CN206799576U - A kind of white liquor distilling comprehensive energy-saving system - Google Patents
A kind of white liquor distilling comprehensive energy-saving system Download PDFInfo
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- CN206799576U CN206799576U CN201720258255.7U CN201720258255U CN206799576U CN 206799576 U CN206799576 U CN 206799576U CN 201720258255 U CN201720258255 U CN 201720258255U CN 206799576 U CN206799576 U CN 206799576U
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- 235000014101 wine Nutrition 0.000 claims abstract description 47
- 230000009466 transformation Effects 0.000 claims abstract description 27
- 235000007164 Oryza sativa Nutrition 0.000 claims abstract description 25
- 235000009566 rice Nutrition 0.000 claims abstract description 25
- 241000209094 Oryza Species 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 30
- 238000005265 energy consumption Methods 0.000 abstract description 14
- 238000013124 brewing process Methods 0.000 abstract description 8
- 229910052799 carbon Inorganic materials 0.000 abstract description 7
- 238000010438 heat treatment Methods 0.000 abstract description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 5
- 238000010276 construction Methods 0.000 abstract description 2
- 238000000605 extraction Methods 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 240000007594 Oryza sativa Species 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 15
- 238000000034 method Methods 0.000 description 13
- 238000009833 condensation Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- 230000008901 benefit Effects 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 6
- 230000007613 environmental effect Effects 0.000 description 6
- 238000011084 recovery Methods 0.000 description 6
- 235000020097 white wine Nutrition 0.000 description 6
- 230000008859 change Effects 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 238000011161 development Methods 0.000 description 5
- 238000007701 flash-distillation Methods 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 230000009467 reduction Effects 0.000 description 5
- 238000004821 distillation Methods 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- 238000010025 steaming Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 238000012545 processing Methods 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
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 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
- 238000004064 recycling Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Abstract
The utility model discloses a kind of white liquor distilling comprehensive energy-saving system, by flashing the heat energy reclaimed as a vapor in the hot water after cold water condenses wine steam, and carry out heating supercharging by phase transformation increasing enthalpy, steam jet ejector together with the indirect steam in wine rice steamer, realize that low-grade heat hydro-thermal and high efficiente callback and can heat supercharging while indirect steam heat energy, and reach the purpose of local use.Compared with tradition steams wine system, energy consumption more than 30% can be saved, and system, without power consumption, movement-less part, simple in construction, easy for installation, maintenance workload is small, is especially suitable for requirement of engineering.Introduced in traditional liquor brewing process outside the larger Spirit system of energy consumption, by hot water by flashing extraction steam in the phase transformation increasing enthalpy system by the system and phase transformation increasing enthalpy steam heat pump, the requirement applied to nearby of temperature and pressure of lifting steam thermal energy, reach and solve energy consumption in traditional liquor brewing process greatly and the problems such as thus cause unnecessary carbon emission.
Description
Technical field
The utility model belongs to white liquor distilling technical field, more particularly to a kind of white liquor distilling comprehensive energy-saving system.
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 are 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, the energy resource consumption and pollution of brewing process
The trend that is substantially increased also is presented in discharge, and high energy consumption, low output, maximum discharge are always to perplex the major issue of Liquor-making Enterprises ＆ development.
Being shown according to relevant data, China, which 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.It is current Liquor-making Enterprises ＆ to save the energy, resource circulation utilization, reduce production cost
Production process is exploited potentialities maximally effective method, and clean manufacturing, the inevitable requirement of environmental protection.Therefore, 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 implementation is issued, by the common concern of industry, clean manufacturing index is divided into six classes, wherein energy profit by the standard
By the use of, control discharge of wastewater and waste reclamation required in a standard as important indicator.Respond actively low-carbon economy,
Enter low-carbon pattern early, it is both that liquor industry and enterprise realize and can held that liquor industry, which implements energy-saving and emission-reduction, improves environmental quality,
The domestic demand of supervention exhibition, and 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, the raw material that the initial steam from boiler is passed through after residual water heating fermentation produce wine and steamed
Vapour, wine steam are condensed into liquid wine through subcooled water.In this course, after initial steam use caused low-grade secondary steam and
Caused hot water may be up to 70% containing a large amount of recyclable heat energy, thermal energy consumption after condensing wine steam.It is however, universal at present
Way is that indirect steam caused by some stages dissipates row completely during wine rice steamer steams wine, cools down hot water convergence caused by wine steam
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 will recycle again after lifting 20-30 rice by pump.The problem of this method is present is big in indirect steam and hot water
Calorimetric can waste completely, and cooling water lifting 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 accounts for the ratio of liquor industry production cost and got over
Come bigger, too high turned into of energy resource consumption restricts enterprise competitiveness and an important factor for business efficiency, reduces energy resource consumption, improves
Energy use efficiency is Reducing Cost in Enterprises, improves the important channel of competitive advantage.Wherein, realize that efficient, low cost recovery is steamed
The heat energy for evaporating process is the key that Liquor-making Enterprises ＆ is energy-saving, realizes clean manufacturing.Due to brewing industry (especially brewed spirit
Industry) profit it is high, the past for quite a long time in for brewing process energy-saving attention degree it is inadequate, it is national until in recent years
It is proposed low carbon development and clean manufacturing requirement, and the fundamental state policy using energy-saving and emission-reduction as China, the extensive development of brewing industry
Existing high energy consumption low yield goes wrong and just paid high attention to by industry and academia under pattern.But intelligence steel, Zhao Shuxin on the one hand,
Etc. a large amount of experts and scholars from general policy, mechanism, evaluation and countermeasure and suggestion analysis etc. studied, for strengthen industry
Management policy and technical support are provided；On the other hand, in face of the environmental protection pressure being on the rise, to the waste water and wine of brewing industry
Poor treatment technology is studied and applied, and environmental benefit has larger lifting more in the past.Two aspect correlative study and
Using the processing of the policy that is primarily intended to, management and waste water and vinasse.In recent years, with the attention to low carbon development, in the industry
Have begun to pay close attention to for the power saving of the larger boiling of thermal energy consumption in brewing process and distillation process, Li Zhenxin is (a kind of
Efficient energy-saving steam alcoholic equipment, correlative study and application are primarily intended to the processing of policy, management and waste water and vinasse),
Ma Shujin (a kind of energy-conserving steaming wine condenser) etc. is designed and improved from wine rice steamer structure and condenser etc., and has applied for phase
Patent is closed, however, brewage process is that may change product with the traditional industry passed on to a certain degree, the change of device mostly
Flavor and benefit, traditional production technology and equipments are not easy to be replaced easily, in the case, high efficiency, low cost recovery discharge
Indirect steam and condensed water in low grade heat energy and reach using standard, this be make wine process energy conservation key, this respect
All the time also without preferable solution.
In summary, brewage process may be changed with the traditional industry passed on to a certain degree, the change of device mostly
The flavor and benefit of product, traditional production technology and equipments are not easy to be replaced easily.
The content of the invention
The purpose of this utility model is to provide a kind of white liquor distilling comprehensive energy-saving system, it is intended to it is most to solve brewage process
It is that may change the flavor and benefit of product, traditional production work with the traditional industry passed on to a certain degree, the change of device
The problem of skill and equipment are not easy to be replaced easily.
The utility model is achieved in that a kind of white liquor distilling comprehensive energy-saving system, the white liquor distilling synthesis energy saving
System includes：Wine rice steamer, condenser, flash tank, efficient phase transformation heat booster, enthalpy increasing heat pump, pipeline；
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 is connected with enthalpy increasing heat pump by pipeline
Wine rice steamer.
Further, the wine rice steamer is connected with vacuum system by pipeline.
White liquor distilling comprehensive energy-saving system provided by the utility model, based on steam injection and phase transformation increasing enthalpy principle recovery profit
With waste heat in the indirect steam during white liquor distilling and wine steam cooling water energy consumption, reduction discharge, reduction life are saved to reach
Produce the purpose of cost.The problem of in order to overcome prior art to exist, for White wine brewing process process；Simultaneously for reclaiming wine rice steamer
The heat energy in indirect steam and condensed water out, it is laggard to reach requirement in vapour form and by the pressure raising of low-grade steam
Row reuse, organic efficiency is high, maintenance management is convenient.
The utility model by flash as a vapor reclaim cold water condense wine steam after hot water in heat energy, and with
Indirect steam in wine rice steamer carries out heating supercharging by phase transformation increasing enthalpy, steam jet ejector together, realize low-grade heat hydro-thermal can and
High efficiente callback and supercharging is heated while indirect steam heat energy, and reach the purpose of local use.The utility model steams with tradition
Wine system is compared, and can save energy consumption more than 30%, and system is without power consumption, movement-less part, simple in construction, easy for installation, dimension
It is small to protect workload, is especially suitable for requirement of engineering.Introduced in traditional liquor brewing process outside the larger Spirit system of energy consumption
The utility model, by hot water by flashing extraction steam in the phase transformation increasing enthalpy system by the system and phase transformation increasing enthalpy steam heat
Pump, the requirement that the temperature and pressure of steam thermal energy is applied to nearby is lifted, reach the energy consumption solved in traditional liquor brewing process
The problems such as causing greatly and thus unnecessary carbon emission.
The utility model is reduced from the steam consumption of boiler and the reduction for the carbon emission brought therefrom；Reduce cooling water
The energy consumption and water resources consumption of circulation；Reduce because the environment that heat, boiler smoke are discharged and brought influences；Greatly reduce wine steaming
The energy consumption cost evaporated, big-and-middle-sized brewery's year can save up to ten million first costs.The utility model proposes produce condensation wine steam
Heat energy in hot water is recycled in vapour form by flashing, heating supercharging；Propose in white liquor distilling energy recovery
During utilized nearby using the recovery of phase transformation increasing enthalpy, gain of heat technology steam thermal energy；Condensed water recycles nearby；Floor space
It is small, organic efficiency is high, effects of energy saving and emission reduction is obvious, and new thinking is provided for brewed spirit industry energy-saving emission reduction.
Brief description of the drawings
Fig. 1 is the white liquor distilling comprehensive energy-saving system structural representation that the utility model embodiment provides；
In figure：1st, wine rice steamer；2nd, condenser；3rd, flash tank；4th, phase transformation heat booster；5th, enthalpy increasing heat pump.
Fig. 2 is the white liquor distilling comprehensive energy-saving method flow chart that the utility model embodiment provides.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, with reference to embodiments, to this
Utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining this practicality
It is new, it is not used to limit the utility model.
Application principle of the present utility model is explained in detail below in conjunction with the accompanying drawings.
As shown in figure 1, the white liquor distilling comprehensive energy-saving system that the utility model embodiment provides includes：Including wine rice steamer 1, cold
Five parts such as condenser 2, flash tank 3, phase transformation heat booster 4 and enthalpy increasing heat pump 5, wine rice steamer 1 connect condenser 2, condensation by pipeline
Device 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
Enthalpy increasing heat pump 5；Phase transformation heat booster 4 connects wine rice steamer 1 with enthalpy increasing heat pump 5 by pipeline.
It is connected between each several part by pipeline, the Spirit heat energy recycling system goes out the cooling that condenser excludes
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 flashed off at the top of flash tank 3
J outlet with wine rice steamer come out indirect steam together enter phase transformation heat booster 4, phase transformation heat booster 4 heats to Low Temperature Steam,
Then from outlet, m enters the import n of enthalpy increasing heat pump, and under the driving of working steam, Low Temperature Steam is become into 120-130 DEG C full
And steam, reach the requirement of wine rice steamer 1, enter from wine rice steamer recovered steam import b, wine rice steamer 1 need to use steam insufficient section by pot
The initial steam that stove comes supplements from import a.
Hot water caused by wine steam condensation is recovered to the steam of low-temp low-pressure by flash distillation, and the steam is by using phase transformation
After increasing enthalpy and gain of heat heating technology are handled, the temperature and pressure of the low temperature and low pressure steam are caused in the case of the higher thermal efficiency
Power gets a promotion, and reaches the requirement of white liquor distilling technique.
As shown in Fig. 2 the white liquor distilling comprehensive energy-saving method that the utility model embodiment provides comprises the following steps：
S101：The distillation of wine, Wine rice steamer bottom pot water is heated by steam recovery or that small part is from boiler and produces wine steaming
Vapour；
S102：Condensation, wine steam within the condenser by after flashing or supplementing a small amount of running water temperature it is relatively low
Running water carries out heat exchange cooling into the finished product white wine of liquid；
S103：Flash distillation, hot water caused by wine condensation workshop section is subjected to flash distillation and produces water vapour to reclaim heat energy, is dropped after flash distillation
The water of temperature circulates the condensation for wine steam nearby；
S104：Heat up the gain of heat, will steam caused by flash distillation by phase transformation gain of heat principle by means of considerably less extraneous steam
It is sent into and is heated up with the indirect steam from wine rice steamer, improves temperature；
S105：Phase transformation increasing enthalpy is sprayed, the recovered steam after appropriate heating, and being injected into row by phase transformation further increases
Temperature supercharging, reaches the saturated vapor that wine distillation technique needs temperature and pressure, is sent into wine rice steamer and carries out reuse.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
All any modification, equivalent and improvement made within the spirit and principle of utility model etc., should be included in the utility model
Protection domain within.
Claims (2)
1. a kind of white liquor distilling comprehensive energy-saving system, it is characterised in that the white liquor distilling comprehensive energy-saving system includes：Wine rice steamer,
Condenser, flash tank, efficient phase transformation heat booster, enthalpy increasing heat pump, pipeline；
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 connects wine rice steamer with enthalpy increasing heat pump by pipeline.
2. white liquor distilling comprehensive energy-saving system as claimed in claim 1, it is characterised in that the wine rice steamer is connected with by pipeline
Vacuum system.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720258255.7U CN206799576U (en) | 2017-03-16 | 2017-03-16 | A kind of white liquor distilling comprehensive energy-saving system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201720258255.7U CN206799576U (en) | 2017-03-16 | 2017-03-16 | A kind of white liquor distilling comprehensive energy-saving system |
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| CN206799576U true CN206799576U (en) | 2017-12-26 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110513913A (en) * | 2019-08-23 | 2019-11-29 | 四川建源节能科技有限公司 | A kind of heat pump heat reclamation type Synergistic and energy-saving production system of conventional solid-state white wine |
| 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 |
-
2017
- 2017-03-16 CN CN201720258255.7U patent/CN206799576U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110513913A (en) * | 2019-08-23 | 2019-11-29 | 四川建源节能科技有限公司 | A kind of heat pump heat reclamation type Synergistic and energy-saving production system of conventional solid-state white wine |
| CN110513913B (en) * | 2019-08-23 | 2020-05-12 | 四川建源节能科技有限公司 | Heat pump heat recovery type synergistic energy-saving production system for traditional solid-state white spirit |
| 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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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240221 Address after: 401336 2nd Floor, No. 38 Xinjian Street, Changshengqiao Town, Nan'an District, Chongqing Economic Development Zone Patentee after: Chongqing Langge Energy Saving and Environmental Protection Technology Co.,Ltd. Country or region after: China Address before: 610000 846, southern section of Tianfu Avenue, Huayang street, Tianfu New District, Chengdu, Sichuan Patentee before: CHENGDU HAOYUAN ENERGY SAVING ENVIRONMENTAL PROTECTION CO.,LTD. Country or region before: China |
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| TR01 | Transfer of patent right |