CN207472107U - Brewery's heat energy recycling system - Google Patents
Brewery's heat energy recycling system Download PDFInfo
- Publication number
- CN207472107U CN207472107U CN201721276931.XU CN201721276931U CN207472107U CN 207472107 U CN207472107 U CN 207472107U CN 201721276931 U CN201721276931 U CN 201721276931U CN 207472107 U CN207472107 U CN 207472107U
- Authority
- CN
- China
- Prior art keywords
- energy
- heat
- water
- storage
- high temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The utility model provides a kind of brewery's heat energy recycling system, including energy storage flow container, at least one first heat-exchanger rig, at least one second heat-exchanger rig, wherein, energy storage flow container contains at least one high temperature upper port and at least one low temperature lower port, and the energy-storage liquid for absorbing and discharging thermal energy is stored in energy storage flow container；The heat that energy-storage liquid is discharged by the absorption of the first heat-exchanger rig from one or more of indirect steam, high temperature wheat juice, primary steam condensed water, and pass through the second heat-exchanger rig and thermal energy is released to one or more of filtering wheat juice, brewing water, CIP liquid, syrup, bottle washing machine lye, sterilization machine spray hot water.Available thermal energy has fully been recycled by above system, and for needing in the device of thermal energy, has saved the consumption of the energy, has improved the utilization rate of the energy, decreased the pollution to environment.
Description
Technical field
The utility model is related to a kind of heat energy recycling system, more particularly to a kind of thermal energy about brewery recycles profit
Use system.
Background technology
Brewery is the rich and influential family of energy consumption, and energy consumption is the leading indicator of factory's feedback on performance.From initial beer
It makes in the entire production procedure of packaging, heating system is needed to provide heat source for some devices, while some devices also can be
A large amount of heat is released in production process, it is undoubtedly a kind of if the heat of these releases is expelled directly out not being collected utilization
The wasting of resources.
The utility model patent of patent No. CN200820082858.7 describes a kind of wheat juice and is poured into hot-water sterilization function recycling system
System, including precipitation tank, heat-up heat exchanger, hot-water sterilization function pump, the hot-water cylinder being sequentially connected by pipeline, precipitation tank passes through heat
Wheat juice pipeline is connected with heat exchanger for cooling, and the other end of heat exchanger for cooling passes through cold wheat juice pipeline and fermentation tank field
All fermentation tanks are connected, and discharge pipe, the discharge pipe and Recovery of the hot water tank are connected on the cold wheat juice pipeline for tank field end of fermenting
Water inlet pipe be connected, the pipeline between the outlet pipe of Recovery of the hot water tank and the hot-water cylinder to hot-water sterilization function pump is connected.Hot water
During sterilization, the flowing water Valve of opening Recovery of the hot water tank is connected with hot-water sterilization function pump to be started to sterilize, until the wheat juice of fermentation tank field
Pipe end, water inlet pipe of the sterilization hot water through discharge pipe, Recovery of the hot water tank, which is flowed into Recovery of the hot water tank, to be collected, and forms one
A closed cycle disinfection system, after return to Recovery of the hot water tank entirely, it is used for sterilizing next time.The utility model will be sterilized and be used
Recovery of the hot water recycle, save water resource and reduce energy consumption.However the utility model is only capable of the hot water of collection
It is re-used for sterilizing, recycle is limited in scope.For entire beer production equipment, there are many more the heat that equipment is discharged
It can need to be collected, and how to be widely applied to the heat of collection in suitable equipment and problem needed to be considered.
It is a system sex work the extra thermal energy effective recycling of generation.Steam consumption is the main energy of brewery
One of source consumption, the steam consumption of brewing workshop accounts for about the 40% of the total steam consumption of full factory, and the steam consumption of packing shop accounts for about 60%.
Brewing workshop steam consumption is largely recuperable, how to recycle these thermal energy, and how the thermal energy of recycling is will be using being mesh
The preceding technical issues that need to address.Suitable equipment to be recycled is found, thermal energy is efficiently recycled, and thermal energy is applied
In suitable equipment, so as to improve the utilization efficiency of heat energy of brewery, brewery's entirety energy-output ratio is reduced, is a meaning
Great research project.
Utility model content
The purpose of the utility model is to provide a kind of brewery's heat energy recycling systems, realize to main in brewery
The thermal energy recycling and utilization for the energy expenditure point wanted.
The utility model provides a kind of brewery's heat energy recycling system, including：At least one energy storage flow container, at least one
A first heat-exchanger rig, at least one second heat-exchanger rig, wherein, energy storage flow container contains at least one high temperature upper port and at least
One low temperature lower port, storage is for absorbing and discharge the energy-storage liquid of thermal energy in energy storage flow container；First heat-exchanger rig and energy-storage liquid
The high temperature upper port of tank is connected with low temperature lower port, and energy-storage liquid is flowed out from low temperature lower port, again from height after the first heat-exchanger rig
Warm upper port is flowed into energy storage flow container, and energy-storage liquid is absorbed by the first heat-exchanger rig from indirect steam, high temperature wheat juice, primary steaming
The heat of one or more of vapour condensed water release, indirect steam is the steam that the wheat juice heated in boiling pot generates, high
Warm wheat juice is that is got from whirlpool tank the possess wheat juice of higher temperature, primary steam condensed water is used in heating boiling pot
Primary steam condensation after high-temperature water；Second heat-exchanger rig is connected with the high temperature upper port and low temperature lower port of energy storage flow container,
Energy-storage liquid is flowed out from high temperature upper port, is flowed into energy storage flow container from low temperature lower port after the second heat-exchanger rig, energy-storage liquid passes through
Thermal energy is released to filtering wheat juice, brewing water, CIP liquid, syrup, bottle washing machine lye, sterilization machine and sprays hot water by the second heat-exchanger rig
One or more of.
Brewery's heat energy recycling system provided by the utility model is realized to heat production main in Beer Brewage workshop
The thermal energy recycling of device, and by the thermal energy of collection be applied to other in brewery's workshop need the device of thermal energy.Wherein
Energy storage flow container contains high temperature upper port and low temperature lower port, in thermal energy removal process, the energy-storage liquid of low temperature lower port relative to
Temperature is relatively low for the energy-storage liquid of high temperature upper port, available for being absorbed to the thermal energy that heat-producing unit discharges, generation temperature compared with
It is returned in energy storage flow container from high temperature upper port after high energy-storage liquid；In heat energy utilization, the energy-storage liquid of high temperature upper port is opposite
Temperature is higher for the energy storage of low temperature lower port, the device of thermal energy is needed to add available for being run in workshop to brewery
Heat is returned to from low temperature lower port in energy storage flow container after generating the relatively low energy-storage liquid of temperature.In this way, energy-storage liquid passes through above two
Circulating path completes the absorption and release to thermal energy, and energy-storage liquid is only used as thermal energy medium, can recycle, in this way may be used always
Ensure not being contaminated with water, and prevent the fouling of heat exchanger for production material, reduce the cleaning frequency.In addition, allow absorb thermal energy after
Energy-storage liquid enter in energy storage flow container from high temperature upper port, allow release thermal energy after energy-storage liquid enter energy-storage liquid from low temperature lower port
In tank so that energy storage flow container middle and upper part divides temperature higher, and lower part temperature is relatively low, does not easily cause in energy-storage liquid tank under different height
The heat exchange of energy-storage liquid is conducive to the layering of energy-storage liquid temperature in energy storage flow container.If being reversed up and down, i.e., in energy storage flow container
The energy-storage liquid temperature of lower part is higher, and upper portion temperature is relatively low, then the high-temperature region heat of lower part is easily passed up, and easily leads to tank body
Internal temperature mixing.
The heat energy recycling system connects the first heat-exchanger rig and the second heat-exchanger rig, wherein the first heat-exchanger rig and the
Two heat-exchanger rigs all may include a variety of heat-exchanger rigs.Boiling pot in brewery is used for heating the wheat juice after filtering, adds
Wheat juice after heat can generate indirect steam, and indirect steam thermal energy is higher, and the heat in indirect steam is carried out using energy-storage liquid
It absorbs.The heating source boiled is, for example, electrical heating, steam heating etc., and when selecting steam heating, heating source is known as primary steam,
Primary steam condensed water can be formed after primary steam heating wheat juice, the temperature of the condensed water is also higher, can be as heat to be recycled
Source.Wheat juice after heating is in whirlpool tank is entered, and the wheat juice temperature of this part is higher, and for postorder fermentation work
Sequence, the wheat juice of this part need to cool down, and energy-storage liquid and the wheat juice are carried out heat exchange by wheat juice precooler, not only recycled
Thermal energy, moreover it is possible to complete the cooling to wheat juice, improve the working efficiency of workshop.The utility model is that the thermal energy after recycling carries
More application apparatus has been supplied, such as wheat juice can have been preheated, the production water of needs has been heated, CIP devices add
Heat, the heating of syrup and is applied in bottle washing machine and sterilization machine.Can be adjusted flexibly in practical operation according to the heat of storage should
For one or more of apparatus above.Wherein CIP devices refer to situ cleaning device.
When energy storage flow container selects all to absorb the thermal energy in indirect steam, high temperature wheat juice, primary steam condensed water, and will inhale
The thermal energy of receipts be released in filtering wheat juice, brewing water, CIP liquid, syrup, bottle washing machine lye and sterilization machine spray hot water, it can be achieved that
The zero-emission of main thermal energy in brewery, the maximization and the maximization using thermal energy for completing the thermal energy of absorption.
Further, high temperature upper port and/or low temperature lower port are connected with equilibrium distributor, and energy-storage liquid is from high temperature upper port
And/or low temperature lower port enters equilibrium distributor, by equilibrium distributor energy-storage liquid sustained height different directions into
Enter in energy storage flow container.It is same that the setting of equilibrium distributor can allow the energy-storage liquid for flowing back to energy storage flow container to be evenly distributed to energy storage flow container
At the different location of height, be conducive to the temperature equalization of energy-storage liquid under sustained height in energy storage flow container.
Further, the energy-storage liquid in energy storage flow container is water.It is preferred that the energy-storage liquid in energy storage flow container is RO water.RO water be through
Cross reverse osmosis deionized water, using RO water can to avoid under long-time use due to caused by heat exchanger and relevant device fouling
Heat exchange efficiency reduces, and in addition can very significantly reduce the cleaning frequency.
Further, multiple temperature measuring equipments are equipped between high temperature upper port and the low temperature lower port.
Further, at 90-99 DEG C, the low temperature lower port flows into the temperature for the energy-storage liquid that high temperature upper port flows into
The energy-storage liquid temperature at 70-80 DEG C.
Further, flow regulator is installed on the circulation duct of energy-storage liquid, heat exchange is participated in for controlling
The flow of energy-storage liquid in the duct.It is preferred that flow regulator includes regulating valve and/or variable frequency pump.
Further, temperature measuring equipment is installed on the circulation duct of energy-storage liquid.
Further, flowmeter is installed on the circulation duct of energy-storage liquid.
Further, at least one steam heater is further included, steam heater connects the high temperature upper end in energy storage flow container
Mouthful, for heating the energy-storage liquid flowed out from high temperature upper port.The use of steam heater can carry out energy supplement to energy storage flow container,
Avoid energy-storage liquid temperature too low so that the efficiency of heating surface reduces during energy-storage liquid release thermal energy.Energy storage flow container is most in systems
In the case of it is relatively stable, sometimes because of accidentalia, can so that energy-storage liquid temperature flow out from high temperature upper port is relatively low, for guarantee
Energy-storage liquid temperature is stablized in whole system, and steam heater heating can be used, supplement a small amount of steam to improve the temperature of energy-storage liquid.
Further, above-mentioned heat energy recycling system further includes indirect steam condensation water- to-water heat exchanger, indirect steam condensation
Water condenses water- to-water heat exchanger by indirect steam and heats brewing water, and indirect steam condensed water exchanges heat for indirect steam with energy-storage liquid
The condensed water formed afterwards.The indirect steam discharged in boiling pot after indirect steam condenser and energy-storage liquid heat exchange by becoming two
Secondary steam condensate (SC), the temperature of the condensed water is still higher, and the brewing water coke slurry heat with room temperature can further reduce secondary steaming
The temperature of vapour condensed water is further reduced the discharge of thermal energy and the influence to environment in the condensed water elimination, while through adding
Brewing water after heat is flowed into hot-water cylinder and is used as production water, realizes and the further of thermal energy is collected and utilized.
Further, wheat juice recoler is further included, high temperature wheat juice forms primary cooling wheat juice after supercooling, once
It cools down wheat juice and brewing water is heated by wheat juice recoler.High temperature wheat juice passes through cooler of wheat juice and energy-storage liquid heat exchange
Afterwards, temperature is still very high, after brewing hydrothermal exchange, wheat juice temperature can be made further to drop to room temperature, and provided for brewery
Hot water is produced, improves the service efficiency of thermal energy.
Brewery's heat energy recycling system provided by the utility model has fully recycled available thermal energy, and fully
For needing in the device using thermal energy, the consumption of the energy is greatly saved, improves the utilization rate of the energy, decreases to ring
The pollution in border.
Description of the drawings
Specific embodiment of the present utility model is described in further detail below in conjunction with attached drawing.
Fig. 1 is the connection diagram of brewery's heat energy recycling system；
Fig. 2 is the structure chart of energy storage flow container；
Fig. 3 is the system schematic that energy storage flow container is connect with indirect steam condenser；
Fig. 4 is the system schematic that energy storage flow container is connect with wheat juice precooler；
Fig. 5 is the system schematic that energy storage flow container is connect with primary steam condensation water- to-water heat exchanger；
Fig. 6 is the system schematic that energy storage flow container is connect with wheat juice preheater；
Fig. 7 is the system schematic that energy storage flow container is connect with hot water heating sheet heat exchanger；
Fig. 8 is the system schematic that energy storage flow container is connect with heating jacket；
Fig. 9 is the system schematic that energy storage flow container is connect with bottle washing machine and sterilization machine.
Specific embodiment
Illustrate the embodiment of the utility model by particular specific embodiment below, those skilled in the art can be by this theory
The bright revealed content of book understands other advantages and effect of the utility model easily.Although the description of the utility model will tie
Preferred embodiment is closed to introduce together, but this feature for not representing this utility model is only limitted to the embodiment.On the contrary, knot
It is in order to cover the claim based on the utility model and it is possible that extending to close the purpose that embodiment makees utility model introduction
The other selections or transformation gone out.It will be included in order to provide the depth understanding to the utility model, in being described below many specific
Details.The utility model can not also be implemented using these details.In addition, the weight in order to avoid chaotic or fuzzy the utility model
Point, some details will be omitted in the de-scription.
Fig. 1 is the connection diagram of brewery's heat energy recycling system.As shown in the figure, energy storage flow container 1 in the present embodiment
Top be equipped with high temperature upper port 11, bottom is equipped with low temperature lower port 12, the first heat-exchanger rig connection high temperature upper port 11 and low
Warm lower port 12, the second heat-exchanger rig connection high temperature upper port 11 and low temperature lower port 12.High temperature upper port and low temperature lower port
Can be multiple, the present embodiment uses a high temperature upper port and a low temperature lower port, with high temperature upper port and low temperature lower end
The inlet/outlet pipe of the energy-storage liquid of mouth connection is antipriming pipe, and such setting just can realize the energy storage of high temperature upper port or low temperature lower port
Liquid, which can flow out, can also flow into energy storage flow container 1.The antipriming pipe of three face trepannings can be used in the present embodiment, further, allows energy-storage liquid
Flow control of the tank in pipe is in below 1.5m/s.Additionally, it is preferred that the total cross section of the trepanning on inlet/outlet pipe is cut more than inlet/outlet pipe
Area, further, trepanning total cross section are more than 1.8 times or more of inlet/outlet pipe sectional area, can reduce fluid to greatest extent
Disturbance.First heat-exchanger rig and the second heat-exchanger rig are at least one respectively, you can with by the production in heat energy recycling system
The part of heat energy exchanges heat by first heat-exchanger rig with energy-storage liquid, and energy-storage liquid is passed through second heat-exchanger rig
Thermal energy, which is released to, needs the part of thermal energy.The present embodiment selects multiple first heat-exchanger rigs and multiple second heat-exchanger rigs.Even
The first heat-exchanger rig connect has indirect steam condenser, wheat juice cooler, primary steam condensation water- to-water heat exchanger.Second heat exchange
Device has wheat juice preheater, hot water heating sheet heat exchanger, CIP heating sheet heat exchanger, heating jacket, wash bottle machine heat exchanger, sterilization
Machine heat exchanger.Thermal energy removal process, energy-storage liquid flow out through the first heat-exchanger rig from low temperature lower port 12 and absorb indirect steam, height
The thermal energy of warm wheat juice, primary steam condensed water, in absorbing the energy-storage liquid after heat from high temperature upper port 11 back to energy storage flow container.
Heat energy utilization process, energy-storage liquid flow out through the second heat-exchanger rig from high temperature upper port 11 and thermal energy are released to filtering wheat juice, wine
It makes in water, CIP liquid, syrup, bottle washing machine lye, sterilization machine spray hot water, discharges the energy-storage liquid after heat from low temperature lower port 12
Back in energy storage flow container 1.In this way, it completes the recycling of thermal energy in system and utilizes process.
It is illustrated in figure 2 the structure diagram of energy storage flow container 1.It is to reduce convection current, the top storage of energy storage flow container 1 is higher
The energy-storage liquid of lower temperature is stored in the energy-storage liquid of temperature, lower part, and centre is mixed zone, and the energy-storage liquid of different temperatures is in energy storage flow container
Interior is layered distribution.Energy storage flow container is preferably set as tall and thin shape by the present embodiment, is conducive to the energy-storage liquid point of different temperatures in tank
Layer, the preferably ratio of height to diameter of energy storage flow container are 4:1~5:1.Further, small compensator 16 there are one the tops of energy storage flow container 1,
It is connect with the big tank in energy storage flow container by an aperture, for preventing the accurate control of heat energy dissipation and effective liquid level.Behaviour
The information such as observation liquid level can be carried out by the height of the arrival compensator 16 of cat ladder 17 by making personnel.Further, high temperature upper port and/
Or low temperature lower port is connected with equilibrium distributor, energy-storage liquid enters equilibrium distributor from high temperature upper port and/or low temperature lower port,
Entered in energy storage flow container in the different directions of sustained height by equilibrium distributor energy-storage liquid.Such as shown in Figure 2
Distribution pipe 13 and distribution pipe 14 have multiple pore structures, such as multiple mesh in two distribution pipes.Energy-storage liquid is recycled by thermal energy
Flow into high temperature upper port afterwards, and then by distribution pipe 13, flowed into from multiple mesh of distribution pipe 13 in energy storage flow container 1 and with storage
Existing energy-storage liquid mixing in energy flow container.The effect of distribution pipe 14 is identical with principle.It can be allowed by distribution pipe 13 and distribution pipe 14
Energy-storage liquid is flowed out at the different location of distribution pipe 13 and distribution pipe 14 and is flowed at the unidirectional different location of energy-storage liquid tank,
Be conducive to energy-storage liquid temperature of different spaces under sustained height in energy storage flow container to keep in balance, promote the energy storage in energy storage flow container
Thermal stratification of the liquid under different height.Meanwhile when needing to take energy-storage liquid, flowed out from high temperature upper port and low temperature lower port
The temperature that is consistent of energy storage liquid energy participate in thermal energy exchange.
Further, in specific embodiment of the utility model survey is provided at the different height position of energy storage flow container 1
Warm device, such as temperature sensor 15 can detect the temperature of energy-storage liquid under different height.It can be according to temperature in practical operation
Sensor 15 understands the profiling temperatures of energy-storage liquid in energy storage flow container 1, and then understands the storage situation of heat, and according to energy storage
Thermal energy is released to one or more of above-mentioned absorption heat energy apparatus by how much selections of thermal energy in flow container 1.
Further, it is preferable to the temperature for the energy-storage liquid that high temperature upper port 11 flows into is in the range of 90-99 DEG C, preferred low temperature
The temperature for the energy-storage liquid that lower port 12 flows into is in the range of 70-80 DEG C.Energy-storage liquid in thermal energy removal process is controlled to absorb heat
Temperature afterwards is 90-99 DEG C, and temperature of the energy-storage liquid after heat release is 70-80 DEG C during heat energy utilization.Further, it controls
Temperature is 97 DEG C after energy-storage liquid absorbs thermal energy, and the temperature of control energy-storage liquid release heat is at 77 DEG C.Specifically, flow tune can be passed through
Regulating device adjusts the flow for the energy-storage liquid for participating in heat exchange, so that participating in the energy-storage liquid constant temperature after heat exchange.
The utility model can will absorb and discharge the liquid medium of thermal energy as energy-storage liquid, in following embodiment
It is middle to select water as energy-storage liquid, further preferably RO water.It is to carry out thermal energy below for energy storage water in the description of embodiment
The energy-storage liquid for recycling and utilizing.The energy storage water to circulate from low temperature lower port is known as low temperature energy storage water, high temperature upper port is circulated
Energy storage water be known as high temperature energy-storage water.
In order to more clearly describe the utility model about each component in brewery's heat energy recycling system structure with
Connection, the connection and thermal energy that following embodiment respectively will specifically introduce energy storage flow container and each heat-exchanger rig
Recycling process.
Fig. 3 is the system schematic that energy storage flow container is connect with indirect steam condenser, for recycling indirect steam release
Heat.The system includes boiling pot 22 and boiling pot 23, and the first heat-exchanger rig is indirect steam condenser 21, can in practical application
The quantity of saucepan is arranged according to specific requirements.The pressure model that pressure in boiling pot can be controlled according to needed for being set process requirements
(0mbar~500mbar) is enclosed, as normal pressure is boiled when pressure is set as 0mbar, and with pressure boil is usually used in high altitude localities,
For overcoming the situation of wheat juice low boiling point caused by High aititude.The pot inner pressure with pressure boiled by improving boiling part, from
And the wheat juice temperature of boiling part is improved, improve the evaporation intensity boiled, and convection current is strong, boiling time can accordingly shorten
Deng can not only improve and boil effect but also can save steam.
During wheat juice is boiled, indirect steam enters from exhaust tube by butterfly valve 24 and 25 for boiling pot 22 and boiling pot 23
Indirect steam condenser 21, butterfly valve 24 and butterfly valve 25 control the discharge of steam of boiling pot 22 and boiling pot 23 respectively, shown in this Fig. 2
An indirect steam condenser 21 is shared for two boiling pots, so two boiling pots there can only be one thermal energy is being used to return simultaneously
It receives, will not substantially occur the situation that two boiling pots boil simultaneously in this actual production, being also in production completely can be with
It avoids.A set of thermal energy recycling also can be individually configured in certain two boiling pots completely, and the present embodiment only enumerates one
To describe.Wherein, indirect steam condenser 21 for example can be tubular heat exchanger.
Boiling pot 22 starts to boil, and valve 24 is opened, and valve 25 is closed, and indirect steam enters indirect steam condenser 21
In shell side；While beginning is boiled, the low temperature energy storage water of 77 DEG C of the bottom of energy storage flow container 1 is by the pump 26 of frequency control from low
Warm lower port 12 exits into the tube side of indirect steam condenser 21, and the indirect steam and low temperature energy storage water of high temperature are in indirect steam
21 inside of condenser carries out thermal energy exchange, and indirect steam becomes condensed water and discharged from the bottom of indirect steam condenser 21, low temperature
Energy storage water is heated to be the upper pyrometer area that high temperature energy-storage water flow back into energy storage flow container 1 from high temperature upper port 11.Boiling part work
Skill has wheat juice temperature certain requirement, and different wheat juice temperature corresponds to certain pressure, in boiling pot 22 control of pressure lead to
The pump 26 for crossing frequency conversion is accurately adjusted, and for governing speed faster, the regulating valve 27 for being aided with Synchronization Control condensator outlet is come more
Quickly adjust the pressure inside boiling pot 22.Temperature measuring equipment 28 is equipped between energy storage flow container 1 and indirect steam condenser 21
For measure absorb indirect steam heat after energy storage water temperature, temperature measuring equipment 29 be used for measure exchange before energy storage water temperature.
Variable frequency pump 26 be used as flow regulator, control participate in exchange heat energy storage water flow, can also use regulating valve or
The mode that regulating valve is combined with variable frequency pump controls the temperature of the high temperature energy-storage water after absorbing heat to be maintained at 97 DEG C or so.
Further, the temperature of indirect steam condensed water is also very high, simultaneous with more flash steam, indirect steam condensation
Water is discharged from condenser outlet at bottom after indirect steam condenses water- to-water heat exchanger 211, and indirect steam condensation water- to-water heat exchanger 211 can
To be plate heat exchanger.When boiling beginning, synchronous to open brewing cold feed regulating valve 212, regulating valve 212 can be adjusted and be changed
The temperature TT1 of hot device outlet hot water, the brewing cold water of room temperature are heated to form 85 DEG C of brewing hot water backheat water pot 67 (such as Fig. 6 institutes
Show) to be used as production water, the indirect steam condensed water of high temperature is exchanged heat into 30 DEG C of normal-temperature water discharge.
Fig. 4 is the system schematic that cooler of energy storage flow container and wheat juice is connect, for recycling the release of high temperature wheat juice
Heat, the first heat-exchanger rig are cooler of wheat juice.There is high temperature wheat juice after boiling higher sensible heat can recycle.
The temperature of wheat juice before cooling in whirlpool tank has 98 DEG C or so.The present embodiment high temperature wheat juice uses two-stage cooling side
Formula, comprising cooler 31 of wheat juice and wheat juice recoler 35, above two cooler can be plate heat exchanger.High temperature
Wheat juice first passes through first segment cooling and transfers thermal energy to energy storage water, and wheat juice is once cooled to 85~88 DEG C, forms primary cooling
Wheat juice, low temperature heat energy water are exchanged heat to 92~95 DEG C；Second segment goes to cool down with ice water again, and the primary wheat juice that cools down continues to be cooled to
7~11 DEG C, ice water is heated to 78 DEG C or more by once cooling wheat juice.The consumption of ice water can be both reduced in this way, prevented
Excessively hot water more than needed, and heat storage extra in hot wheat juice can be used in energy storage water for other devices.
When Wort cooling starts, 98 DEG C or so high temperature wheat juice being got from whirlpool tank (not shown) pass through valve
32 enter wheat cooler 31 of juice, while 78 DEG C of low temperature energy storage water of energy storage flow container 1 are by being pumped into cooler of wheat juice
31, high temperature wheat juice and low temperature energy storage water carry out heat exchange in cooler 31 of wheat juice, and wheat juice is cooled to 85~88 DEG C, low
Warm energy storage water is heated to 95 DEG C of formation high temperature energy-storage water and returns in energy storage flow container 1, precools process mainly by pipeline
Regulating valve 33 control wheat juice outlet temperature, temperature measuring equipment 34 is used for detecting wheat juice outlet temperature.Further, primary cooling
Wheat juice afterwards carries out second segment cooling.Wheat juice recoler 35 will once cool down wheat juice by ice water (such as 2~3 DEG C) and carry out
It is cooled to technological requirement temperature, the end temperature after Wort cooling is by the regulating valve 36 of ice water inlet pipe road or ice water pump 37
Carry out variable frequency adjustment control, temperature measuring equipment 38 measures the temperature after Wort cooling.Ice water is heated to 80 DEG C and returns to hot-water cylinder 67
It is (as shown in Figure 6) to be used as production water.The hot water that Wort cooling generates is the most important brewage process water source of brewery.
Fig. 5 is the system schematic that energy storage flow container is connect with primary steam condensation water- to-water heat exchanger, for recycling primary steam
The heat of condensed water release, the first heat-exchanger rig condenses water- to-water heat exchanger for primary steam in the present embodiment.Select a water vapour
As heat source, in boiling pot 22 in boiling part, primary steam condensed water is formed after primary steam heating boiling pot, it is primary to steam
Vapour condensed water is exported by drain valve 45, water- to-water heat exchanger 41 is condensed into primary steam, with entering primary steam condensed water simultaneously
The low temperature energy storage water heat exchange of heat exchanger 41,99 DEG C of primary steam condensed water are cooled to 83 DEG C, are then sent through steam condensate (SC) tank
44 in case subsequent handling uses.The inlet of energy storage water is controlled by regulating valve 42, temperature measuring equipment 43 measures the energy storage after heating
The temperature of water, 78 DEG C of energy storage water are heated to 95 DEG C or more the high-temperature regions for returning to energy storage flow container.
In boiling part, the temperature of primary steam condensed water is higher and with certain pressure, in transmission process and discharge
To a large amount of secondary flash vapour that can be generated during normal pressure tank, the heat transfer of the primary steam condensed water is stored up to energy storage water
It deposits, it is possible to reduce primary steam condensed water flash and heat dissipation avoid the waste of thermal energy.
It is the description as described in energy storage water carries out recovery system and thermal energy removal process to thermal energy above, beer is described below
To heat energy utilization process in factory.
Fig. 6 is the system schematic that energy storage flow container is connect with wheat juice preheater, for the heat of high temperature energy-storage water to be discharged
Filtering wheat juice is given, wherein wheat juice preheater is the second heat-exchanger rig.The wheat juice temperature that lautertuns filters out generally at 73~75 DEG C,
First it can be preheated before input boiling pot boils.Energy storage flow container 1 is attached with wheat juice preheater 51, from filtering
The wheat juice that slot filters out carries out heat exchange by wheat juice preheater 51 and high temperature energy-storage water, and the heat transfer of high temperature energy-storage water is given
Wheat juice.Boiled after the heat absorption of wheat juice into boiling pot, the energy storage water after heat release become the low temperature energy storage water of 70-80 DEG C of range from
Low temperature lower port 12 returns to the bottom of energy storage flow container 1.Wheat juice is preheated by high temperature energy-storage water, it is effectively save to boil
The primary steam consumption of heating period.
Since the temperature control of above-described embodiment high temperature energy storage water is in 90-99 DEG C of range, with after filtering
Wheat juice after being preheated after wheat juice exchange heat tends not to reach the temperature close to boiling point.For example, using by 90-99 DEG C
High temperature energy-storage water can be preheating to 92 DEG C with wheat juice after the heat exchange of wheat juice, if wheat juice at this temperature is directly entered boiling pot, this wheat
There are one the longer temperature rise periods in boiling pot for juice.The easy fouling of internal heater in the temperature rise period in boiling pot, therefore
Internal heater needs frequent clean.
In order to further improve preheating after wheat juice temperature, steam heater 52 can be set.As shown in figure 5, open wheat juice
Valve 53, the valve 54 in path open simultaneously valve 55, the valve 56 of energy storage water-flowing path diameter, open steam and supply 57 He of valve
Valve 58.Steam heats 97 DEG C of the high temperature energy-storage water flowed out from energy storage flow container 1 by steam heater 52 first,
By further up to 103 DEG C of high temperature energy-storage coolant-temperature gage after the control heating of control valve 58, by 103 DEG C of high temperature energy-storage water
Heat exchange is carried out by wheat juice preheater 51 with wheat juice, wheat juice outlet temperature is controlled to rise to 98 DEG C by control valve 56, it will
98 DEG C of the wheat juice preheated, which enters in boiling pot, to be boiled.The present embodiment can not also be stored up with high temperature of the steam to 97 DEG C
Energy water is heated, and 97 DEG C of high temperature energy-storage water and 73~75 DEG C of wheat juice can exchange heat, wheat juice is heated to 92 DEG C, Zhi Hourang
Steam directly further heats the wheat juice after the heating by steam heater so that wheat juice temperature reaches 98 DEG C of left sides
The right side can also achieve the effect that identical.Wheat juice, which is preheating to close to boiling temperature, can save in boiling pot the heating-up time, have simultaneously
Effect alleviates internal heater fouling condition, reduces wash number, extends the usage time of internal heater.
Fig. 7 is the system schematic that energy storage flow container is connect with hot water heating heat exchanger, and the heat of high temperature energy-storage water passes through heat
Water heating heat exchanger is released to brewing water as the second heat exchanger.Hot water is prepared by the high temperature energy-storage water in energy storage flow container 1
It is used as production water.Valve 62, valve 63, valve 64 are opened, then opens pump 65 and pump 66, the brewing water of room temperature is added by hot water
Heat exchanger 61 is heated to 80 DEG C by 97 DEG C of high temperature energy-storage water and enters hot-water cylinder 67 as production water, is controlled by regulating valve 63
The hot water temperature that the amount of room temperature brewing water processed exports hot water heat exchanger 61 keeps stablizing, and becomes after high temperature energy-storage water release heat
For 77 DEG C of low temperature energy storage water, temperature measuring equipment 68 measures the hot water temperature that hot water heat exchanger 61 exports, and discharges the low temperature after heat
Energy storage water enters 1 bottom of energy storage flow container from low temperature lower port 12.
Heating for CIP liquid in CIP devices, connection system is identical with the heating system of above-mentioned brewing water, utilizes CIP
Heat the heat exchange that sheet heat exchanger (the second heat-exchanger rig) realizes CIP liquid and energy storage water.Saccharification in process of production, produces water
Use with CIP liquid very frequently and dosage is larger, with energy storage water come heat brewing water be substitute it is traditional it is steam-heated compared with
Good mode.The technological requirement temperature in use of hot water and CIP liquid is at 80~85 DEG C, high temperature energy-storage water of the production hot water at 97 DEG C or so
By hot water heat sheet heat exchanger the brewing water of room temperature is heated to 80 DEG C or more, can also cyclic water heating tank hot water, together
The mode of sample can be used for the heating of CIP liquid.
Fig. 8 is the system schematic that energy storage flow container is connect with heating jacket, for the heat of high temperature energy-storage water to be released to
Syrup.72 outside of syrup can is cased with heating jacket 71, and when syrup can temperature is reduced to setting value temperature, program automatically turns on syrup
Valve 73, valve 74, pump 75 are opened in heating, and high temperature energy-storage water enters the heating jacket 71 (the second heat-exchanger rig) of syrup can 72
It exchanges heat, by pumping 75 frequency control energy storage water outlet temperatures at 77 DEG C or so, when the temperature of syrup can reaches technological requirement
During set temperature, program is automatically stopped heating.
Syrup is stored temperature after a few days in storage tank and can be reduced, and viscosity becomes larger, and is unfavorable for conveying, and comes so needing to heat up
Reduce Viscosity of Syrup.Traditional mode for being heated and being kept the temperature using steam is replaced with energy storage water, effectively steam can be avoided to add
It is thermogenetic to be charred and control the shortcomings that unstable, while steam consumption is saved, equipment investment is less.
Fig. 9 is the system schematic that is connect with bottle washing machine and sterilization machine of energy storage flow container, for by the thermal energy of high temperature energy-storage water
It is released to bottle washing machine lye and sterilization machine spray hot water.Bottle washing machine and sterilization machine belong to packing shop, energy storage water supply packaging vehicle
Between path on the equipment such as pump valve generally all controlled by packing shop, bottle washing machine and sterilization machine can use energy-storage liquid simultaneously
Energy storage water in tank 1 carries out heat exchange.As shown in figure 9, wash bottle machine heat exchanger 81 is the second heat exchange with sterilization machine heat exchanger 82
Device is all connect with energy storage flow container 1.When bottle washing machine or sterilization machine needs in use, whether procedure judges condition meets,
When entire heat energy system meets use condition, program starts.Bottle washing machine starts energy storage water and heats, valve 83, valve on path
84th, valve 85 is opened, and pump 86 is opened, and 86 control water main's pressure of pump, manifold pressure can be measured by pressure sensor 816.It washes
Bottle machine energy storage water inlet regulating valve 85 controls bottle washing machine lye spray temperature according to technological requirement, and temperature can pass through temperature measuring equipment
89 observe.When sterilization machine starts the heating of energy storage water, path valve 83, valve 87, valve 88 are opened, and pump 86 starts constant pressure and supplies
Water, sterilization machine inlet adjusting valve 88 automatically adjust aperture to control the temperature of sterilization machine spray hot water, and temperature can pass through thermometric
Device 811 is observed.
When brewing room is in production, high temperature energy-storage water water temperature can meet the thermal demand of packaging generally at 97 DEG C or more,
When saccharification produces interval, 1 temperature of energy storage flow container can reduce, and the high temperature energy-storage coolant-temperature gage to ensure Gong to be packed for is stablized, and can make
It is heated with steam heater 810, supplements a small amount of steam to improve the temperature of energy storage water.Temperature measuring equipment 812 measures going out for energy storage water
Mouth temperature, procedure judges, if energy storage water outlet temperature, less than 97 DEG C of setting, valve 817 is opened, and valve 83 is closed, steam
Regulating valve 818 is opened, auto-adjustment control energy storage water outlet temperature.
It has to be ensured that recycling thermal energy efficiently uses while thermal energy recycles, brewing room, which generates a large amount of thermal energy, to be made
Other workshops use such as supply fermentation plant, packing shop in time is needed when cannoing be used up.By energy storage water sent in a manner of constant pressure to
Packing shop carries out thermal energy exchange with packaging bottle washing machine, the lye of sterilization machine or hot water, reduces the consumption of steam.
Energy storage water to packing shop supply pump (two pumps may be used) according to pressure frequency control, for packing shop
Steam heater 810 on energy storage supply mains is installed, ensures that in the energy storage coolant-temperature gage deficiency that energy storage flow container comes satisfaction can be heated
Packing shop normal use.Such design is main to consider that thermal energy is insufficient when brewing room stops production, energy storage flow container
Temperature reduces and influences packing shop use.Steam heater use can also be equally installed in the lateral that energy storage flow is led to
Energy storage water is heated, the thermal energy of energy storage water is later allowed to be released in brewery in corresponding equipment again.
Brewery's heat energy recycling system provided by the utility model, is greatly saved the consumption of the energy, improves energy
The utilization rate in source decreases the pollution to environment.With 100m3For the saccharification of/pot, every pot of recycling thermal energy is for the preheating of wheat juice
Heat Q is 236.9 ten thousand kilocalories.If this thermal energy is provided by raw steam, every raw quantity of steam M of batch of material consumption is boiled：(set saturated vapor
Pressure is 3bar, then latent heat of vaporization q is 511.1kcal/kg)
M=Q/q=2369000/511.1=4635 (kg)
By daily 12 pots, calculate within annual 300 days, whole year can save 16686 tons of steam.It is calculated with 150 yuan/ton of steam, entirely
Year can save about 2,500,000 yuan of RMB.The thermal energy redundance of boiling part recycling is additionally operable to other approach, can also save more
Thermal energy, therefore using the utility model heat energy recycling system economic benefit it is very considerable.
In addition, using above-mentioned heat energy recycling system this by such as Wort boiling process generate indirect steam exchanged heat
It condenses out and is no longer discharged into air, not only environmental protection, moreover it is possible to improve Business Economic Benefit and social benefit, belong to energy conservation and environmental protection
New technology.
It is to be released using heat energy recycling system to the recycling of the thermal energy involved in brewery, storage and by thermal energy above
It puts to the specific introduction for the equipment that thermal energy is needed in brewery.The process of Beer Brewage is often successive in practical operation
, it is above-mentioned generate and consume about thermal energy be also continuously, therefore can constantly have in energy storage flow container 1 energy storage water inflow and
Outflow, energy storage water are also what is be carried out at the same time to the recycling and utilization of thermal energy.If energy storage water recycling heat it is more, and using compared with
Few, the temperature that can cause energy storage water in energy storage flow container is higher and higher, and just thermal energy can not be absorbed again until thermal energy is full of；Phase
If the heat of anti-energy storage water recycling is less, it cannot meet and the equipment of above-mentioned institute thermal energy in need is heated, and to storing up
The excessive consumption of the thermal energy stored in energy flow container also results in energy storage coolant-temperature gage in energy storage flow container and reduces.Therefore, it is necessary to thermal energy
Recycling and using reasonably being distributed.
As described above, multiple temperature sensors 15 are set at the different height position of energy storage flow container, due to energy storage flow container 1
The temperature of middle energy storage water will appear layering in the short transverse in energy storage flow container, by observing under different height in energy storage flow container
Energy storage water temperature, the storage situation of thermal energy in energy storage flow container can be grasped in real time.If the high-temperature region of energy storage water is constantly downward
Expand, low-temperature space is gradually reduced, then energy storage increases in energy storage flow container, and can select thermal energy being released to more needs heat
Can equipment in or reduce thermal energy recycling；If the low-temperature space of energy storage water constantly expands upwards, high-temperature region is gradually reduced, meaning
It energy expenditure in energy storage flow container to increase, can select to reduce the release of thermal energy in energy storage flow container or the recycling of increase thermal energy.
Further, the present embodiment is by installation temperature measuring equipment and volume control device on the pipeline that leads in energy storage flow,
And high temperature range and low temperature range are set, adjust the flow that energy storage water participates in heat exchange so that temperature is protected after the heat absorption of energy storage water
The temperature of the energy storage water after high temperature range, heat release is held in low temperature range so that the storage that the high temperature upper port 11 of energy storage flow container 1 flows into
Can water in high temperature range, the energy storage water that port 12 flows at low temperature is in low temperature range.Energy storage water can be allowed in this way in energy-storage liquid
Thermal stratification is realized from top to bottom in tank 1, so as to judge the storage of thermal energy therein according to the variation of energy storage flow container medium temperature degree
Deposit situation.That is, temperature and thermal energy are linked together, temperature value and situation of change can be utilized conveniently, intuitively
It is inferred to heat content and thermal energy situation of change.Exist due to mentioning the wheat juice temperature after lautertuns filters in above-described embodiment
73-75 DEG C, the temperature of the low temperature energy storage water after being preheated to wheat juice is generally not less than the temperature of wheat juice before preheating, in addition in view of
Energy storage water absorbs the Temperature Distribution after thermal energy, and the setting of high temperature range and low temperature range can be drawn according to actual production workshop situation
Fixed, the preferably above-mentioned high temperature range of various embodiments of the utility model is at 90-99 DEG C, and low temperature range is at 70-80 DEG C, further high temperature
Range may be designated as 97 DEG C, and low temperature range is defined as 77 DEG C.
Further, the sequence for not having to heat energy recycle situation and carrying out priority that Fig. 3-9 can be described.It is returned in thermal energy
During receipts, priority is followed successively by indirect steam, high temperature wheat juice, primary steam condensed water；During heat energy utilization, priority
It is followed successively by filtering wheat juice, brewing water, CIP liquid, syrup, bottle washing machine lye, sterilization machine spray hot water.Such as it is stored up when in energy storage flow container
When the thermal energy deposited is not enough to the device heat supply to above-mentioned thermal energy in need, the thermal energy of storage is released to filtering wheat by preferential selection
Juice has more than needed if thermal energy also has, then thermal energy is released to brewing water, and release thermal energy is selected with this order.When the thermal energy of storage fills
When sufficient, thermal energy can be released to filtering wheat juice, brewing water, CIP liquid, syrup, bottle washing machine lye and sterilization machine spray hot water.This reality
Apply example can also install steam heater on the pipeline that high temperature energy-storage flow is led to, prevent energy storage flow container high temperature energy storage coolant-temperature gage compared with
Low situation allows the temperature of the high temperature energy-storage water flowed out from high temperature upper port 12 to ensure range at 90-99 DEG C.If the heat of storage
Can be more, extra thermal energy can be generally released to the device of above-mentioned thermal energy in need, while reduce the recycling of thermal energy, as above
Secondly order, the thermal energy of priority reclamation indirect steam can further recycle the thermal energy of high temperature wheat juice, followed by come from as needed
The thermal energy of primary steam condensed water.
Furthermore, it is understood that in the case where not changing absorption heat content, the registration of temperature sensor 15, this implementation are observed
Example is uniformly arranged five temperature sensors 15 from top to bottom in energy storage flow container short transverse.Since the variation of certain working conditions is led
For the energy storage coolant-temperature gage for causing there was only 1/5 part in energy storage flow container 1 at 90-99 DEG C, i.e., 90-99 DEG C of high temperature energy-storage water only accounts for energy-storage liquid
Tank 1 1/5 when, thermal energy is only released to filtering wheat juice by preferential selection；When there is 2/5 90-99 DEG C of high temperature energy-storage water, by thermal energy
It is released to filtering wheat juice and brewing water；When containing 3/5 90-99 DEG C of high temperature energy-storage water, thermal energy is released to filtering wheat juice, is made
Make water, CIP liquid.And so on, when being full of high temperature energy-storage water in energy storage flow container, thermal energy is released to above-mentioned institute thermal energy in need
Equipment in.In the case where not changing release heat content, if the thermal energy in energy storage flow container persistently increases and not up to balances
State preferentially can only recycle the thermal energy of indirect steam, if the space for also having 2/5 in energy storage flow container is low temperature space, increase back
The thermal energy from high temperature wheat juice is received, if still there is the space of storage thermal energy, continues to recycle the thermal energy from primary steam condensed water.
Above-mentioned recycled about thermal energy with the selection utilized and concrete numerical value is the utility model one of which specific embodiment, not
As the limitation to the utility model.
Further, thermal energy will be recycled by taking a kind of concrete condition of practical operation as an example below and the distribution that utilizes into
Row description, but the description of type and concrete numerical value for absorbing and discharging below in relation to specific choice is not intended as to this practicality
Novel limitation.
Five temperature sensors 15 are uniformly arranged from top to bottom in 1 short transverse of energy storage flow container, and provide from top to bottom five
A temperature sensor is followed successively by the first temperature sensor, second temperature sensor, third temperature sensor, the 4th temperature sensor
With the 5th temperature sensor.Under normal conditions when heat absorption is more, the temperature of energy storage water can continue to increase in energy storage flow container 1,
When the temperature that the 5th temperature sensor is shown reaches 97 DEG C or more, illustrate that energy storage flow container 1 can not store more heat again
Energy can stop the absorption process of thermal energy at this time；On the other hand it when the temperature that the first temperature sensor is shown is below 85 DEG C, says
Heat content in bright energy storage flow container 1 is relatively low, can select to terminate the utilization process of thermal energy.When the first temperature sensor is higher than 85
DEG C when, can select release thermal energy.For example, all absorbing indirect steam condensed waters, high temperature wheat juice, primary steam condensed water
In the case of, it, only will be in energy storage water when the first temperature sensor registration is higher than 95 DEG C and second temperature sensor is less than 95 DEG C
Thermal energy is released to filtering wheat juice；When second temperature sensor is higher than 95 DEG C and third temperature sensor is less than 95 DEG C, by thermal energy
It is released to filtering wheat juice and brewing water；It, will when third temperature sensor is higher than 95 DEG C and the 4th temperature sensor is less than 95 DEG C
Thermal energy is released to filtering wheat juice, brewing water, CIP liquid；When the 4th temperature sensor higher than 95 DEG C and the 5th temperature sensor is less than
At 95 DEG C, thermal energy is released to filtering wheat juice, brewing water, CIP liquid, syrup；It, will be hot when the 5th temperature sensor is higher than 95 DEG C
Filtering wheat juice, brewing water, CIP liquid, syrup, bottle washing machine lye and sterilization machine spray hot water can be released to.In the first temperature sensing
It, can be to filtering wheat juice release heat, due to the high temperature energy-storage coolant-temperature gage flowed out at this time when device temperature is higher than 85 DEG C less than 95 DEG C
It is relatively low, supplement thermal energy using steam heater 810 so that high temperature energy-storage coolant-temperature gage reaches 90 DEG C or more.
The content that release thermal energy can also equally be fixed is constant, selects absorbing thermal energy.For example, by energy storage flow container
In the case that thermal energy is released to filtering wheat juice, brewing water, CIP liquid, syrup, bottle washing machine lye and sterilization machine spray hot water, when the
When five temperature sensor registrations are higher than 97 DEG C less than 97 DEG C and the 4th temperature sensor, energy storage water is only absorbed from indirect steam
Thermal energy；When the 4th temperature sensor registration is less than 97 DEG C and third temperature sensor is higher than 97 DEG C, energy storage water absorbs secondary steaming
The thermal energy of vapour and high temperature wheat juice；When third temperature sensor registration is less than 97 DEG C and second temperature sensor is higher than 97 DEG C, storage
Energy water absorbs the thermal energy of indirect steam, high temperature wheat juice and primary steam condensed water.
The selection of above-mentioned priority is merely illustrative, and priority order also can be changed in those skilled in the art.It is in addition, fixed complete
Portion absorbs or discharge thermal energy or fixed part absorbs or release thermal energy can be also adjusted.Above-mentioned heat absorption and the conjunction utilized
Reason distribution avoids the situation that energy storage flow container internal heat energy is superfluous or thermal energy is in short supply, realizes thermal energy recycling and the maximum of utilization ratio
Change, be conducive to the recycling of thermal energy in production process with using stablize and carry out.
The selection thermal energy that all recycling indirect steam, high temperature wheat juice, primary steam condensed water discharge, and thermal energy is all transported
For needing in the device of thermal energy, it can be achieved that the mainly utilization of heat-producing unit in brewery's production, has greatly saved thermal energy
Consumption improves the utilization rate of thermal energy.
It is counted for the ease of the energy consumption in each workshop, electromagnetic current is installed on energy storage water supplying pipe road and water return pipeline
Gauge, such as shown in figure 9, flowmeter 814 and flowmeter 815 are separately positioned on high temperature energy-storage water and low temperature energy storage water flows through
On pipeline, the temperature that is measured by temperature measuring equipment 812 and temperature measuring equipment 813 is understood before energy storage water release thermal energy and release thermal energy
Temperature afterwards, can be according to specific heat capacity calculation formula, and in the case where understanding the parameter such as thermal capacitance, calculates the use of thermal energy
Amount, same mode can also calculate the specific alluvial of thermal energy, obtain more accurate thermal energy flow-data, be conducive to
The accurate matching with utilizing is recycled to the accurate control of production process and thermal energy, the convenient thermal energy of adjustment in real time recycles and utilize work
Skill.
In addition, the quantity using energy storage flow container can not be as the limitation to the utility model, for the number of energy storage flow container
The parameters such as amount, size can be determined according to the scale of actual production brewery.
The above embodiments are only illustrative of the principle and efficacy of the utility model, new not for this practicality is limited
Type.Any person skilled in the art can all carry out above-described embodiment under the spirit and scope without prejudice to the utility model
Modifications and changes.Therefore, such as those of ordinary skill in the art without departing from the revealed essence of the utility model
All equivalent modifications completed under refreshing and technological thought or change, should be covered by the claim of the utility model.
Claims (13)
1. a kind of brewery's heat energy recycling system, which is characterized in that including：At least one energy storage flow container, at least one
One heat-exchanger rig, at least one second heat-exchanger rig, wherein,
The energy storage flow container contains at least one high temperature upper port and at least one low temperature lower port, is stored in the energy storage flow container
For absorbing and discharging the energy-storage liquid of thermal energy；
First heat-exchanger rig is connected with the high temperature upper port of the energy storage flow container and the low temperature lower port, the storage
Energy liquid is flowed out from the low temperature lower port, and the energy-storage liquid is flowed into from the high temperature upper port again after first heat-exchanger rig
In tank, the energy-storage liquid is absorbed by first heat-exchanger rig in indirect steam, high temperature wheat juice, primary steam condensed water
One or more of releases heats, the indirect steam is the steam that the wheat juice heated in boiling pot generates, the high temperature
Wheat juice is that is got from whirlpool tank the possess wheat juice of higher temperature, the primary steam condensed water is heating boiling pot institute
High-temperature water after primary steam condensation；
Second heat-exchanger rig is connected with the high temperature upper port of the energy storage flow container and the low temperature lower port, the storage
Energy liquid is flowed out from the high temperature upper port, and the energy storage flow container is flowed into from the low temperature lower port after second heat-exchanger rig
In, thermal energy is released to filtering wheat juice, brewing water, CIP liquid, syrup, wash bottle by the energy-storage liquid by second heat-exchanger rig
One or more of machine lye, sterilization machine spray hot water.
2. brewery's heat energy recycling system as described in claim 1, which is characterized in that the high temperature upper port and/or
The low temperature lower port is connected with equilibrium distributor, and the energy-storage liquid is from the high temperature upper port and/or the low temperature lower port
Into the equilibrium distributor, enter institute by different directions of the equilibrium distributor energy-storage liquid in sustained height
It states in energy storage flow container.
3. brewery's heat energy recycling system as described in claim 1, which is characterized in that the energy storage in the energy storage flow container
Liquid is water.
4. brewery's heat energy recycling system as claimed in claim 3, which is characterized in that the energy storage in the energy storage flow container
Liquid is RO water.
5. brewery's heat energy recycling system as described in claim 1, which is characterized in that the high temperature upper port and described
Multiple temperature measuring equipments are equipped between low temperature lower port.
6. brewery's heat energy recycling system as described in claim 1, which is characterized in that the high temperature upper port flowed into
The temperature of the energy-storage liquid is at 90-99 DEG C, and the temperature for the energy-storage liquid that the low temperature lower port flows into is at 70-80 DEG C.
7. such as claim 1-6 any one of them brewery heat energy recycling system, which is characterized in that in the energy-storage liquid
Circulation duct on flow regulator is installed, for controlling the energy-storage liquid flow in the duct for participating in heat exchange.
8. brewery's heat energy recycling system as claimed in claim 7, which is characterized in that the flow regulator includes
Regulating valve and/or variable frequency pump.
9. brewery's heat energy recycling system as claimed in claim 7, which is characterized in that in the runner pipe of the energy-storage liquid
Temperature measuring equipment is installed on road.
10. brewery's heat energy recycling system as claimed in claim 9, which is characterized in that in the circulation of the energy-storage liquid
Flowmeter is installed on pipeline.
11. brewery's heat energy recycling system as described in claim 1, which is characterized in that further include at least one steam
Heater, the steam heater connect the high temperature upper port in the energy storage flow container, for heating from the high temperature
The energy-storage liquid of port outflow.
12. brewery's heat energy recycling system as described in claim 1, which is characterized in that further include indirect steam condensation
Water- to-water heat exchanger, indirect steam condensed water condense water- to-water heat exchanger by the indirect steam and heat brewing water, and the indirect steam is cold
The condensed water that condensate is formed after exchanging heat with the energy-storage liquid for the indirect steam.
13. brewery's heat energy recycling system as described in claim 1, which is characterized in that further include wheat juice secondary cooling
Device, the high temperature wheat juice form primary cooling wheat juice after supercooling, and the primary cooling wheat juice is secondary cold by the wheat juice
But device heating brewing water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721276931.XU CN207472107U (en) | 2017-09-30 | 2017-09-30 | Brewery's heat energy recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721276931.XU CN207472107U (en) | 2017-09-30 | 2017-09-30 | Brewery's heat energy recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207472107U true CN207472107U (en) | 2018-06-08 |
Family
ID=62267406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721276931.XU Active CN207472107U (en) | 2017-09-30 | 2017-09-30 | Brewery's heat energy recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207472107U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109595956A (en) * | 2017-09-30 | 2019-04-09 | 宁波乐惠国际工程装备股份有限公司 | Brewery's heat energy recycling system and method |
| CN110762513A (en) * | 2019-11-01 | 2020-02-07 | 福建蓝海节能科技有限公司 | Boiler steam condensation bin |
| CN109595956B (en) * | 2017-09-30 | 2024-11-19 | 宁波乐惠国际工程装备股份有限公司 | Heat energy recycling system and method for breweries |
-
2017
- 2017-09-30 CN CN201721276931.XU patent/CN207472107U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109595956A (en) * | 2017-09-30 | 2019-04-09 | 宁波乐惠国际工程装备股份有限公司 | Brewery's heat energy recycling system and method |
| CN109595956B (en) * | 2017-09-30 | 2024-11-19 | 宁波乐惠国际工程装备股份有限公司 | Heat energy recycling system and method for breweries |
| CN110762513A (en) * | 2019-11-01 | 2020-02-07 | 福建蓝海节能科技有限公司 | Boiler steam condensation bin |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207990991U (en) | Cold-hot water exchange device | |
| CN205262270U (en) | Movable heat energy deposit device | |
| CN201091512Y (en) | Electric boiling water machine | |
| CN106010913A (en) | Distillation liquor brewing device adopting circulating steam | |
| CN203703937U (en) | Duplex heat energy recycling and wastewater using device for combined cooling and heating boiler | |
| CN103184299B (en) | Heat recovery method and heat recovery device for slag flushing water of iron and steel plant | |
| CN207472107U (en) | Brewery's heat energy recycling system | |
| CN108937583A (en) | A kind of instant heating type drinking machine | |
| CN102363125B (en) | Water circulation method used in laboratory circulation-water-type water distiller | |
| CN109595956A (en) | Brewery's heat energy recycling system and method | |
| CN202671242U (en) | Preheating energy-saving distillation apparatus | |
| CN109595956B (en) | Heat energy recycling system and method for breweries | |
| CN206783619U (en) | A kind of waste heat of coke oven crude gas retracting device | |
| CN203949348U (en) | Continous way electric water-boiling device | |
| CN204780279U (en) | Overflow dyeing machine waste heat recovery device | |
| CN208803050U (en) | Wine liquid circulation heat exchanger | |
| CN209153194U (en) | A kind of instant heating type drinking machine | |
| CN203656899U (en) | Waste heat boiler blowdown heat exchange device | |
| CN206142860U (en) | Device is used multipurposely to used heat | |
| CN206755647U (en) | A kind of absorption heat exchange device | |
| CN104605738B (en) | A kind of drinker hot guard system using heat of compressor | |
| CN103933747B (en) | Acid bath flash evaporation device with evaporator and process | |
| CN201056559Y (en) | Inner boiling device of malt wort boiling device and equipment for producing malt wort | |
| CN207877674U (en) | A kind of peanut oil production line steam supply equipment | |
| CN208465198U (en) | A kind of new pyridine extraction tower reboiler |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |