CN202643689U - Plant straw solar energy gasification and waste residue and waste water collection and utilization device - Google Patents
Plant straw solar energy gasification and waste residue and waste water collection and utilization device Download PDFInfo
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- CN202643689U CN202643689U CN201220323903XU CN201220323903U CN202643689U CN 202643689 U CN202643689 U CN 202643689U CN 201220323903X U CN201220323903X U CN 201220323903XU CN 201220323903 U CN201220323903 U CN 201220323903U CN 202643689 U CN202643689 U CN 202643689U
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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
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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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
- C12M23/36—Means for collection or storage of gas; Gas holders
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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
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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
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/16—Screw conveyor
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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
- C12M43/00—Combinations of bioreactors or fermenters with other apparatus
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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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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/59—Biological synthesis; Biological purification
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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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T50/00—Aeronautics or air transport
- Y02T50/60—Efficient propulsion technologies, e.g. for aircraft
- Y02T50/678—Aviation using fuels of non-fossil origin
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
The utility model provides a plant straw solar energy gasification and waste residue and waste water collection and utilization device, and relates to equipment turning straw into methane. Preprocessed materials in a straw preprocessed material pond are injected into a fermentation tank through a feeding pump. Gasified residue and water in the fermentation tank are discharged through a propeller type discharger. Feeding and discharging are both driven by electricity so that labor intensity is low and production efficiency is high. Methane residue discharged from the discharger enters the upper portion of a filter screen of a residue-water separating pond, and methane liquid sinks to the bottom of the residue-water separating pond. When the liquid level of the methane liquid in the separating pond is over high, redundant methane liquid enters a liquid storage pond through a valve and a pipeline. The residue-water separating pond separates and stores waste water and waste residue so that organic fertilizer can be completely returned to a field and recycled. A liquid outlet pump is arranged on the liquid storage pond, and the methane liquid in the liquid storage pond is discharged through a liquid transfer pipe. A propeller type pusher which is arranged on the fermentation tank pushes materials to be evenly filled in the fermentation tank. A plurality of stirrers II which are arranged on the fermentation tank stir evenly the materials in the fermentation tank. The plant straw solar energy gasification and waste residue and waste water collection and utilization device is good in gasification effect and high in methane production rate.
Description
Technical field
The utility model relates to a kind of plant stalk gasifying device, is specifically related to be installed in the interior gasifying stalk of sun power hot house and waste residue, wastewater collection use device.
Background technology
China is a large agricultural country, every harvest season of vast rural area, all can produce a large amount of straws.The manual labour because the most of blue or green shape year people in rural area all goes down town, lack of labor, straw recovery operation amount is large, and the stalk recycle value of recovery is low, have to directly burn in the field.Because the smog that crop straw burning causes can not land aircraft, expressway traffic accident takes place frequently, and the air severe contamination causes respiratory tract disease suddenly to increase.In order to prohibit the burning stalk, governments at all levels have all spent great effort every year and have checked burning severely.Country all drops into substantial contribution every year, promotes gasifying stalk and stalk marsh gas technology.The applicant has invented a kind of " gasification of straw sun power and waste reside comprehensive utilization Processes and apparatus ", and obtained national inventing patent (publication number CN101318853), this Processes and apparatus can have been realized also field recycling of gasifying stalk, human and animal excreta harmless treatment, the waste residue that is rich in organic fertilizer, waste water, carried out the popularization pilot in the Jiangsu Part area, the peasant exchanges biogas for straw, economical and practical, the peasant has obtained material benefit, the harm of avoiding crop straw burning to cause has obtained good economic benefit and social benefit.
The gasification of straw sun power and the waste reside comprehensive utilization equipment of former invention, in use find the following weak point:
1, material loading, discharging are by artificial, and labour intensity is large, and production efficiency is low.
2, whipping appts is not installed in the fermentor tank, is caused stalk and human and animal excreta to mix inhomogeneous, affect gasification result.
3, contain a large amount of organic fertilizer in the methane liquid, the methane liquid that remains in the fermentor tank can not be recycled fully, causes waste.
Summary of the invention
In order to solve the problems of the technologies described above this, the utility model provides the gasification of a kind of straw sun power and waste residue, wastewater collection use device, and its material into and out of fermentor tank adopts electronic fresh feed pump and electronic removal device to carry out; Many agitators are installed on the fermentor tank, and the waste water after the gasification, waste residue enter the pulp water separate tank to be separated.
The utility model is achieved by the following technical solution: the gasification of a kind of straw sun power and waste residue, wastewater collection use device, it comprises stalk pre-treatment material pond and the fermentor tank that is installed in the sun power hot house, also comprises being installed in sun power hot house outer gas-holder and waste material collection device.Described fermentor tank is cylindrical Horizontal enclosed tank body, and an end of tank body is made manhole, and clearly tank water-freeing arrangement is arranged at the bottom of tank body, and tank body is installed on the basis in the sun power hot house by tank landing leg.Described stalk pre-treatment material pond is to cover casing dimerous by material pond body and material pond, and stalk pre-treatment material arranges water intaking valve and hopper on the pond; Pre-treatment material in the stalk pre-treatment material pond enters fermentor tank by feed-pipe, and the biogas that produces in the fermentor tank enters gas-holder by pneumatic tube, and the biogas in the described gas-holder is delivered to gas equipment by air delivering pipeline; Stalk in the fermentor tank after the gasification becomes methane slag and the methane liquid that is rich in organic fertilizer; Described methane slag and methane liquid enter waste material collection device by carrier pipe.It is characterized in that: described stalk pre-treatment material pond is installed in an end of fermentor tank, and the Lower Half in stalk pre-treatment material pond is imbedded under the sun power hot house ground level; Stalk pre-treatment material arranges fresh feed pump on the pond, and described fresh feed pump injects fermentor tank with the pre-treatment material by feed-pipe.On the described fermentor tank removal device is set, described removal device is the propeller type thruster; Methane slag and methane liquid that removal device is discharged enter the fertilizer collection device by carrier pipe.The pulp water separate tank that described fertilizer collection device is box typed structure, the pulp water separate tank is comprised of separate tank body and filtering net two portions; Described filtering net is horizontally fixed on the middle part of separate tank body; The methane slag that removal device is discharged enters filtering net top, and methane liquid sinks at the bottom of the pond.
Methane liquid liquid level in the pulp water separate tank is too high, and this device also is provided with liquid storage tank, and described liquid storage tank is comprised of liquid storage tank body and liquid storage tank lid, and liquid storage tank is connected with the pulp water separate tank by valve and pipeline.
Set out liquid pump on the described liquid storage tank, described Pump for giving-out is discharged the methane liquid in the liquid storage tank by tubing.
Described stalk pre-treatment material also arranges the agitator I on the pond, and described agitator I is installed in the material pond and covers.
On the described fermentor tank pushing device is set, described pushing device is the propeller type thruster, and the pushing device level is installed on the end cap of fermentor tank feed end.
The agitator II is set on the described fermentor tank, and described agitator II is many, and many agitator II are uniform to be installed on the tank body of fermentor tank.
Positively effect of the present utility model is:
1, material adopts electronic fresh feed pump and electronic removal device to carry out into and out of fermentor tank, and is laborsaving, save time, and labour intensity is low, and production efficiency is high.
2, many agitators are installed on the fermentor tank, are stirred, gasification result is good, and factor of created gase is high.
3, the pulp water separate tank separates storage with waste water, waste residue, makes the organic fertilizer that is present in waste water, the waste residue all go back the field recycling.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
Accompanying drawing is the utility model structural representation.
Among the figure: 1, stalk pre-treatment material pond, 1-1, material pond body, 1-2, water intaking valve, 1-3 expects Chi Gai, 1-4, hopper, 2, the agitator I, 3, fresh feed pump, 3-1, feed-pipe, 4, pushing device, 5, fermentor tank, 5-1, tank landing leg, 5-2, manhole, 5-3, clear tank water-freeing arrangement, 6, the agitator II, 7, methane outlet, 8, pneumatic tube, 9, removal device, 10, carrier pipe, 11, the pulp water separate tank, 11-1, the separate tank body, 11-2, filtering net, 12, methane slag, 13, methane liquid, 14, valve and pipeline, 15, liquid storage tank, 15-1, the liquid storage tank body, 15-2, the liquid storage tank lid, 16, Pump for giving-out, 17, tubing, 18, gas-holder.
Embodiment
As shown in drawings: the gasification of a kind of straw sun power and waste residue, wastewater collection use device, it comprises stalk pre-treatment material pond 1 and the fermentor tank 5 that is installed in the sun power hot house, also comprises being installed in sun power hot house outer gas-holder 18 and waste material collection device; Described fermentor tank 5 is cylindrical Horizontal enclosed tank body, and an end of tank body is made manhole 5-2, and clearly tank water-freeing arrangement 5-3 is arranged at the bottom of tank body, and tank body is installed on the basis in the sun power hot house by tank landing leg 5-1.Described stalk pre-treatment material pond 1 is by material pond body 1-1 and material pond lid 1-3 casing dimerous, on the stalk pre-treatment material pond 1 water intaking valve 1-2 and hopper 1-4 is set.Pre-treatment material in the stalk pre-treatment material pond 1 enters fermentor tank 5 by feed-pipe 3-1, and the biogas that produces in the fermentor tank 5 enters gas-holder 18 by pneumatic tube 8, and the biogas in the described gas-holder 18 is delivered to gas equipment by air delivering pipeline; Stalk in the fermentor tank 5 after the gasification becomes methane slag 12 and the methane liquid 13 that is rich in organic fertilizer.Described methane slag 12 and methane liquid 13 enter waste material collection device by carrier pipe 10; It is characterized in that: described stalk pre-treatment material pond 1 is installed in an end of fermentor tank 5, the Lower Half in stalk pre-treatment material pond 1 is imbedded under the sun power hot house ground level, on the stalk pre-treatment material pond 1 fresh feed pump 3 is set, described fresh feed pump 3 injects fermentor tank 5 with the pre-treatment material by feed-pipe 3-1.On the described fermentor tank 5 removal device 9 is set, described removal device 9 is the propeller type thruster.Methane slag 12 and methane liquid 13 that removal device 9 is discharged enter the fertilizer collection device by carrier pipe 10.The pulp water separate tank 11 that described fertilizer collection device is box typed structure, pulp water separate tank 11 is comprised of separate tank body 11-1 and filtering net 11-2 two portions.Described filtering net 11-2 is horizontally fixed on the middle part of separate tank body 11-1; The methane slag 12 that removal device 9 is discharged enters filtering net 11-2 top, and methane liquid 13 sees through filtering net 11-2 and sinks at the bottom of the pond.
Also set out liquid pump 16 on the described liquid storage tank 15, described Pump for giving-out 16 is discharged the methane liquid 13 in the liquid storage tank 15 by tubing 17.
On the described stalk pre-treatment material pond 1 agitator I 2 is set also, described agitator I 2 is installed on the lid 1-3 of material pond.
On the described fermentor tank 5 pushing device 4 is set also, described pushing device 4 is the propeller type thruster, and pushing device 4 levels are installed on the end cap of fermentor tank 5 feed ends.
On the described fermentor tank 5 agitator II 6 is set also, described agitator II 6 is many, and many agitator II 6 are uniform to be installed on the tank body of fermentor tank 5.
As shown in drawings: during use, the straw after pulverizing is dropped into stalk pre-treatment material pond 1 by hopper 1-4, open water intaking valve 1-2, stalk, water and ammonium hydrogencarbonate cooperate in the ratio of 1:2:0.01, then the turn on agitator I 2, and material stirring in the pond is even, guarantee pretreating effect.Because stalk pre-treatment material pond 1 is positioned at the sun power hot house, temperature is high in the hot house, even also need not heating in the winter of cold, also more than 20 degree, stalk ferments under the effect of ammonium hydrogencarbonate temperature in advance in the pond.After the pre-fermentation of stalk is finished, inject the human and animal excreta of some amount, after stirring, start fresh feed pump 3, the material in the stalk pre-treatment material pond 1 is injected fermentor tank 5, open simultaneously pushing device 4, promote material and evenly be full of fermentor tank 5.Time opening agitator II 6, material stirring in the tank is even, and stalk, human and animal excreta fermentation produce biogas continuously, and biogas enters gas-holder 18 by pneumatic tube 8, and the biogas in the gas-holder 18 is delivered to gas equipment by air delivering pipeline again.Empirical evidence, fermentor tank 5 once feeds intake, but continuous gas generation four months.
Process through solar anaerobic, can kill parasitic ovum and pathogenic agent more than 95 percent in stalk and the human and animal excreta, reach national decontamination of human excreta hygienic standard.
According to actual needs and may, also can not add ammonium hydrogencarbonate and human and animal excreta, straw adds the water direct gasification.
After stalk is gasified totally, open removal device 9, the methane slag 12 of discharge enters the filtering net 11-2 top of pulp water separate tank 11, and methane liquid 13 sinks at the bottom of the pond.
After methane liquid 13 liquid levels in the pulp water separate tank 11 reach a certain height, open infusion pipeline 14, the methane liquid 13 in the pulp water separate tank 11 is entered liquid storage tank 15 store, when needing fertilising, open Pump for giving-out 16, by tubing 17 methane liquid 13 in the liquid storage tank 15 is discharged.
Claims (6)
1. straw sun power gasification and waste residue, wastewater collection use device, it comprises stalk pre-treatment material pond (1) and the fermentor tank (5) that is installed in the sun power hot house, also comprises being installed in sun power hot house outer gas-holder (18) and waste material collection device; Described fermentor tank (5) is cylindrical Horizontal enclosed tank body, and an end of tank body is made manhole (5-2), and clearly tank water-freeing arrangement (5-3) is arranged at the bottom of tank body, and tank body is installed on the interior basis of sun power hot house by tank landing leg (5-1); Described stalk pre-treatment material pond (1) is by material pond body (1-1) and material Chi Gai (1-3) casing dimerous, and water intaking valve (1-2) and hopper (1-4) are set on the stalk pre-treatment material pond (1); Pre-treatment material in the stalk pre-treatment material pond (1) enters fermentor tank (5) by feed-pipe (3-1), the biogas that produces in the fermentor tank (5) enters gas-holder (18) by pneumatic tube (8), and the biogas in the described gas-holder (18) is delivered to gas equipment by air delivering pipeline; Stalk in the fermentor tank (5) after the gasification becomes methane slag (12) and the methane liquid (13) that is rich in organic fertilizer; Described methane slag (12) and methane liquid (13) enter waste material collection device by carrier pipe (10); It is characterized in that: described stalk pre-treatment material pond (1) is installed in an end of fermentor tank (5), and the Lower Half in stalk pre-treatment material pond (1) is imbedded under the sun power hot house ground level; Fresh feed pump (3) is set on the stalk pre-treatment material pond (1), and described fresh feed pump (3) injects fermentor tank (5) with the pre-treatment material by feed-pipe (3-1); Removal device (9) is set on the described fermentor tank (5), and described removal device (9) is the propeller type thruster; Methane slag (12) and methane liquid (13) that removal device (9) is discharged enter the fertilizer collection device by carrier pipe (10); The pulp water separate tank (11) that described fertilizer collection device is box typed structure, pulp water separate tank (11) is comprised of separate tank body (11-1) and filtering net (11-2) two portions; Described filtering net (11-2) is horizontally fixed on the middle part of separate tank body (11-1); The methane slag (12) that removal device (9) is discharged enters filtering net (11-2) top, and methane liquid (13) sinks at the bottom of the pond.
2. straw sun power according to claim 1 gasification and waste residue, wastewater collection use device, it is characterized in that: methane liquid (13) liquid level in pulp water separate tank (11) is too high, and this device also is provided with liquid storage tank (15); Described liquid storage tank (15) is comprised of liquid storage tank body (15-1) and liquid storage tank lid (15-2), and liquid storage tank (15) is connected with pulp water separate tank (11) by valve and pipeline (14).
3. straw sun power according to claim 2 gasification and waste residue, wastewater collection use device, it is characterized in that: also set out liquid pump (16) on the described liquid storage tank (15), described Pump for giving-out (16) is discharged the methane liquid (13) in the liquid storage tank (15) by tubing (17).
4. straw sun power according to claim 1 gasification and waste residue, wastewater collection use device is characterized in that: agitator I (2) also is set on the described stalk pre-treatment material pond (1); Described agitator I (2) is installed on the material Chi Gai (1-3).
5. straw sun power according to claim 1 gasification and waste residue, wastewater collection use device, it is characterized in that: pushing device (4) also is set on the described fermentor tank (5), described pushing device (4) is the propeller type thruster, and pushing device (4) level is installed on the end cap of fermentor tank (5) feed end.
6. straw sun power according to claim 1 gasification and waste residue, wastewater collection use device, it is characterized in that: agitator II (6) also is set on the described fermentor tank (5), described agitator II (6) is many, and many agitator II (6) are uniform to be installed on the tank body of fermentor tank (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220323903XU CN202643689U (en) | 2012-07-06 | 2012-07-06 | Plant straw solar energy gasification and waste residue and waste water collection and utilization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220323903XU CN202643689U (en) | 2012-07-06 | 2012-07-06 | Plant straw solar energy gasification and waste residue and waste water collection and utilization device |
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| Publication Number | Publication Date |
|---|---|
| CN202643689U true CN202643689U (en) | 2013-01-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201220323903XU Expired - Lifetime CN202643689U (en) | 2012-07-06 | 2012-07-06 | Plant straw solar energy gasification and waste residue and waste water collection and utilization device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102732323A (en) * | 2012-07-06 | 2012-10-17 | 苗晓 | Plant-straw solar gasification and waste-slag and waste-water collection and utilization device |
| CN109971621A (en) * | 2019-03-29 | 2019-07-05 | 张智广 | Full underground type high-efficiency environment friendly large methane tank and pretreatment of raw material and heat method |
| CN112679239A (en) * | 2021-01-29 | 2021-04-20 | 四川省畜牧科学研究院 | Residual heavy metal passivation device in livestock and poultry manure |
-
2012
- 2012-07-06 CN CN201220323903XU patent/CN202643689U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102732323A (en) * | 2012-07-06 | 2012-10-17 | 苗晓 | Plant-straw solar gasification and waste-slag and waste-water collection and utilization device |
| CN102732323B (en) * | 2012-07-06 | 2014-08-27 | 苗晓 | Plant-straw solar gasification and waste-slag and waste-water collection and utilization device |
| CN109971621A (en) * | 2019-03-29 | 2019-07-05 | 张智广 | Full underground type high-efficiency environment friendly large methane tank and pretreatment of raw material and heat method |
| CN112679239A (en) * | 2021-01-29 | 2021-04-20 | 四川省畜牧科学研究院 | Residual heavy metal passivation device in livestock and poultry manure |
| CN112679239B (en) * | 2021-01-29 | 2024-03-19 | 四川省畜牧科学研究院 | Passivation device for residual heavy metal in livestock and poultry feces |
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