CN202170326U - Biomass dry distillation device - Google Patents
Biomass dry distillation device Download PDFInfo
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- CN202170326U CN202170326U CN2011202572810U CN201120257281U CN202170326U CN 202170326 U CN202170326 U CN 202170326U CN 2011202572810 U CN2011202572810 U CN 2011202572810U CN 201120257281 U CN201120257281 U CN 201120257281U CN 202170326 U CN202170326 U CN 202170326U
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 40
- 239000002028 Biomass Substances 0.000 title claims abstract description 32
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 13
- 238000010438 heat treatment Methods 0.000 claims abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 8
- 238000003763 carbonization Methods 0.000 claims description 31
- 238000002485 combustion reaction Methods 0.000 claims description 17
- 238000005485 electric heating Methods 0.000 claims description 6
- 230000006837 decompression Effects 0.000 claims description 3
- 238000009413 insulation Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 239000010813 municipal solid waste Substances 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 5
- 238000004064 recycling Methods 0.000 abstract description 3
- 230000036632 reaction speed Effects 0.000 abstract description 2
- 230000009467 reduction Effects 0.000 abstract description 2
- 239000010802 sludge Substances 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 3
- 239000007789 gas Substances 0.000 description 36
- 238000005516 engineering process Methods 0.000 description 13
- 238000000034 method Methods 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 238000009264 composting Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 150000002013 dioxins Chemical class 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004332 deodorization Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000010796 biological waste Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Processing Of Solid Wastes (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种城市垃圾处理装置,具体为一种生物质干馏装置。 The utility model relates to an urban garbage treatment device, in particular to a biomass dry distillation device.
背景技术 Background technique
散落在城市生活垃圾中的生物质广泛分布于人类生活中,现有的散落在城市生活垃圾中的生物质处理技术主要有堆肥技术、焚烧技术、填埋技术。 Biomass scattered in municipal solid waste is widely distributed in human life. The existing biomass treatment technologies scattered in municipal solid waste mainly include composting technology, incineration technology, and landfill technology.
采用堆肥技术处理生物质,基本上可以达到无害化的指标,但是,由于对堆肥的技术控制上不是很精细,往往会造成堆肥质量不好,使堆肥技术难以推广。 The use of composting technology to treat biomass can basically achieve the target of harmlessness. However, because the technical control of composting is not very fine, the quality of composting often results in poor quality, making it difficult to promote composting technology.
焚烧技术是各国多年一直研究的项目,经过多年的研究成果表明,焚烧技术似乎解决了二恶英的污染问题,但是,由于操作不当等的原因,现有的焚烧厂周围二恶英的积累还是没有得到完全彻底的解决,近几年国内也出现多次人民群众反对建立焚烧厂的呼声和事件。 Incineration technology is a project that has been studied by various countries for many years. After years of research results, it seems that incineration technology has solved the pollution problem of dioxins. However, due to improper operation and other reasons, the accumulation of dioxins around the existing incineration plants is still It has not been completely and thoroughly resolved. In recent years, there have been many voices and incidents of people opposing the establishment of incineration plants in China.
填埋工艺是多年来为人们所接受且广泛应用的技术,随着对填埋工艺标准的不断提高和费用的增加,填埋工艺对环境的危害已逐渐减少,但是,填埋工艺会占用大量的土地的弊端难以克服。 Landfill technology is a technology that has been accepted and widely used for many years. With the continuous improvement of landfill technology standards and the increase of costs, the environmental hazards of landfill technology have gradually decreased. However, landfill technology will take up a lot of The disadvantages of the land are difficult to overcome.
发明内容 Contents of the invention
针对上述问题,本实用新型提供了一种污染少、资源再利用程度高的生物质干馏装置。 In view of the above problems, the utility model provides a biomass dry distillation device with less pollution and high resource reuse.
本实用新型为解决其技术问题所采用的技术方案是: The technical scheme that the utility model adopts for solving its technical problem is:
一种生物质干馏装置,其特征在于包括干馏反应器、进料装置、加热装置、气体输出装置、出料装置以及气体处理装置,进料装置的输出口与干馏反应器的进料口连接,出料装置的输入口与干馏反应器的内腔连接,出料装置的输出口与一设置于外部的碳物质收集装置连接,气体输出装置的输入端与干馏感应器的内腔相通,气体输出装置的输出端与气体处理装置相连。 A biomass dry distillation device is characterized in that it comprises a dry distillation reactor, a feed device, a heating device, a gas output device, a discharge device and a gas treatment device, the output port of the feed device is connected to the feed port of the dry distillation reactor, The input port of the discharge device is connected to the inner cavity of the carbonization reactor, the output port of the discharge device is connected to an external carbon collection device, the input end of the gas output device is connected to the inner cavity of the carbonization sensor, and the gas output The output end of the device is connected with the gas processing device.
优选的是,所述进料装置为阿基米德螺旋线推进器,阿基米德螺旋线推进器的固态出口与干馏反应器的进料口相连,进料口上有密闭闸门。 Preferably, the feeding device is an Archimedes helical propeller, the solid outlet of the Archimedes helical propeller is connected to the feed port of the dry distillation reactor, and there is a closed gate on the feed port.
优选的是,出料装置的输出口与碳物质收集装置之间设置有液封。 Preferably, a liquid seal is provided between the output port of the discharge device and the carbon material collection device.
优选的是,所述加热装置为至少一条电加热棒,电加热棒设置于干馏反应器内腔靠近下部的位置。 Preferably, the heating device is at least one electric heating rod, and the electric heating rod is arranged at a position close to the lower part of the carbonization reactor inner cavity.
优选的是,所述干馏反应器为球体密闭结构。 Preferably, the dry distillation reactor is a spherical closed structure.
优选的是,该生物质干馏装置设置有一与干馏反应器内腔连通的防爆减压装置。 Preferably, the biomass carbonization device is provided with an explosion-proof decompression device communicating with the inner cavity of the carbonization reactor.
优选的是,所述出料装置设置于干馏反应器的下部位置,出料装置的上方设置有燃烧室。 Preferably, the discharge device is arranged at the lower part of the carbonization reactor, and a combustion chamber is arranged above the discharge device.
优选的是,所述气体处理装置设置有一用于向燃烧室提供可燃气的供气回路。 Preferably, the gas treatment device is provided with a gas supply circuit for supplying combustible gas to the combustion chamber.
优选的是,所述干馏反应器的外侧设有真空保温隔层。 Preferably, the outer side of the dry distillation reactor is provided with a vacuum insulation barrier.
优选的是,所述气体输出装置主动抽取干馏反应器内的气体。 Preferably, the gas output device actively extracts the gas in the dry distillation reactor.
本实用新型的有益效果是:本实用新型可以较好的将生物质转化成可再利用能源和碳等,不会产生二恶英等污染问题,同时也解决了散落在城市生活垃圾中的生物质填埋所占大量土地的弊端,能够有效的解决“碳水”化合物和“碳氢”物质转化的难题,实现能源物质循环与再生利用,大大的减轻人类活动对环境及大气的破坏,可有效的改变目前用粮食作物制取能源所造成的全球粮食的短缺现状;本实用新型所采用结构大大提高了干馏的反应速度,并能顺利产出可燃气、油和炭,从无害化、资源化、减量化的角度可以广泛应用于生活垃圾(厨余垃圾)、医疗垃圾、污泥等的处理。 The beneficial effects of the utility model are: the utility model can better convert biomass into reusable energy and carbon, without producing dioxin and other pollution problems, and also solves the problem of biological waste scattered in urban domestic garbage. The disadvantages of material landfill occupying a large amount of land can effectively solve the problem of the conversion of "carbohydrate" compounds and "hydrocarbon" substances, realize the recycling and regeneration of energy materials, and greatly reduce the damage to the environment and the atmosphere caused by human activities. Change the current situation of global food shortage caused by the production of energy from food crops; the structure adopted by the utility model greatly improves the reaction speed of dry distillation, and can smoothly produce combustible gas, oil and charcoal, from harmless, resource It can be widely used in the treatment of domestic waste (kitchen waste), medical waste, sludge, etc. from the perspective of minimization and reduction.
附图说明 Description of drawings
下面结合附图和具体实施方式进行进一步的说明: Further explanation is carried out below in conjunction with accompanying drawing and specific embodiment:
图1为本实用新型的系统组成示意图。 Fig. 1 is a schematic diagram of the system composition of the present utility model.
具体实施方式 Detailed ways
参照图1,本实用新型的一种生物质干馏装置,包括干馏反应器1、进料装置2、加热装置3、气体输出装置7、出料装置4以及气体处理装置6,进料装置2的输出口与干馏反应器1的进料口连接,出料装置4的输入口与干馏反应器1的内腔连接,出料装置4的输出口与一设置于外部的碳物质收集装置15连接,气体输出装置7的输入端与干馏感应器1的内腔相通,气体输出装置7的输出端与气体处理装置6相连。加热装置3一般为电加热棒,电加热棒的数量可以为一条或多条,具体数量以干馏反应器1的体积所定,电加热棒设置于干馏反应器1内腔靠近下部的位置,以易于进料出料为宜。为了干馏过程的安全进行,该生物质干馏装置还优选设置有一与干馏反应器1内腔连通的防爆减压装置9。为了避免热能的散失,干馏反应器1的外侧优选设有真空保温隔层5。当然,除了干馏反应器1的外侧外,需要包裹保温材料的设备、装置或者管道上,一般也会包裹保温材料。
With reference to Fig. 1, a kind of biomass dry distillation device of the present utility model comprises
另外,本装置除了上述各种部件外,其一般还包括观察运行状态的各种仪器、仪表、控制运行状态的各种阀门以及自动化控制系统。 In addition, in addition to the above-mentioned various components, the device generally includes various instruments and meters for observing the operating state, various valves for controlling the operating state, and an automatic control system.
本实用新型工作时,待处理物料通过进料装置2送入到干馏反应器1中,进料后进料装置2处于关闭状态。干馏反应器1对物料处理后生成碳物质,碳物质通过出料装置送到碳物质收集装置15中,气体则通过气体输出装置7送到气体处理装置6进行处理。为了保证干馏处理效果,使得干馏过程在密闭无氧的空间内进行,干馏反应器1一般优选为球体等密闭结构,并且气体输出装置7工作时利用真空泵等主动抽取干馏反应器1内的气体,使得干馏反应器1内部处于负压无氧状态,有效抑制了二恶英的合成。如图1所示,本实用新型所采用的气体处理装置可以包括可升降式气包、除尘除臭塔12等,气体存储于可升降式气包中,使用时经过除尘除臭塔处理后会得到纯度高的可燃气送到所需位置使用。
When the utility model works, the material to be processed is sent into the
优选的是,进料装置2为阿基米德螺旋线推进器,阿基米德螺旋线推进器的固态出口与干馏反应器1的进料口相连,进料口上有密闭闸门。阿基米德螺旋线推进器的设置可以使得待处理物料的进料过程更加方便。
Preferably, the feeding device 2 is an Archimedes helical propeller, the solid outlet of the Archimedes helical propeller is connected to the feed port of the
一般地,出料装置4的输出口与碳物质收集装置15之间还会设置有液封8。在图1的实施例中,碳物质收集装置15为一存储池,池中充有水体,碳物质被排入到存储池后沉淀到池底位置处。存储池的池底设置为倾斜面,这样可以使得碳物质集中到底部一角,当碳物质达到一定量时,可以利用抓斗等设备将碳物质从池中取出。
Generally, a
本实用新型的出料装置4一般设置于干馏反应器1的下部位置,其可以通过手动/自动化控制的方式进行排料过程。出料装置4的上方设置有燃烧室10,该燃烧室10可以为可拆卸的或者不可拆卸的结构,并且燃烧室10优选为方形状。当设置有上述燃烧室10时,干馏反应器1内所需的热量可由加热装置3和燃烧室共同提供或者单独提供。燃烧室使用时,燃烧室产生的热能从生物质干馏装置的底部上升,可以使整个装置发热,达到生物质干馏反应所需的热量,燃烧所产生的烟气排入到设置于外部的冷凝器中。为了节约能源,增加能源利用率,气体处理装置6优选设置有一用于向燃烧室10提供可燃气的供气回路。实际应用时,气体处理装置6所产生的可燃气除了用于供给到上述燃烧室外,其还可以经发电机组后转化成电能,供给生物质干馏装置内部的加热装置,使其利用电能产生热能。
The discharge device 4 of the present invention is generally arranged at the lower part of the
下面针对图1中的实施例对本实用新型的处理过程进行描述。 The processing procedure of the present invention will be described below for the embodiment in FIG. 1 .
本实用新型工作时,生物质通过进料装置的入料口进入到干馏反应器1中,关闭进料装置,在真空泵等的作用下使干馏反应器处于负压无氧的状态。进入干馏反应器1的生物质在加热装置3和/或燃烧室10的作用下,转化成可燃气体和炭。生物质转化成的可燃气通过气体输出装置7排出,通过出油口13的油进入到油罐14中。排出的可燃气可以通过发电机组转化成电能,供给加热装置3,使其利用电能转化成热能;取出的可燃气也可通过燃烧室10内的燃烧,达到生物质干馏所需的热能,燃烧产生的烟气进入冷凝器中。生物质转化成的炭,通过出料装置4落入到碳物质收集装置15(充有水的存储池)中。当炭物质的量达到一定量时,利用抓斗等设备将炭物质取出。
When the utility model is working, the biomass enters the
本实用新型的实施方式并不受上述实施例的限制,只要其以基本相同的手段达到本实用新型的技术效果,都应属于本实用新型的保护范围。 The implementation of the utility model is not limited by the above-mentioned examples, as long as it achieves the technical effect of the utility model by basically the same means, it should belong to the protection scope of the utility model.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102277184A (en) * | 2011-07-20 | 2011-12-14 | 珠海经济特区联谊机电工程有限公司 | Biomass dry distillation device |
CN103484134A (en) * | 2013-08-09 | 2014-01-01 | 中国科学院过程工程研究所 | Solid heat carrier-based destructive distillation reactor and method of raw hydrocarbon |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102277184A (en) * | 2011-07-20 | 2011-12-14 | 珠海经济特区联谊机电工程有限公司 | Biomass dry distillation device |
CN103484134A (en) * | 2013-08-09 | 2014-01-01 | 中国科学院过程工程研究所 | Solid heat carrier-based destructive distillation reactor and method of raw hydrocarbon |
CN103484134B (en) * | 2013-08-09 | 2015-02-18 | 中国科学院过程工程研究所 | Solid heat carrier-based destructive distillation reactor and method of raw hydrocarbon |
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