CN214371109U - Liquid energy source base station - Google Patents
Liquid energy source base station Download PDFInfo
- Publication number
- CN214371109U CN214371109U CN202120001631.0U CN202120001631U CN214371109U CN 214371109 U CN214371109 U CN 214371109U CN 202120001631 U CN202120001631 U CN 202120001631U CN 214371109 U CN214371109 U CN 214371109U
- Authority
- CN
- China
- Prior art keywords
- energy
- pipeline
- inlet
- outlet
- dividing
- Prior art date
- 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
- 239000007788 liquid Substances 0.000 title claims abstract description 44
- 238000004146 energy storage Methods 0.000 claims abstract description 65
- 230000001502 supplementing effect Effects 0.000 claims description 14
- 238000009826 distribution Methods 0.000 claims description 12
- 230000000295 complement effect Effects 0.000 claims description 11
- 230000005540 biological transmission Effects 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 239000012530 fluid Substances 0.000 abstract 2
- 238000005265 energy consumption Methods 0.000 abstract 1
- 230000003044 adaptive effect Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000008676 import Effects 0.000 description 4
- 238000010248 power generation Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000011031 large-scale manufacturing process Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 206010063385 Intellectualisation Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
Images
Classifications
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Abstract
The utility model provides a liquid energy basic station, energy storage system's fluid energy is by the internal circulation system hydrologic cycle more than 2 respectively, internal circulation system fluid energy carries out the energy exchange through heat exchanger and energy consumption system liquid, and this basic station scientific and reasonable, simple and practical high efficiency has realized the scale production.
Description
Technical Field
The utility model relates to a liquid energy basic station in liquid cold, heat energy application trade.
Background
In the market, in the liquid cold and heat energy application industry, for example, freeze filtration, liquid evaporation, gas cooling and the like are mostly one-to-one energy utilization, the scale is small, centralized management cannot be realized, the process is complicated, and the traditional technology cannot meet the requirement of large-scale production and needs to be improved.
Disclosure of Invention
In order to solve the problem, the utility model aims at providing a liquid energy basic station of easy operation, easy-to-use, this basic station scientific and reasonable, simple and practical high-efficient has realized large-scale production.
The utility model provides a liquid energy source base station, the liquid energy of an energy storage system is respectively circulated by more than two internal circulation systems, and the liquid energy of the internal circulation systems exchanges energy with the liquid of an energy utilization system through a heat exchanger; the energy storage system stores energy, energy division application is carried out through the first internal circulation system and the first energy utilization system, energy division application is carried out through the second internal circulation system and the second energy utilization system, and the third internal circulation system is similar to the N.
A liquid energy source base station, for example, with 2 internal circulation systems, includes: the energy storage system, the first internal circulation system, the first energy utilization system, the second internal circulation system and the second energy utilization system are formed by respectively connecting an energy storage tank, a circulating energy storage pump, a power generation device, a first energy distribution tank, a first energy distribution circulating pump, a first energy exchanger, a first heat exchanger, a first outer transmission pipeline, a first inner circulating pump, a second energy distribution tank, a second energy distribution circulating pump, a second energy exchanger, a second heat exchanger, a second outer transmission pipeline and a second inner circulating pump through pipelines;
the energy storage system comprises: the first liquid outlet of the energy storage tank is connected with the inlet of the circulating energy storage pump through a pipeline, the inlet of the energy generating device is connected with the outlet of the circulating energy storage pump through a pipeline, and the outlet of the energy generating device is connected with the first inlet of the energy storage tank through a pipeline;
the first internal circulation system: the second liquid outlet of the energy storage tank is connected with the inlet of the first internal circulating pump through a pipeline, the energy supplementing inlet of the first heat exchanger is connected with the outlet of the first internal circulating pump through a pipeline, and the energy supplementing outlet of the first heat exchanger is connected with the second inlet of the energy storage tank through a pipeline;
the first energy usage system: an inlet of the first energy-dividing tank is connected with an energy-collecting outlet of the first heat exchanger through a pipeline, an inlet of the first energy-dividing circulating pump is connected with a liquid outlet of the first energy-dividing tank through a pipeline, an energy-compensating inlet of the first energy exchanger is connected with an outlet of the first energy-dividing circulating pump through a pipeline, an energy-compensating outlet of the first energy exchanger is connected with an energy-collecting inlet of the first heat exchanger through a pipeline, and a first external conveying pipeline is connected with an energy-collecting inlet and an energy-collecting outlet of the first energy exchanger;
the second internal circulation system: the third liquid outlet of the energy storage tank is connected with the inlet of the second internal circulating pump through a pipeline, the energy supplementing inlet of the second heat exchanger is connected with the outlet of the second internal circulating pump through a pipeline, and the energy supplementing outlet of the second heat exchanger is connected with the third inlet of the energy storage tank through a pipeline;
the second energy usage system: the inlet of the second energy-dividing tank is connected with the complementary energy outlet of the second heat exchanger through a pipeline, the inlet of the second energy-dividing circulating pump is connected with the liquid outlet of the second energy-dividing tank through a pipeline, the complementary energy inlet of the second energy exchanger is connected with the outlet of the second energy-dividing circulating pump through a pipeline, the complementary energy outlet of the second energy exchanger is connected with the complementary energy inlet of the second heat exchanger through a pipeline, and the complementary energy inlet of the second energy exchanger is connected with the complementary energy inlet of the second heat exchanger through a second external transmission pipeline.
The energy storage tank is not limited to one, and more than two energy storage tanks can be connected in series or in parallel and are designed according to working conditions.
The number of the energy storage systems is not limited to 1, and more than two energy storage systems can be selected to be connected in series or in parallel according to working condition adaptive design, and pipelines are adaptive to pumps and valves.
The energy production device is designed according to the adaptive requirements of working conditions, a heat energy system can be designed by using heat energy, and a cold energy system can be designed by using cold energy.
The energy of the energy storage system conducts the liquid and is selected adaptively according to working condition requirements.
Specifically, the equipment condition is checked before the equipment is operated, all processes before the equipment is started are completed, then the energy storage system is started to store the energy of the energy storage tank liquid, the first internal circulation system and the first energy utilization system, and the second internal circulation system and the second energy utilization system are respectively started to carry out energy distribution application according to production requirements after working condition requirements are met, the first internal circulation system is adaptively adjusted according to the energy temperature requirement of the first energy utilization system, and the second internal circulation system is adaptively adjusted according to the energy temperature requirement of the second energy utilization system; when heat energy is adopted, the energy utilization temperature of the first energy utilization system and the second energy utilization system is not higher than the temperature of the liquid energy storage of the energy storage tank; when cold energy is adopted, the energy utilization temperature of the first energy utilization system and the second energy utilization system is not lower than the temperature of the energy storage of the liquid of the energy storage tank.
The process of the liquid energy base station with 3, 4 and 5 … … internal circulation systems is the same.
Drawings
Fig. 1 is the utility model discloses a liquid energy base station schematic diagram, energy storage tank P1, circulation energy storage pump P2, power generation device P3, first branch can jar A1, first branch can circulating pump A2, first can interchanger A3, first outer defeated pipeline A4, first heat exchanger A5, first interior circulating pump A6, second branch can jar B1, second branch can circulating pump B2, second can interchanger B3, second outer defeated pipeline B4, second heat exchanger B5, second interior circulating pump B6.
Detailed Description
The present invention will now be described in further detail with reference to the attached drawings and the above description of the invention. The utility model provides a liquid energy basic station to a liquid energy basic station of 2 inner circulating system as an example includes: the energy storage system comprises an energy storage tank P1, a circulating energy storage pump P2, a power generation device P3, a first energy dividing tank A1, a first energy dividing circulating pump A2, a first energy exchanger A3, a first external transmission pipeline A4, a first heat exchanger A5, a first internal circulating pump A6, a second energy dividing tank B1, a second energy dividing circulating pump B2, a second energy exchanger B3, a second external transmission pipeline B4, a second heat exchanger B5 and a second internal circulating pump B6 which are respectively connected through pipelines to form an energy storage system, a first internal circulating system, a first energy utilization system, a second internal circulating system and a second energy utilization system;
the energy storage system comprises: the first liquid outlet of the energy storage tank P1 is connected with the inlet of the circulating energy storage pump P2 through a pipeline, the inlet of the energy generating device P3 is connected with the outlet of the circulating energy storage pump P2 through a pipeline, and the outlet of the energy generating device P3 is connected with the first inlet of the energy storage tank P1 through a pipeline;
the first internal circulation system: the second liquid outlet of the energy storage tank P1 is connected with the inlet of the first internal circulating pump A6 through a pipeline, the energy supplementing inlet of the first heat exchanger A5 is connected with the outlet of the first internal circulating pump A6 through a pipeline, and the energy supplementing outlet of the first heat exchanger A5 is connected with the second inlet of the energy storage tank P1 through a pipeline;
the first energy usage system: an inlet of the first energy dividing tank A1 is connected with an energy collecting outlet of the first heat exchanger A5 through a pipeline, an inlet of the first energy dividing circulating pump A2 is connected with a liquid outlet of the first energy dividing tank A1 through a pipeline, an energy supplementing inlet of the first energy exchanger A3 is connected with an outlet of the first energy dividing circulating pump A2 through a pipeline, an energy supplementing outlet of the first energy exchanger A3 is connected with an energy collecting inlet of the first heat exchanger A5 through a pipeline, and the first outward conveying pipeline A4 is connected with an energy collecting inlet and an energy collecting outlet of the first energy exchanger A3;
the second internal circulation system: a third liquid outlet of the energy storage tank P1 is connected with an inlet of the second internal circulating pump B6 through a pipeline, an energy supplementing inlet of the second heat exchanger B5 is connected with an outlet of the second internal circulating pump B6 through a pipeline, and an energy supplementing outlet of the second heat exchanger B5 is connected with a third inlet of the energy storage tank P1 through a pipeline;
the second energy usage system: second energy distribution jar B1 import pass through the pipeline with second heat exchanger B5 can adopt the exit linkage, second energy distribution circulating pump B2 import pass through the pipeline with second energy distribution jar B1 liquid outlet connects, second energy exchanger B3 can the energy supply import pass through the pipeline with second energy distribution circulating pump B2 exit linkage, second energy exchanger B3 can the energy supply export pass through the pipeline with second heat exchanger B5 can adopt the energy access linkage, second outer defeated pipeline B4 connects second energy exchanger B3's can the energy of adopting import and export.
The number of the energy storage tanks P1 is not limited to one, and more than two energy storage tanks P1 can be connected in series or in parallel according to adaptive design of working conditions.
The number of the energy storage systems is not limited to 1, and more than two energy storage systems can be selected to be designed in series or in parallel according to working conditions.
The energy production device P3 is designed according to the working condition requirement, the heating system can be designed by using heat energy, and the refrigerating system can be designed by using cold energy.
The energy of the energy storage system conducts the liquid and is selected adaptively according to the working condition requirement; and the tank body is adaptive to heat preservation.
The valve, the sensor and the like are adapted according to the system requirements, and automation and intellectualization can be realized.
Specifically, the equipment condition is checked before the equipment is operated, all processes before the equipment is started are completed, then the energy storage system is started to store the energy of the energy storage tank liquid, the first internal circulation system and the first energy utilization system, and the second internal circulation system and the second energy utilization system are respectively started to carry out energy distribution application according to production requirements after working condition requirements are met, the first internal circulation system is adaptively adjusted according to the energy temperature requirement of the first energy utilization system, and the second internal circulation system is adaptively adjusted according to the energy temperature requirement of the second energy utilization system; when heat energy is adopted, the energy utilization temperature of the first energy utilization system and the second energy utilization system is not higher than the temperature of the liquid energy storage of the energy storage tank; when cold energy is adopted, the energy utilization temperature of the first energy utilization system and the second energy utilization system is not lower than the temperature of the energy storage of the liquid of the energy storage tank.
The first external transmission pipeline A4 and the second external transmission pipeline B4 are connected according to the adaptive design of working condition requirements; the first outer conveying pipeline A4 and the second outer conveying pipeline B4 are adapted to convey gaseous substances or liquid substances according to working conditions.
3, 4 and 5 liquid energy base stations of the … … internal circulation system have the same process and are adapted to meet the requirements of the internal circulation system on different temperatures according to working conditions.
The utility model discloses beneficial effect, this technology scientific and reasonable, simple and practical high-efficient has realized scale production.
Claims (3)
1. A liquid energy source base station, comprising: the energy storage system, the first internal circulation system, the first energy utilization system, the second internal circulation system and the second energy utilization system are connected in sequence through pipelines;
the first internal circulation system and the second internal circulation system exchange energy with the first energy utilization system and the second energy utilization system through heat exchangers respectively;
the energy storage system stores energy, and energy division application is carried out through the first internal circulation system and the first energy utilization system, and energy division application is carried out through the second internal circulation system and the second energy utilization system.
2. The energy base station of claim 1, comprising:
the energy storage system comprises an energy storage tank, a circulating energy storage pump and a capacity device; the first liquid outlet of the energy storage tank is connected with the inlet of the circulating energy storage pump through a pipeline, the inlet of the energy generating device is connected with the outlet of the circulating energy storage pump through a pipeline, and the outlet of the energy generating device is connected with the first inlet of the energy storage tank through a pipeline.
3. The energy base station of claim 2, comprising:
the first internal circulation system comprises a first energy-dividing circulation pump, a first heat exchanger and a first internal circulation pump;
a second liquid outlet of the energy storage tank is connected with an inlet of the first internal circulation pump through a pipeline, an energy supplementing inlet of the first heat exchanger is connected with an outlet of the first internal circulation pump through a pipeline, and an energy supplementing outlet of the first heat exchanger is connected with a second inlet of the energy storage tank through a pipeline;
the first energy utilization system comprises a first energy distribution tank, a first output pipeline and a first energy exchanger; an inlet of the first energy-dividing tank is connected with an energy-collecting outlet of the first heat exchanger through a pipeline, an inlet of the first energy-dividing circulating pump is connected with an outlet of liquid of the first energy-dividing tank through a pipeline, an energy-supplementing inlet of the first energy exchanger is connected with an outlet of the first energy-dividing circulating pump through a pipeline, an energy-supplementing outlet of the first energy exchanger is connected with an energy-collecting inlet of the first heat exchanger through a pipeline, and a first output pipeline is connected with an energy-collecting inlet and an energy-collecting outlet of the first energy exchanger;
the second internal circulation system comprises a second energy-dividing circulation pump, a second heat exchanger and a second internal circulation pump; a third liquid outlet of the energy storage tank is connected with an inlet of the second internal circulating pump through a pipeline, an energy supplementing inlet of the second heat exchanger is connected with an outlet of the second internal circulating pump through a pipeline, and an energy supplementing outlet of the second heat exchanger is connected with a third inlet of the energy storage tank through a pipeline;
the second energy utilization system comprises a second energy distribution tank, a second external transmission pipeline and a second energy exchanger; the inlet of the second energy-dividing tank is connected with the complementary energy outlet of the second heat exchanger through a pipeline, the inlet of the second energy-dividing circulating pump is connected with the liquid outlet of the second energy-dividing tank through a pipeline, the complementary energy inlet of the second energy-dividing exchanger is connected with the outlet of the second energy-dividing circulating pump through a pipeline, the complementary energy outlet of the second energy-dividing exchanger is connected with the complementary energy inlet of the second heat exchanger through a pipeline, and the second external pipeline is connected with the complementary energy inlet and outlet of the second energy-dividing exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120001631.0U CN214371109U (en) | 2021-01-04 | 2021-01-04 | Liquid energy source base station |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120001631.0U CN214371109U (en) | 2021-01-04 | 2021-01-04 | Liquid energy source base station |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214371109U true CN214371109U (en) | 2021-10-08 |
Family
ID=77953647
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120001631.0U Expired - Fee Related CN214371109U (en) | 2021-01-04 | 2021-01-04 | Liquid energy source base station |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214371109U (en) |
-
2021
- 2021-01-04 CN CN202120001631.0U patent/CN214371109U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN113483502B (en) | Solar energy and air source heat pump coupled hot water, heating and refrigerating system and control method thereof | |
| CN203687442U (en) | Multi-source combined heat supply system | |
| CN215571366U (en) | Solar energy and air source heat pump combined hot water, heating and refrigerating system | |
| CN203516008U (en) | Dual-recovery system for oil and gas heat | |
| CN214371109U (en) | Liquid energy source base station | |
| CN103017434A (en) | Cold accumulation device matched with LNG vaporizing heat-exchange system | |
| CN204063229U (en) | Utilize the remaining used heat of industry for the packaged type heat accumulation energy conserving system of heat energy | |
| CN201448224U (en) | Air compressor radiator waste heat recycling system | |
| CN213873358U (en) | Industrial double-effect power station structure | |
| CN112503812A (en) | Process of liquid energy source base station | |
| CN216049347U (en) | Step heat storage system of fused salt coupling thermal power generating unit | |
| CN214701383U (en) | Device for storing liquefied natural gas cold energy and ice making device | |
| CN113865399A (en) | Step heat storage system of fused salt coupled thermal power generating unit and working method | |
| CN203258945U (en) | Cold accumulation device matched with LNG vaporizing heat-exchange system | |
| CN209445472U (en) | One kind provides multiple forms of energy to complement each other, energy gradient utilization system | |
| CN103697523A (en) | Heat pump type heat gain and heat exchange unit | |
| CN112460898A (en) | Industrial double-effect power station construction method | |
| CN212901722U (en) | Hot water making system by using waste heat of factory | |
| CN204786688U (en) | Single tube type cascade utilization distributing type can source station system | |
| CN213179523U (en) | Cooling and heat dissipating system for enterprise production | |
| CN212108616U (en) | Waste heat recovery system | |
| CN211174244U (en) | L NG cold energy power generation and ice making gradient utilization system | |
| CN212806134U (en) | Heat pump system using latent heat and sensible heat of ammonia refrigeration system as heat source | |
| CN203454527U (en) | Cooling circulation water system | |
| CN204738935U (en) | Energy -conserving two -stage cooler |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20211008 |