CN206338975U - Cultivation industry fecaluria residual neat recovering system - Google Patents
Cultivation industry fecaluria residual neat recovering system Download PDFInfo
- Publication number
- CN206338975U CN206338975U CN201621233060.9U CN201621233060U CN206338975U CN 206338975 U CN206338975 U CN 206338975U CN 201621233060 U CN201621233060 U CN 201621233060U CN 206338975 U CN206338975 U CN 206338975U
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- CN
- China
- Prior art keywords
- pipeline
- fecaluria
- condenser
- evaporator
- heat
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 206010059410 Faecaluria Diseases 0.000 title claims abstract description 31
- 238000010521 absorption reaction Methods 0.000 claims abstract description 4
- 239000012530 fluid Substances 0.000 claims description 19
- 238000009413 insulation Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 8
- 239000007789 gas Substances 0.000 abstract description 7
- 229910021529 ammonia Inorganic materials 0.000 abstract description 4
- 238000009360 aquaculture Methods 0.000 abstract description 3
- 244000144974 aquaculture Species 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 230000000505 pernicious effect Effects 0.000 abstract description 3
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 239000003507 refrigerant Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241001071864 Lethrinus laticaudis Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241000282887 Suidae Species 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000005108 dry cleaning Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Other Air-Conditioning Systems (AREA)
Abstract
The utility model discloses a kind of cultivation industry fecaluria residual neat recovering system, heat exchange pipeline including being arranged at fecaluria bottom of pond portion, the heat exchange pipeline is connected with the absorption energy source of source pump, and the output energy source of the source pump is connected with the heat supply pipeline in plant；The source pump includes evaporator and condenser, connected between the evaporator and condenser by circulation line, on the circulation line compressor is provided with the outlet side of the evaporator, on the circulation line expansion valve is provided with the outlet side of the condenser, residual neat recovering system disclosed in the utility model comes out the heat exchange in fecaluria pond, the temperature in fecaluria pond is reduced, while decreasing the discharge of the pernicious gases such as ammonia；Swap out the heat come, by related heating facility, is used directly to heat the regional area for needing heat, reduces aquaculture cost.
Description
Technical field
The utility model is related to a kind of residual neat recovering system, more particularly to a kind of cultivation industry fecaluria residual neat recovering system.
Background technology
In cultivation field, feed (or the water the drunk up) major part that animal eats up all can be in the form of excrement (or urine)
Excrete.Domestic cultivation industry, is often directly arranged fecaluria in the form of bubble excrement (water rushes the techniques such as excrement, dry cleaning up excrement)
Go out plant.Because fecaluria storage time is long, temperature is higher, and the pernicious gas such as ammonia of generation just compares many, so
Just necessary stronger ventilation amount, also substantial amounts of to be discharged in the external world inevitably by the heat in plant, so as to cause to waste.
Utility model content
In order to solve the above technical problems, the utility model provide a kind of cultivation industry fecaluria residual neat recovering system, with up to
Come out to by the heat exchange in fecaluria, the purpose for being transported to the region for needing to heat.
To reach above-mentioned purpose, the technical solution of the utility model is as follows：
A kind of cultivation industry fecaluria residual neat recovering system, including it is arranged at the heat exchange pipeline in fecaluria bottom of pond portion, the heat exchange
Pipeline is connected with the absorption energy source of source pump, and the output of the source pump can source and the heat supply pipeline in plant
It is connected；The source pump includes evaporator and condenser, is connected between the evaporator and condenser by circulation line,
It is provided with the circulation line on the outlet side of the evaporator on compressor, the circulation line and is located at the condensation
Expansion valve is provided with the outlet side of device.
In such scheme, the hot fluid in the heat exchange pipeline is input in the evaporator by pipeline, the evaporation
The cold fluid of device output is input in the heat exchange pipeline by pipeline.
In such scheme, the hot fluid of the condenser output is input in the heat supply pipeline by pipeline, described to supply
Cold fluid in hot channel is input in the condenser by pipeline.
In such scheme, the low pressure wet of output becomes high-pressure hot gas entrance after the compressor in the evaporator
In the condenser, the high pressure geothermal liquid of output becomes low pressure cold air described in after the expansion valve in the condenser
In evaporator.
In further technical scheme, heat exchange pipeline and the heat supply pipeline bottom is equipped with heat insulation layer.
By above-mentioned technical proposal, the cultivation industry fecaluria residual neat recovering system that the utility model is provided reduces fecaluria pond
Temperature, reduce the generation of the pernicious gases such as ammonia；Meanwhile, the heat reclaimed from fecaluria pond is delivered directly to needs and added
In other regional areas of heat, waste heat is utilized.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the accompanying drawing to be used needed for description of the prior art is briefly described.
Fig. 1 is schematic layout pattern in the plant disclosed in the utility model embodiment；
Fig. 2 is the source pump signal of the cultivation industry fecaluria residual neat recovering system disclosed in the utility model embodiment
Figure.
In figure, 1, fecaluria pond；2nd, heat exchange pipeline；3rd, source pump；4th, heat supply pipeline；5th, heat insulation layer；6th, evaporator；7th, it is cold
Condenser；8th, compressor；9th, expansion valve.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe.
The utility model provides a kind of cultivation industry fecaluria residual neat recovering system, and structure as depicted in figs. 1 and 2 should
Recovery system advantageously reduces environmental pollution, moreover it is possible to reduce aquaculture cost.
Cultivation industry fecaluria residual neat recovering system as depicted in figs. 1 and 2, including it is arranged at the heat exchange of the bottom of fecaluria pond 1
Pipeline 2, heat exchange pipeline 2 is connected with the absorption energy source A of source pump 3, the output energy source B of source pump 3 and plant
Interior heat supply pipeline 4 is connected.Heat exchange pipeline 2 and the bottom of heat supply pipeline 4 are equipped with heat insulation layer 5.
Source pump 3 includes evaporator 6 and condenser 7, is connected, followed by circulation line between evaporator 6 and condenser 7
It is provided with compressor 8, circulation line and is set on the outlet side of condenser 7 on the outlet side of evaporator 6 on endless tube road
It is equipped with expansion valve 9.
Specific heat transfer process is as follows：
1) in Fig. 2, source pump 3 absorbs energy source A cold fluid, enters the heat exchange pipeline 2 shown in Fig. 1.Due to excrement
The temperature of fluid is higher than the temperature of fluid in heat exchange pipeline 2 in urinal 1, and heat always flows to cryogenic object from high temp objects,
So the heat in fecaluria pond 1 will be exchanged to constantly in the fluid in heat exchange pipeline 2, so as to improve in heat exchange pipeline 2
The temperature of fluid.
2) in Fig. 1, the hot fluid after the heating of heat exchange pipeline 2 is transported in the evaporator 6 of Fig. 2 source pumps 3, and is being steamed
Send out in device 6, exchanged heat with the refrigerant in source pump 3, temperature reduction becomes to absorb energy source A cold fluids again, entered
Into Fig. 1 heat exchange pipeline 2；Low pressure cold air (refrigerant) from Fig. 2 expansion valves 9 out, which absorbs, to be come in flash-pot 6 to swap out
After the heat come, temperature rise becomes low pressure wet (refrigerant).
3) in Fig. 2, low pressure wet (refrigerant) compresses, temperature and pressure is raised through compressor 8, becomes high-pressure hot gas
(refrigerant), after condensed device 7 exchanges heat, high-pressure hot gas (refrigerant) release heat becomes high pressure geothermal liquid (refrigerant), through swollen
After swollen valve 9, it is changed into low pressure cold air (refrigerant) again and enters heat exchange in evaporator 6；And the heat exchanged by condenser 7
Amount, then exported the cold fluid heating that energy source B is input to source pump 3 by source pump 3, then exported with source pump 3
Hot fluid form, is transported in heat supply pipeline 4.
4) in Fig. 2, the hot fluid (output can source B) that source pump 3 is exported, in the heat supply pipeline 4 for entering Fig. 1, by
It is higher than the temperature of external environment in the temperature of heat supply pipeline 4, and heat always flows to cryogenic object from high temp objects, so heat supply
Heat in pipeline 4 will be lost in the environment of surrounding, and the temperature of fluid can also be reduced in pipeline, finally flow again into figure
In 2 source pumps 3 output energy source B condenser 7, circulation is formed.
Embodiment：
Southern XXX boars plant, by sow house, pregnant pig house, plant pig house, nursery house, delivery room, fatten house etc. constitute.Its
Middle sow house, pregnant pig house, plant pig house, fatten house etc. pig house, to external world the requirement of environment temperature be less than nursery house, therefore, we
Can by sow house, pregnant pig house, plant pig house, fatten the heat in pig house fecaluria pond such as house and reclaimed, the heat that will be reclaimed
For improving the temperature of nursery house, it is ensured that the survival rate of piggy.And in fecaluria pond after the temperature reduction of fecaluria, ammonia etc. has
The aerial percentage reduction of evil gas, on the one hand improves the growing environment of pig, reduces disease, reduce the dirt to air
Dye, while ventilation can also be reduced to a certain extent, improves the heat-insulating property of pig house, reduces aquaculture cost.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or new using this practicality
Type.A variety of modifications to these embodiments will be apparent for those skilled in the art, determine herein
The General Principle of justice can in other embodiments be realized in the case where not departing from spirit or scope of the present utility model.Cause
This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein
The most wide scope consistent with features of novelty.
Claims (5)
1. a kind of cultivation industry fecaluria residual neat recovering system, it is characterised in that the heat exchange pipeline including being arranged at fecaluria bottom of pond portion,
The heat exchange pipeline is connected with the absorption energy source of source pump, in the output energy source of the source pump and plant
Heat supply pipeline is connected；The source pump includes evaporator and condenser, passes through circulation between the evaporator and condenser
Pipeline is connected, and is located on the circulation line on the outlet side of the evaporator and is provided with compressor, the circulation line is upper
In being provided with expansion valve on the outlet side of the condenser.
2. cultivation industry fecaluria residual neat recovering system according to claim 1, it is characterised in that in the heat exchange pipeline
Hot fluid is input in the evaporator by pipeline, and the cold fluid of the evaporator output is input to the heat exchange by pipeline
In pipeline.
3. cultivation industry fecaluria residual neat recovering system according to claim 1, it is characterised in that the condenser output
Hot fluid is input in the heat supply pipeline by pipeline, and the cold fluid in the heat supply pipeline is input to described cold by pipeline
In condenser.
4. according to any described cultivation industry fecaluria residual neat recovering systems of claim 1-3, it is characterised in that the evaporator
The low pressure wet of interior output becomes high-pressure hot gas after the compressor and entered in the condenser, is exported in the condenser
High pressure geothermal liquid become low pressure cold air after the expansion valve into the evaporator.
5. cultivation industry fecaluria residual neat recovering system according to claim 1, it is characterised in that the heat exchange pipeline and confession
Hot channel bottom is equipped with heat insulation layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621233060.9U CN206338975U (en) | 2016-11-17 | 2016-11-17 | Cultivation industry fecaluria residual neat recovering system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621233060.9U CN206338975U (en) | 2016-11-17 | 2016-11-17 | Cultivation industry fecaluria residual neat recovering system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206338975U true CN206338975U (en) | 2017-07-18 |
Family
ID=59306945
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621233060.9U Expired - Fee Related CN206338975U (en) | 2016-11-17 | 2016-11-17 | Cultivation industry fecaluria residual neat recovering system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206338975U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107318663A (en) * | 2017-09-01 | 2017-11-07 | 农业部环境保护科研监测所 | Cattle farm thermoregulating system and cattle farm |
-
2016
- 2016-11-17 CN CN201621233060.9U patent/CN206338975U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107318663A (en) * | 2017-09-01 | 2017-11-07 | 农业部环境保护科研监测所 | Cattle farm thermoregulating system and cattle farm |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170718 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |