CN204787420U - Antithetical couplet that utilizes biomass power generation supplies system - Google Patents
Antithetical couplet that utilizes biomass power generation supplies system Download PDFInfo
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- CN204787420U CN204787420U CN201520503365.6U CN201520503365U CN204787420U CN 204787420 U CN204787420 U CN 204787420U CN 201520503365 U CN201520503365 U CN 201520503365U CN 204787420 U CN204787420 U CN 204787420U
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- 238000010248 power generation Methods 0.000 title claims abstract description 64
- 239000002028 Biomass Substances 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 238000006243 chemical reaction Methods 0.000 claims abstract description 4
- 238000010438 heat treatment Methods 0.000 claims description 27
- 238000005057 refrigeration Methods 0.000 claims description 17
- 238000009413 insulation Methods 0.000 claims description 8
- 230000005619 thermoelectricity Effects 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 22
- 238000000855 fermentation Methods 0.000 abstract description 16
- 230000004151 fermentation Effects 0.000 abstract description 10
- 239000002351 wastewater Substances 0.000 abstract description 9
- 239000010828 animal waste Substances 0.000 abstract description 7
- 239000002699 waste material Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 210000002700 urine Anatomy 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 38
- 238000000034 method Methods 0.000 description 8
- 238000002485 combustion reaction Methods 0.000 description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 6
- 239000002689 soil Substances 0.000 description 6
- 235000013311 vegetables Nutrition 0.000 description 5
- 241001465754 Metazoa Species 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 239000003337 fertilizer Substances 0.000 description 4
- 230000012010 growth Effects 0.000 description 4
- 230000005611 electricity Effects 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 230000008635 plant growth Effects 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Natural products CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 210000003608 fece Anatomy 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- 230000029553 photosynthesis Effects 0.000 description 2
- 238000010672 photosynthesis Methods 0.000 description 2
- 244000144977 poultry Species 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 208000034809 Product contamination Diseases 0.000 description 1
- 241001464837 Viridiplantae Species 0.000 description 1
- 238000003975 animal breeding Methods 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 229940059936 lithium bromide Drugs 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 210000004681 ovum Anatomy 0.000 description 1
- 230000003071 parasitic effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 210000004243 sweat Anatomy 0.000 description 1
- -1 toluene organic compound Chemical class 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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
- Y02A40/25—Greenhouse technology, e.g. cooling systems therefor
-
- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
-
- 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
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/14—Measures for saving energy, e.g. in green houses
-
- 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
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
-
- 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
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/30—Use of alternative fuels, e.g. biofuels
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- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The utility model discloses an antithetical couplet that utilizes biomass power generation supplies system, including energy collecting device, anaerobic fermentation device, nature gas power generation system, the energy collecting device output with the input of anaerobic fermentation device is connected, the output of anaerobic fermentation device with the air inlet of nature gas power generation system is connected, the nature gas power generation system pass through thermoelectric conversion with the electric energy that produces export for energy collecting device. The excrement and urine and the waste water that produce in the plant emit into natural fermentation carries out in the anaerobic fermentation device, so can the significantly reduce emission of animal waste and waste water, the pollution abatement promotes the improvement of air quality and quality of water. A large amount of marsh gas that produce after the fermentation get into in the nature gas power generation system, through the power access of thermoelectric conversion reaction back production in the plant, can satisfy the inside power consumption demand of plant, and not need external power, both can realize salvaging, changing waste into valuables, save the energy again.
Description
Technical field
The utility model relates to a kind of co-feeding system utilizing biomass power generation.
Background technology
At a lot of plants periphery, in order to local use feces of livestock and poultry, be often provided with crops base or green house of vegetables.But only using feces of livestock and poultry simply as Crop fertilizer, not only treating capacity can not meet the ight soil discharge of plant, and easily cause the pollution such as water, air, simultaneously the whole outer confession of the energy of plant, electricity needs is large.By ight soil by anaerobic fermentation, both created biogas, also can be used as fertilizer, and by fermentation after, most parasitic ovum is killed, and can improve the sanitary condition of plant, reduces the infection of disease.Therefore, the biogas research on utilization of animal wastes achieves significant progress in recent years.
Organic matter in anaerobe decomposing biomass can produce a large amount of biogas, and in the composition of biogas, methane accounts for 50%-70%, and all the other are carbon dioxide and a small amount of hydrogen sulfide etc., comprises the non-methane such as ethane, toluene organic compound in addition.Biogas is a kind of inflammable, explosive toxic gas, and it directly enters air by serious harm health, welding aggravate greenhouse effects.Simultaneously, biogas is as the typical biogas regenerative resource of one, there is the advantages such as combustion product contamination is little, 1 cubic metre of complete Combustion Energy of biogas produces the heat being equivalent to 0.7 kilogram of anthracite and providing, utilize marsh gas power generation not only can solve electricity shortage problem, can reduce again methane isothermal chamber gas purging, purify air environment.Moreover, cooling heating and power generation system is a kind of supply system be based upon on cascaded utilization of energy conceptual foundation, its maximum feature can realize comprehensive cascade utilization to the heat energy of different grade, complete generating, refrigeration and heat supply (comprising for warm hot water) three processes simultaneously, meet hot and cold, the electric demand of user on the spot, thus reduce the transmission loss of remote energy supply, improve economic results in society and efficiency of energy utilization greatly.Therefore, in field, rural culture etc., there is the place of enriching biogas resource and promote the use of biogas cooling heating and power generation system, to promotion agricultural restructuring and building a New Socialist Countryside significant.
The smoke evacuation of gas internal-combustion engine drives lithium-bromide absorption-type refrigerating machine as high temperature heat source, and for refrigeration or heat supply, the jacket water of internal combustion engine also can produce domestic hot-water.But generator in existing internal combustion engine generator group is mostly air-cooled by fan, generator used heat is carried away by the wind, be difficult to recycle, thus fail at utmost to show the energy conservation characteristic of co-feeding system, and not yet find to take biomass marsh gas as the design that the cool and thermal power of motive drive source plants co-feeding system and waste heat recovery, water circulation uses at present.
Summary of the invention
Based on this, the utility model is the defect overcoming prior art, provide a kind of reduce animal wastes and waste water discharge and pollution, minimizing cost and a kind of cool and thermal power of marsh gas power generation that utilizes of improving working environment can plant co-feeding system.
The technical solution of the utility model is as follows:
A kind of co-feeding system utilizing biomass power generation, comprise energy collecting device, anaerobic ferment devices, gas power generation system, described energy collecting device output is connected with the input of described anaerobic ferment devices, the output of described anaerobic ferment devices is connected with the air inlet of described gas power generation system, and the electric energy of generation is exported to described energy collecting device by thermoelectricity conversion by described gas power generation system.
Also comprise denitrification apparatus, refrigerating plant and the first backwater booster, the air inlet of described denitrification apparatus is connected with the gas outlet of described gas power generation system, the gas outlet of described denitrification apparatus is connected with the air inlet of described refrigerating plant, the delivery port of described refrigerating plant is connected with the water inlet of described energy collecting device, and water inlet and the delivery port of described first backwater booster are connected with the delivery port of described energy collecting device, the water inlet of described refrigerating plant respectively.
Also comprise heat-exchanger rig and plant booth, the air inlet of described heat-exchanger rig is connected with the gas outlet of described refrigerating plant, and the gas outlet of described heat-exchanger rig is communicated with the inside of described plant booth.
Also comprise the second backwater booster, the water inlet of described second backwater booster is connected with the delivery port of described anaerobic ferment devices, the delivery port of described second backwater booster is connected with the water inlet of described gas power generation system, described gas power generation system is provided with jacket water heat exchanger, and the insulation hot water produced in described gas power generation system flows into described anaerobic ferment devices by the delivery port of jacket water heat exchanger.
The input of described plant booth is connected with the output of described anaerobic ferment devices.
Described energy collecting device comprises refrigeration plant, heating equipment, and described refrigeration plant and described heating equipment are connected with the sending end of described gas power generation system respectively.
Also comprise normal-temperature water feedway and hot water supply apparatus, the delivery port of described normal-temperature water feedway is connected with the water inlet of described heat-exchanger rig, and the delivery port of described heat-exchanger rig is connected with the water inlet of described hot water supply apparatus.
The beneficial effects of the utility model are:
1) animal wastes and waste water are input to described anaerobic ferment devices by power supply device, by anaerobic fermentation technology, animal wastes and waste water are processed, waste discharge can be reduced, not only can promote the improvement of air quality and water quality, the biogas produced after process can also as the fuel of gas power generation system, realize twice laid, thus save the energy.
2) by the distributed energy supply arrangement mode of the devices such as denitrification apparatus, refrigeration plant, heat-exchanger rig, can realize the supply of cooling, heating and electrical powers of plant, the heat that system self produces also can meet the insulation of anaerobic ferment devices, greatly reduces with energy cost.
3) the animal wastes residue after anaerobic fermentation process drains into green plants booth, can as the fertilizer of plant, supply plant growth, and the flue gas simultaneously after denitration process and heat exchange cooling is mainly CO
2and N
2, they are drained into plant booth, can promote that plant carries out photosynthesis.
4) by the refrigeration plant installed in described energy collecting device and heating equipment, by the electric power that described gas power generation system provides, can be animal in plant and staff's refrigeration or heating in summer or winter, to provide good growth and working environment.
Accompanying drawing explanation
Fig. 1 plants co-feeding system structural representation for the cool and thermal power of marsh gas power generation that utilizes described in the utility model preferred embodiment one;
Fig. 2 plants co-feeding system structural representation for the cool and thermal power of marsh gas power generation that utilizes described in the utility model preferred embodiment two.
Description of reference numerals:
100, energy collecting device, 110, anaerobic ferment devices, 120, gas power generation system, 130, denitrification apparatus, 140, refrigerating plant, 150, heat-exchanger rig, 160, plant booth, 170, the second backwater booster, the 180, first backwater booster, 190, ight soil and waste water, 200, biogas, 210, high-temperature flue gas, 220, low-temperature flue gas, 230, CO
2and N
2, 250, chilled water/heating hot water, 260, chilled water backwater/heating hot water backwater, 270, insulation hot water, 280, insulation hot water backwater, 290, residue, 300, running water, 310, domestic hot-water.
Detailed description of the invention
Below embodiment of the present utility model is described in detail:
As shown in Figure 1, the cool and thermal power of marsh gas power generation that utilizes described in the utility model preferred embodiment one plants co-feeding system structural representation.A kind of co-feeding system utilizing biomass power generation, comprise energy collecting device 100, anaerobic ferment devices 110, gas power generation system 120, described energy collecting device 100 output is connected with the input of described anaerobic ferment devices 110, the output of described anaerobic ferment devices 110 is connected with the air inlet of described gas power generation system 120, and the electric energy of generation is exported to described energy collecting device 100 by thermoelectricity conversion by described gas power generation system 120.
Above-mentioned energy collecting device is animal-breeding field, the ight soil produced in described plant and waste water 190 are drained in described anaerobic ferment devices 110 and carry out spontaneous fermentation, so can greatly reduce the discharge of animal wastes and waste water, decreasing pollution, promote the improvement of air quality and water quality.The a large amount of biogas 200 produced after fermentation enter in described gas power generation system 120, access in described plant by the electric power produced after thermoelectricity conversion reaction, the need for electricity of plant inside can be met, and do not need externally fed, namely can realize twice laid, turn waste into wealth, in turn save the energy.Gas power generation system described in the utility model is preferably internal combustion engine, what preferably adopt in embodiment two is miniature combustion engine, can also be that other anyly reach the equipment identical with the utility model technique effect in other embodiments, the arrow that described gas power generation system 120 points to described energy collecting device 100 represents the direction of electric power conveying.
Described energy collecting device 100 comprises refrigeration plant, heating equipment, and described refrigeration plant and described heating equipment are connected with the sending end of described gas power generation system 120 respectively.By refrigeration plant and the heating equipment of installation in described energy collecting device 100, by the electric power that described gas power generation system 120 provides, can be animal in plant and staff's refrigeration or heating in summer or winter, to provide good growth and working environment.
The above-mentioned co-feeding system of biomass power generation that utilizes also comprises denitrification apparatus 130, refrigerating plant 140 and the first backwater booster 180, the air inlet of described denitrification apparatus 130 is connected with the gas outlet of described gas power generation system 120, the gas outlet of described denitrification apparatus 130 is connected with the air inlet of described refrigerating plant 140, the delivery port of described refrigerating plant 140 is connected with the water inlet of described energy collecting device 100, the water inlet of described first backwater booster 180 and delivery port respectively with the delivery port of described energy collecting device 100, the water inlet of described refrigerating plant 140 connects.
The high-temperature flue gas 210 that described gas power generation system 120 produces is after described denitrification apparatus 130 denitration process, enter into described refrigerating plant 140, chilled water/heating hot water 250 can be provided for plant in summer or winter after being processed by described refrigerating plant 140, in conjunction with refrigeration plant and the heating equipment of plant inside, to meet the refrigeration and heating demand of plant, also good growing environment is provided for animals while improving the working environment of workman, in addition, the heating installation that described refrigerating plant produces can also be the vegetables heating in plant booth 160, ensure the normal growth of vegetables.Chilled water backwater/heating hot water backwater 260 that plant and plant booth use flows back into described refrigerating plant 140 by the first backwater booster and recycles.
The described co-feeding system of biomass power generation that utilizes also comprises heat-exchanger rig 150 and plant booth 160, the air inlet of described heat-exchanger rig 150 is connected with the gas outlet of described refrigerating plant 140, and the gas outlet of described heat-exchanger rig 150 is communicated with the inside of described plant booth 160.Low-temperature flue gas 220 main component after denitrification apparatus 130 and heat-exchanger rig 150 process is CO
2and N
2230, directly enter in described plant booth 160, can promote that the plant in booth carries out photosynthesis, make plant obtain the required nutrient that grows, the growth of plant is better more.The input of described plant booth 160 is connected with the output of described anaerobic ferment devices 110.In described anaerobic ferment devices 110, the rear ight soil residue 290 produced of process is discharged in described plant booth 160 by fermentation, can as the fertilizer of plant, Promoting plant growth.
The above-mentioned co-feeding system of biomass power generation that utilizes also comprises the second backwater booster 170, the water inlet of described second backwater booster 170 is connected with the delivery port of described anaerobic ferment devices 110, the delivery port of described second backwater booster 170 is connected with the water inlet of described gas power generation system 120, described gas power generation system 120 is provided with jacket water heat exchanger, and the insulation hot water 270 produced in described gas power generation system 120 flows into described anaerobic ferment devices 110 by the delivery port of jacket water heat exchanger.The insulation hot water 270 that described gas power generation system 120 produces flows in described anaerobic ferment devices 110, the thermal environment needed for fermentation process provides required heat, make the sweat of ight soil and waste water 190 more complete, thus produce more biogas supply generating.
The above-mentioned co-feeding system of biomass power generation that utilizes also comprises normal-temperature water feedway and hot water supply apparatus, the delivery port of described normal-temperature water feedway is connected with the water inlet of described heat-exchanger rig 150, and the delivery port of described heat-exchanger rig 150 is connected with the water inlet of described hot water supply apparatus.The running water 300 that described normal-temperature water feedway provides, after the process of described heat-exchanger rig 150, enters described hot water supply apparatus and accumulates for domestic hot-water, and can provide hot water needed for life for the people, be that cost is saved in the life of the people.
As shown in Figure 2, the cool and thermal power of marsh gas power generation that utilizes described in the utility model preferred embodiment two plants co-feeding system structural representation.The present embodiment two is with the difference of above-described embodiment one, the gas outlet of described gas power generation system 120 is directly connected with the air inlet of described refrigerating plant 140, the delivery port of described refrigerating plant 140 is connected with the water inlet of described energy collecting device 100, and water inlet and the delivery port of described first backwater booster 180 are connected with the delivery port of described energy collecting device 100, the water inlet of described refrigerating plant 140 respectively.
The high-temperature flue gas 210 that described gas power generation system 120 produces directly enters into described refrigerating plant 140, chilled water/heating hot water 250 can be provided for plant in summer or winter after being processed by described refrigerating plant 140, in conjunction with refrigeration plant and the heating equipment of plant inside, to meet the refrigeration and heating demand of plant, also good growing environment is provided for animals while improving the working environment of workman, while the beneficial effect that the technical scheme that the technical program can not only reach embodiment one reaches, whole system can also be made simpler.In addition, the heating installation that described refrigerating plant produces can also be the vegetables heating in plant booth 160, ensures the normal growth of vegetables.Chilled water backwater/heating hot water backwater 260 that plant and plant booth use flows back into described refrigerating plant 140 by the first backwater booster and recycles.
The water inlet of described anaerobic ferment devices 110 is directly connected with the delivery port of described hot water supply apparatus, and the domestic hot-water 310 exported by described hot water supply apparatus is directly supplied to described anaerobic ferment devices 110, maintains the heat needed for good fermentation.Meanwhile, the delivery port of described anaerobic ferment devices 110 is connected with the water inlet of described second backwater booster 170, and the delivery port of described second backwater booster is connected with the delivery port of described normal-temperature water feedway.The insulation hot water 270 maintained needed for fermentation used in anaerobic ferment devices 110 can reflux to described normal-temperature water feedway by described second backwater booster 170 by this technical scheme, water source can be provided for described normal-temperature water feedway, to reduce extra running water quantity delivered, save the operating cost of system.
Each technical characteristic of the above embodiment can combine arbitrarily, for making description succinct, the all possible combination of each technical characteristic in above-described embodiment is not all described, but, as long as the combination of these technical characteristics does not exist contradiction, be all considered to be the scope that this description is recorded.
The above embodiment only have expressed several embodiment of the present utility model, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to utility model patent scope.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.Therefore, the protection domain of the utility model patent should be as the criterion with claims.
Claims (7)
1. one kind utilizes the co-feeding system of biomass power generation, it is characterized in that, comprise energy collecting device, anaerobic ferment devices, gas power generation system, described energy collecting device output is connected with the input of described anaerobic ferment devices, the output of described anaerobic ferment devices is connected with the air inlet of described gas power generation system, and the electric energy of generation is exported to described energy collecting device by thermoelectricity conversion by described gas power generation system.
2. utilize the co-feeding system of biomass power generation according to claim 1, it is characterized in that, also comprise denitrification apparatus, refrigerating plant and the first backwater booster, the air inlet of described denitrification apparatus is connected with the gas outlet of described gas power generation system, the gas outlet of described denitrification apparatus is connected with the air inlet of described refrigerating plant, the delivery port of described refrigerating plant is connected with the water inlet of described energy collecting device, and water inlet and the delivery port of described first backwater booster are connected with the delivery port of described energy collecting device, the water inlet of described refrigerating plant respectively.
3. utilize the co-feeding system of biomass power generation according to claim 1, it is characterized in that, also comprise heat-exchanger rig and plant booth, the air inlet of described heat-exchanger rig is connected with the gas outlet of described refrigerating plant, and the gas outlet of described heat-exchanger rig is communicated with the inside of described plant booth.
4. utilize the co-feeding system of biomass power generation according to claim 1, it is characterized in that, also comprise the second backwater booster, the water inlet of described second backwater booster is connected with the delivery port of described anaerobic ferment devices, the delivery port of described second backwater booster is connected with the water inlet of described gas power generation system, described gas power generation system is provided with jacket water heat exchanger, and the insulation hot water produced in described gas power generation system flows into described anaerobic ferment devices by the delivery port of jacket water heat exchanger.
5. utilize the co-feeding system of biomass power generation according to claim 3, it is characterized in that, the input of described plant booth is connected with the output of described anaerobic ferment devices.
6. according to claim 1 or 5, utilize the co-feeding system of biomass power generation, it is characterized in that, described energy collecting device comprises refrigeration plant, heating equipment, and described refrigeration plant and described heating equipment are connected with the sending end of described gas power generation system respectively.
7. utilize the co-feeding system of biomass power generation according to claim 1, it is characterized in that, also comprise normal-temperature water feedway and hot water supply apparatus, the delivery port of described normal-temperature water feedway is connected with the water inlet of described heat-exchanger rig, and the delivery port of described heat-exchanger rig is connected with the water inlet of described hot water supply apparatus.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104990306A (en) * | 2015-07-13 | 2015-10-21 | 中国能源建设集团广东省电力设计研究院有限公司 | Cogeneration system for generating power through biomass |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104990306A (en) * | 2015-07-13 | 2015-10-21 | 中国能源建设集团广东省电力设计研究院有限公司 | Cogeneration system for generating power through biomass |
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