CN203096053U - Efficient energy-saving brewing distillation system - Google Patents
Efficient energy-saving brewing distillation system Download PDFInfo
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- CN203096053U CN203096053U CN2013200527824U CN201320052782U CN203096053U CN 203096053 U CN203096053 U CN 203096053U CN 2013200527824 U CN2013200527824 U CN 2013200527824U CN 201320052782 U CN201320052782 U CN 201320052782U CN 203096053 U CN203096053 U CN 203096053U
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- water
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- input terminus
- way valve
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- 238000004821 distillation Methods 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 118
- 238000009833 condensation Methods 0.000 claims abstract description 10
- 230000005494 condensation Effects 0.000 claims abstract description 10
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 238000001704 evaporation Methods 0.000 claims description 13
- 241000209094 Oryza Species 0.000 claims description 10
- 235000007164 Oryza sativa Nutrition 0.000 claims description 10
- 235000009566 rice Nutrition 0.000 claims description 10
- 230000001502 supplementation Effects 0.000 abstract 1
- 238000004134 energy conservation Methods 0.000 description 3
- 239000008234 soft water Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 210000002381 Plasma Anatomy 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000035924 thermogenesis Effects 0.000 description 1
Abstract
The utility model discloses an efficient energy-saving brewing distillation system. The water outlet of a water softener is connected with the water inlet of a softened water tank, the water outlet of the softened water tank is connected with the water inlet of a low-pressure pump assembly, the water outlet of the low-pressure pump assembly is connected with the water inlet of a heat pump hot-water unit, the water outlet of the heat pump hot-water unit is connected with the water inlet of a hot water tank, the water outlet of the hot water tank is connected with the water inlet of a high-pressure pump assembly, the water outlet of the high-pressure pump assembly is connected with the water inlet of an electric boiler, a hot water supply pipe of a wine steamer and a water supplementing port of a steam heat accumulator, the steam outlet of the electric boiler is connected with a gas inlet of the steam heat accumulator, and the gas outlet of the steam heat accumulator is connected with a heating coil inlet of the wine steamer; the heat pump hot-water unit comprises an air heat exchanger, a first compressor, a first four-way valve, a condensation evaporator, a first throttling device, a second throttling device, a water source heat exchanger, a second compressor, a second four-way valve, a first valve, a second valve and a refrigerator. The water outlet temperature of the heat pump hot-water unit of the system is higher, and the cold water can be obtained.
Description
Technical field
The utility model relates to a kind of wine brewing Distallation systm.
Background technology
Liquor is of long standing and well established in China, and its history can be traced back to period in ancient times, and huge variation has all taken place in development its technology and output so far, and data presentation annual China in 2011 liquor output reaches 102.56 hundred million liters (amounting to 65 degree).China's liquor is of a great variety, and manufacture craft has nothing in common with each other, but the making of various liquor all needs a large amount of heats.
Heat pump is a kind of device that the transfer of heat energy of low-temperature heat source is arrived high temperature heat source.The low-temperature heat source that is generally used for thermal-pump unit is medium---air, river, seawater, the municipal effluent etc. around us, and the principle of work of heat pump is according to contrary carnot's working cycle work.Because this principle of heat pump makes its Energy Efficiency Ratio higher, can reach 3～5 usually, promptly can obtain the heat of 3～5kW with the 1kW electric weight.But because the restriction of compressor capacity, the hot water top temperature that present heat-pump hot-water unit can provide is (to reach as high as 95 ℃) about 90 ℃.So existing wine brewing Distallation systm mainly relies on heat-pump hot-water unit and electric boiler heating unit combined utilization to realize; Thermal source adopts two thermal source step heating and energy saving system design of air source heat pump and electric boiler combination, the high temperature heat pump hot water unit that low-temperature heat source adopts, can realize energy-conservation because of it has higher Energy Efficiency Ratio, high temperature heat source adopts electric boiler, need not the delivery of steam link, reduced transport loss, be convenient to adopt modern control mode simultaneously, reach accurate temperature controlling, the processing requirement of section's length of schooling wine.
The utility model content
The purpose of this utility model is to provide a kind of wine brewing Distallation systm, and the leaving water temperature(LWT) of the heat-pump hot-water unit of this system is higher, so a whole set of wine brewing systematic energy efficiency ratio is higher, more energy-conservation; And can provide cold water for the workshop.
In order to realize above purpose, the technical solution of the utility model is as follows:
A kind of energy-efficient wine brewing Distallation systm, the water outlet of water softener connects the water inlet of softened water tank, the water outlet of softened water tank connects the water-in of low-pressure pump assembly, the water outlet of low-pressure pump assembly connects the water-in of heat-pump hot-water unit, the water outlet of heat-pump hot-water unit connects the water-in of hot well tank, the water outlet of hot well tank connects the water-in of high pressure pump assembly, and the water outlet of high pressure pump assembly connects the water-in of electric boiler, the hot water of wine rice steamer infeeds the water supplement port of the mouth of pipe and steam accumulator; The vapour outlet of electric boiler connects the steam accumulator inlet mouth, and the steam accumulator air outlet connects the import of wine rice steamer heating coil; It is characterized in that described heat-pump hot-water unit comprises air heat exchanger, first compressor, first four-way valve, condenser/evaporator, first throttle device, second throttling set, water source interchanger, second compressor, second four-way valve, first valve, second valve and water tank;
The output terminal of air heat exchanger connects an input terminus of first four-way valve, an output terminal of first four-way valve connects the input terminus of first compressor, the output terminal of first compressor connects another input terminus of first four-way valve, another output terminal of first four-way valve connects the input terminus of the condensation portion of condenser/evaporator, the output terminal of the condensation portion of condenser/evaporator connects the input terminus of first throttle device, and the output terminal of first throttle device connects the input terminus of air heat exchanger;
The output terminal of second throttling set connects the input terminus of first valve and second valve, the output terminal of first valve connects the input terminus of the evaporation section of condenser/evaporator, the output terminal of second valve also connects the input terminus of the evaporation section of condenser/evaporator by pipeline, and described pipeline passes water tank; The output terminal of the evaporation section of condenser/evaporator connects an input terminus of second four-way valve, an output terminal of second four-way valve connects the input terminus of second compressor, the output terminal of second compressor connects another input terminus of second four-way valve, another output terminal of second four-way valve connects the input terminus of water source interchanger, and the output terminal of water source interchanger connects the input terminus of second throttling set;
The water-in of water source interchanger connects the water outlet of low-pressure pump assembly, and the water outlet of water source interchanger connects the water-in of hot well tank.
Condenser/evaporator comprises condensation portion and evaporation section, and condensation portion has input terminus and output terminal, and evaporation section also has input terminus and output terminal, and condenser/evaporator belongs to present technique field prior art and do not do detailed description.
Compare the beneficial effects of the utility model with the prior art scheme: the leaving water temperature(LWT) of the heat-pump hot-water unit of this system is higher, so a whole set of wine brewing systematic energy efficiency ratio is higher, more energy-conservation; And can provide cold water for the workshop.
Description of drawings
Fig. 1 is a wine brewing Distallation systm block diagram;
Fig. 2 is the utility model heat pump water-heating machine prescription frame synoptic diagram.
Wherein, the 1st, the tap water supply pipe; The 2nd, water softener; The 3rd, softened water tank; The 4th, the heat-pump hot-water unit; The 5th, hot well tank; The 6th, high pressure pump assembly; The 7th, the low-pressure pump assembly; The 8th, electric boiler; The 9th, steam accumulator; The 10th, the wine rice steamer; 11 is first valves; 12 is second valves.
Embodiment
Below in conjunction with accompanying drawing the utility model is described in further detail.
As shown in Figure 1, tap water supply pipe 1 enters water softener 2 by pipeline, in water softener 2, remove easy fouling Ca2+, the Mg2+ plasma, these ions are separated out the formation incrustation scale when preventing to heat in water, the soft water that water softener 2 produces enters softened water tank 3 by pipeline, soft water in the softened water tank is extracted by low-pressure pump assembly 7 and enters heat-pump hot-water unit 4, soft water is heated to about 90 ℃ in the heat-pump hot-water unit, the hot water that comes out from heat-pump hot-water unit 4 enters hot well tank 5, hot water in the hot well tank 5 extracts by high pressure pump assembly 6 and delivers to electric boiler 8 respectively, steam accumulator 9 and wine rice steamer 10, electric boiler 8 adds thermogenesis steam with hot water, the steam that produces in the electric boiler 8 enters steam accumulator 9, and the steam in the steam accumulator 9 directly is sent to wine rice steamer 10.When steam that the quantity of steam that consumes in the wine rice steamer 10 produces not as good as electric boiler, excessive steam can store in steam accumulator, when wine rice steamer 10 required quantity of steams produce steam greater than electric boiler, and steam accumulator 9 release of heat, produce steam and replenish, to satisfy the 10 steam consumption requirements of wine rice steamer.
As shown in Figure 2, described heat-pump hot-water unit comprises air heat exchanger, first compressor, first four-way valve, condenser/evaporator, first throttle device, second throttling set, water source interchanger, second compressor, second four-way valve, first valve, second valve and water tank;
The output terminal of air heat exchanger connects an input terminus of first four-way valve, an output terminal of first four-way valve connects the input terminus of first compressor, the output terminal of first compressor connects another input terminus of first four-way valve, another output terminal of first four-way valve connects the input terminus of the condensation portion of condenser/evaporator, the output terminal of the condensation portion of condenser/evaporator connects the input terminus of first throttle device, and the output terminal of first throttle device connects the input terminus of air heat exchanger;
The output terminal of second throttling set connects the input terminus of first valve and second valve, the output terminal of first valve connects the input terminus of the evaporation section of condenser/evaporator, the output terminal of second valve also connects the input terminus of the evaporation section of condenser/evaporator by pipeline, and described pipeline passes water tank; The output terminal of the evaporation section of condenser/evaporator connects an input terminus of second four-way valve, an output terminal of second four-way valve connects the input terminus of second compressor, the output terminal of second compressor connects another input terminus of second four-way valve, another output terminal of second four-way valve connects the input terminus of water source interchanger, and the output terminal of water source interchanger connects the input terminus of second throttling set;
The water-in of water source interchanger connects the water outlet of low-pressure pump assembly, and the water outlet of water source interchanger connects the water-in of hot well tank.
Heat-pump hot-water unit principle of work: air heat exchanger absorbs heat in the air, output low area overheat gas, this low area overheat gas becomes high temperature and high pressure gas through first compressor, this high temperature and high pressure gas is transferred to heat by the condensation portion of condenser/evaporator the evaporation section of condenser/evaporator, the gas temperature that comes out of the evaporation section of condenser/evaporator is just higher like this, by having become high temperature and high pressure gas after second compressor, this high temperature and high pressure gas heats the normal-temperature water in the water source interchanger by the water source interchanger then.At first with first valve closes, second valve open, the cryogenic liquid of second throttling set output can evaporate heat absorption through water tank, the temperature of normal-temperature water in the water tank can be reduced, when water tank temperature reaches the temperature of setting, with second valve closes, first valve open.So system of the present utility model not only Energy Efficiency Ratio is higher, and can produce cold water.
Claims (1)
1. energy-efficient wine brewing Distallation systm, the water outlet of water softener connects the water inlet of softened water tank, the water outlet of softened water tank connects the water-in of low-pressure pump assembly, the water outlet of low-pressure pump assembly connects the water-in of heat-pump hot-water unit, the water outlet of heat-pump hot-water unit connects the water-in of hot well tank, the water outlet of hot well tank connects the water-in of high pressure pump assembly, and the water outlet of high pressure pump assembly connects the water-in of electric boiler, the hot water of wine rice steamer infeeds the water supplement port of the mouth of pipe and steam accumulator; The vapour outlet of electric boiler connects the steam accumulator inlet mouth, and the steam accumulator air outlet connects the import of wine rice steamer heating coil; It is characterized in that described heat-pump hot-water unit comprises air heat exchanger, first compressor, first four-way valve, condenser/evaporator, first throttle device, second throttling set, water source interchanger, second compressor, second four-way valve, first valve, second valve and water tank;
The output terminal of air heat exchanger connects an input terminus of first four-way valve, an output terminal of first four-way valve connects the input terminus of first compressor, the output terminal of first compressor connects another input terminus of first four-way valve, another output terminal of first four-way valve connects the input terminus of the condensation portion of condenser/evaporator, the output terminal of the condensation portion of condenser/evaporator connects the input terminus of first throttle device, and the output terminal of first throttle device connects the input terminus of air heat exchanger;
The output terminal of second throttling set connects the input terminus of first valve and second valve, the output terminal of first valve connects the input terminus of the evaporation section of condenser/evaporator, the output terminal of second valve also connects the input terminus of the evaporation section of condenser/evaporator by pipeline, and described pipeline passes water tank; The output terminal of the evaporation section of condenser/evaporator connects an input terminus of second four-way valve, an output terminal of second four-way valve connects the input terminus of second compressor, the output terminal of second compressor connects another input terminus of second four-way valve, another output terminal of second four-way valve connects the input terminus of water source interchanger, and the output terminal of water source interchanger connects the input terminus of second throttling set;
The water-in of water source interchanger connects the water outlet of low-pressure pump assembly, and the water outlet of water source interchanger connects the water-in of hot well tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200527824U CN203096053U (en) | 2013-01-30 | 2013-01-30 | Efficient energy-saving brewing distillation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200527824U CN203096053U (en) | 2013-01-30 | 2013-01-30 | Efficient energy-saving brewing distillation system |
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| Publication Number | Publication Date |
|---|---|
| CN203096053U true CN203096053U (en) | 2013-07-31 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013200527824U Expired - Fee Related CN203096053U (en) | 2013-01-30 | 2013-01-30 | Efficient energy-saving brewing distillation system |
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| CN (1) | CN203096053U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105907587A (en) * | 2016-06-13 | 2016-08-31 | 黄振锋 | Wine brewing device and wine brewing method |
-
2013
- 2013-01-30 CN CN2013200527824U patent/CN203096053U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105907587A (en) * | 2016-06-13 | 2016-08-31 | 黄振锋 | Wine brewing device and wine brewing method |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 801-810, room 8, building 7, building 57, Ande Avenue, Yuhuatai District, Nanjing, Jiangsu, 210012 Patentee after: Nanjing Xin Lixun Science and Technology Co.,Ltd. Address before: 211161 Jiangning Street industrial concentration area, Jiangning District, Jiangsu, Nanjing Patentee before: NANJING NEWLIXON ELECTRIC Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190718 Address after: 518045 Changping Business Building, Futian Bonded Zone, Futian District, Shenzhen City, Guangdong Province, 1802 Patentee after: Shenzhen Linfeng Technology Co.,Ltd. Address before: 801-810, room 8, building 7, building 57, Ande Avenue, Yuhuatai District, Nanjing, Jiangsu, 210012 Patentee before: Nanjing Xin Lixun Science and Technology Co.,Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130731 Termination date: 20220130 |