CN208635373U - Standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system - Google Patents
Standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system Download PDFInfo
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- CN208635373U CN208635373U CN201821096263.7U CN201821096263U CN208635373U CN 208635373 U CN208635373 U CN 208635373U CN 201821096263 U CN201821096263 U CN 201821096263U CN 208635373 U CN208635373 U CN 208635373U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
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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
- 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
Abstract
The utility model discloses a kind of standard wine workshops and quality liquor workshop brewing process recirculated water effective utilization system, standard wine workshop condenser and quality liquor workshop condenser compose in parallel parallel condensing device group, parallel condensing device group, BrLi chiller, first cooling tower, BrLi chiller, parallel condensing device group passes sequentially through pipeline and connects to form water circulation system, the cooling water in parallel condensing device group as standard wine workshop condenser and quality liquor workshop condenser is returned to after cooling down after water outlet mixing in parallel condensing device group at least through a BrLi chiller cooling and first cooling tower.The system is by standard wine workshop and quality liquor workshop leaving condenser water comprehensive cyclic utilization, the utilization rate of recirculated water is improved, and when leaving condenser water temperature is too low, which carries out assisted refrigeration using electrical chillers, so that condenser inflow temperature is down to 16 DEG C, meets condenser water requirement.
Description
Technical field
The utility model relates to brewing process circulating water utilization systems, more specifically, the utility model relates to a kind of standards
Wine workshop and quality liquor workshop brewing process recirculated water effective utilization system.
Background technique
The wine brewing existing distiller condenser in base quality liquor workshop, 16 DEG C of inlet water temperature, output water temperature is 70~80 DEG C；Mark
The quasi- existing distiller condenser in wine workshop, inlet water temperature are 16 DEG C, and output water temperature is 75~95 DEG C.Currently without to quality liquor vehicle
Between and standard wine workshop recirculated water comprehensively utilize system.And when the leaving water temperature of condenser is too low, merely with bromination
Lithium refrigeration unit refrigeration is difficult to produce out in the circulatory system 16 DEG C of chilled water, causes condenser inflow temperature unqualified, because
This needs assisted refrigeration.
The current condition in wine brewing base is as follows:
1, water resource waste: conventional brew technique generally uses tap water or recirculated cooling water to drop wine condenser
Temperature achievees the purpose that condensation wine, and there is the quality of a large amount of waste tap water resource or condensation wine is not high for old technique
Problem.
2, decontaminate expense: the hot water of the hot water, 75~95 DEG C of standard wine workshop that 70~80 DEG C of quality liquor brewing workshop is directly arranged
To sewage treatment plant, sewage disposal expense can be generated；The steam for steaming chaff workshop contains pollutant, is unable to direct emission.
3, influence production efficiency: the 30 DEG C of water outlets of original cooling tower influence production efficiency.
Utility model content
The utility model overcomes the deficiencies in the prior art, provides a kind of standard wine workshop and quality liquor workshop brewing process
Recirculated water effective utilization system efficiently integrates standard wine workshop and quality liquor workshop brewing process recirculated water with expectation
Property utilization, another purpose be solve leaving condenser water temperature it is too low when system be difficult to produce out 16 DEG C of chilled waters as condensation
The problem of device is intake.
In order to solve the above technical problems, the utility model uses following technical scheme:
A kind of standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system, including standard wine workshop are cold
Condenser, quality liquor workshop condenser, BrLi chiller and the first cooling tower, standard wine workshop condenser and quality liquor
Workshop condenser composes in parallel parallel condensing device group, the parallel condensing device group, BrLi chiller, the first cooling tower, bromine
Change lithium refrigeration unit, parallel condensing device group passes sequentially through pipeline and connects to form water circulation system, the water outlet in parallel condensing device group
It is returned in parallel condensing device group after cooling down after mixing at least through a BrLi chiller cooling and first cooling tower
Cooling water as standard wine workshop condenser and quality liquor workshop condenser.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system, parallel condensing device group
In water outlet mixing after pass sequentially through BrLi chiller cooling, the cooling of the first cooling tower, then pass through BrLi chiller
The cooling water in parallel condensing device group as standard wine workshop condenser and quality liquor workshop condenser is returned to after cooling.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system further includes electric refrigerating machine
Group, the parallel condensing device group, BrLi chiller, the first cooling tower, electrical chillers, parallel condensing device group pass sequentially through
Pipeline connects to form water circulation system, passes sequentially through BrLi chiller, first after the water outlet mixing in parallel condensing device group
Cooling tower and electrical chillers are returned in parallel condensing device group after being cooled down as standard wine workshop condenser and quality liquor vehicle
Between condenser cooling water.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system further includes electric refrigerating machine
Group, heat exchanger and the second cooling tower, the parallel condensing device group, BrLi chiller, the first cooling tower, electrical chillers,
Heat exchanger, BrLi chiller, parallel condensing device group pass sequentially through pipeline and connect to form water circulation system, parallel condensing device group
In water outlet mixing after pass sequentially through BrLi chiller, the first cooling tower and electrical chillers and cool down, then pass through
It is cooling that BrLi chiller is returned to after heat exchanger heat exchange, is eventually passed back in parallel condensing device group as standard wine workshop condenser
With the cooling water of quality liquor workshop condenser；The cooling circulating water of second cooling tower is discharged cooling by the heat exchanger.Second is cold
But continue on for workshop after the water outlet cooling of tower.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system further includes that two classes absorb
Formula heat pump unit, the two class absorption heat pumps unit are separately connected water outlet and the BrLi chiller of parallel condensing device group
Water inlet end, the water outlet of parallel condensing device enters BrLi chiller, hot water after cooling down by two class absorption heat pump units
Being heated by the heat absorption of two class absorption heat pump units becomes steam.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system, the first cooling tower is
Closed circulation cooling tower or open cycle cooling tower；Its BrLi chiller is hot water lithium bromide refrigeration unit or steam type
BrLi chiller.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system, electrical chillers is
Centrifugal refrigerating machines.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system, heat exchanger are package
Formula heat exchanger or plate heat exchanger.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system is provided on pipeline
Valve.
The standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system, the first cooling tower with
Water circulating pump is set on pipeline between electrical chillers；Pipe between the parallel condensing device group and BrLi chiller
Water circulating pump is set on road.
Compared with prior art, the utility model at least has the advantages that the system condenses standard wine workshop
Comprehensive cyclic utilization is carried out after device water outlet (75~95 DEG C) and (70~80 DEG C) of quality liquor workshop leaving condenser water mixing, is improved
The utilization rate of recirculated water, has saved water resource, reduces the cost of wine-making technology, also, when leaving condenser water temperature is too low,
The system carries out assisted refrigeration using electrical chillers, so that condenser inflow temperature is down to 16 DEG C, meets condenser water requirement.
Detailed description of the invention
Fig. 1 is 1 recirculated water effective utilization system structural schematic diagram of the utility model embodiment.
Fig. 2 is 2 recirculated water effective utilization system structural schematic diagram of the utility model embodiment.
Fig. 3 is 3 recirculated water effective utilization system structural schematic diagram of the utility model embodiment.
Fig. 4 is 4 recirculated water effective utilization system structural schematic diagram of the utility model embodiment.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only used to explain
The utility model is not used to limit the utility model.
Embodiment 1
Recirculated water effective utilization system structure is as shown in Figure 1, the system includes standard wine workshop condenser, quality liquor workshop
Condenser, BrLi chiller and the first cooling tower, standard wine workshop condenser are composed in parallel with quality liquor workshop condenser
Parallel condensing device group, the water outlet (70~80 of water outlet (75~95 DEG C) and quality liquor workshop condenser of standard wine workshop condenser
DEG C) export and freeze after mixing, parallel condensing device group, BrLi chiller, the first cooling tower, BrLi chiller,
Parallel condensing device group passes sequentially through pipeline and connects to form water circulation system, by primary after the water outlet mixing in parallel condensing device group
BrLi chiller cooling (reduces about 10~20 DEG C), subsequently into first cooling tower cooler (being reduced to 32 DEG C or less), then
It returns to BrLi chiller to be cooled down and (be lowered not more than 16 DEG C), be then return in parallel condensing device group as standard wine
The cooling water of workshop condenser and quality liquor workshop condenser, if recirculated water is after the first cooling tower cooler, temperature reaches
It intakes to condenser and requires (16 DEG C), can also be returned directly in parallel condensing device group after the first cooling tower cooler as standard
The cooling water of wine workshop condenser and quality liquor workshop condenser.
Embodiment 2
Recirculated water effective utilization system structure is as shown in Fig. 2, the system includes standard wine workshop condenser, quality liquor workshop
Condenser, BrLi chiller and the first cooling tower, standard wine workshop condenser are composed in parallel with quality liquor workshop condenser
Parallel condensing device group, the water outlet (70~80 of water outlet (75~95 DEG C) and quality liquor workshop condenser of standard wine workshop condenser
DEG C) export and freeze after mixing.The system further includes electrical chillers (centrifugal refrigerating machines), parallel condensing device group, bromine
Change lithium refrigeration unit, the first cooling tower, electrical chillers, parallel condensing device group to pass sequentially through pipeline and connect to form water cyclic system
System, passed sequentially through after the water outlet mixing in parallel condensing device group BrLi chiller, the first cooling tower and electrical chillers into
Row returns to the cooling in parallel condensing device group as standard wine workshop condenser and quality liquor workshop condenser after being cooled to 16 DEG C
Water.Centrifugal refrigerating machines, can be when parallel condensing device group leaving water temperature be too low as electrical chillers, and guarantee system is normally transported
Row, makes the inflow temperature of parallel condensing device group be down to 16 DEG C or less.
Embodiment 3
Recirculated water effective utilization system structure is as shown in figure 3, the system includes standard wine workshop condenser, quality liquor workshop
Condenser, BrLi chiller and the first cooling tower, standard wine workshop condenser are composed in parallel with quality liquor workshop condenser
Parallel condensing device group, the water outlet (70~80 of water outlet (75~95 DEG C) and quality liquor workshop condenser of standard wine workshop condenser
DEG C) export and freeze after mixing.The system further includes electrical chillers, heat exchanger and the second cooling tower, the parallel condensing
Device group, BrLi chiller, the first cooling tower, electrical chillers, heat exchanger, BrLi chiller, parallel condensing device group
It passes sequentially through pipeline to connect to form water circulation system, passes sequentially through lithium bromide refrigerator after the water outlet mixing in parallel condensing device group
Group, the first cooling tower and electrical chillers are cooled down and (are cooled to 10 DEG C or less), return to bromine after then exchanging heat by heat exchanger
It is cooling to change lithium refrigeration unit, rises to 25 DEG C or so by the circulating water temperature of heat exchanger, is dropped further through BrLi chiller
Temperature eventually passes back in parallel condensing device group to being not higher than 16 DEG C as standard wine workshop condenser and quality liquor workshop condenser
Cooling water；The cooling circulating water of second cooling tower is down to 20 DEG C or so from 30 DEG C or so by heat exchanger, water outlet, into workshop
It is recycled.In addition, water circulating pump is arranged on pipeline between the first cooling tower and electrical chillers；Parallel condensing device group and bromine
Change and water circulating pump is set on the pipeline between lithium refrigeration unit.
Embodiment 4
For recirculated water effective utilization system structure as shown in figure 4, its structure is roughly the same with embodiment 3, difference is that this is
System parallel condensing device group (being made of standard wine workshop condenser and quality liquor workshop condenser) and BrLi chiller it
Between be also provided with two class absorption heat pump units.Two class absorption heat pump units be separately connected parallel condensing device group water outlet and
The water inlet end of BrLi chiller, the water outlet of parallel condensing device enter lithium bromide after cooling down by two class absorption heat pump units
Refrigeration unit, hot water is heated by the heat absorption of two class absorption heat pump units becomes steam.The system is for parallel condensing device group
When leaving water temperature is more than 95 DEG C, the leaving water temperature of parallel condensing device group is down to 85 DEG C by two class absorption heat pump units, and two classes are inhaled
Receipts formula heat pump unit converts steam for hot water using the partial heat energy.Steam has important exploitation value in wine-making technology
Value, such as vinasse can be steamed.Hot water described here can be 90 DEG C of hot water, and current heat absorption rear portion will become steam quilt
It uses in the other processes of wine-making technology.
When parallel condensing device group, and only standard wine workshop condenser and quality liquor workshop condenser are not used in system
When, two class absorption heat pump units can also be installed after corresponding condenser.
In above-described embodiment, the first cooling tower is closed circulation cooling tower or open cycle cooling tower, lithium bromide refrigerator
Group is hot water lithium bromide refrigeration unit or steam type BrLi chiller.The heat exchanger is shell and tube exchanger or board-like
Heat exchanger.Valve is provided on pipeline.
Although reference be made herein to the utility model is described in the explanatory embodiment of the utility model, however, it should
Understand, those skilled in the art can be designed that a lot of other modification and implementations, these modifications and implementations will be fallen
Within scope and spirit disclosed in the present application.It more specifically, can be to theme group in range disclosed in the present application
The building block and/or layout for closing layout carry out a variety of variations and modifications.In addition to the modification carried out to building block and/or layout
Outer with improving, to those skilled in the art, other purposes also will be apparent.
Claims (10)
1. a kind of standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system, it is characterised in that including standard
Wine workshop condenser, quality liquor workshop condenser, BrLi chiller and the first cooling tower, standard wine workshop condenser
Parallel condensing device group is composed in parallel with quality liquor workshop condenser, it is the parallel condensing device group, BrLi chiller, first cold
But tower, BrLi chiller, parallel condensing device group pass sequentially through pipeline and connect to form water circulation system, in parallel condensing device group
Water outlet mixing after at least through returning to parallel condensing after the cooling of BrLi chiller and the first cooling tower cooling
Cooling water in device group as standard wine workshop condenser and quality liquor workshop condenser.
2. standard wine according to claim 1 workshop and quality liquor workshop brewing process recirculated water effective utilization system,
BrLi chiller cooling, the first cooling tower drop are passed sequentially through after the water outlet mixing being characterized in that in the parallel condensing device group
Temperature, then returned to after being cooled down by BrLi chiller in parallel condensing device group as standard wine workshop condenser and quality liquor vehicle
Between condenser cooling water.
3. standard wine according to claim 1 workshop and quality liquor workshop brewing process recirculated water effective utilization system,
It is characterized in that further including electrical chillers, the parallel condensing device group, BrLi chiller, the first cooling tower, electric refrigerating machine
Group, parallel condensing device group pass sequentially through pipeline and connect to form water circulation system, after the water outlet mixing in parallel condensing device group successively
It is returned to after being cooled down by BrLi chiller, the first cooling tower and electrical chillers in parallel condensing device group as standard
The cooling water of wine workshop condenser and quality liquor workshop condenser.
4. standard wine according to claim 1 workshop and quality liquor workshop brewing process recirculated water effective utilization system,
Be characterized in that further including electrical chillers, heat exchanger and the second cooling tower, the parallel condensing device group, BrLi chiller,
First cooling tower, electrical chillers, heat exchanger, BrLi chiller, parallel condensing device group pass sequentially through pipeline and connect to be formed
Water circulation system passes sequentially through BrLi chiller, the first cooling tower and electricity system after the water outlet mixing in parallel condensing device group
Cold group cools down, and BrLi chiller cooling is returned to after then exchanging heat by heat exchanger, eventually passes back to parallel condensing device
Cooling water in group as standard wine workshop condenser and quality liquor workshop condenser；The heat exchanger is cold by the second cooling tower
But recirculated water water outlet cooling.
5. standard wine according to claim 4 workshop and quality liquor workshop brewing process recirculated water effective utilization system,
It is characterized in that further including two class absorption heat pump units, the two class absorption heat pumps unit is separately connected parallel condensing device group
The water inlet end of water outlet and BrLi chiller, the water outlet of parallel condensing device are cooled down laggard by two class absorption heat pump units
Enter BrLi chiller, hot water is heated by the heat absorption of two class absorption heat pump units becomes steam.
6. standard wine according to claim 1 workshop and quality liquor workshop brewing process recirculated water effective utilization system,
It is characterized in that first cooling tower is closed circulation cooling tower or open cycle cooling tower；The BrLi chiller is heat
Water type BrLi chiller or steam type BrLi chiller.
7. standard wine according to claim 3 workshop and quality liquor workshop brewing process recirculated water effective utilization system,
It is characterized in that the electrical chillers are centrifugal refrigerating machines.
8. standard wine according to claim 4 workshop and quality liquor workshop brewing process recirculated water effective utilization system,
It is characterized in that the heat exchanger is shell and tube exchanger or plate heat exchanger.
9. standard wine according to claim 1 workshop and quality liquor workshop brewing process recirculated water effective utilization system,
It is characterized in that being provided with valve on the pipeline.
10. standard wine according to claim 3 or 4 workshop and quality liquor workshop brewing process recirculated water efficiently utilize system
System, it is characterised in that water circulating pump is set on the pipeline between first cooling tower and electrical chillers；The parallel connection is cold
Water circulating pump is set on pipeline between condenser group and BrLi chiller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821096263.7U CN208635373U (en) | 2018-07-11 | 2018-07-11 | Standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821096263.7U CN208635373U (en) | 2018-07-11 | 2018-07-11 | Standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system |
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| Publication Number | Publication Date |
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| CN208635373U true CN208635373U (en) | 2019-03-22 |
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| CN201821096263.7U Expired - Fee Related CN208635373U (en) | 2018-07-11 | 2018-07-11 | Standard wine workshop and quality liquor workshop brewing process recirculated water effective utilization system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111750563A (en) * | 2020-05-14 | 2020-10-09 | 江苏双良节能环保工程技术有限公司 | White spirit waste heat utilization system |
| CN111763598A (en) * | 2020-07-01 | 2020-10-13 | 贵州国台酒庄有限公司 | Circulating water system |
| CN113310246A (en) * | 2021-05-24 | 2021-08-27 | 江苏双良节能环保工程技术有限公司 | Wine condensation heat energy comprehensive utilization system and heat energy comprehensive utilization method |
-
2018
- 2018-07-11 CN CN201821096263.7U patent/CN208635373U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111750563A (en) * | 2020-05-14 | 2020-10-09 | 江苏双良节能环保工程技术有限公司 | White spirit waste heat utilization system |
| CN111763598A (en) * | 2020-07-01 | 2020-10-13 | 贵州国台酒庄有限公司 | Circulating water system |
| CN113310246A (en) * | 2021-05-24 | 2021-08-27 | 江苏双良节能环保工程技术有限公司 | Wine condensation heat energy comprehensive utilization system and heat energy comprehensive utilization method |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190322 Termination date: 20210711 |
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| CF01 | Termination of patent right due to non-payment of annual fee |