CN204027394U - A kind of heat energy recycling system - Google Patents
A kind of heat energy recycling system Download PDFInfo
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- CN204027394U CN204027394U CN201420384034.0U CN201420384034U CN204027394U CN 204027394 U CN204027394 U CN 204027394U CN 201420384034 U CN201420384034 U CN 201420384034U CN 204027394 U CN204027394 U CN 204027394U
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- heat exchanger
- heat
- energy
- temperature
- storage tank
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
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- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The utility model is applicable to heat recovery technical field, provides a kind of heat energy recycling system.Describedly comprise temperature energy storage tank and device to be heated, described temperature energy storage tank comprises heat energy output end mouth and energy recovery port, described device to be heated comprises First Heat Exchanger and energy consumption system, described First Heat Exchanger is connected between described heat energy output end mouth and energy recovery port, described energy consumption system is connected to described First Heat Exchanger two ends, for receiving the energy that First Heat Exchanger heat exchange obtains.In technical solutions of the utility model, described temperature energy storage tank is used for the flash steam energy of recovery plant discharge, and temperature energy storage tank exports hot water, and it is energy consumption system heat supply that hot water completes hot-cast socket by First Heat Exchanger, complete heat recovery, can effectively reduce factory's operation cost.
Description
Technical field
The utility model belongs to energy recovery technical field, particularly relates to a kind of heat energy recycling system.
Background technology
In chemical industry process field, such as when producing beer, beverage, having and boiling processing procedure, can produce a large amount of flash steam boiling in processing procedure, general evaporation rate accounts for 8%, and this part steam heat is directly discharged in air usually.But there is a lot of equipment needing heating in other workshops of factory simultaneously, such as wheat juice pre-heating device, make-up room bottle washing machine, sterilization machine firing equipment, heating firing equipment, cleaning in place firing equipment etc., these equipment are all adopt independently steam-heating system at present, so just cause steam resource loss, add factory's operation cost.
Utility model content
In view of the above problems, the utility model object is to provide a kind of heat energy recycling system, and this system can recycle existing steam resource well, is intended to the technical problem solving the existing steam wasting of resources.
The utility model realizes like this, described heat energy recycling system comprises temperature energy storage tank and device to be heated, described temperature energy storage tank comprises heat energy output end mouth and energy recovery port, described device to be heated comprises First Heat Exchanger and energy consumption system, described First Heat Exchanger is connected between described heat energy output end mouth and energy recovery port, described energy consumption system is connected to described First Heat Exchanger two ends, for receiving the energy that First Heat Exchanger heat exchange obtains.
Further, also temperature energy storage tank is provided with between described heat energy output end mouth and First Heat Exchanger.
Further, be also provided with the second heat exchanger between described heat energy output end mouth and temperature energy storage tank, described second heat exchanger two ends are also connected with steam concurrent heating system.
Further, by pipeline communication between the output port of described First Heat Exchanger and the input port of the second heat exchanger, described pipeline is provided with valve, and the water inlet pipe of described second heat exchanger is also provided with water pump.
Further, described device to be heated also comprises vapor heat exchanger, and described vapor heat exchanger is connected between described First Heat Exchanger and energy consumption system, and described steam concurrent heating system is connected to described vapor heat exchanger two ends.
Further, pipeline between described second heat exchanger and heat energy buffer tank is also provided with temperature sensor, pipeline between the output port of described steam concurrent heating system and described second heat exchanger is also provided with steam pneumatic operated valve, described heat energy recycling system also comprises the parametric controller being connected to described temperature sensor and steam pneumatic operated valve, described parametric controller controls the aperture of described activated vapor valve according to the temperature detected, to make the heat outputting coolant-temperature gage of the second heat exchanger constant.
The beneficial effects of the utility model are: in technical solutions of the utility model, described temperature energy storage tank is used for the flash steam energy of recovery plant discharge, store wherein in a liquid-like manner, hot water is exported to device to be heated in described temperature energy storage tank, in First Heat Exchanger, heat exchange is carried out with device medium to be heated, the energy that heat exchange obtains provides heat for energy consumption system, completes steam thermal energy and recycles, can reduce factory's operation cost.
Accompanying drawing explanation
Fig. 1 is the structure chart of a kind of heat energy recycling system that the utility model first embodiment provides;
Fig. 2 is the structure chart of a kind of heat energy recycling system that the utility model second embodiment provides;
Fig. 3 is the heat energy recycling system application schematic diagram that the utility model second embodiment provides.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
The steam thermal energy that technical solutions of the utility model mainly utilize recovery plant to discharge, by heat by heat exchanger heat exchange, water in heating temperature energy storage tank, the hot water that temperature energy storage tank exports carries out heat exchange by the First Heat Exchanger of device to be heated, then with the medium after heat exchange, to factory, other need the power consumption device of heating to carry out heat supply, have rationally recycled steam resource.In order to technical scheme described in the utility model is described, be described below by specific embodiment.
embodiment one:
Fig. 1 shows the structure of a kind of heat energy recycling system that the utility model first embodiment provides, and illustrate only the part relevant to the utility model embodiment for convenience of explanation.
The heat energy recycling system that the present embodiment provides comprises temperature energy storage tank 1 and device to be heated 2, described temperature energy storage tank 1 comprises heat energy output end mouth and energy recovery port, described device to be heated 2 comprises First Heat Exchanger 21 and energy consumption system 22, between the heat energy output end mouth that described First Heat Exchanger 21 is connected to described temperature energy storage tank 1 and energy recovery port, described energy consumption system 22 is connected to described First Heat Exchanger two ends 21, for receiving the energy that First Heat Exchanger heat exchange obtains.
Heat after heat exchange for reclaiming and storing steam heat, and is stored by heat exchanger heat exchange form by described temperature energy storage tank 1 in liquid form.Usual described temperature energy storage tank 1 is vertical structure, heat energy output end mouth is on top, energy recovery port, at tail end, exports hot water, after First Heat Exchanger 21 heat exchange from described heat energy output end mouth, for energy consumption system 22 heat supply, backwater through described First Heat Exchanger 21 is back to described energy recovery port, completes whole thermal cycle like this, generally, achieve and utilize waste steam heat energy in factory, other need the device heat supply to be heated of heating, reduce factory's operation cost.During specific implementation, described First Heat Exchanger can be pipe heat exchanger or plate type heat exchanger.Described device to be heated can comprise wheat juice firing equipment, make-up room bottle washing machine, sterilization machine firing equipment, heating firing equipment, cleaning in place firing equipment etc.
Preferably, temperature energy storage tank 3 is also provided with between the heat energy output end mouth of described temperature energy storage tank 1 and First Heat Exchanger 21.By arranging heat energy buffer tank 3, the flow rate of hot water entering device 2 to be heated can be adjusted, there will not be current excessive or too small and heating non-uniform phenomenon that is that cause, ensure system even running.When specific implementation, in order to ensure heat transfer effect, can arrange liquid level gauge, thermometer, water supplement port, discharge outlet etc. on described heat energy buffer tank 3, the liquid level in guarantee heat energy buffer tank 3 and leaving water temperature are in normal range (NR).
As a kind of preferred embodiment of the present embodiment, be also provided with the second heat exchanger 4 between the heat energy output end mouth of described temperature energy storage tank 1 and temperature energy storage tank 3, described second heat exchanger 4 two ends are also connected with steam concurrent heating system 5.
In system operation, the problem of energy shortage in temperature energy storage tank may be there is, device heat supply to be heated cannot be embodied as, in order to head it off, as a kind of preferred embodiment, described heat energy recycling system also comprises steam concurrent heating system 5, described steam concurrent heating system 5 is connected to described second heat exchanger 4 two ends, exchanged by steam heat, for entering the water additional heat in the second heat exchanger, with the hot water satisfied temperature requirement making the second heat exchanger export.During specific implementation, pipeline between described second heat exchanger 4 and heat energy buffer tank 3 is also provided with temperature sensor TET01, pipeline between the output port of described steam concurrent heating system 5 and described second heat exchanger 4 is also provided with steam pneumatic operated valve REV01, described heat energy recycling system also comprises the parametric controller 6 being connected to described temperature sensor TET01 and steam pneumatic operated valve REV01, described parametric controller 6 controls the aperture of described activated vapor valve REV01 according to the temperature detected, to make the heat outputting coolant-temperature gage of the second heat exchanger 4 constant.In this preferred embodiment, parametric controller 6 can by temperature sensor TET01 to the heat outputting coolant-temperature gage of detection second heat exchanger 4, when temperature inadequate or excessive time, can be constant to ensure the heat outputting coolant-temperature gage of the second heat exchanger 4 by the aperture controlling steam pneumatic operated valve REV01, can ensure that the accurate stable of whole system runs like this.
Preferred further, by pipeline communication between the output port of described First Heat Exchanger 21 and the input port of the second heat exchanger 4, described pipeline is provided with valve 7, and the water inlet pipe of described second heat exchanger 4 is also provided with water pump 8.Under normal circumstances, described valve 7 is closed condition, and water pump 8 works, and carries out normal thermal cycle, and water pump 8 variable ratio frequency changer exports.When described temperature energy storage tank 1 breaks down or do not have storing heat in tank, open described valve 7, directly carry out heat supply by steam concurrent heating system 5.Concrete, the vapours that steam concurrent heating system 5 exports is by described second heat exchanger 4, heat exchange is carried out to the water in the second heat exchanger 4 and reaches expection output water temperature, hot water carries out heat exchange by First Heat Exchanger 21, carries out heat supply after the Absorption of Medium heat exchange energy in First Heat Exchanger 21 to energy consumption system 22.
embodiment two:
Fig. 2 shows the structure of a kind of heat energy recycling system that the utility model second embodiment provides, and illustrate only the part relevant to the utility model embodiment for convenience of explanation.
Heat energy recycling system one application schematic diagram as shown in Figure 2 also shown in composition graphs 3, the present embodiment provides heat energy recycling system to comprise the temperature energy storage tank 1 described in embodiment one, device 2 to be heated, heat energy buffer tank 3, second heat exchanger 4, steam bucking-out system 5, parametric controller 6, and a kind of various valve of mentioning of embodiment and sensor, the device to be heated 2 that the present embodiment provides also comprises vapor heat exchanger 23, described vapor heat exchanger 23 is connected between described First Heat Exchanger 21 and energy consumption system 22, described steam concurrent heating system is connected to described vapor heat exchanger two ends.
If the fault that the heating circulation system provided in embodiment one occurs, such as First Heat Exchanger or the second heat exchanger break down, in order to ensure that energy consumption system normally runs, vapor heat exchanger 23 is also provided with between described First Heat Exchanger 21 and energy consumption system 22, the steam that steam bucking-out system 5 exports directly passes into described vapor heat exchanger 23 and carries out heat exchange, and the water in vapor heat exchanger 23 is energy consumption system 22 heat supply after obtaining heat.Ensure that security of system is reliable, run without interruption.Adopt the present embodiment technical scheme can undergo technological transformation to existing factory, reduce costs.
To sum up, the utility model provides a kind of heat energy recycling system, after the steam energy that factory is discarded is recovered to temperature energy storage tank, then in factory, other need the device to be heated of heating to carry out heat supply.By using the utility model system, energy-saving effect is remarkable, is applicable to extensively promoting.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (6)
1. a heat energy recycling system, it is characterized in that, described system comprises temperature energy storage tank and device to be heated, described temperature energy storage tank comprises heat energy output end mouth and energy recovery port, described device to be heated comprises First Heat Exchanger and energy consumption system, described First Heat Exchanger is connected between described heat energy output end mouth and energy recovery port, and described energy consumption system is connected to described First Heat Exchanger two ends, for receiving the energy that First Heat Exchanger heat exchange obtains.
2. heat energy recycling system as claimed in claim 1, is characterized in that, be also provided with temperature energy storage tank between described heat energy output end mouth and First Heat Exchanger.
3. heat energy recycling system as claimed in claim 2, it is characterized in that, be also provided with the second heat exchanger between described heat energy output end mouth and temperature energy storage tank, described second heat exchanger two ends are also connected with steam concurrent heating system.
4. heat energy recycling system as claimed in claim 3, it is characterized in that, by pipeline communication between the output port of described First Heat Exchanger and the input port of the second heat exchanger, described pipeline is provided with valve, and the water inlet pipe of described second heat exchanger is also provided with water pump.
5. heat energy recycling system as claimed in claim 4, it is characterized in that, described device to be heated also comprises vapor heat exchanger, and described vapor heat exchanger is connected between described First Heat Exchanger and energy consumption system, and described steam concurrent heating system is connected to described vapor heat exchanger two ends.
6. heat energy recycling system as claimed in claim 5, it is characterized in that, pipeline between described second heat exchanger and heat energy buffer tank is also provided with temperature sensor, pipeline between the output port of described steam concurrent heating system and described second heat exchanger is also provided with steam pneumatic operated valve, described heat energy recycling system also comprises the parametric controller being connected to described temperature sensor and steam pneumatic operated valve, described parametric controller controls the aperture of described activated vapor valve according to the temperature detected, to make the heat outputting coolant-temperature gage of the second heat exchanger constant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420384034.0U CN204027394U (en) | 2014-07-14 | 2014-07-14 | A kind of heat energy recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420384034.0U CN204027394U (en) | 2014-07-14 | 2014-07-14 | A kind of heat energy recycling system |
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| CN204027394U true CN204027394U (en) | 2014-12-17 |
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| CN201420384034.0U Expired - Fee Related CN204027394U (en) | 2014-07-14 | 2014-07-14 | A kind of heat energy recycling system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104089513A (en) * | 2014-07-14 | 2014-10-08 | 武汉广弘环保工程有限公司 | Heat energy recycling system |
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2014
- 2014-07-14 CN CN201420384034.0U patent/CN204027394U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104089513A (en) * | 2014-07-14 | 2014-10-08 | 武汉广弘环保工程有限公司 | Heat energy recycling system |
| CN104089513B (en) * | 2014-07-14 | 2016-03-30 | 武汉广弘环保工程有限公司 | A kind of heat energy recycling system |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| 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: 20141217 Termination date: 20160714 |