CN206014920U - Biomass ferment consersion unit - Google Patents

Biomass ferment consersion unit Download PDF

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Publication number
CN206014920U
CN206014920U CN201621064200.4U CN201621064200U CN206014920U CN 206014920 U CN206014920 U CN 206014920U CN 201621064200 U CN201621064200 U CN 201621064200U CN 206014920 U CN206014920 U CN 206014920U
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CN
China
Prior art keywords
fermentation tank
tank
biogas slurry
aeration
return duct
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201621064200.4U
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Chinese (zh)
Inventor
宋文路
赵强
王贤
王超
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jining University
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Jining University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jining University filed Critical Jining University
Priority to CN201621064200.4U priority Critical patent/CN206014920U/en
Application granted granted Critical
Publication of CN206014920U publication Critical patent/CN206014920U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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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
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Treatment Of Sludge (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

This utility model is related to a kind of biomass ferment consersion unit, belong to field of fermentation equipment, including fermentation tank, feed pipe, escape pipe, feed pipe is connected with the cloth surge tank for being arranged on fermentation tank top center, the surrounding of cloth surge tank is evenly arranged with four cloth tubes for going deep into tank body, agitating device is provided with inside fermentation tank, aerator is installed with the inner bottom of fermentation tank, fermentation tank is provided with temperature sensor probe and PH detectors, the bottom of fermentation tank is provided with slag-drip opening, the upper portion side wall first line of a couplet of fermentation tank is connected to biogas slurry return duct, biogas slurry return duct is provided with intersegmental heat exchanger and biogas slurry reflux pump.This utility model charging is uniform, is provided with agitating device, aerator and biogas slurry return duct, and the fermentative degradation process of biomass castoff is more thorough, more efficiently, does not result in secondary pollution, and the product after fermentation is separated can be obtained efficient waste material and biogas energy.

Description

Biomass ferment consersion unit
Technical field
This utility model is related to a kind of biomass ferment consersion unit, belongs to field of fermentation equipment.
Background technology
Biomass castoff is referred to from solid waste that is vegeto-animal and being degraded by microorganisms, main including meal The gardens biomass wastes such as the urban biomass waste such as kitchen rubbish, municipal sewage sludge, deadwood leaveves, weeds and residual flower and Agricultural biomass garbage such as straw from village, fowl and animal excrement etc..
Anaerobic fermentation is a kind of more biomass castoff treatment technology of application, and this technology can pass through anaerobe The degraded of biomass castoff is realized, so as to preferably realize the innoxious of biomass castoff, minimizing and resource.Biological While clean energy resource (methane) is produced, its biogas residue produced after digesting can also be further processed into matter garbage anaerobic fermentation High-quality waste material.Existing biogas fermentation tank arrangement is mainly made up of fermentation tank, feeding tube, discharge nozzle, due to discharging opening excessively Concentration easily cause charging uneven, there is the problems such as degradation rate is low, and degradation cycle is long, gas output is not high.
Utility model content
The purpose of this utility model is Shortcomings in prior art to be solved, there is provided a kind of biomass ferment is set with reaction Standby.
This utility model is achieved through the following technical solutions:
I.e. a kind of biomass ferment consersion unit, including fermentation tank, feed pipe, escape pipe, feed pipe is sent out with being arranged on The cloth surge tank of fermentation tank top center is connected, and the surrounding of cloth surge tank is evenly arranged with four cloth for going deep into tank body Expects pipe, is provided with shaft inside fermentation tank, shaft is provided with multiple stirring vanes, and shaft is coupled with motor, fermentation tank Aeration supervisor is installed with inner bottom, and the both sides of aeration supervisor are provided with multiple curved aeration looped pipelines, and aeration is responsible for Solarization air cap is provided with aeration looped pipeline, aeration supervisor coupled with the aeration pump outside tank body, fermentation tank is provided with temperature sensor spy Head and PH detectors, the bottom of fermentation tank are provided with slag-drip opening, and the top of fermentation tank is provided with escape pipe, and escape pipe is provided with biogas stream Scale, the upper portion side wall first line of a couplet of fermentation tank are connected to biogas slurry return duct, and biogas slurry return duct is provided with intersegmental heat exchanger and biogas slurry is returned Stream pump, the end of biogas slurry return duct is deep into inside fermentation tank.
This utility model charging is uniform, is provided with agitating device, aerator and biogas slurry return duct, biomass castoff Fermentative degradation process more thorough, more efficiently, do not result in secondary pollution, fermentation separate after product can be obtained efficiently useless Material and biogas energy.
The end of the biogas slurry return duct is provided with automatic swivel joint, and automatic swivel joint is provided with feeding shower nozzle.Return The biogas slurry of stream is sprayed by feeding shower nozzle, and shower nozzle rotates automatically, and biogas slurry discharging is more uniform, is conducive to the effect for improving fermentative degradation Really.
Compared with prior art, this utility model is had an advantageous effect in that:
1st, this utility model charging is uniform, is provided with agitating device, aerator and biogas slurry return duct, and biomass are discarded The fermentative degradation process of thing is more thorough, more efficiently, does not result in secondary pollution, and the product after fermentation is separated can be obtained efficiently Waste material and biogas energy.
2nd, the end of biogas slurry return duct is provided with automatic swivel joint, and automatic swivel joint is provided with feeding shower nozzle.Backflow Biogas slurry sprayed by feeding shower nozzle, shower nozzle rotates automatically, and biogas slurry discharging is more uniform, is conducive to the effect for improving fermentative degradation.
Description of the drawings
Fig. 1 is theory structure schematic diagram of the present utility model;
Structural representations of the Fig. 2 for aeration tube;
Fig. 3 is the structural representation of automatic swivel joint and feeding shower nozzle.
In figure:1st, motor;2nd, fermentation tank;3rd, feed pipe;4th, cloth surge tank;5th, cloth tube;6th, biogas slurry return duct;7th, section Between heat exchanger;8th, biogas slurry reflux pump;9th, automatic swivel joint;10th, feeding shower nozzle;11st, shaft;12nd, stirring vane;13、 Aeration is responsible for;14th, aeration looped pipeline;15th, aeration pump;16th, temperature sensor probe;17th, PH detectors;18th, slag-drip opening;19th, go out Trachea;20th, biogas flow meter;21st, solarization air cap.
Specific embodiment
Below against accompanying drawing, specific embodiment of the present utility model is described in further detail.
Biomass ferment consersion unit as shown in Figure 1, Figure 2, Figure 3 shows, including fermentation tank 2, feed pipe 3, escape pipe 19, Feed pipe 3 is connected with the cloth surge tank 4 for being arranged on 2 top center of fermentation tank, and the surrounding of cloth surge tank 4 uniformly sets Four cloth tubes 5 for going deep into tank body are equipped with, shaft 11 inside fermentation tank 2, is provided with, shaft 11 is provided with multiple stirring vanes 12, shaft 11 is coupled with motor 1, is installed with aeration supervisor 13 in the inner bottom of fermentation tank 2, and aeration is responsible for the two of 13 Side is provided with multiple curved aeration looped pipelines 14, and aeration supervisor 13 is provided with solarization air cap 21, aeration supervisor 13 with aeration looped pipeline 14 Couple with the aeration pump 15 outside tank body, fermentation tank 2 is provided with temperature sensor probe 16 and PH detectors 17, the bottom of fermentation tank 2 End is provided with slag-drip opening 18, and the top of fermentation tank 2 is provided with escape pipe 19, and escape pipe 19 is provided with biogas flow meter 20, fermentation tank 2 The upper portion side wall first line of a couplet is connected to biogas slurry return duct 6, and biogas slurry return duct 6 is provided with intersegmental heat exchanger 7 and biogas slurry reflux pump 8, biogas slurry The end of return duct 6 is deep into inside fermentation tank 2, and the end of biogas slurry return duct 6 is provided with automatic swivel joint 9, is rotated automatically Joint 9 is provided with feeding shower nozzle 10.

Claims (2)

1. a kind of biomass ferment consersion unit, including fermentation tank (2), feed pipe (3), escape pipe (19), it is characterised in that: Feed pipe (3) are connected with the cloth surge tank (4) for being arranged on the fermentation tank (2) top center, and cloth is buffered The surrounding of tank (4) is evenly arranged with inside four cloth tubes for going deep into tank body (5), fermentation tank (2) and is provided with shaft (11), stirs Axle (11) is provided with multiple stirring vanes (12), and shaft (11) is coupled with motor (1), solid in the inner bottom of fermentation tank (2) Dingan County is responsible for (13) equipped with aeration, and the both sides of aeration supervisor (13) are provided with multiple curved aeration looped pipelines (14), and aeration is responsible for (13) solarization air cap (21) is provided with aeration looped pipeline (14), and aeration supervisor (13) is coupled with the aeration pump (15) outside tank body, is fermented Tank (2) is provided with temperature sensor probe (16) and PH detectors (17), and the bottom of fermentation tank (2) is provided with slag-drip opening (18), sends out The top of fermentation tank (2) is provided with escape pipe (19), and escape pipe (19) is provided with biogas flow meter (20), the upper side of fermentation tank (2) The wall first line of a couplet is connected to biogas slurry return duct (6), and biogas slurry return duct (6) is provided with intersegmental heat exchanger (7) and biogas slurry reflux pump (8), natural pond It is internal that the end of liquid return duct (6) is deep into fermentation tank (2).
2. biomass ferment consersion unit according to claim 1, it is characterised in that:Biogas slurry return duct (6) End is provided with automatic swivel joint (9), and automatic swivel joint (9) are provided with feeding shower nozzle (10).
CN201621064200.4U 2016-09-20 2016-09-20 Biomass ferment consersion unit Expired - Fee Related CN206014920U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621064200.4U CN206014920U (en) 2016-09-20 2016-09-20 Biomass ferment consersion unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621064200.4U CN206014920U (en) 2016-09-20 2016-09-20 Biomass ferment consersion unit

Publications (1)

Publication Number Publication Date
CN206014920U true CN206014920U (en) 2017-03-15

Family

ID=58260290

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621064200.4U Expired - Fee Related CN206014920U (en) 2016-09-20 2016-09-20 Biomass ferment consersion unit

Country Status (1)

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CN (1) CN206014920U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107260980A (en) * 2017-05-04 2017-10-20 周口师范学院 A kind of hypoglycemic medicine and preparation method thereof
CN108004125A (en) * 2017-11-09 2018-05-08 中钢集团天澄环保科技股份有限公司 A kind of Novel anaerobic installation for fermenting
CN109251856A (en) * 2018-09-26 2019-01-22 安徽朱隆记食品有限公司 It is a kind of for producing the bacteria culture apparatus of soy sauce
CN115052956A (en) * 2019-12-26 2022-09-13 安耐罗技术股份有限公司 Process and apparatus for removing impurities from solid biomass feedstock
CN118064265A (en) * 2024-04-17 2024-05-24 山西资环科技股份有限公司 Biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107260980A (en) * 2017-05-04 2017-10-20 周口师范学院 A kind of hypoglycemic medicine and preparation method thereof
CN108004125A (en) * 2017-11-09 2018-05-08 中钢集团天澄环保科技股份有限公司 A kind of Novel anaerobic installation for fermenting
CN109251856A (en) * 2018-09-26 2019-01-22 安徽朱隆记食品有限公司 It is a kind of for producing the bacteria culture apparatus of soy sauce
CN115052956A (en) * 2019-12-26 2022-09-13 安耐罗技术股份有限公司 Process and apparatus for removing impurities from solid biomass feedstock
CN118064265A (en) * 2024-04-17 2024-05-24 山西资环科技股份有限公司 Biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170315

Termination date: 20180920