CN202099280U - Horizontal continuous dry fermentation methane device for straws - Google Patents
Horizontal continuous dry fermentation methane device for straws Download PDFInfo
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- CN202099280U CN202099280U CN201120219746.3U CN201120219746U CN202099280U CN 202099280 U CN202099280 U CN 202099280U CN 201120219746 U CN201120219746 U CN 201120219746U CN 202099280 U CN202099280 U CN 202099280U
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- 238000000855 fermentation Methods 0.000 title claims abstract description 16
- 230000004151 fermentation Effects 0.000 title claims abstract description 16
- 239000010902 straw Substances 0.000 title claims abstract description 15
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title description 4
- 238000003756 stirring Methods 0.000 claims abstract description 25
- 238000006073 displacement reaction Methods 0.000 claims abstract description 9
- 230000008878 coupling Effects 0.000 claims description 5
- 238000010168 coupling process Methods 0.000 claims description 5
- 238000005859 coupling reaction Methods 0.000 claims description 5
- 238000007789 sealing Methods 0.000 claims description 5
- 239000003638 chemical reducing agent Substances 0.000 claims description 2
- 239000002994 raw material Substances 0.000 abstract description 7
- 239000007787 solid Substances 0.000 abstract description 5
- 239000010815 organic waste Substances 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000010865 sewage Substances 0.000 description 4
- 238000009434 installation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 238000010907 mechanical stirring Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- WWHFPJVBJUJTEA-UHFFFAOYSA-N n'-[3-chloro-4,5-bis(prop-2-ynoxy)phenyl]-n-methoxymethanimidamide Chemical compound CONC=NC1=CC(Cl)=C(OCC#C)C(OCC#C)=C1 WWHFPJVBJUJTEA-UHFFFAOYSA-N 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000011150 reinforced concrete Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/16—Solid state fermenters, e.g. for koji production
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/38—Caps; Covers; Plugs; Pouring means
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
- C12M27/06—Stirrer or mobile mixing elements with horizontal or inclined stirrer shaft or axis
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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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
本实用新型属于以秸秆为主的固体有机废物处理装置,是一种能够采用连续、干发酵工艺的卧式连续干发酵沼气装置。它包括卧式柱形罐体,中轴线上有一个带有叶片的搅拌轴或前、后两个带有叶片的搅拌半轴和驱动其旋转的减速电机,前端有与容积泵相连的进料口、顶部有集气罩、后端有与容积泵相连的出料口。本实用新型,产气率高、节能、便于自动化和没有“二次污染”,尤其适用于以秸秆为主要原料的生物能源工程。
The utility model belongs to a solid organic waste treatment device based on straw, and is a horizontal continuous dry fermentation biogas device capable of adopting continuous and dry fermentation processes. It consists of a horizontal cylindrical tank, with a stirring shaft with blades on the central axis or two stirring half shafts with blades at the front and rear and a deceleration motor driving its rotation, and a feeder connected to a positive displacement pump at the front end There is an air collecting hood on the top, and a discharge port connected to the positive displacement pump at the rear end. The utility model has the advantages of high gas production rate, energy saving, easy automation and no "secondary pollution", and is especially suitable for bioenergy projects using straw as the main raw material.
Description
技术领域 technical field
本实用新型属于以秸秆为主的固体有机废物处理装置,涉及采用连续、干发酵工艺(CDPF)的一种秸秆卧式连续干发酵沼气装置。The utility model belongs to a straw-based solid organic waste treatment device, and relates to a straw horizontal continuous dry fermentation methane device adopting a continuous dry fermentation process (CDPF).
背景技术 Background technique
目前,利用沼气发酵技术处理以秸秆为主的固体有机废物,主要采用离心泵进料的立式沼气装置。因受液泵性能限制,该装置进料的干物质浓度(TS%)只能小于或等于10%。为此,一是粉碎秸秆上浮成浮渣并不断堆积于装置顶部的气箱中,难以去除和不利于沼气的逸出。二是难以对浮渣进行有效搅拌与混合,故原料的利用率与池容产气率较低。三是需配兑3~4倍于发酵原料重量的污水,增加了多余污水加热到发酵温度(35℃或55℃左右)的热能消耗,也增加了沼液的排放量和输送费用。四是排放的沼液,若不能全部利用将会产生二次污染;采用“卧式机械搅拌沼气装置”(专利号ZL 200520142327.9),因没有强制进、出料设备和叶片在轴向排列方式不同,使得干物质浓度(TS%)为20%~40%的发酵原料难以进入罐体内且不断向后端蠕动。At present, the use of biogas fermentation technology to treat solid organic waste mainly composed of straw mainly adopts vertical biogas devices fed by centrifugal pumps. Due to the limitation of the performance of the liquid pump, the dry matter concentration (TS%) of the feed to the device can only be less than or equal to 10%. For this reason, one is that the scum floats on the crushed straw and continuously accumulates in the air box at the top of the device, which is difficult to remove and is not conducive to the escape of biogas. The second is that it is difficult to effectively stir and mix the scum, so the utilization rate of raw materials and the gas production rate of the tank are low. The third is that it is necessary to mix 3 to 4 times the weight of sewage as the fermentation raw material, which increases the heat energy consumption of heating the excess sewage to the fermentation temperature (about 35°C or 55°C), and also increases the discharge of biogas slurry and transportation costs. Fourth, if the discharged biogas slurry cannot be fully utilized, it will cause secondary pollution; the "horizontal mechanical stirring biogas device" (patent number ZL 200520142327.9) is adopted, because there is no forced feeding and discharging equipment and the axial arrangement of the blades is different , so that the dry matter concentration (TS%) is 20% to 40% of the fermentation raw material is difficult to enter the tank and constantly creeps to the rear end.
发明内容 Contents of the invention
为了克服现有处理以秸秆为主的立式沼气装置,不能大幅度提高进料浓度,浮渣难以去除和“卧式机械搅拌沼气装置”(专利号ZL 200520142327.9)不能进一步提高进料浓度的问题,本实用新型提供一种连续、干发酵工艺的卧式沼气装置,容积泵15产生的压力可使进料的干物质浓度提高到20%~40%;按轴向螺旋排列的叶片10不断旋转将发酵物料上下翻动且向罐体4后端蠕动。它是一种带有机械搅拌的卧式柱形罐体4,前端有与1#容积泵15相连的进料口14、顶部有1~10个集气罩5、后端有与2#容积泵8相连的出料口9和分别位于顶部或后端的1#人孔6或2#人孔7方便于设备的安装与检修;位于罐体4中轴线上有一个搅拌轴13或有前、后两个搅拌半轴16并通过2~10个轴承座11架设在支架12上,搅拌轴13或前、后两个搅拌半轴16上有按轴向螺旋排列的6~42个叶片10,搅拌轴13或前、后两个搅拌半轴16的一端通过罐体4的密封座3与罐体4外的联轴器2和减速机1连接,搅拌轴13或前、后两个搅拌半轴16的转速等于或小于10转/分。本实用新型提出的秸秆卧式连续干发酵沼气装置与离心泵进料的立式沼气装置和卧式机械搅拌沼气装置相比,在相同发酵温度(35℃或55℃左右)下的池容产气率提高100~200%、节约热能30~70%、没有沼液外排引发的“二次污染”、操作便于自动化和适合多种固体有机废物的处理,尤其适用于以秸秆为主要原料的生物能源工程。In order to overcome the problems that the existing vertical biogas device that mainly handles straw cannot greatly increase the feed concentration, the scum is difficult to remove, and the "horizontal mechanical stirring biogas device" (patent number ZL 200520142327.9) cannot further increase the feed concentration. , the utility model provides a horizontal biogas device for continuous and dry fermentation process, the pressure generated by the
附图说明Description of drawings
附图1和附图2是本实用新型的结构示意图。Accompanying drawing 1 and accompanying
图中1、减速电机,2、联轴器,3、密封座,4、罐体,5、集气罩,6、1#人孔,7、2#人孔,8、2#容积泵,9、出料口,10、叶片,11、轴承座,12、支架,13、搅拌轴,14、进料口,15、1#容积泵,16、搅拌半轴。In the figure 1. Geared motor, 2. Coupling, 3. Sealing seat, 4. Tank body, 5. Gas collecting hood, 6. 1# manhole, 7. 2# manhole, 8. 2# positive displacement pump, 9. Discharge port, 10. Blade, 11. Bearing seat, 12. Bracket, 13. Stirring shaft, 14. Feed port, 15. 1# positive displacement pump, 16. Stirring half shaft.
具体实施方式 Detailed ways
实施例一Embodiment one
在附图1中,以碎秸秆为主的发酵原料,配兑定量的污水后,由1#容积泵15经进料口14打入罐体4前端并在减速电机1通过联轴器2和密封座3驱动带有叶片10搅拌轴13的旋转搅拌下,将发酵物上下翻动且不断向罐体4后端蠕动。发酵物在翻动中被加热,产生的沼气经集气罩5输出,沼渣液由2#容积泵8经出料口9排出。搅拌轴13通过轴承座11架设在支架12上,位于顶部的1#人孔6和后端的2#人孔7便于设备的安装与检修。In the accompanying drawing 1, the fermented raw materials mainly composed of crushed straw are blended with a certain amount of sewage, and then pumped into the front end of the tank body 4 by the 1#
实施例二Embodiment two
在附图2中,以碎秸秆为主的固体发酵原料,配兑定量的污水后,由1#容积泵15经进料口14打入罐体4前端并在前、后端各用一套减速电机1通过联轴器2和密封座3分别驱动带有叶片10的前、后两个搅拌半轴16的同方向旋转搅拌下,将发酵物上下翻动且不断向罐体4后端蠕动。发酵物在翻动中被加热,产生的沼气经集气罩5输出,沼渣液由2#容积泵8经出料口9排出。前、后两个搅拌半轴16通过轴承座11架设在支架12上,位于顶部的1#人孔6便于设备的安装与检修。In accompanying
在附图1和附图2中,本实用新型的罐体4的材料可以是钢结构或钢筋混凝上结构,而且有保温设施。罐体4内的混凝土表面均做密封层,不得渗漏气和水;金属构件均刷防腐涂料。In accompanying drawing 1 and accompanying
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103172422A (en) * | 2013-05-08 | 2013-06-26 | 江苏大学 | Horizontal reciprocated type agitating equipment of straw powder dust wastes |
CN104140928A (en) * | 2014-08-15 | 2014-11-12 | 杨华昌 | Container modular biogas digester |
CN107760579A (en) * | 2016-08-23 | 2018-03-06 | 山东明硕新能源科技有限公司 | A kind of horizontal biogas fermentation device |
CN110052475A (en) * | 2019-04-24 | 2019-07-26 | 中国科学院合肥物质科学研究院 | Poultry based on biomass straw is died of illness harmless treatment device and processing method |
-
2011
- 2011-06-27 CN CN201120219746.3U patent/CN202099280U/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103172422A (en) * | 2013-05-08 | 2013-06-26 | 江苏大学 | Horizontal reciprocated type agitating equipment of straw powder dust wastes |
CN104140928A (en) * | 2014-08-15 | 2014-11-12 | 杨华昌 | Container modular biogas digester |
CN107760579A (en) * | 2016-08-23 | 2018-03-06 | 山东明硕新能源科技有限公司 | A kind of horizontal biogas fermentation device |
CN110052475A (en) * | 2019-04-24 | 2019-07-26 | 中国科学院合肥物质科学研究院 | Poultry based on biomass straw is died of illness harmless treatment device and processing method |
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