CN209246209U - Still kettle steam discharge reclaiming system for condensation heat - Google Patents
Still kettle steam discharge reclaiming system for condensation heat Download PDFInfo
- Publication number
- CN209246209U CN209246209U CN201821699207.2U CN201821699207U CN209246209U CN 209246209 U CN209246209 U CN 209246209U CN 201821699207 U CN201821699207 U CN 201821699207U CN 209246209 U CN209246209 U CN 209246209U
- Authority
- CN
- China
- Prior art keywords
- exchanging part
- heat exchanging
- heat
- water
- still kettle
- 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
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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of still kettle steam discharge reclaiming system for condensation heat, including still kettle, the first heat exchanging part, the second heat exchanging part, water storage part, still kettle is connect with the first heat exchanging part hot side, second heat exchanging part hot side is connect with the first heat exchanging part hot side, the steam of still kettle discharge obtains condensed water using the second heat exchanging part after the cooling of the first heat exchanging part, water storage part connect heat exchange with the first heat exchanging part cold side to obtain the hot water used as thermal energy, first heat exchanging part, the second heat exchanging part use plate heat exchanger, and water storage part and the first heat exchanging part cold side utilize soft water cycle heat exchange.Above-mentioned utility model uses plate heat exchanger, and the waste vapour that still kettle can be discharged is recycled and is converted to available thermal energy, and environmental protection and energy saving avoid thermal energy from wasting, and heat exchanger cold side utilizes soft water cycle heat exchange, efficiently avoids water fouling and scale blocking.
Description
Technical field
The utility model relates to heat recovery system more particularly to a kind of still kettle steam discharge reclaiming system for condensation heat.
Background technique
Still kettle is steam-cured to the construction materials such as air-entrained concrete building block, multilayer composite sheet progress anti-corrosion, mainly makes plate
It is corroded from organisms such as worm, bacterium, extend the service life of plate and reduces consumption.When steam-cured to plate progress anti-corrosion, one
As still kettle use the steam of 0.8~1.0MPa as heat source, pressure maintaining is steam-cured in turn for multiple still kettle steam.The last one kettle goes out
Come steam discharge based on steam, at least 140 DEG C of exhaust temperature, but it is traditional with still kettle carry out it is steam-cured after be all without overheat
Recovery processing with regard to direct emission steam, cause heat resource to waste, and in this way direct emission steam be easy to because the water hardness compared with
High yield, which scales, to be caused to carry gas with foreign flavor secretly when steam discharge blocking, steam discharge.
Based on this, in order to realize that the heat to still kettle steam discharge is recycled, the waste of steam discharge thermal energy and scale are avoided
The problem of blocking, providing a kind of can be current urgent problem to be solved to the system of steam discharge progress recuperation of heat.
Utility model content
For overcome the deficiencies in the prior art, the purpose of this utility model is to provide a kind of still kettle steam discharge condensation heats to return
Receipts system solves the problems, such as the waste of still kettle steam discharge thermal energy and scale blocking.
To achieve the above objectives, the present invention adopts the following technical solutions:
A kind of still kettle steam discharge reclaiming system for condensation heat, including still kettle, the first heat exchanging part, the second heat exchanging part, water storage part,
The still kettle is connect with the first heat exchanging part hot side, and the second heat exchanging part hot side and the first heat exchanging part hot side connect
It connects, the steam of the still kettle discharge obtains condensed water, institute using second heat exchanging part after first heat exchanging part cooling
It states water storage part and connect heat exchange with first heat exchanging part cold side to obtain the hot water used as thermal energy, first heat exchanging part,
Second heat exchanging part uses plate heat exchanger, and the water storage part and first heat exchanging part cold side utilize soft water cycle heat exchange.
It is recycled using heat of the plate heat exchanger to the steam that still kettle is discharged, avoids steam discharge thermal energy unrestrained
Take, while using soft water cycle heat exchange in heat exchanger cold side to solve the problems, such as that scale blocks.
It preferably, further include third heat exchanging part, water tower, second heat exchanging part cold side and the third heat exchanging part hot side connect
It connects, third heat exchanging part cold side is connect with the water tower, and second heat exchanging part utilizes described the connect with the water tower
The heat dissipation of three heat exchanging part, the third heat exchanging part use plate heat exchanger.
Condensed water further will be cooled down into via the still kettle steam that the first heat exchanging part cools down using the second heat exchanging part, the
The plate heat exchanger of two heat exchanging part needs to carry out heat exchange cooling by the plate heat exchanger for the third heat exchanging part connecting with water tower.
Preferably, in 35-40 DEG C of temperature range second heat exchanging part using connect with the water tower exchange heat described in
Third heat exchanging part radiates, and the third heat exchanging part and second heat exchanging part cold side utilize soft water cycle heat exchange.
The second heat exchanging part that the steam utilization of still kettle discharge is connect with the first heat exchanging part hot side import becomes condensed water, the
Two heat exchanging part cold side imports are connect with third heat exchanging part hot side outlet, the second heat exchanging part cold side outlet port and third heat exchanging part hot side into
Mouth connection, third heat exchanging part cold side import are connect with water tower water outlet, and third heat exchanging part cold side outlet port is connect with water tower water inlet,
The second heat exchanging part is radiated using the third heat exchanging part for connecting heat exchange with water tower in 35-40 DEG C of temperature range, third heat exchange
Portion and the second heat exchanging part cold side utilize soft water cycle heat exchange.Water fouling most serious in 50-60 DEG C of temperature range selects 35-40
DEG C temperature range, can effectively avoid generating and excessively will cause the scale of blocking.
It preferably, further include boiler, the 4th heat exchanging part, the boiler connect heat exchange with the 4th heat exchanging part cold side, institute
It states still kettle and connect heat exchange with the 4th heat exchanging part hot side, the steam of the still kettle discharge exchanges heat through the 4th heat exchanging part
Become condensed water, the 4th heat exchanging part passes after using plate heat exchanger, the 4th heat exchanging part that additional room temperature moisturizing exchanges heat
It send to the boiler producing steam.
Plate heat exchanger cold side connect heat exchange with boiler inlet, the moisturizing that about 20 DEG C of room temperature be discharged to plate heat exchanger cold side into
Mouthful, normal-temperature water obtains 90 DEG C of hot water after heat exchange, is sent to boiler by plate heat exchanger cold side outlet port, is directly entered burner hearth and produces and steams
Vapour.
It preferably, further include drainer, the second heat exchanging part hot side outlet is connect to transmit condensation with the drainer
Water, the 4th heat exchanging part hot side outlet are connect with the drainer to transmit condensed water.
Drainer water storage focuses on condensed water.
It preferably, further include the energy saving portion being connect with the water storage part water outlet, the water storage part is that the energy conservation portion mentions
For thermal energy, the energy conservation portion includes refrigeration section and heating portion, and the still kettle is connect with the first heat exchanging part hot side import to be made
Steam cooling, the water storage part connect heat exchange with first heat exchanging part cold side to save hot water, the refrigeration section and the storage
Water portion water outlet is connected to freeze, and heating portion hot side import is connect with the water storage part water outlet with heating.
The steam that still kettle is discharged is applied into refrigeration, in heating equipment, effectively utilizes steam thermal energy, reduces thermal energy money
Source waste, energy conservation and environmental protection.
Preferably, heating portion hot side connects the water storage part to obtain heat source, the external world using the water storage part hot water
Fluid is exchanged heat using heating portion cold side.
Preferably, the refrigeration section is lithium bromide refrigerator.
Preferably, the heating portion carries out heating using fan coil.
Compared with prior art, the utility model has the beneficial effects that:
Still kettle is connect with the first heat exchanging part, and the steam of still kettle discharge cools down by the first heat exchanging part, the second heat exchanging part
Hot side is connect with the first heat exchanging part hot side, and the second heat exchanging part of steam utilization after making cooling obtains condensed water, water storage part and first
The connection heat exchange of heat exchanging part cold side makes the water of water storage part heat up and obtains the hot water of offer thermal energy, and the first heat exchanging part, the second heat exchanging part are adopted
With plate heat exchanger, the plate heat exchanger thermal efficiency is higher, and the waste vapour that still kettle can be discharged is recycled and is converted to available
Thermal energy, expand heat energy utilization range, improve the utilization rate of thermal energy, avoid the wasting of resources, water storage part and the first heat exchanging part cold side
Using soft water cycle heat exchange, plate heat exchanger cold side efficiently avoids water fouling and scale blocking using soft water circulation.
Detailed description of the invention
Fig. 1 is the schematic diagram of the still kettle steam discharge reclaiming system for condensation heat of the utility model preferred embodiment.
In figure: 100, still kettle；201, the first heat exchanging part；202, water storage part；203, energy conservation portion；2031, refrigeration section；
2032, heating portion；301, the second heat exchanging part；302, third heat exchanging part；303, water tower；304, water supply tank；401, the 4th heat exchanging part；
402, boiler；500, drainer.
Specific embodiment
In the following, being described further in conjunction with attached drawing 1 and specific embodiment to the utility model:
The utility model discloses a kind of still kettle steam discharge reclaiming system for condensation heat, including still kettle 100, the first heat exchanging part
201, water storage part 202, energy conservation portion 203 (energy saving portion 203 include refrigeration section 2031, heating portion 2032), the second heat exchanging part 301, the
Three heat exchanging part 302, water tower 303, water supply tank 304, the 4th heat exchanging part 401, boiler 402, drainer 500.
Wherein, the first heat exchanging part, the second heat exchanging part, third heat exchanging part, the 4th heat exchanging part are plate heat exchanger, that is, are respectively
First plate changes (the first heat exchanging part 201), the second plate changes (the second heat exchanging part 301), third plate changes (third heat exchanging part 302), the 4th
Plate changes (the 4th heat exchanging part 401), the first heat exchanging part, the second heat exchanging part, third heat exchanging part, the 4th heat exchanging part cold side import/export,
Hot side import/export is respectively heat exchanger cold medium import/export and thermal medium import/export.Water storage part 202 is using the water storages such as water tank dress
It sets, refrigeration section 2031 is lithium bromide refrigerator, and heating portion 2032 is heating with plate heat exchanger (i.e. heating is changed with plate), utilizes wind
Machine coil pipe carries out heating, and water tower 303 is cooling tower.
Heat exchanger uses detachable plate structure, and occupied area is small, and plant maintenance is simply and the cost of investment is low.Plate-type heat-exchange
The device thermal efficiency is higher, and the waste vapour that still kettle can be discharged is recycled and is converted to available thermal energy, and the utility model is preferable
Embodiment expands heat energy utilization range, improves the utilization rate of thermal energy, avoids the wasting of resources, maximumlly energy-saving consumption-reducing.
" soft water " is mentioned in the present embodiment refers to the water be free of or containing few solubility calcium, magnesium compound.(contain in common water
There is calcium and magnesium ion, water calcium ions and magnesium ions when heating will become calcium carbonate, magnesium carbonate, that is to say that scale, scale generate most tight
The temperature range of weight is 50-60 DEG C, is free of or contains only few calcium and magnesium ion in soft water.) in addition to what is connect with water tower 303
The plate heat exchanger of third heat exchanging part 302, heat exchanger cold side all uses soft water cycle heat exchange in the present embodiment, uses in water tower 303
In heat exchange water can not be soft water, can be suitable in practical ranges relative to the higher water of the soft water water hardness.
Cold side is changed using enclosed soft water in plate, equipment caused by avoiding the problem that because of water fouling blocks and high cleaning frequency,
The care and maintenance cost of post facility and heat recovery system is effectively reduced.
The present embodiment mentions " bypass pipe ", guides to point of use from a main pipeline point smaller branch pipe by heat.
As shown in Figure 1, the preferred embodiment of 100 reclaiming system for condensation heat of the utility model still kettle are as follows:
Steam is discharged from the exhaust outlet of still kettle 100, and it is all the way main pipeline that steam discharge, which is divided into two-way, is all the way branch pipe(tube), adopts
It is realized and is connected with each other with water pipe.
Main pipeline:
100 exhaust outlet of still kettle is connect with 201 hot side import of the first heat exchanging part by pipeline, 201 hot side of the first heat exchanging part
Outlet is connect with 301 hot side import of the second heat exchanging part by pipeline, 201 cold side outlet port of the first heat exchanging part and water tank (i.e. water storage part
202) water inlet is connected by pipeline, and 201 cold side import of the first heat exchanging part and water tank (i.e. water storage part 202) water outlet pass through pipeline
Connection, the connecting pipe between 201 cold side of the first heat exchanging part and water tank utilize soft water cycle heat exchange.Water storage part 202 and energy conservation portion 203
Connection, i.e., lithium bromide refrigerator (refrigeration section 2031) water inlet, heating with plate change (heating portion 2032) hot side import respectively with water
The connection of case (i.e. water storage part 202) water outlet, heating plate heat exchange side outlet, lithium bromide refrigerator water outlet and water tank (i.e. water storage
Portion 202) water inlet pass through pipeline connect.
Second heat exchanging part, 301 hot side outlet is connect with drainer 500 by pipeline, 301 cold side outlet port of the second heat exchanging part with
302 hot side import of third heat exchanging part is connected by pipeline, and 301 cold side import of the second heat exchanging part goes out with 302 hot side of third heat exchanging part
Mouth is connected by pipeline, and 302 cold side outlet port of third heat exchanging part is connect with water tower 303 (i.e. water tower 303) water inlet by pipeline, the
Three heat exchanging part, 302 cold side import is connect with 303 water outlet of water tower by pipeline.
It should be understood that
100 steam drain of still kettle changes (the first heat exchanging part 201) hot side import with the first plate and connect, 100 steam drain of still kettle
The steam of discharge changes (the first heat exchanging part 201) by the first plate, and vapor (steam) temperature is cooled to 90 DEG C or so from 140 DEG C.First plate
It changes (the first heat exchanging part 201) cold side import to connect with water outlet of water tank, the first plate changes (the first heat exchanging part 201) cold side outlet port and water
Case water inlet connection, wherein water outlet of water tank and the first plate are provided between changing (the first heat exchanging part 201) cold side import connecting pipe
Pump, water outlet of water tank, which be discharged and pass through to pump, forces its about 80 DEG C water outlet to be transmitted to the first plate that change (the first heat exchanging part 201) cold
Side simultaneously changes (the first heat exchanging part 201) by the first plate water tank circulating chilled water is heated to 80-90 DEG C, obtains hot water, then by the first plate
(the first heat exchanging part 201) cold side outlet port is changed to deliver hot water to water tank water inlet and be stored into water tank.Water outlet of water tank difference
It is connect with lithium bromide refrigerator, heating with plate heat exchange side-entrance: tank hot water is transmitted to by lithium bromide refrigerator, bromination using pump
Lithium bromide water solution is heated because of hot water temperature's height in lithium refrigeration machine, and the water vapor in lithium bromide water solution, vaporization absorption heat reaches
To the cooling refrigeration to hot water, and hot water and steam is brominated liquid of the condensation as high pressure low temperature after the cooling water temperature of lithium refrigeration machine
State water obtains 80 DEG C of water and is transmitted in water tank by pipeline.Tank hot water is also transmitted to from water outlet of water tank by pipeline
Heating plate exchanges heat side-entrance, and heating uses plate high-temperature-hot-water of changing commanders to use as heat source, after the hot water used as heat source cools down
Be transmitted to water tank with the plate side outlet that exchanges heat by heating, and extraneous cryogenic media (such as cold water, cryogen, wet air) by
Heating with plate change cold side import access by heat exchange be converted into after high-temperature medium (such as hot water, hot fluid, wet air) by cold
Side outlet is sent out.Using the steam-refrigerated of the discharge of still kettle 100 and as heating reservoir, thermal energy is reasonably utilized, keeps away
Exempt from the wasting of resources, is effectively reduced cost.
First plate, which changes (the first heat exchanging part 201) hot side outlet and changes (the second heat exchanging part 301) hot side import with the second plate, to be connect,
The steam that still kettle 100 is discharged changes (the first heat exchanging part 201) hot side import by the first plate, by vapor (steam) temperature from 140 DEG C of coolings
To 90 DEG C or so and (the first heat exchanging part 201) hot side import is changed by the first plate to enter, and is transmitted to the second plate and is changed (the second heat exchanging part
301) hot side import；90 DEG C of steam changes (the second heat exchanging part 301) heat exchange in the second plate and directly condenses to 40 DEG C, and steam becomes substantially
At condensed water, condensed water, which from the second plate changes (the second heat exchanging part 301) hot side outlet and is transmitted to drainer 500 by pipeline, enters water
Mouthful, it is stored in drainer 500.Second plate changes cold side and is connect with third plate heat exchange side by pipeline, and the second plate changes soft used in cold side
Water needs extras to generate, and changes between cold side and third plate heat exchange side ducts in the second plate and is equipped with a water supply tank 304,35-40 DEG C
Soft water is closed system, and soft water is added from closed water supply tank 304 and carries out soft water circulation.Second plate changes (the second heat exchanging part 301)
Cold side import is changed (third heat exchanging part 302) hot side outlet with third plate and is connect, and the second plate changes (the second heat exchanging part 301) cold side outlet port
It changes (third heat exchanging part 302) hot side import with third plate to connect, third plate changes (third heat exchanging part 302) cold side outlet port and water tower
The connection of 303 water inlets, third plate changes (third heat exchanging part 302) cold side import and connect with 303 water outlet of water tower, in 35-40 DEG C of temperature
In degree section the second plate change the recirculated water of (the second heat exchanging part 301) and water tower 303 by third plate change (third heat exchanging part 302) come
It radiates.That is, when the second plate changes (the second heat exchanging part 301) temperature in 35-40 DEG C of section, followed for about 32 DEG C in water tower 303
Ring water is transmitted to third plate by 303 water outlet of water tower and changes cold side import, and recirculated water changes (third heat exchanging part by third plate after heat exchange
302) cold side outlet port is transmitted to 303 water inlet of water tower and enters in water tower 303.Third plate changes (third heat exchanging part 302) and the second plate
It changes between (the second heat exchanging part 301) and is connected by pipeline, there is soft water to circulate in pipeline, 35 DEG C of recirculated water is changed by third plate
(third heat exchanging part 302) hot side outlet is transmitted to the second plate and changes (the second heat exchanging part 301) cold side import, 40 DEG C of circulation after heat exchange
Water, which from the second plate changes (the second heat exchanging part 301) cold side outlet port and is transmitted to third plate, changes (third heat exchanging part 302) hot side import, at this
Temperature range changes heat dissipation to the second plate, avoids scale from forming (scale fouling most serious in 50-60 DEG C of temperature range), reduces
Cleaning frequency.(note: 303 recirculated water of water tower is not necessarily intended to using soft water herein, but other than 303 recirculated water of water tower, other water sides
Soft water circulation is all made of to avoid scale is generated.)
Branch pipe(tube): (note: moisturizing used in branch pipe(tube) is soft water)
100 exhaust outlet of still kettle is connect with 401 hot side import of the 4th heat exchanging part by pipeline, 401 hot side of the 4th heat exchanging part
Outlet is connect with 500 water inlet of drainer, and 401 cold side outlet port of the 4th heat exchanging part is connect with 402 entrance of boiler, and boiler 402 is used for
Producing steam, normal-temperature water are entered by 401 cold side of the 4th heat exchanging part.
It should be understood that
A tubule capable of bypass is used at 100 steam drain of still kettle, so that 100 steam discharge of still kettle is except through supervisor
Road can also draw part to boiler room 402 by bypass pipe, the detailed process are as follows: the steam that still kettle 100 is discharged is from the 4th plate
The entrance of (the 4th heat exchanging part 401) hot side import is changed, forms condensed water after heat exchange condensation, condensed water changes that (the 4th changes by the 4th plate
Hot portion 401) cold side outlet port discharge be transmitted to drainer 500, concentrated together with the condensed water for the main pipeline collected in drainer 500
Processing.4th plate changes (the 4th heat exchanging part 401) cold side outlet port and connect with 402 entrance of boiler, and normal-temperature water enters the 4th plate and changes the (the 4th
Heat exchanging part 401) cold side import, become 90 DEG C of hot water after heat exchange, it is cold that 90 DEG C of hot water by the 4th plate changes (the 4th heat exchanging part 401)
Side outlet is sent to boiler 402 by pipeline, is directly entered burner hearth producing steam.
The temperature used in the present embodiment is most reasonable, optimization temperature, in actual operation can be according to actual use
It carry out certain adjustment and be not to be limited in numerical value exemplified by the present embodiment and numberical range.
It will be apparent to those skilled in the art that can make various other according to the above description of the technical scheme and ideas
Corresponding change and deformation, and all these changes and deformation all should belong to the protection of the utility model claims
Within the scope of.
Claims (9)
1. a kind of still kettle steam discharge reclaiming system for condensation heat, which is characterized in that including still kettle, the first heat exchanging part, the second heat exchange
Portion, water storage part, the still kettle are connect with the first heat exchanging part hot side, the second heat exchanging part hot side and first heat exchange
The connection of portion's hot side, the steam of the still kettle discharge are obtained after first heat exchanging part cooling using second heat exchanging part cold
Condensate, the water storage part connect heat exchange with first heat exchanging part cold side to obtain the hot water used as thermal energy, and described first
Heat exchanging part, second heat exchanging part use plate heat exchanger, and the water storage part is followed with first heat exchanging part cold side using soft water
Ring heat exchange.
2. still kettle steam discharge reclaiming system for condensation heat according to claim 1, which is characterized in that further include third heat exchange
Portion, water tower, second heat exchanging part cold side are connect with the third heat exchanging part hot side, third heat exchanging part cold side and the water
Tower connection, second heat exchanging part utilize the third heat exchanging part connecting with the water tower to radiate, and the third heat exchanging part is adopted
Use plate heat exchanger.
3. still kettle steam discharge reclaiming system for condensation heat according to claim 2, which is characterized in that 35-40 DEG C of humidity province
Interior second heat exchanging part is radiated using the third heat exchanging part for connecting heat exchange with the water tower, the third heat exchange
Portion and second heat exchanging part cold side utilize soft water cycle heat exchange.
4. still kettle steam discharge reclaiming system for condensation heat described in any one of -3 according to claim 1, which is characterized in that also wrap
Boiler, the 4th heat exchanging part are included, the boiler connect heat exchange with the 4th heat exchanging part cold side, and the still kettle is changed with the described 4th
Hot portion's hot side connection heat exchange, the steam of the still kettle discharge exchanges heat through the 4th heat exchanging part becomes condensed water, and the described 4th
Heat exchanging part is sent to the boiler producing steam after using plate heat exchanger, the 4th heat exchanging part that additional room temperature moisturizing exchanges heat.
5. still kettle steam discharge reclaiming system for condensation heat according to claim 4, which is characterized in that it further include drainer, institute
The second heat exchanging part hot side outlet is stated to be connect with the drainer to transmit condensed water, the 4th heat exchanging part hot side outlet with it is described
Drainer is connected to transmit condensed water.
6. still kettle steam discharge reclaiming system for condensation heat according to claim 1, which is characterized in that further include and the water storage
The energy saving portion of portion's water outlet connection, the water storage part provide thermal energy for the energy conservation portion, and the energy conservation portion includes refrigeration section and adopts
Warm portion, the still kettle is connect with the first heat exchanging part hot side import makes steam cooling, and the water storage part is changed with described first
Hot portion cold side connection heat exchange is to save hot water, and the refrigeration section is connect with the water storage part water outlet to freeze, the heating portion
Hot side import is connect with the water storage part water outlet with heating.
7. still kettle steam discharge reclaiming system for condensation heat according to claim 6, which is characterized in that heating portion hot side connects
The water storage part is connect to obtain heat source using the water storage part hot water, external fluid is exchanged heat using heating portion cold side.
8. still kettle steam discharge reclaiming system for condensation heat according to claim 6, which is characterized in that the refrigeration section is bromination
Lithium refrigeration machine.
9. still kettle steam discharge reclaiming system for condensation heat according to claim 6, which is characterized in that the heating portion utilizes wind
Machine coil pipe carries out heating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821699207.2U CN209246209U (en) | 2018-10-19 | 2018-10-19 | Still kettle steam discharge reclaiming system for condensation heat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821699207.2U CN209246209U (en) | 2018-10-19 | 2018-10-19 | Still kettle steam discharge reclaiming system for condensation heat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209246209U true CN209246209U (en) | 2019-08-13 |
Family
ID=67525357
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821699207.2U Expired - Fee Related CN209246209U (en) | 2018-10-19 | 2018-10-19 | Still kettle steam discharge reclaiming system for condensation heat |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209246209U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110542331A (en) * | 2019-09-10 | 2019-12-06 | 广东石湾酒厂集团有限公司 | Multistage waste heat recovery water saving system |
| CN110715286A (en) * | 2019-11-22 | 2020-01-21 | 贵州迪森元能源科技有限公司 | Still kettle and boiler heat energy recovery system |
-
2018
- 2018-10-19 CN CN201821699207.2U patent/CN209246209U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110542331A (en) * | 2019-09-10 | 2019-12-06 | 广东石湾酒厂集团有限公司 | Multistage waste heat recovery water saving system |
| CN110715286A (en) * | 2019-11-22 | 2020-01-21 | 贵州迪森元能源科技有限公司 | Still kettle and boiler heat energy recovery system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202768090U (en) | Recovery system of dead steam waste heat | |
| CN203190489U (en) | Efficient lithium bromide absorption heat pump heat exchanger unit | |
| CN108507220A (en) | A kind of lithium bromide absorption cold but unit and its type of cooling | |
| CN201265955Y (en) | High temperature water heating system by waste heat recovery | |
| CN209246209U (en) | Still kettle steam discharge reclaiming system for condensation heat | |
| CN102914081A (en) | Two-section flue gas hot-water single/double-effect composite lithium bromide absorption type refrigerating unit | |
| CN108800275A (en) | A kind of big temperature-difference central heating system and working method using residual heat of electric power plant | |
| CN101968236A (en) | System for realizing combined heating based on extraction steam for heating and lithium bromide unit | |
| CN101526282B (en) | Hot-water direct-fired single-double effect compound type lithium bromide absorption type cold water and cold-hot water unit | |
| CN202101331U (en) | Heat pump water-heating system using central air-conditioner cooling water and low-temperature flue gas afterheat | |
| CN207716527U (en) | A kind of hot water Optimization of Energy Saving system | |
| CN113310246A (en) | Wine condensation heat energy comprehensive utilization system and heat energy comprehensive utilization method | |
| CN202915597U (en) | Two-section flue gas hot-water single-effect and double-effect composite lithium bromide absorption type refrigerating unit | |
| CN201779751U (en) | Heating system combining lithium bromide machine set with heating steam bleeding | |
| CN208907657U (en) | A kind of big temperature-difference central heating system using residual heat of electric power plant | |
| CN208513372U (en) | Cold rolling of strip steel handles cooling water recycling system | |
| CN103090486A (en) | Heat balance all-in-on machine | |
| CN202973647U (en) | Flue gas hot water single/double-effect composite lithium bromide absorption refrigerating unit | |
| CN108534570A (en) | A kind of absorption big temperature difference heat-exchange unit | |
| CN109185952A (en) | A kind of data center's cold and heat combined supply great temperature difference heat supply system in conjunction with boiler | |
| CN201945201U (en) | Air & steam parallelly connected one-piece high efficiency compound condenser | |
| CN201340135Y (en) | Hot water direct combustion single/double effect composite type lithium bromide absorption cold water/hot and cold water set | |
| CN100402951C (en) | Steam or hot water type lithium bromide absorption cooling and warming water machine | |
| CN210486164U (en) | Vertical double-cylinder falling film absorption heat pump system | |
| CN110173312B (en) | Novel power plant cold end waste heat recycling system and method |
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: 20190813 Termination date: 20211019 |