CN106635708A - Comprehensive energy saving method for distillation of liquor - Google Patents
Comprehensive energy saving method for distillation of liquor Download PDFInfo
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- CN106635708A CN106635708A CN201710158008.4A CN201710158008A CN106635708A CN 106635708 A CN106635708 A CN 106635708A CN 201710158008 A CN201710158008 A CN 201710158008A CN 106635708 A CN106635708 A CN 106635708A
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- rice steamer
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- 238000000034 method Methods 0.000 title claims abstract description 34
- 238000004821 distillation Methods 0.000 title claims abstract description 12
- 235000014101 wine Nutrition 0.000 claims abstract description 87
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 58
- 238000010025 steaming Methods 0.000 claims abstract description 5
- 241000209094 Oryza Species 0.000 claims description 38
- 235000007164 Oryza sativa Nutrition 0.000 claims description 38
- 235000009566 rice Nutrition 0.000 claims description 38
- 230000009466 transformation Effects 0.000 claims description 37
- 238000007701 flash-distillation Methods 0.000 claims description 22
- 238000009833 condensation Methods 0.000 claims description 11
- 230000005494 condensation Effects 0.000 claims description 11
- 238000004064 recycling Methods 0.000 claims description 10
- 235000020097 white wine Nutrition 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000000047 product Substances 0.000 claims description 7
- 235000013339 cereals Nutrition 0.000 claims description 5
- 229920006395 saturated elastomer Polymers 0.000 claims description 5
- 230000000694 effects Effects 0.000 claims description 3
- 238000000855 fermentation Methods 0.000 claims description 3
- 230000004151 fermentation Effects 0.000 claims description 3
- 239000013589 supplement Substances 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims description 2
- 239000007924 injection Substances 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 238000003786 synthesis reaction Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 15
- 230000008569 process Effects 0.000 abstract description 10
- 229910052799 carbon Inorganic materials 0.000 abstract description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000009434 installation Methods 0.000 abstract description 2
- 230000007704 transition Effects 0.000 abstract 3
- 238000001704 evaporation Methods 0.000 abstract 2
- 230000008020 evaporation Effects 0.000 abstract 2
- 238000010792 warming Methods 0.000 abstract 2
- 238000005507 spraying Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 15
- 230000008901 benefit Effects 0.000 description 8
- 238000013124 brewing process Methods 0.000 description 7
- 230000007613 environmental effect Effects 0.000 description 7
- 230000008859 change Effects 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 6
- 238000011161 development Methods 0.000 description 5
- 230000009467 reduction Effects 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- 238000007599 discharging Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 238000010793 Steam injection (oil industry) Methods 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H6/00—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
- C12H6/02—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
Abstract
The invention discloses a comprehensive energy saving method for distillation of liquor. Flash evaporation is carried out in order to recover heat energy in hot water after cold water condenses wine steam in the form of steam, the steam and secondary steam in a wine steamer are used for carrying out warming and supercharging through increasing enthalpy by phase transition and a stream ejector, in order to realize simultaneous high efficient recovery as well as warming and supercharging of low grade hot water heat energy and secondary steam heat energy, and realize the purpose of spot utilization. Compared with the traditional wine steaming system, the energy consumption is reduced by 30% or above, the system does not have power consumption and moving parts, the structure is simple, installation is simple, maintenance workload is small, and the method is very suitable for engineering needs. In the traditional liquor brewage process, except the wine distilling system with large energy consumption, hot water is extracted through flash evaporation in order to obtain steam, the steam passes through the phase transition enthalpy increasing system and the phase transition enthalpy increasing heat pump with steam spraying, the temperature and the pressure of the steam heat energy are increased and reach nearby the requirements for applications, and the problems of large energy consumption and unnecessary carbon emission caused by the energy consumption in the traditional liquor brewage process and the like are solved.
Description
Technical field
The invention belongs to white liquor distilling technical field, more particularly to a kind of white liquor distilling comprehensive energy-saving method.
Background technology
China is the big country of liquor consumption and production, and white wine increase of production in recent years is rapid, national white wine yield in 2015
1312.80 ten thousand kilolitres have been reached.However, due to historical reasons, China's majority liquor-making enterprise is still in high investment, high consumption, height
In discharge, inefficient extensive development model, with the increase of alcohol product yield, energy resource consumption and the pollution of brewing process
Discharge is also presented the trend that is substantially increased, and the major issue of Liquor-making Enterprises ＆ development is always perplexed in high energy consumption, low output, maximum discharge.
According to relevant data display, China often produces one ton of white wine will consume grain 2-3 tons, consume coal 0.6-1.5 tons, produce vinasse 8-10 tons,
The phenomenon of the high consumption of quality liquor low yield becomes apparent from.Energy saving, resource circulation utilization, reduction production cost are current Liquor-making Enterprises ＆s
Production process is exploited potentialities maximally effective method, is also clean manufacturing, the inevitable requirement of environmental protection.For this purpose, 2007, country
Environmental protection general bureau ratifies《Clean production standard white wine manufacturing industry》(HJ/T 402-2007) is national environmental protection industry mark
Standard, and enforcement is issued, by the common concern of industry, clean manufacturing index is divided into six classes, wherein energy profit by the standard
With, control discharge of wastewater and waste reclamation required in a standard as important indicator.Respond actively low-carbon economy,
Low-carbon (LC) pattern is entered early, and it is both that liquor industry and enterprise realize holding that liquor industry implements energy-saving and emission-reduction, improves environmental quality
The domestic demand of supervention exhibition, is also the opportunity for promoting liquor industry to realize Economic Growth Mode Transformation.In China, distillation is big absolutely
The critical process of most liquor production processes, from the initial steam of boiler be passed through residual water plus hot fermentation after raw material produce wine steam
Vapour, wine steam is condensed into liquid wine through cold water.In this course, initial steam using rear generation low-grade secondary steam and
Containing a large amount of callable heat energy, thermal energy consumption may be up to 70% to the hot water produced after condensation wine steam.However, universal at present
Way is the completely scattered row of indirect steam that wine rice steamer steams that some stages produce during wine, cools down the hot water produced by wine steam and converges
Cooling tower to low level carries out air-cooled or cooling by water, these temperature after cooling 45 DEG C or so (summer temp is higher) from
Water lifts recycling after 20-30 rice by pump.The problem that this method is present is a large amount of in indirect steam and hot water
Heat energy is wasted completely, and cooling water is lifted needs to consume substantial amounts of electric energy, and condensation may also result in extra water consumption and energy consumption
Increase, cause the waste of the substantial amounts of energy and water resource.At present, energy cost account for liquor industry production cost ratio it is more next
Bigger, the too high key factor for becoming restriction enterprise competitiveness and business efficiency of energy resource consumption reduces energy resource consumption, improves energy
Source service efficiency is Reducing Cost in Enterprises, improve the important channel of competitive advantage.Wherein, realize that efficient, low cost reclaims distillation
The heat energy of operation is the key that Liquor-making Enterprises ＆ is energy-saving, realize clean manufacturing.Due to brewing industry (especially brewed spirit industry)
Profit it is high, within the long duration in past for brewing process energy-saving attention degree not enough, until in recent years, country carries
Go out low carbon development and clean manufacturing to require, and using energy-saving and emission-reduction as China fundamental state policy, the extensive development mould of brewing industry
The high energy consumption low yield existed under formula goes wrong and just paid high attention to by industry and academia.But intelligence steel, Zhao's book are new etc. on the one hand,
A large amount of experts and scholars are studied in terms of general policy, mechanism, evaluation and countermeasure and suggestion analysis etc., are to strengthen industry
Management offer policy and technical support；On the other hand, the waste water and vinasse in the face of the environmental protection pressure being on the rise, to brewing industry
Treatment technology is studied and applied, and environmental benefit has more in the past larger lifting.The correlative study of two aspects and should
With the policy that is primarily intended to, management and the process of waste water and vinasse.In recent years, it is right in the industry with the attention to low carbon development
The power saving of the larger boiling of thermal energy consumption and distillation process has begun to concern in brewing process, and Li Zhenxin is (a kind of high
Effect energy-saving steam alcoholic equipment, correlative study and application be primarily intended to policy, management and waste water and vinasse process), horse
Set into (a kind of energy-conserving steaming wine condenser) etc. and be designed and improve in terms of wine rice steamer structure and condenser etc., and applied for correlation
Patent, however, brewage process is mostly have the traditional industry for a certain degree passing on, the change of device may change the wind of product
Taste and benefit, traditional production technology and equipments are not easy to be replaced easily, and in the case, high efficiency, low cost reclaims discharge
Low grade heat energy in indirect steam and condensed water simultaneously reaches and uses standard, and this is the key of process energy conservation of making wine, this respect one
Also without preferable solution since straight.
In sum, brewage process is mostly have the traditional industry for a certain degree passing on, and the change of device may change
The local flavor and benefit of product, traditional production technology and equipments are not easy to be replaced easily.
The content of the invention
It is an object of the invention to provide a kind of white liquor distilling comprehensive energy-saving method, it is intended to which it is mostly tool to solve brewage process
Have a traditional industry for a certain degree passing on, the change of device may change the local flavor and benefit of product, traditional production technology and
Equipment is not easy the problem replaced easily.
The present invention is achieved in that a kind of white liquor distilling comprehensive energy-saving method, the white liquor distilling comprehensive energy-saving method
By flash distillation reclaim as a vapor cold water condense wine steam after hot water in heat energy, and with wine rice steamer in indirect steam one
Rise carries out heating supercharging by phase transformation increasing enthalpy, steam jet ejector, while realizing low-grade heat hydro-thermal energy and indirect steam heat energy
High efficiente callback and heat supercharging；
Grain after fermentation is loaded after wine rice steamer, heating generation is carried out to the grain in wine rice steamer using the steam from boiler
Wine steam, wine steam carries out heat exchange and is cooled into liquid wine by condenser and cold water, while producing the heat of 80 DEG C of temperature
Water；By the hot water produced during wine steam liquid condensed wine first by flash tank, the water at low temperature for producing 60 DEG C -80 DEG C is steamed
Vapour, the most of heat energy in hot water is transformed into steam；Steam together with the indirect steam in wine rice steamer by phase transformation increasing enthalpy and
Steam jet ejector carries out heating supercharging, obtains 120 DEG C -130 DEG C of saturated vapor, realizes low-grade heat hydro-thermal energy and indirect steam
The high efficiente callback of heat energy and supercharging is heated, being re-fed into wine rice steamer carries out recycling for heat energy.
Further, the white liquor distilling comprehensive energy-saving method is comprised the following steps：
Step one, the distillation of wine is heated Wine rice steamer bottom pot water and produces wine by reclaim or small part from the steam of boiler
Steam；
Step 2, condensation, wine steam within the condenser by after flash distillation or a small amount of running water of supplement temperature it is relatively low
The running water cooling that carries out exchanging heat form the finished product white wine of liquid；
The hot water that wine condenses workshop section's generation is carried out flash distillation and produces water vapour to reclaim heat energy, after flash distillation by step 3, flash distillation
The water of cooling circulates nearby the condensation for wine steam；
Step 4, the intensification gain of heat, by means of considerably less extraneous steam, the steaming for being produced flash distillation by phase transformation gain of heat principle
Vapour and the indirect steam from wine rice steamer are sent into and are heated up, and improve temperature；
Step 5, phase transformation increasing enthalpy injection, the recovered steam after 10 DEG C -30 DEG C heat up is injected into advancing through phase transformation
One step heats supercharging, and reaching wine distillation technique needs the saturated vapor of temperature and pressure, and sending into wine rice steamer carries out reuse.
Another object of the present invention is to provide a kind of Spirit heat energy using the white liquor distilling comprehensive energy-saving method
Recycle, hot water is extracted steam again by phase transformation increasing enthalpy system and phase transformation by the Spirit heat energy recycling by flash distillation
Increasing enthalpy steam heat pump.
Further, the Spirit heat energy recycling includes wine rice steamer, condenser, flash tank, phase transformation heat booster and increasing enthalpy
Heat pump；
The wine rice steamer connects condenser by pipeline, and condenser connects flash tank by pipeline, and flash tank is connected by pipeline
Phase transformation heat booster is connect, phase transformation heat booster connects enthalpy increasing heat pump by pipeline；Phase transformation heat booster and enthalpy increasing heat pump are connected by pipeline
Wine rice steamer.
The white liquor distilling comprehensive energy-saving method that the present invention is provided, is recycled white based on steam injection and phase transformation increasing enthalpy principle
Waste heat is produced into reaching saving energy consumption, reducing discharge, reduction in indirect steam and wine steam cooling water in wine still-process
This purpose.For the problem for overcoming prior art to exist, for White wine brewing process process；It is used to reclaim wine rice steamer out simultaneously
Indirect steam and condensed water in heat energy, in vapour form and improve to reach by the pressure of low-grade steam is carried out back after requirement
With organic efficiency is high, maintenance management is convenient.
The present invention by flash distillation reclaim as a vapor cold water condensation wine steam after hot water in heat energy, and with wine rice steamer
In indirect steam carry out heating supercharging by phase transformation increasing enthalpy, steam jet ejector together, realize low-grade heat hydro-thermal can and it is secondary
High efficiente callback and supercharging is heated while steam thermal energy, and reach the purpose of local use.The present invention steams wine system phase with tradition
Than, can saving energy consumption more than 30%, and system, without power consumption, movement-less part, simple structure is easy for installation, maintenance workload
It is little, it is especially suitable for requirement of engineering.The present invention is introduced outside the larger Spirit system of energy consumption in traditional liquor brewing process, will
Hot water extracts steam by the phase transformation increasing enthalpy system and phase transformation increasing enthalpy steam heat pump of the system by flash distillation, lifts steam thermal energy
The requirement applied to nearby of temperature and pressure, reach the energy consumption solved in traditional liquor brewing process big and thus cause not
The problems such as necessary carbon emission.
The present invention reduces the steam consumption from boiler and the reduction of the carbon emission brought therefrom；Reduce cooling water circulation
Energy consumption and water resources consumption；Reduce the ambient influnence for discharging and bringing due to heat, boiler smoke；Greatly reduce wine distillation
Energy consumption cost, big-and-middle-sized brewery's year can save up to ten million first costs.The present invention is proposed and condensation wine steam is produced in hot water
Heat energy by flash distillation, heat supercharging recycled in vapour form；Propose and adopted during white liquor distilling energy recovery
Utilized nearby with the recovery of phase transformation increasing enthalpy, gain of heat technology steam thermal energy；Condensed water is recycled nearby；Floor space is little, to work
The low, operating cost of condition requirement is low, organic efficiency is high, and effects of energy saving and emission reduction substantially, is reduced discharging for brewed spirit industry energy-saving and provided
New thinking.The more existing heat pump of heat recovery efficiency is high more than 1 times, without pivoting part, safeguards few, and not power consumption produces ten thousand per year
The wine brewing process of ton white wine scale, can produce the energy-saving benefit of millions of units and therefore and bring the Environmental Effect of discharge reduction
Benefit.
Description of the drawings
Fig. 1 is white liquor distilling comprehensive energy-saving method flow chart provided in an embodiment of the present invention；
Fig. 2 is white liquor distilling heat energy recycling system structure diagram provided in an embodiment of the present invention；
In figure：1st, wine rice steamer；2nd, condenser；3rd, flash tank；4th, phase transformation heat booster；5th, enthalpy increasing heat pump.
Specific embodiment
In order that the objects, technical solutions and advantages of the present invention become more apparent, with reference to embodiments, to the present invention
It is further elaborated.It should be appreciated that specific embodiment described herein is not used to only to explain the present invention
Limit the present invention.
The application principle of the present invention is explained in detail below in conjunction with the accompanying drawings.
As shown in figure 1, white liquor distilling comprehensive energy-saving method provided in an embodiment of the present invention is comprised the following steps：
S101：The distillation of wine, heats Wine rice steamer bottom pot water and produces wine steaming by reclaim or small part from the steam of boiler
Vapour；
S102：Condensation, wine steam within the condenser by after flash distillation or a small amount of running water of supplement temperature it is relatively low
Running water carries out exchanging heat and cools down the finished product white wine for forming liquid；
S103：Flash distillation, carries out the hot water that wine condenses workshop section's generation flash distillation and produces water vapour to reclaim heat energy, drops after flash distillation
The water of temperature circulates nearby the condensation for wine steam；
S104：The intensification gain of heat, by means of considerably less extraneous steam, the steam for being produced flash distillation by phase transformation gain of heat principle
Send into the indirect steam from wine rice steamer and heated up, improve temperature；
S105：Phase transformation increasing enthalpy is sprayed, the recovered steam after appropriate intensification, is injected into row through phase transformation and is further increased
Temperature supercharging, reaching wine distillation technique needs the saturated vapor of temperature and pressure, and sending into wine rice steamer carries out reuse.
As shown in Fig. 2 Spirit heat energy recycling system provided in an embodiment of the present invention, whole system include wine rice steamer 1,
Five parts such as condenser 2, flash tank 3, phase transformation heat booster 4 and enthalpy increasing heat pump 5, wine rice steamer 1 connects condenser 2 by pipeline, cold
Condenser 2 connects flash tank 3 by pipeline, and flash tank 3 connects phase transformation heat booster 4 by pipeline, and phase transformation heat booster 4 is connected by pipeline
Connect enthalpy increasing heat pump 5；Phase transformation heat booster 4 and enthalpy increasing heat pump 5 connect wine rice steamer 1 by pipeline.
It is connected by pipeline between each several part, the Spirit heat energy recycling system goes out the cooling that condenser is excluded
Water (i.e. about 80 DEG C of hot water) is entered by the water inlet i on the top of flash tank 3, in the Low Temperature Steam for flashing off from the top of flash tank 3
J outlets together enter phase transformation heat booster 4 with wine rice steamer indirect steam out, phase transformation heat booster 4 heats to Low Temperature Steam,
Then the import n of enthalpy increasing heat pump is entered from outlet m, under the driving of working steam, Low Temperature Steam is become into 120-130 DEG C full
And steam, the use requirement of wine rice steamer 1 is reached, enter from wine rice steamer recovered steam import b, wine rice steamer 1 need to be with steam insufficient section by pot
The initial steam that stove comes is supplemented from import a.
Presently preferred embodiments of the present invention is the foregoing is only, not to limit the present invention, all essences in the present invention
Any modification, equivalent and improvement made within god and principle etc., should be included within the scope of the present invention.
Claims (4)
1. a kind of white liquor distilling comprehensive energy-saving method, it is characterised in that the white liquor distilling comprehensive energy-saving method by flash distillation with
The form of steam reclaims the heat energy in the hot water after cold water condensation wine steam, and passes through phase transformation together with the indirect steam in wine rice steamer
Increasing enthalpy, steam jet ejector carry out heating supercharging, realize low-grade heat hydro-thermal can and while indirect steam heat energy high efficiente callback and
Heat supercharging；
Grain after fermentation is loaded after wine rice steamer, heating is carried out to the grain in wine rice steamer using the steam from boiler and is produced wine steaming
Vapour, wine steam carries out heat exchange and is cooled into liquid wine by condenser and cold water, while producing the hot water of 80 DEG C of temperature；Will
The hot water produced during wine steam liquid condensed wine by flash tank, produces 60 DEG C -80 DEG C of low temperature water vapour, by heat first
Most of heat energy in water is transformed into steam；Steam is sprayed together with the indirect steam in wine rice steamer by phase transformation increasing enthalpy and steam
Device carries out heating supercharging, obtains 120 DEG C -130 DEG C of saturated vapor, realizes that low-grade heat hydro-thermal can be with the height of indirect steam heat energy
Effect is reclaimed and heats supercharging, and being re-fed into wine rice steamer carries out recycling for heat energy.
2. white liquor distilling comprehensive energy-saving method as claimed in claim 1, it is characterised in that the white liquor distilling synthesis energy saving side
Method is comprised the following steps：
Step one, the distillation of wine is heated Wine rice steamer bottom pot water and produces wine steam by reclaim or small part from the steam of boiler；
Step 2, condensation, wine steam within the condenser by after flash distillation or a small amount of running water of supplement temperature it is relatively low from
Water carries out exchanging heat and cools down the finished product white wine for forming liquid；
The hot water that wine condenses workshop section's generation is carried out flash distillation and produces water vapour to reclaim heat energy by step 3, flash distillation, is lowered the temperature after flash distillation
Water circulate condensation for wine steam nearby；
Step 4, the intensification gain of heat, by means of considerably less extraneous steam, the steam that produced flash distillation by phase transformation gain of heat principle and
Send into from the indirect steam of wine rice steamer and heated up, improve temperature；
Step 5, phase transformation increasing enthalpy injection, the recovered steam after 10 DEG C -30 DEG C heat up is injected into row further through phase transformation
Heat supercharging, reaching wine distillation technique needs the saturated vapor of temperature and pressure, and sending into wine rice steamer carries out reuse.
3. a kind of Spirit heat circulation of white liquor distilling comprehensive energy-saving method described in utilization claim 1～2 any one is sharp
With, it is characterised in that hot water is extracted steam and passes through phase transformation increasing enthalpy system again by the Spirit heat energy recycling by flash distillation
With phase transformation increasing enthalpy steam heat pump.
4. wine system is evaporated as claimed in claim 3, it is characterised in that the Spirit heat energy recycling includes wine rice steamer, cold
Condenser, flash tank, phase transformation heat booster and enthalpy increasing heat pump；
The wine rice steamer connects condenser by pipeline, and condenser connects flash tank by pipeline, and flash tank connects phase by pipeline
Become heat booster, phase transformation heat booster connects enthalpy increasing heat pump by pipeline；Phase transformation heat booster and enthalpy increasing heat pump connect wine rice steamer by pipeline.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710158008.4A CN106635708A (en) | 2017-03-16 | 2017-03-16 | Comprehensive energy saving method for distillation of liquor |
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| CN201710158008.4A CN106635708A (en) | 2017-03-16 | 2017-03-16 | Comprehensive energy saving method for distillation of liquor |
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Family
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| CN115247113A (en) * | 2021-11-22 | 2022-10-28 | 久粤节能科技(广东)有限公司 | Energy-saving production device and method applied to liquor distillation |
| CN115851401A (en) * | 2022-11-21 | 2023-03-28 | 广东一钛科技有限公司 | Intelligent energy-saving and emission-reducing system of wine cooler |
| CN116218629A (en) * | 2023-03-29 | 2023-06-06 | 同方节能工程技术有限公司 | Carbon reduction and synergy system for solid-state fermented glutinous rice steamer brewing process |
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| CN115247113A (en) * | 2021-11-22 | 2022-10-28 | 久粤节能科技(广东)有限公司 | Energy-saving production device and method applied to liquor distillation |
| CN115851401A (en) * | 2022-11-21 | 2023-03-28 | 广东一钛科技有限公司 | Intelligent energy-saving and emission-reducing system of wine cooler |
| CN116218629A (en) * | 2023-03-29 | 2023-06-06 | 同方节能工程技术有限公司 | Carbon reduction and synergy system for solid-state fermented glutinous rice steamer brewing process |
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