为燃烧室,保温炉壁底部设有热解气燃烧喷嘴和燃烧器。The external heating type pyrolysis device is an external heating rotary furnace, the outer part of the rotary furnace is covered with a heat preservation furnace wall, the hollow part between the rotary furnace wall and the heat preservation furnace wall is a combustion chamber, and the bottom of the heat preservation furnace wall is provided with a Combustion nozzles and burners.
所述的保温炉壁上设有螺旋型风道,使燃烧器产生的高温烟气沿螺旋型风道在燃烧室内绕回转炉外壁呈螺旋型向前运动,提高传热效率。The heat preservation furnace wall is provided with a spiral air duct, so that the high-temperature flue gas generated by the burner moves forward in a spiral shape around the outer wall of the rotary furnace in the combustion chamber along the spiral air duct, thereby improving the heat transfer efficiency.
所述的燃烧器可以为柴油燃烧器、液化气燃烧器、天然气燃烧器或颗粒燃烧器等燃烧加热器,用于冷炉启动。The burner can be a combustion heater such as a diesel burner, a liquefied gas burner, a natural gas burner, or a pellet burner, and is used for starting a cold furnace.
所述的内热式气化装置为内热式回转炉,回转炉内壁衬有耐火保温材料,回转炉炉壁上设有水蒸气空气混合进气管。The internal heating type gasification device is an internal heating type rotary furnace, the inner wall of the rotary furnace is lined with refractory and heat-insulating materials, and the furnace wall of the rotary furnace is provided with a water vapor air mixing inlet pipe.
所述的水蒸气空气混合进气管设有定向开关阀和电磁流量阀,当进气管转至上方时定向开关阀自动关闭,当进气管转至下方时开关阀开启。通过电磁流量阀可以调节进气量大小。The water-steam-air mixed intake pipe is provided with a directional on-off valve and an electromagnetic flow valve. The directional on-off valve is automatically closed when the intake pipe is turned upward, and the on-off valve is opened when the intake pipe is turned downward. The intake air volume can be adjusted through the electromagnetic flow valve.
所述的外热式回转炉炉壁的外直径小于内热式回转炉保温层内壁的直径,且外热式回转炉筒体伸入内热式回转炉筒体。The outer diameter of the outer heating type rotary furnace wall is smaller than the inner wall diameter of the inner heating type rotary furnace insulation layer, and the outer heating type rotary furnace cylinder extends into the inner heating type rotary furnace cylinder.
所述的外热式热解装置与内热式气化装置通过密封装置隔绝空气,密封方式可采用迷宫密封、填料密封或端面密封等形式。The external heating type pyrolysis device and the internal heating type gasification device are isolated from the air through the sealing device, and the sealing method can be in the form of labyrinth seal, packing seal or end face seal.
所述的出料装置也为螺旋状导料管,沿正螺旋方向在炉壁外盘绕,随回转炉转动。物料在内热式回转炉末端进入出料导管,随着炉体的转动向前移动并送出导管。The discharge device is also a spiral material guide pipe, which is coiled outside the furnace wall along the positive spiral direction and rotates with the rotary furnace. The material enters the discharge conduit at the end of the internal heating rotary furnace, moves forward with the rotation of the furnace body and is sent out of the conduit.
如图1所示,物料首先送入进料仓,当进料螺旋盘管进料口转至下方时物料掉进进料盘管,随着螺旋盘管的转动物料向前移动并进入外热式回转炉热解室,在外热式热解装置内物料发生热解反应产生热解气和炭,随着转炉的转动炭向前移动再进入内热式回转炉气化室,在气化室内炉壁上分布有水蒸气与空气的混合进气口,水蒸气与空气按比例混合送入气化室与炭发生气化活化反应,生成燃气和活性炭,生成的活性炭在由气化室尽头的出料螺旋盘管送出回转炉,燃气由燃气出口进入气固分离室,燃气中夹带的固体小颗粒在气固分离室先沉降除尘再进入旋风分离器进一步除尘后,部分返回外热式回转炉热解室的燃烧室作为外加热能源,剩余部分送入用气系统。As shown in Figure 1, the material is first sent into the feeding bin, and when the feed inlet of the feeding spiral coil turns to the bottom, the material falls into the feeding coil, and with the rotation of the spiral coil, the material moves forward and enters the external heat Type rotary furnace pyrolysis chamber, in the external heat type pyrolysis device, the material undergoes pyrolysis reaction to produce pyrolysis gas and charcoal. With the rotation of the converter, the charcoal moves forward and then enters the internal heat type rotary furnace gasification chamber. The water vapor and air mixing inlets are distributed on the wall. The water vapor and air are mixed in proportion and sent into the gasification chamber to undergo gasification and activation reaction with carbon to generate gas and activated carbon. The generated activated carbon is discharged from the end of the gasification chamber. The material spiral coil is sent out of the rotary furnace, and the gas enters the gas-solid separation chamber from the gas outlet. The small solid particles entrained in the gas are first settled in the gas-solid separation chamber for dust removal, and then enter the cyclone separator for further dust removal, and part of them is returned to the external heating type rotary furnace for heating. The combustion chamber of the decomposing chamber is used as an external heating energy source, and the remaining part is sent to the gas system.
实施例:采用木片生产生物质燃气及炭吸附材料Embodiment: Using wood chips to produce biomass gas and carbon adsorption materials
采用本发明的内外热一体生物质回转热解气化设备,原料为木片,长度约20~40mm,水分在15~20%。首先开启颗粒燃烧器,将外热式回转炉温度升至500~700℃,将木片加入进料仓中,木片在外热式回转炉内完成热解反应并进入内热式气化装置,送入水蒸气与空气混合气,水蒸气与空气比例2:1,在内热式气化装置内炭发生气化活化反应,反应温度在1100~1200℃,生成燃气与活性炭,产生的燃气部分送入外热式热解装置的燃烧室作为外加热能源。生物质燃气热值8250kJ/m3,活性炭亚甲基蓝吸附值12ml/g,碘吸附值980mg/g。The biomass rotary pyrolysis and gasification equipment with internal and external heat integration of the present invention is adopted, the raw material is wood chips, the length is about 20-40mm, and the moisture content is 15-20%. First turn on the pellet burner, raise the temperature of the externally heated rotary furnace to 500-700°C, put the wood chips into the feed bin, the wood chips complete the pyrolysis reaction in the externally heated rotary furnace and enter the internally heated gasification device, and send them into the water The mixture of steam and air, the ratio of water vapor to air is 2:1, and the charcoal gasification and activation reaction occurs in the internal heating gasification device. The reaction temperature is 1100-1200 ℃ to generate gas and activated carbon, and part of the generated gas is sent to the external heat The combustion chamber of the type pyrolysis device is used as an external heating energy source. The calorific value of biomass gas is 8250kJ/m 3 , the adsorption value of activated carbon methylene blue is 12ml/g, and the adsorption value of iodine is 980mg/g.
上述实例仅供说明本发明之用,而非对本发明的限制,有关技术领域的普通技术人员,在不脱离本发明的主旨和范围的前提下,还可以做出各种变化和变形,因此所用等同的技术方案也应属于本发明的范畴,本发明的保护范围应该由各权利要求限定。The above examples are only for the purpose of illustrating the present invention, rather than limiting the present invention. Those of ordinary skill in the relevant technical field can also make various changes and deformations without departing from the gist and scope of the present invention. Equivalent technical solutions should also belong to the category of the present invention, and the protection scope of the present invention should be defined by each claim.
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