CN202081031U - Horizontal barrel rolling type aerobic fermentation equipment with heat exchange function - Google Patents
Horizontal barrel rolling type aerobic fermentation equipment with heat exchange function Download PDFInfo
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- CN202081031U CN202081031U CN201120125067XU CN201120125067U CN202081031U CN 202081031 U CN202081031 U CN 202081031U CN 201120125067X U CN201120125067X U CN 201120125067XU CN 201120125067 U CN201120125067 U CN 201120125067U CN 202081031 U CN202081031 U CN 202081031U
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- fermentor tank
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- cylinder
- aerobic fermentation
- cylinder fermentor
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- 238000010564 aerobic fermentation Methods 0.000 title claims abstract description 20
- 238000005096 rolling process Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 62
- 230000000694 effects Effects 0.000 claims abstract description 10
- 241000005139 Lycium andersonii Species 0.000 claims description 16
- 239000007789 gas Substances 0.000 claims description 13
- 229910000831 Steel Inorganic materials 0.000 claims description 9
- 238000007599 discharging Methods 0.000 claims description 9
- 239000010959 steel Substances 0.000 claims description 9
- 230000000630 rising effect Effects 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 5
- 238000009413 insulation Methods 0.000 claims description 5
- 230000008878 coupling Effects 0.000 claims description 4
- 238000010168 coupling process Methods 0.000 claims description 4
- 238000005859 coupling reaction Methods 0.000 claims description 4
- 230000001877 deodorizing effect Effects 0.000 claims description 4
- 230000008093 supporting effect Effects 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 2
- 238000011084 recovery Methods 0.000 claims description 2
- 238000000855 fermentation Methods 0.000 abstract description 21
- 230000004151 fermentation Effects 0.000 abstract description 21
- 230000007613 environmental effect Effects 0.000 abstract description 5
- 239000003337 fertilizer Substances 0.000 abstract description 4
- 238000007789 sealing Methods 0.000 abstract 4
- 239000003638 chemical reducing agent Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 14
- 230000005611 electricity Effects 0.000 description 8
- 230000001276 controlling effect Effects 0.000 description 7
- 239000010813 municipal solid waste Substances 0.000 description 6
- 239000000523 sample Substances 0.000 description 6
- 125000004122 cyclic group Chemical group 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 239000002361 compost Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000012467 final product Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000011499 joint compound Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000003440 toxic substance Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 238000002640 oxygen therapy Methods 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 238000007514 turning Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
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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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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- Fertilizers (AREA)
Abstract
Disclosed is horizontal barrel rolling type aerobic fermentation equipment with a heat exchange function. A horizontal barrel fermentation tank is supported by a riding wheel set, bearings are mounted at the left end and the right end of the barrel fermentation tank, the barrel fermentation tank is connected with left and right side sealing covers via bearing outer rings and bearing inner rings, the fermentation tank, the bearings and the sealing covers form a closed space, a spiral feeder and an exhaust tube are mounted on the left side sealing cover, a spiral discharger and an air inlet tube are mounted on the right side sealing cover, a coaxial cylindrical heat exchange water jacket is arranged on the outside of the barrel fermentation tank, a motor, a coupler, a speed reducer and a pinion are successively connected, and the pinion is meshed with an outer gear ring on the barrel fermentation tank. The horizontal barrel rolling type aerobic fermentation equipment is small in occupied area, is not affected by environmental factors and low temperature conditions, is high in fermentation efficiency, does not cause secondary pollution, is low in moisture of products, realizes reduction, harmless and resource treatment of excrement, and is free of bad smell and heat discharge and fine in environmental protection effect, and the products can be commercially sold as high-quality organic fertilizers.
Description
Technical field
The utility model belongs to the biodegradation technique field, be specifically related to a kind of horizontally-arranged rolling cylinder formula aerobic fermentation equipment, be widely used in minimizing, innoxious, the recycling treatment of excrement dirt, mud and rubbish and be prepared into the technical equipment of fertilizer with the control of thermal exchange and leavening temperature.
Background technology
The main byproduct of livestock and poultry farms in scale, sewage work, treatment of urban garbage factory: ight soil, mud and organic waste, the big and high concentration of amount if can not timely and effectively handle, very easily pollutes, and becomes environmental disaster.
At the processing with the rubbish of applying manure to the fields, people have proposed numerous solutions, as the dynamic fermentation method of oxygenation (compost), biogas fermentation method, high temperature and rapid drying method, micro-wave drying method, landfill and electricity generating method by burning etc.
Because the common water ratio of rubbish, Fen high (50%～90%), direct landfill is polluted underground water system very easily, and drying needs a large amount of energy, burning electricity generation is because burning produces toxic substances such as Dioxins, carbon monoxide, sulfurous gas, be difficult to effectively control the discharging of toxic substance, more owing to the water ratio height of rubbish, combustion heat value is low, make cost of electricity-generating high, lose more than gain.
Biogas technology (anaerobically fermenting) is considered to a kind of biotechnology that can handle Fen and produce clean energy biogas, satisfy anaerobically fermenting requirement (the concentration general requirement of fermentation raw material is about 8%) but be actually, need to add a large amount of and precious water resources to satisfy the needs of its concentration, therefore the reactor volume of its fermentation is huge, volume yield rate is low, even in the winter of southern china, reactor generally also can stop fermentation, and stacking Fen also needs a large amount of places.Though final product natural pond liquid also is fabulous agricultural organic fertilizer, because the extremely difficult solid-liquid separation that realizes of natural pond liquid, so be subjected to the restriction of transportation cost, natural pond liquid is difficult to realize commercial sales, and the solubility COD of natural pond liquid is very high, and discharging very easily causes second environmental pollution.
Aerobic fermentation (compost) can be by the microbiological deterioration organism, and Shi Fen rubbish is realized minimizing, and the composting technology that extensively adopts at present, mainly have following problems:1. floor space is big; 2. fermentation time is grown (general fermentation time needs about 15 days to one month); 3. fermenting speed descends when microthermal climate.Improve at present mostly the efficient or the effect of aerobic composts, but heat and foul smell that fermentation produces let alone to airborne release, caused environmental pollution by the means such as forcing oxygen therapy, turning or stirring of ventilating.
Summary of the invention
Technical problem to be solved in the utility model is: solve the problem that above-mentioned prior art exists, and provide a kind of horizontally-arranged rolling cylinder formula aerobic fermentation to equip with thermal exchange, this equipment floor space is little, not influenced by environmental factors and cold condition, the fermentation efficiency height, do not produce secondary pollution, the final product water ratio is low, can realize minimizing, innoxious, the recycling treatment of excrement dirt as high-quality fertilizer commercial sales, no foul smell and heat efflux, and environment protecting is good.
The technical solution adopted in the utility model is: horizontally-arranged cylinder fermentor tank is supported by the support roller group, bearing is equipped with at two ends, the cylinder fermentor tank left and right sides, bearing outer ring is passed through at cylinder fermentor tank two ends, bearing inner race is connected with the left and right sides capping, the cylinder fermentor tank, an enclosed space is formed in bearing and capping, screw feeder and vapor pipe and spiral discharging machine and inlet pipe are installed in respectively in the left and right sides capping, cylinder fermentor tank outside has co-axial tubular heat exchanging water-jacket, electric motor, shaft coupling, speed reduction unit, pinion(gear) connects successively, the external tooth wheel rim engagement on pinion(gear) and the cylinder fermentor tank.
In the technique scheme, the support roller group has left support roller group, right support roller group, and is corresponding with it, has the support steel ring on the right and left correspondence position of horizontally-arranged cylinder fermentor tank, and left and right support roller group is supporting the support steel ring of horizontally-arranged cylinder fermentor tank the right and left.
In the technique scheme, difference installation shaft bearing outer-ring in the two ends, the left and right sides of horizontally-arranged cylinder fermentor tank, the left and right sides capping is then installed respectively and is fixed in bearing inner race, and bearing outer ring is fixedlyed connected with the cylinder fermentor tank, and bearing inner race is fixedlyed connected with capping.
In the technique scheme, the left support roller group of horizontally-arranged cylinder fermentor tank feed end is an adjustable height support roller group, and the feed end of horizontally-arranged cylinder fermentor tank is higher than discharge end, and the axis of cylinder fermentor tank and the angle of horizontal plane are that 0～5 degree is adjustable.
In the technique scheme, the right support roller group of horizontally-arranged cylinder fermentor tank discharge end has the backstop wheel, and the effect of backstop wheel is to avoid cylinder along axis generation play.
In the technique scheme, coaxial cylindrical heat exchanging water-jacket's coated outside of horizontally-arranged cylinder fermentor tank external device (ED) has polyurethane insulation coating.
In the technique scheme, the supported steel ring of the coaxial cylindrical heat exchanging water-jacket of horizontally-arranged cylinder fermentor tank, external tooth wheel rim have been separated into several parts, and the adjacent part coaxial cylindrical heat exchanging water-jacket connect by the water jacket pipe connecting, is linked to be an integral body.
In the technique scheme, coaxial cylindrical heat exchanging water-jacket's water jacket water inlet pipe and water jacket rising pipe cause place, cylinder fermentor tank axle center by cylinder fermentor tank inside respectively, the water jacket water inlet pipe connects via the right rotation joint and the circulating water inlet that are installed in place, capping axle center, right side, and the water jacket rising pipe connects via the anticlockwise joint and the circulating water outlet pipe that are installed in place, capping axle center, left side.
In the technique scheme, cylinder fermentor tank inside is mounted with the material flight.
In the technique scheme, heat exchanger and gas blower are housed on the inlet pipe of horizontally-arranged cylinder fermentor tank, a branch pipeline of heat exchanging water-jacket's cyclic water outlet passes through in heat exchanger, gas blower is sent to the gas heating of cylinder fermentor tank; Another heat exchanger and vacuum fan are housed on the vapor pipe of horizontally-arranged cylinder fermentor tank, the heat exchanging water-jacket is circulated to intake and is deflated heating by another heat exchanger, and cooled exhaust is sent to deodorizing equipment and is focused under the effect of vacuum fan, reclaims non-pollution discharge behind the ammonia nitrogen.
The beneficial effects of the utility model are: equipment has been set up the physical condition of aerobic fermentation fully, makes fermentation reaction can be able to carry out at a high speed, is equipped in the utilization that the heat that fermentation is produced is realized resource utilization.And foul smell is also through discharging again after concentrate gathering, focusing on, and makes gas such as ammonia nitrogen obtain recycling rather than being discharged into the topsoil environment.
Simultaneously; the utility model equipment floor space is little; not influenced by environmental factors and cold condition, fermentation efficiency height, aerobic fermentation in airtight container; do not produce secondary pollution; forced ventilation is taken away moisture and is not influenced ferment effect and efficient, so final product moisture content is low, can be as high-quality fertilizer commercial sales; the minimizing of excrement dirt, innoxious, recycling treatment have been realized, for significant contribution is made in low-carbon economy and environment protection.
Description of drawings:
Fig. 1 is the utility model structural representation;
Fig. 2 is a cylinder fermentor tank left view;
Fig. 3 is a cylinder fermentor tank right view;
Fig. 4 is a cylinder fermentor tank view profile.
The accompanying drawing marking explanation:
1---screw feeder, 2---vapor pipe, 3---the left side capping, 4---bearing inner race,
5---bearing outer ring, 6---the cylinder fermentor tank, 7---flight, 8---the water jacket pipe connecting,
9---the heat exchanging water-jacket, 10---thermal insulation layer, 11---the water jacket water inlet pipe, 12---the right side capping,
13---inlet pipe, 14---the right rotation joint, 15---circulating water inlet,
16---spiral discharging machine, 17---right support roller group, 18---support steel ring, 19---electric motor,
20---shaft coupling, 21---speed reduction unit, 22---pinion(gear), 23---the external tooth wheel rim,
24---left support roller group, 25---sealing-ring, 26---the water jacket rising pipe,
27---the anticlockwise joint, 28---circulating water outlet pipe.
Embodiment:
Referring to accompanying drawing, horizontally-arranged cylinder fermentor tank 6 is supported on right support roller group 17, the left support roller group 24, two groups of support roller groups are supporting the support steel ring 18 of cylinder fermentor tank 6 both sides, regulating left support roller group 24 makes the feed end of cylinder fermentor tank 6 be higher than discharge end, the axis of cylinder fermentor tank 6 is that 0～5 degree is adjustable with the angle of horizontal plane, and the backstop wheel on the right support roller group 17 avoids cylinder along axis generation play.
Be welded with co-axial tubular heat exchanging water-jacket 9 outside the cylinder fermentor tank 6, heat exchanging water-jacket's 9 supported steel rings 18, external tooth wheel rim 23 have been divided into several sections, and the several sections water jacket is communicated with into an integral body by water jacket pipe connecting 8.
Water jacket water inlet pipe 11, water jacket rising pipe 26 cause place, cylinder axle center by cylinder interior respectively, the right rotation joint 14 of water jacket water inlet pipe 11 through being installed in place, right side capping 12 axle center is connected with circulating water inlet 15, and the anticlockwise joint 27 of water jacket rising pipe 26 through being installed in place, capping 3 axle center, left side is connected with circulating water outlet pipe 28.
Be coiled into material machine 1 and send into De Fen in the cylinder fermentor tank 6, kick up by the flight 7 in the cylinder fermentor tank 6 of rotation, with the warm air contact that gas blower is sent into, aerobic bacteria is under the effect that contains the oxygen air, and beginning is bred in a large number and begun degraded digestion Fen and produce heat.
When Controlling System detects the measured temperature of temp probe in the cyclic water outlet pipeline, when being higher than the measured temperature of temp probe in the circulation suction culvert, illustrate that the fermentation heat raises the temperature of recirculated water, this moment, Controlling System began to regulate the input that electricity accent valve reduces the heat of external heat source.And the hot blast that vacuum fan is extracted out is sent to another heat exchanger heats recirculated water, is sent to and discharges after deodorizing equipment focuses on, reclaims ammonia nitrogen and obtain the refrigerative exhaust.
Controlling System constantly detects measured temperature of cyclic water outlet temp probe and poor with the measured temperature of circulation inflow temperature probe, transfer the aperture of valve by controlling electricity, unnecessary heat energy is delivered to the thermal source load, makes the measured homo(io)thermism of leaving water temperature(LWT) probe at a suitable temperature (as 55 ° of C).And along with the carrying out of aerobic fermentation, the heat that biological respinse produces constantly increases, and at high temperature enters dormant state for avoiding microorganism, Controlling System will be regulated electricity and be transferred valve, strengthen external heat energy output, make system constant a certain temperature (, can regulate) as 55 ℃.
The part of cyclic water outlet is pumped into heat exchanger, gas blower is sent to the gas heating of cylinder fermentor tank 6.Because the air that is sent in the cylinder fermentor tank is warm air all the time, high air output can not make a jar interior leavening temperature descend, therefore the rotating speed of gas blower depends on jar interior oxygen-consumption and the water ratio of discharging, when the water ratio of material is too high, can strengthens air output and regulate it.
After fully fermenting, a material arrival discharge port is sent by spiral discharging machine 16 in jar, and is sent to the scene of road technology down.
Be lower than discharge port in the cylinder fermentor tank and accumulate the material that gets off, act on as yeast and newly advance material, provide competent high-temperature aerobic bacterial classification, making fermentation be able to succession at a high speed and going down for newly advancing De Fen .
Claims (10)
1. the horizontally-arranged rolling cylinder formula aerobic fermentation with thermal exchange is equipped, it is characterized in that: horizontally-arranged cylinder fermentor tank is supported by the support roller group, bearing is equipped with at two ends, the cylinder fermentor tank left and right sides, bearing outer ring is passed through at cylinder fermentor tank two ends, bearing inner race is connected with the left and right sides capping, the cylinder fermentor tank, an airtight fermenting space is formed in bearing and capping, screw feeder and vapor pipe and spiral discharging machine and inlet pipe are installed in respectively in the left and right sides capping, cylinder fermentor tank outside has co-axial with it tubular heat exchanging water-jacket, electric motor, shaft coupling, speed reduction unit, pinion(gear) connects successively, the external tooth wheel rim engagement on pinion(gear) and the cylinder fermentor tank.
2. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1, it is characterized in that: the support roller group has left support roller group, right support roller group, corresponding with it, have the support steel ring on the right and left correspondence position of horizontally-arranged cylinder fermentor tank, left and right support roller group is supporting the support steel ring of horizontally-arranged cylinder fermentor tank the right and left.
3. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1, it is characterized in that: difference installation shaft bearing outer-ring in the two ends, the left and right sides of horizontally-arranged cylinder fermentor tank, the left and right sides capping is then installed respectively and is fixed in the bearing inner race, bearing outer ring is fixedlyed connected with the cylinder fermentor tank, and bearing inner race is fixedlyed connected with capping.
4. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1, it is characterized in that: the left support roller group of horizontally-arranged cylinder fermentor tank feed end is an adjustable height support roller group, the feed end of horizontally-arranged cylinder fermentor tank is higher than discharge end, and the axis of cylinder fermentor tank and the angle of horizontal plane are that 0～5 degree is adjustable.
5. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1, it is characterized in that: the right support roller group of horizontally-arranged cylinder fermentor tank discharge end has the backstop wheel.
6. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1, it is characterized in that: coaxial cylindrical heat exchanging water-jacket's coated outside of horizontally-arranged cylinder fermentor tank external device (ED) has thermal insulation layer.
7. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1, it is characterized in that: the supported steel ring of the coaxial cylindrical heat exchanging water-jacket of horizontally-arranged cylinder fermentor tank, external tooth wheel rim have been separated into several parts, the adjacent part coaxial cylindrical heat exchanging water-jacket connect by the water jacket pipe connecting, is linked to be an integral body.
8. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1, it is characterized in that: coaxial cylindrical heat exchanging water-jacket's water jacket water inlet pipe and water jacket rising pipe cause place, cylinder fermentor tank axle center by cylinder fermentor tank inside respectively, the water jacket water inlet pipe connects via the right rotation joint and the circulating water inlet that are installed in place, capping axle center, right side, and the water jacket rising pipe connects via the anticlockwise joint and the circulating water outlet pipe that are installed in place, capping axle center, left side.
9. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1, it is characterized in that: cylinder fermentor tank inside is mounted with the material flight.
10. the horizontally-arranged rolling cylinder formula aerobic fermentation equipment of band thermal exchange according to claim 1 is characterized in that: heat exchanger and gas blower are housed on the inlet pipe of horizontally-arranged cylinder fermentor tank; Another heat exchanger and vacuum fan are housed on the vapor pipe of horizontally-arranged cylinder fermentor tank; Exhaust is sent to deodorizing equipment and is focused under the effect of vacuum fan, non-pollution discharge behind the recovery ammonia nitrogen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120125067XU CN202081031U (en) | 2011-04-26 | 2011-04-26 | Horizontal barrel rolling type aerobic fermentation equipment with heat exchange function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120125067XU CN202081031U (en) | 2011-04-26 | 2011-04-26 | Horizontal barrel rolling type aerobic fermentation equipment with heat exchange function |
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| Publication Number | Publication Date |
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| CN202081031U true CN202081031U (en) | 2011-12-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120125067XU Expired - Lifetime CN202081031U (en) | 2011-04-26 | 2011-04-26 | Horizontal barrel rolling type aerobic fermentation equipment with heat exchange function |
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| Country | Link |
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| CN (1) | CN202081031U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102584373A (en) * | 2012-01-16 | 2012-07-18 | 湖北兴田生物科技有限公司 | Rotary biological fermentation bed of solid organic fertilizer |
| CN102757270A (en) * | 2011-04-26 | 2012-10-31 | 汪深 | Horizontally-arranged cylinder rolling type aerobic fermentation apparatus with heat exchange function |
| CN102924146A (en) * | 2012-12-03 | 2013-02-13 | 北京科技大学 | Movable rotary drum type composting reactor |
| CN102976809A (en) * | 2012-12-07 | 2013-03-20 | 中冶赛迪工程技术股份有限公司 | Planetary type full-automatic sludge aerobic fermentation device and system |
| CN106477840A (en) * | 2016-11-23 | 2017-03-08 | 上海市政工程设计研究总院（集团）有限公司 | A kind of heat pump assists sludge organism drying method |
| CN106746474A (en) * | 2016-11-23 | 2017-05-31 | 上海市政工程设计研究总院（集团）有限公司 | A kind of heat pump aids in sludge organism desiccation apparatus |
| CN109265205A (en) * | 2018-11-14 | 2019-01-25 | 长沙凯天工研院环保服务有限公司 | A kind of twin-roll dual rotary fowl and animal excrement aerobic compost equipment |
| CN111019819A (en) * | 2019-12-10 | 2020-04-17 | 清华大学 | Continuous solid state fermentation reactor with accurate automatic temperature control device |
| CN115025707A (en) * | 2021-03-05 | 2022-09-09 | 宁波格鲁德科技有限公司 | Stirring device with heat dissipation function |
-
2011
- 2011-04-26 CN CN201120125067XU patent/CN202081031U/en not_active Expired - Lifetime
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102757270B (en) * | 2011-04-26 | 2014-06-18 | 湖南深拓智能设备股份有限公司 | Horizontally-arranged cylinder rolling type aerobic fermentation apparatus with heat exchange function |
| CN102757270A (en) * | 2011-04-26 | 2012-10-31 | 汪深 | Horizontally-arranged cylinder rolling type aerobic fermentation apparatus with heat exchange function |
| CN102584373A (en) * | 2012-01-16 | 2012-07-18 | 湖北兴田生物科技有限公司 | Rotary biological fermentation bed of solid organic fertilizer |
| CN102584373B (en) * | 2012-01-16 | 2013-07-31 | 湖北兴田生物科技有限公司 | Rotary biological fermentation bed of solid organic fertilizer |
| CN102924146A (en) * | 2012-12-03 | 2013-02-13 | 北京科技大学 | Movable rotary drum type composting reactor |
| CN102924146B (en) * | 2012-12-03 | 2014-05-07 | 北京科技大学 | Movable rotary drum type composting reactor |
| CN102976809A (en) * | 2012-12-07 | 2013-03-20 | 中冶赛迪工程技术股份有限公司 | Planetary type full-automatic sludge aerobic fermentation device and system |
| CN102976809B (en) * | 2012-12-07 | 2014-10-01 | 中冶赛迪工程技术股份有限公司 | Planetary type full-automatic sludge aerobic fermentation device and system |
| CN106477840A (en) * | 2016-11-23 | 2017-03-08 | 上海市政工程设计研究总院（集团）有限公司 | A kind of heat pump assists sludge organism drying method |
| CN106746474A (en) * | 2016-11-23 | 2017-05-31 | 上海市政工程设计研究总院（集团）有限公司 | A kind of heat pump aids in sludge organism desiccation apparatus |
| CN106477840B (en) * | 2016-11-23 | 2024-05-28 | 上海市政工程设计研究总院（集团）有限公司 | Heat pump assisted sludge biological drying method |
| CN109265205A (en) * | 2018-11-14 | 2019-01-25 | 长沙凯天工研院环保服务有限公司 | A kind of twin-roll dual rotary fowl and animal excrement aerobic compost equipment |
| CN111019819A (en) * | 2019-12-10 | 2020-04-17 | 清华大学 | Continuous solid state fermentation reactor with accurate automatic temperature control device |
| CN115025707A (en) * | 2021-03-05 | 2022-09-09 | 宁波格鲁德科技有限公司 | Stirring device with heat dissipation function |
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