CN203999121U - A kind of biochemical reactor of using capable of circulation - Google Patents
A kind of biochemical reactor of using capable of circulation Download PDFInfo
- Publication number
- CN203999121U CN203999121U CN201420424086.6U CN201420424086U CN203999121U CN 203999121 U CN203999121 U CN 203999121U CN 201420424086 U CN201420424086 U CN 201420424086U CN 203999121 U CN203999121 U CN 203999121U
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- China
- Prior art keywords
- reactor
- pipeline
- inner core
- discharging
- biochemical
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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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- Treatment Of Sludge (AREA)
Abstract
The utility model relates to a kind of biochemical reactor of using capable of circulation, comprises shell, and housing exterior is provided with thermal insulation layer, is provided with inner core in shell; Inner core is provided with small opening, and small opening surface is provided with one deck biochemical film, and the central position of inner core is fixed with transmission shaft; Inner core below is provided with spiral discharging pipe, and the left end of spiral discharging pipe is provided with discharging pipeline, and discharging pipeline ingress is provided with discharge valve, and the exit of discharging pipeline is provided with discharging pump; The right-hand member of discharge nozzle is provided with recycle feed pipeline and material inlet valve, and recycle feed pipeline is connected with described fresh feed pump; The top of reactor is provided with methane outlet, and the right-hand member of methane outlet is provided with blowing pipeline, and the lower end of reactor is provided with bearing.This utility model device has the digestion rate of accelerating anaerobism, can carry out circulating reaction and increase operation rate, and can efficiently be processed, and process thoroughly, and speed is high, decomposes fast several times with first-class advantage than conventional methane-generating pit.
Description
Technical field
The utility model relates to a kind of capable of circulation with biochemical reactor, belongs to biochemical sewage process field.
Background technology
At present, along with industrial development, the processing problem of the ight soil of increasing sewage, mud and domestic animal etc. is more and more paid attention to by society.The treatment process of existing sewage, mud has the following disadvantages aspect actually operating: the problem the first, existing in compost treatment has, and in mud, containing the objectionable impuritiess such as heavy metal and polychlorobiphenyl such as a large amount of pathogenic bacterias, parasite (ovum), Yi Jige, mercury can not process.The second, sanitary landfill, need large-area place and a large amount of trucking costs, and ground need do antiseepage processing in order to avoid polluted underground water.Three, burn, after burning disposal, its volume can reduce 85%～95%, exists and does not invest greatly, secondary pollution, carcinogenic Dioxins.Four, dry, if there is thermal source, such as building on heat power plant limit, the heat that utilizes flue gas is a kind of way preferably, but the efficiency that will sacrifice power plant, the transportation cost of mud is also huge.Five, anaerobic digestion, organic substance decomposing, makes sewage sludge harmlessness, and resource utilization turns waste into wealth, and green energy resource is provided.The problem existing is that present anaerobic technique reaction is slow, invests greatly, digests also not thorough.
Based on above reason, need a kind of be capable of circulationly devised with biochemical reactor, it allows anaerobic digestion accelerate, and forces rapid reaction, and optimization reaction conditions, at the most active high temperature of bacterium clock, obtain best PH value, thereby allow biochemical film maximize in limited space and with the uniform contact of mud maximum, and can loop reaction, thoroughly, utilization ratio is high, i.e. a kind of biochemical reactor of using capable of circulation in reaction.
Summary of the invention
The problem existing in order to solve above-mentioned prior art, the utility model provides a kind of biochemical reactor of using capable of circulation.
The technical scheme in the invention for solving the above technical problem is as follows.
A kind of biochemical reactor of using capable of circulation, comprises shell, and housing exterior is provided with thermal insulation layer, in described shell, is provided with inner core; Described inner core is provided with small opening, and described small opening surface is provided with one deck biochemical film, and the central position of described inner core is fixed with transmission shaft; Described inner core below is provided with spiral discharging pipe, and the left end of described spiral discharging pipe is provided with discharging pipeline, and described discharging pipeline ingress is provided with discharge valve, and the exit of described discharging pipeline is provided with discharging pump; The right-hand member of described discharge nozzle is provided with recycle feed pipeline and material inlet valve, and described recycle feed pipeline is connected with described fresh feed pump; The top of described reactor is provided with methane outlet, and the right-hand member of described methane outlet is provided with blowing pipeline, and the lower end of described reactor is provided with bearing.
Further, the left side of described reactor is provided with the first power package, and described the first power package is connected by bearing and transmission shaft are stable.
Further, the left side of described reactor is also provided with the second power package, and described the second power package is connected with spiral discharging pipe by bearing.
Further, the right side of described reactor is provided with heat exchanger, comprises shell side and tube side, and described shell side two ends are respectively equipped with hot steam import and hot steam outlet, described tube side two ends are respectively equipped with material inlet and material outlet, and described shell side bottom is also provided with end-of-the-pipe.
The utility model heats up by a heat exchanger before sludge treatment, and biochemical producer need to be incubated and just can carry out stable reaction, so be provided with thermal insulation layer at the outside surface of biochemical reactor.An inner core with holes of design in biochemical device, places the catalyzer that promotes biochemical reaction in inner core, the surface in inner core hole is provided with microbial film, makes material and catalyzer good contact.Inner core is evenly rotated and makes catalyzer fully contact organism in digested sludge with mud by driven by motor, produces methane gas.Methane gas (biogas) is derived from top collection hole.Mud after treatment can be by spiral discharging pipe the forward under the second power package control enter fresh feed pump from recycle feed pipeline and circulate, make reaction more abundant, also can be sent by spiral discharge device and be sent to desiccation apparatus by discharging pump by the reversion of the second power package driven rotary discharge nozzle.Mud heats up has interchanger to ensure, the control of temperature determines by inlet water temperature and flow velocity, and water is derived circulation by interchanger water outlet.
The beneficial effects of the utility model are: a kind of capable of circulation with biochemical reactor, there is the digestion rate of accelerating anaerobism, and can carry out circulating reaction and increase operation rate, can efficiently be processed, and process thoroughly, speed is high, decomposes fast several times with first-class advantage than conventional methane-generating pit.
Brief description of the drawings
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is structural representation of the present utility model.
Fig. 2 is interior isostructure schematic diagram of the present utility model.
Fig. 3 is heat converter structure schematic diagram of the present utility model.
Description of symbols in figure: 1, shell; 2, thermal insulation layer; 3, inner core; 301, hole; 302, microbial film; 303, transmission shaft; 4, the first power package; 5, the second power package; 6, discharging pipeline; 7, discharge valve; 8, spiral discharging bar; 9, heat exchanger; 901, shell side; 902, tube side; 903, material inlet; 904, material outlet; 905, sewage draining exit; 10, recycle feed pipeline; 11, recycle feed valve; 12, blowing pipeline; 13, methane outlet; 14, discharging pump; 15, fresh feed pump; 16, base.
Embodiment
As shown in Figure 1, Figure 2 and Figure 3, one described in the utility model is capable of circulation comprises shell 1 with biochemical reactor, and housing exterior is provided with thermal insulation layer 2, in described shell 1, is provided with inner core 3; Described inner core is provided with small opening 301, and described small opening 301 surfaces are provided with one deck biochemical film 302, and the central position of described inner core 3 is fixed with transmission shaft 303; Described inner core below is provided with spiral discharging pipe 8, and the left end of described spiral discharging pipe is provided with discharging pipeline 6, and described discharging pipeline 6 ingresss are provided with discharge valve 7, and the exit of described discharging pipeline is provided with discharging pump 14; The right-hand member of described discharge nozzle 8 is provided with recycle feed pipeline 10 and material inlet valve 11, and described recycle feed pipeline 10 is connected with described fresh feed pump 15; The top of described reactor is provided with methane outlet 13, and the right-hand member of described methane outlet is provided with blowing pipeline 12, and the lower end of described reactor is provided with bearing 16.
The left side of described reactor is provided with the first power package 4, and described the first power package 4 is connected with transmission shaft 303 is stable by bearing.The left side of described reactor is also provided with the second power package 5, and described the second power package 5 is connected with spiral discharging pipe 8 by bearing.The right side of described reactor is provided with heat exchanger 9, comprise shell side 901 and tube side 902, described shell side 901 two ends are respectively equipped with hot steam import and hot steam outlet, and described tube side 902 two ends are respectively equipped with material inlet 903 and material outlet 904, and described shell side 901 bottoms are also provided with end-of-the-pipe 905.
When work, the utility model heats up by a heat exchanger, and biochemical producer need to be incubated and just can carry out stable reaction, so be provided with thermal insulation layer at the outside surface of biochemical reactor.An inner core with holes of design in biochemical device, places the catalyzer that promotes biochemical reaction in inner core, the surface in inner core hole is provided with microbial film, makes material and catalyzer good contact.Inner core is evenly rotated and makes catalyzer fully contact organism in digested sludge with mud by driven by motor, produces methane gas.Methane gas (biogas) is derived from top collection hole.Mud after treatment can be by spiral discharging pipe the forward under the second power package control enter fresh feed pump from recycle feed pipeline and circulate, make reaction more abundant, also can be sent by spiral discharge device and be sent to desiccation apparatus by discharging pump by the reversion of the second power package driven rotary discharge nozzle.Mud heats up has interchanger to ensure, the control of temperature determines by inlet water temperature and flow velocity, and water is derived circulation by interchanger water outlet.
The above is preferred implementation of the present utility model; it should be pointed out that for those skilled in the art, do not departing under the prerequisite of the utility model principle; can also make some improvements and modifications, these improvements and modifications are also considered as protection domain of the present utility model.
Claims (4)
1. the biochemical reactor of using capable of circulation, comprises shell, it is characterized in that: described housing exterior is provided with thermal insulation layer, in described shell, is provided with inner core; Described inner core is provided with small opening, and described small opening surface is provided with one deck biochemical film, and the central position of described inner core is fixed with transmission shaft; Described inner core below is provided with spiral discharging pipe, and the left end of described spiral discharging pipe is provided with discharging pipeline, and described discharging pipeline ingress is provided with discharge valve, and the exit of described discharging pipeline is provided with discharging pump; The right-hand member of described discharge nozzle is provided with recycle feed pipeline and material inlet valve, and described recycle feed pipeline is connected with described fresh feed pump; The top of described reactor is provided with methane outlet, and the right-hand member of described methane outlet is provided with blowing pipeline, and the lower end of described reactor is provided with bearing.
2. one according to claim 1 is capable of circulation is characterized in that: the left side of described reactor is provided with the first power package with biochemical reactor, and described the first power package is connected by bearing and transmission shaft are stable.
3. one according to claim 1 is capable of circulation is characterized in that: the left side of described reactor is also provided with the second power package with biochemical reactor, and described the second power package is connected with spiral discharging pipe by bearing.
4. one according to claim 1 is capable of circulation with biochemical reactor, it is characterized in that: the right side of described reactor is provided with heat exchanger, comprise shell side and tube side, described shell side two ends are respectively equipped with hot steam import and hot steam outlet, described tube side two ends are respectively equipped with material inlet and material outlet, and described shell side bottom is also provided with end-of-the-pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420424086.6U CN203999121U (en) | 2014-07-30 | 2014-07-30 | A kind of biochemical reactor of using capable of circulation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420424086.6U CN203999121U (en) | 2014-07-30 | 2014-07-30 | A kind of biochemical reactor of using capable of circulation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203999121U true CN203999121U (en) | 2014-12-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420424086.6U Expired - Fee Related CN203999121U (en) | 2014-07-30 | 2014-07-30 | A kind of biochemical reactor of using capable of circulation |
Country Status (1)
| Country | Link |
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| CN (1) | CN203999121U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104928159A (en) * | 2015-06-25 | 2015-09-23 | 南安市绿野沼气技术开发研究所 | High-efficiency biogas fermentation system |
| CN104928155A (en) * | 2015-06-24 | 2015-09-23 | 南安市绿野沼气技术开发研究所 | High-efficiency biogas generating device |
-
2014
- 2014-07-30 CN CN201420424086.6U patent/CN203999121U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104928155A (en) * | 2015-06-24 | 2015-09-23 | 南安市绿野沼气技术开发研究所 | High-efficiency biogas generating device |
| CN104928155B (en) * | 2015-06-24 | 2017-08-08 | 南安市绿野沼气技术开发研究所 | A kind of high-efficiency methane generator |
| CN104928159A (en) * | 2015-06-25 | 2015-09-23 | 南安市绿野沼气技术开发研究所 | High-efficiency biogas fermentation system |
| CN104928159B (en) * | 2015-06-25 | 2018-04-13 | 南安市绿野沼气技术开发研究所 | A kind of efficient methane fermentation system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Liang Dewei Inventor after: He Shi Inventor after: Liang Dequan Inventor after: Lu Bingjun Inventor after: Li Wenhua Inventor after: Liang Donghui Inventor after: Zou Shitong Inventor after: Mo Qiuhuan Inventor after: Zheng Qingjun Inventor after: Jing Lin District Inventor before: Gong Canfeng |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170504 Address after: Beijiao town Shunde District Guangdong city Foshan province 528311 neighborhood along the River Road No. 3 two China Patentee after: FOSHAN SHUNDE ONEZ PRESSURE VESSEL MANUFACTURING CO.,LTD. Address before: Fengle Yuecheng District Jianhu Town Village 312000 Zhejiang city of Shaoxing Province Wang under No. 59 Patentee before: Gong Canfeng |
|
| 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: 20141210 Termination date: 20210730 |