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CN110511787A - A new double fluidized bed device for hydrogen production from organic solid waste - Google Patents

A new double fluidized bed device for hydrogen production from organic solid waste Download PDF

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Publication number
CN110511787A
CN110511787A CN201910895888.2A CN201910895888A CN110511787A CN 110511787 A CN110511787 A CN 110511787A CN 201910895888 A CN201910895888 A CN 201910895888A CN 110511787 A CN110511787 A CN 110511787A
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gasification chamber
solid waste
organic solid
combustion chamber
chamber
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CN201910895888.2A
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尚凯
张晖
苏霈
赵笑书
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Guizhou Siyu Huanneng Technology Co Ltd
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Guizhou Siyu Huanneng Technology Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/54Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
    • C10J3/56Apparatus; Plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/05Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste oils
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/15Details of feeding means
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/0946Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0973Water
    • C10J2300/0976Water as steam
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/16Integration of gasification processes with another plant or parts within the plant
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/16Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1625Integration of gasification processes with another plant or parts within the plant with solids treatment
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00Specific waste
    • F23G2209/10Liquid waste
    • F23G2209/102Waste oil

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

本发明公开了一种新型有机固体废弃物制氢双流化床装置,包括:进料机构、气化室、床料回收循环器及燃烧室;进料机构通过进料管连接气化室下部进料口,气化室上部连通床料回收循环器,床料回收循环器连通燃烧室上部,燃烧室下部通过联通管连通气化室下部。本发明提高制氢率,减少焦油产生量,提高热能利用率。

The invention discloses a novel double fluidized bed device for producing hydrogen from organic solid waste, comprising: a feeding mechanism, a gasification chamber, a bed material recovery circulator and a combustion chamber; the feeding mechanism is connected to the lower part of the gasification chamber through a feeding pipe The feed inlet and the upper part of the gasification chamber are connected to the bed material recovery circulator, the bed material recovery circulator is connected to the upper part of the combustion chamber, and the lower part of the combustion chamber is connected to the lower part of the gasification chamber through a communication pipe. The invention improves the hydrogen production rate, reduces the amount of tar produced, and improves the utilization rate of heat energy.

Description

一种新型有机固体废弃物制氢双流化床装置A new double fluidized bed device for hydrogen production from organic solid waste

技术领域technical field

本发明涉及有机固体废弃物资源化及无害化处理装置,特别是一种新型有机固体废弃物制氢装置。The invention relates to an organic solid waste recycling and harmless treatment device, in particular to a novel organic solid waste hydrogen production device.

背景技术Background technique

目前,针对有机固体废弃物制氢的装置主要是固定床气化、流化床气化,这些装置都有以下问题:1、气化气中氢含量低,一般仅为10%~20%,资源化利用的提纯难度大,经济性差;2、产生焦油量大,对后续处理设备堵塞;3、需要外部提供热源维持气化。At present, the devices for producing hydrogen from organic solid waste are mainly fixed bed gasification and fluidized bed gasification. These devices have the following problems: 1. The hydrogen content in the gasification gas is low, generally only 10% to 20%. Purification of resource utilization is difficult and economical; 2. A large amount of tar is produced, which blocks subsequent processing equipment; 3. External heat sources are required to maintain gasification.

发明内容Contents of the invention

本发明的目的在于提供一种新型有机固体废弃物制氢双流化床装置,提高制氢率,减少焦油产生量,提高热能利用率。The purpose of the present invention is to provide a novel double-fluidized bed device for hydrogen production from organic solid waste, which can increase the hydrogen production rate, reduce the amount of tar produced, and improve the utilization rate of heat energy.

为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:

一种新型有机固体废弃物制氢双流化床装置,其特征在于,包括:进料机构、气化室、床料回收循环器及燃烧室;进料机构通过进料管连接气化室下部进料口,气化室下部的还通过斜向下的联通管连通燃烧室下部;燃烧室上部通过床料回收循环器连接气化室上部;燃烧室底部连接鼓风机;气化室底部、联通管中部连接蒸汽管;床料回收循环器与气化室的连接处连接蒸汽管。A novel double fluidized bed device for hydrogen production from organic solid waste, characterized in that it includes: a feeding mechanism, a gasification chamber, a bed material recovery circulator and a combustion chamber; the feeding mechanism is connected to the lower part of the gasification chamber through a feeding pipe The feed port and the lower part of the gasification chamber are also connected to the lower part of the combustion chamber through an obliquely downward communication pipe; the upper part of the combustion chamber is connected to the upper part of the gasification chamber through a bed material recovery circulator; the bottom of the combustion chamber is connected to the blower; the bottom of the gasification chamber, the communication pipe The middle part is connected to the steam pipe; the connection between the bed material recovery circulator and the gasification chamber is connected to the steam pipe.

优选为,进料机构包括储料仓,储料仓连接密闭的进料仓A和进料仓B;进料仓A和进料仓B通过进料管连接气化室下部进料口。通过设置两个密闭的进料仓,实现进料切换,保证进料仓密闭性,避免气化室产生的气体从进料仓处泄露;同时也保证气化室进料的持续性,避免进料中断而影响整个设备的热循环。Preferably, the feeding mechanism includes a storage bin, and the storage bin is connected to the closed feeding bin A and the feeding bin B; the feeding bin A and the feeding bin B are connected to the lower feed port of the gasification chamber through a feeding pipe. By setting up two airtight feeding bins, the switching of feeding materials is realized, the airtightness of the feeding bins is ensured, and the gas generated in the gasification chamber is prevented from leaking from the feeding bins. Material interruption affects the thermal cycle of the entire equipment.

优选为,储料仓的卸料口、进料仓A和进料仓B的进料口及卸料口均设有电动阀,方便自动化控制及切换进料卸料。Preferably, the discharge port of the storage bin, the feed port and the discharge port of the feed bin A and the feed bin B are all equipped with electric valves, which is convenient for automatic control and switching of feeding and discharging.

优选为,气化室顶部出气口处设气体分析仪,在线监测出气情况。Preferably, a gas analyzer is installed at the gas outlet on the top of the gasification chamber to monitor the gas outlet on-line.

优选为,燃烧室顶部烟气口处设烟气监测器,在线监测烟气情况。Preferably, a flue gas monitor is installed at the flue gas port on the top of the combustion chamber to monitor the flue gas condition online.

优选为,所述气化室内部侧壁设多个三角形挡板,可以阻挡气化室内产生的部分焦油,且焦油顺着三角形挡板及侧壁冷凝。Preferably, a plurality of triangular baffles are arranged on the inner side wall of the gasification chamber, which can block part of the tar generated in the gasification chamber, and the tar condenses along the triangular baffles and side walls.

优选为,气化室、燃烧室中采用橄榄石作为床料。Preferably, olivine is used as the bed material in the gasification chamber and combustion chamber.

优选为,气化室、燃烧室均设有压力监测器和温度监测仪,可以在线监测气化室、燃烧室的压力及温度情况。Preferably, both the gasification chamber and the combustion chamber are equipped with pressure monitors and temperature monitors, which can monitor the pressure and temperature of the gasification chamber and combustion chamber on-line.

本发明可提高气化气中氢气的含量(达到40%以上),减少焦油产生量,同时整个设备仅启动时需要采用天然气作为热源,运行平衡后无需要增加任何热源。首先,有机固体废弃物通过进料机构定量进料至气化制氢室,在气化室中温度控制在750~800℃,填装橄榄树床料,有机废弃物在气化制氢室进行无氧气化,生成高含氢的混合气体,同时部分焦油通过气化室的挡板阻挡,部分焦油与燃烧室循环回来的高温床料接触后进行再分解,使得出口焦油的含量低。碳燃烧室温度控制再900~950℃,主要作用是对气化室产生的焦炭及阻挡的焦油进行焚烧,产生热量加热床料,通过床料循环维持气化室的温度,达到自持气化制氢的目的。The invention can increase the content of hydrogen in the gasification gas (up to 40%), reduce the amount of tar produced, and at the same time, the whole equipment only needs to use natural gas as a heat source when it is started, and no heat source needs to be added after the operation is balanced. First, the organic solid waste is quantitatively fed to the gasification hydrogen production chamber through the feeding mechanism. Oxygen-free gasification generates a mixed gas with high hydrogen content. At the same time, part of the tar is blocked by the baffle of the gasification chamber, and part of the tar is re-decomposed after contacting the high-temperature bed material recycled from the combustion chamber, so that the content of tar at the outlet is low. The temperature of the carbon combustion chamber is controlled at 900-950°C. The main function is to incinerate the coke and blocked tar produced in the gasification chamber, generate heat to heat the bed material, and maintain the temperature of the gasification chamber through the circulation of the bed material to achieve a self-sustaining gasification system. purpose of hydrogen.

与现有技术比较,本发明的具有如下优点:第一、整套双流化床通过床料的循环作用,形成很好的流化作用,针对低燃值的有机固体废弃物,能自持气化,热能效率高;第二、采用橄榄石作为床料,在400℃的饱和蒸汽参与下,产生高含氢混合气体,同时焦油量小;第三、气化室和燃烧室通过蒸汽隔绝,不会窜气,具有更高的气化效率和含氢量;第四、整套装置配置电磁阀、压力监测器、温度监测仪设备、气体分析仪、烟气监测器,通过配置DCS系统,可实现自动化控制及在线监测设备状况,保证设备的安全运行。Compared with the prior art, the present invention has the following advantages: First, the entire set of double fluidized beds can form a good fluidization effect through the circulation of the bed material, and can self-sustain gasification for organic solid wastes with low fuel value , high thermal energy efficiency; second, olivine is used as bed material, and with the participation of saturated steam at 400 ° C, a mixed gas with high hydrogen content is produced, and the amount of tar is small; third, the gasification chamber and the combustion chamber are separated by steam, without Blow-by gas, with higher gasification efficiency and hydrogen content; Fourth, the whole set of equipment is equipped with solenoid valves, pressure monitors, temperature monitors, gas analyzers, and flue gas monitors. By configuring the DCS system, it can realize Automatic control and online monitoring of equipment status to ensure safe operation of equipment.

附图说明Description of drawings

图1为本发明的结构示意图。Fig. 1 is a structural schematic diagram of the present invention.

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

请参阅图1,本发明实施例中,一种新型有机固体废弃物制氢双流化床装置,包括:进料机构、气化室8、床料回收循环器3及燃烧室10;进料机构包括储料仓1,储料仓1连接进料仓A5和进料仓B6;储料仓1的卸料口、进料仓A5和进料仓B6的进料口及卸料口均设电磁阀;进料仓A5和进料仓B6通过进料管7连接气化室8下部进料口,气化室8下部还通过斜向下的联通管9连通燃烧室10下部;燃烧室10上部通过床料回收循环器3连接气化室8上部;燃烧室10底部连接鼓风机;气化室8底部、联通管9中部连接蒸汽管11;床料回收循环器3与气化室8的连接处连接蒸汽管11。气化室8、燃烧室10中采用橄榄石作为床料;且均设有压力监测器13和温度监测仪14;气化室8顶部出气口处设气体分析仪2;燃烧室10顶部烟气口处设烟气监测器4。整套装置配置中电磁阀、压力监测器13、温度监测仪设备14、气体分析仪2、烟气监测器4,通过配置DCS系统,可实现自动化控制及在线监测设备状况。Please refer to Fig. 1, in the embodiment of the present invention, a novel double fluidized bed device for hydrogen production from organic solid waste, including: feeding mechanism, gasification chamber 8, bed material recovery circulator 3 and combustion chamber 10; The mechanism includes a storage bin 1, which is connected to the feed bin A5 and the feed bin B6; the discharge port of the storage bin 1, the feed port and the discharge port of the feed bin A5 and the feed bin B6 are all set Solenoid valve; feeding bin A5 and feeding bin B6 are connected to the lower part of the gasification chamber 8 through the feeding pipe 7, and the lower part of the gasification chamber 8 is also connected to the lower part of the combustion chamber 10 through the obliquely downward connecting pipe 9; the combustion chamber 10 The upper part is connected to the upper part of the gasification chamber 8 through the bed material recovery circulator 3; the bottom of the combustion chamber 10 is connected to the blower; the bottom of the gasification chamber 8 and the middle part of the communication pipe 9 are connected to the steam pipe 11; Connect the steam pipe 11. Olivine is used as the bed material in the gasification chamber 8 and the combustion chamber 10; and a pressure monitor 13 and a temperature monitor 14 are installed; a gas analyzer 2 is installed at the gas outlet at the top of the gasification chamber 8; the flue gas at the top of the combustion chamber 10 A smoke detector 4 is installed at the mouth. The solenoid valve, pressure monitor 13, temperature monitor 14, gas analyzer 2, and flue gas monitor 4 in the whole device configuration can realize automatic control and online monitoring of equipment status by configuring the DCS system.

本发明将有机固体废弃物放入储料仓1中,打开储料仓1卸料口电磁阀,选择性打开进料仓A5或进料仓B6进料口及卸料口的电磁阀,即可通过进料管7加料至气化室8中;当进料仓的料卸完时,切换另一个进料仓,保证进料仓的密闭性;有机固体废弃物在750-800℃的气化室8内,在橄榄石床料及蒸汽的作用下,进行无氧气化,生成高氢的混合气体从气化室8顶部出气口经过气体分析仪2的监测分析后排出,部分产生的焦油接触气化室8内的三角形挡板12及侧壁进行冷凝后,随同产生的焦炭颗粒以及橄榄石床料,通过气化室8下部斜向下的联通管9,进入至温度在900-950℃的燃烧室10内,在燃烧室10底部鼓风机的作用下,焦油及焦炭颗粒在燃烧室进行充分焚烧,使得燃烧室10内维持温度在900-950℃,同时燃烧室10内橄榄石床料也随之温度上升,在燃烧室10底部鼓风机的吹动下,通过床料回收循环器3再进入到气化室8,高温橄榄石床料使得气化室8温度维持控制在750-800℃,达到自持气化制氢的目的;而燃烧室10焚烧产生的烟气从顶部烟气口经过烟气监测器4的在监测达标排出;整个过程中,由于联通管9中部连接蒸汽管11,床料回收循环器3与气化室8的连接处连接蒸汽管11,使得燃烧室10内产生烟气与气化室8内产生的高氢混合气体不会产生窜气现象。The present invention puts the organic solid waste into the storage bin 1, opens the solenoid valve at the discharge port of the storage bin 1, and selectively opens the solenoid valves at the feed port and the discharge port of the feed bin A5 or feed bin B6, namely It can be fed into the gasification chamber 8 through the feed pipe 7; when the material in the feed bin is unloaded, switch to another feed bin to ensure the airtightness of the feed bin; the gasification of organic solid waste at 750-800 ° C In the gasification chamber 8, under the action of the olivine bed material and steam, oxygen-free oxidation is carried out to generate a high-hydrogen mixed gas from the gas outlet on the top of the gasification chamber 8 after being monitored and analyzed by the gas analyzer 2, and part of the generated tar is exposed to After the triangular baffle plate 12 and the side wall in the gasification chamber 8 condense, the coke particles and olivine bed material produced along with it pass through the downward connecting pipe 9 at the lower part of the gasification chamber 8, and enter to a temperature of 900-950°C. In the combustion chamber 10, under the action of the blower at the bottom of the combustion chamber 10, the tar and coke particles are fully incinerated in the combustion chamber, so that the temperature in the combustion chamber 10 is maintained at 900-950 °C, and the olivine bed material in the combustion chamber 10 is also As the temperature rises, under the blowing of the blower at the bottom of the combustion chamber 10, it passes through the bed material recovery circulator 3 and then enters the gasification chamber 8. The high-temperature olivine bed material keeps the temperature of the gasification chamber 8 at 750-800°C. The purpose of hydrogen production by self-sustaining gasification is achieved; the flue gas produced by the combustion of the combustion chamber 10 is discharged from the top flue gas port through the flue gas monitor 4 and is monitored to meet the standard; The connection between the material recovery circulator 3 and the gasification chamber 8 is connected to the steam pipe 11, so that the flue gas generated in the combustion chamber 10 and the high-hydrogen mixed gas generated in the gasification chamber 8 will not produce blow-by.

尽管参照前述实施例对本发明进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art can still modify the technical solutions described in the aforementioned embodiments, or perform equivalent replacements for some of the technical features. Within the spirit and principles of the present invention, any modifications, equivalent replacements, improvements, etc., shall be included in the protection scope of the present invention.

Claims (7)

1.一种新型有机固体废弃物制氢双流化床装置,其特征在于,包括:进料机构、气化室(8)、床料回收循环器(3)及燃烧室(10);进料机构通过进料管(7)连接气化室(8)下部进料口,气化室(8)下部还通过斜向下的联通管(9)连通燃烧室(10)下部;燃烧室(10)上部通过床料回收循环器(3)连接气化室(8)上部;燃烧室(10)底部连接鼓风机;气化室(8)底部、联通管(9)中部连接蒸汽管(11);床料回收循环器(3)与气化室(8)的连接处连接蒸汽管(11)。1. A novel double fluidized bed device for producing hydrogen from organic solid waste, characterized in that it comprises: a feeding mechanism, a gasification chamber (8), a bed material recovery circulator (3) and a combustion chamber (10); The feeding mechanism is connected to the lower part of the gasification chamber (8) through the feeding pipe (7), and the lower part of the gasification chamber (8) is also connected to the lower part of the combustion chamber (10) through the obliquely downward communication pipe (9); the combustion chamber ( 10) The upper part is connected to the upper part of the gasification chamber (8) through the bed material recovery circulator (3); the bottom of the combustion chamber (10) is connected to the blower; the bottom of the gasification chamber (8) and the middle part of the communication pipe (9) are connected to the steam pipe (11) ; The joint of bed material recovery circulator (3) and gasification chamber (8) is connected with steam pipe (11). 2.根据权利要求1所述的一种新型有机固体废弃物制氢双流化床装置,其特征在于,进料机构包括储料仓(1),储料仓(1)连接密闭的进料仓A(5)和进料仓B(6);进料仓A(5)和进料仓B(6)通过进料管(7)连接气化室(8)下部进料口。2. A novel dual-fluidized bed device for hydrogen production from organic solid waste according to claim 1, characterized in that the feeding mechanism includes a storage bin (1), and the storage bin (1) is connected to a closed feeding The bin A (5) and the feed bin B (6); the feed bin A (5) and the feed bin B (6) are connected to the lower feed port of the gasification chamber (8) through the feed pipe (7). 3.根据权利要求2所述的一种新型有机固体废弃物制氢双流化床装置,其特征在于,储料仓(1)的卸料口、进料仓A(5)和进料仓B(6)的进料口及卸料口均设有电动阀。3. A novel double fluidized bed device for hydrogen production from organic solid waste according to claim 2, characterized in that the discharge port of the storage bin (1), the feed bin A (5) and the feed bin Both the inlet and outlet of B(6) are equipped with electric valves. 4.根据权利要求1所述的一种新型有机固体废弃物制氢双流化床装置,其特征在于,所述气化室(8)内部侧壁设多个三角形挡板(12)。4. A novel double fluidized bed device for hydrogen production from organic solid waste according to claim 1, characterized in that a plurality of triangular baffles (12) are arranged on the inner side wall of the gasification chamber (8). 5.根据权利要求1所述的一种新型有机固体废弃物制氢双流化床装置,其特征在于,气化室(8)顶部出气口处设气体分析仪(2)。5. A novel double fluidized bed device for hydrogen production from organic solid waste according to claim 1, characterized in that a gas analyzer (2) is installed at the gas outlet at the top of the gasification chamber (8). 6.根据权利要求1所述的一种新型有机固体废弃物制氢双流化床装置,其特征在于,燃烧室(10)顶部烟气口处设烟气监测器(4)。6. A novel double fluidized bed device for producing hydrogen from organic solid waste according to claim 1, characterized in that a smoke monitor (4) is provided at the smoke port at the top of the combustion chamber (10). 7.根据权利要求1所述的一种新型有机固体废弃物制氢双流化床装置,其特征在于,气化室(8)、燃烧室(10)中采用橄榄石作为床料。7. A novel double fluidized bed device for hydrogen production from organic solid waste according to claim 1, characterized in that olivine is used as the bed material in the gasification chamber (8) and the combustion chamber (10).
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