CN209010474U - Malt digesting apparatus secondary steam utilizing system - Google Patents
Malt digesting apparatus secondary steam utilizing system Download PDFInfo
- Publication number
- CN209010474U CN209010474U CN201821027941.4U CN201821027941U CN209010474U CN 209010474 U CN209010474 U CN 209010474U CN 201821027941 U CN201821027941 U CN 201821027941U CN 209010474 U CN209010474 U CN 209010474U
- Authority
- CN
- China
- Prior art keywords
- outlet
- steam
- water
- hot water
- heat exchanger
- 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.)
- Expired - Fee Related
Links
Landscapes
- Feeding And Controlling Fuel (AREA)
Abstract
The utility model discloses a kind of malt digesting apparatus secondary steam utilizing system, include: oil burning boiler, wort copper provided, the first tubular heat exchanger and the second tubular heat exchanger, wort copper provided include: wort copper provided ontology, set on wort copper provided ontology bottom wall higher pressure steam inlet and condensation-water drain, the wheat juice entrance to be boiled set on one side wall, boiling the outlet of wheat juice and exported set on the secondary steam of roof set on another side wall；First tubular heat exchanger includes: the first high-temperature steam entrance, the first condensation-water drain, cold water inlet and hot water outlet, first high-temperature steam entrance is connected with the outlet of the secondary steam of wort copper provided, and hot water outlet is connected by pipeline with the water inlet of oil burning boiler；Second tubular heat exchanger includes: that the second high-temperature steam entrance, the second condensation-water drain, cold wheat juice entrance and the outlet of hot wheat juice, the second high-temperature steam entrance are connected with the outlet of the secondary steam of wort copper provided.
Description
Technical field
The utility model relates to a kind of afterheat utilizing systems more particularly to a kind of steam waste heat to utilize system.
Background technique
Wort boiling is one of critical process in Beer Brewage, and purpose includes that evaporation water, concentrated wort, wheat juice kill
Different miscellaneous foul smell etc. in bacterium, inactive enzyme, the denaturation flocculation of protein, the leaching of hops effective component and exclusion wheat juice.
The process of Wort boiling needs to consume a large amount of steam, steam consumption be about the total steam consumption of beer brewing 40%~
50%, generated " water vapour " people are referred to as " secondary steam " during Wort boiling, and boiling pot secondary steam band
The heat walked accounts for again boils 50% of steam consumption or so.
Currently, Wort boiling mainly uses normal pressure boiling process, the secondary steam that boiling part generates is directly discharged into atmosphere.
A large amount of secondary steam is discharged into atmosphere, not only causes the waste of the energy, but also form white pollution.Due to secondary steam
In containing with other volatile components similar in water boiling point, therefore directly utilized after cannot being liquefied, but heat can be passed through and handed over
It changes using heat, generates high temperature thermal medium, then make using after high temperature thermal medium preheating wheat juice or heating clean water for each workshop
With.
A kind of malt boiling afterheat utilizing system as disclosed in Chinese patent application discloses No. 201310524029.5, packet
The kit of whole design, overall package and integrated testability is included, core component includes residual heat collection system, waste heat use system
System, automatic control system three parts.The system passes through the flash tank of piping connection, hot water basin, heating device, water inlet pipe, row
Water pipe, wash bottle unit.The waste heat and flash steam of malt cooker absorb heat by spray equipment in flash tank and tank, into heat
After water surge tank, distributes to bottle washing machine and sterilization machine uses.However, the malt boiling afterheat utilizing system that the patent application discloses
Using residual steam for bottle-washing, remaining hot water for recycling fire demand water and cooling tower moisturizing, for steam thermal energy
Utilization efficiency it is lower.
A kind of Wort boiling side for recyclable secondary steam that for another example Chinese patent application CN104629968A is disclosed
Method, this method are transported to heater after mixing the secondary steam in boiling pot with raw steam again and heat to wheat juice, in this way
Method for boiling not only increase the utilization rate of secondary steam, and also improve the quality of beer.However, the patent application is taken off
The Wort boiling method of the recyclable secondary steam shown does not utilize the flue gas heat for generating raw steam rationally, and secondary
The utilization of steam is more single, is not suitable for handling a large amount of steam, can not popularize industrial application.
Therefore it provides it is a kind of can make full use of wheat juice boiling generation secondary steam, and supply boiling reuse with
The malt digesting apparatus secondary steam utilizing system for realizing that the limit of waste heat recycles becomes urgent problem in the industry.
Summary of the invention
The purpose of the utility model is to provide a kind of malt digesting apparatus secondary steam utilizing systems, can make full use of
The secondary steam that wheat juice boiling generates, while also recycling for waste heat energy is realized using boiler smoke heat.
To achieve the goals above, the utility model provides a kind of malt digesting apparatus secondary steam utilizing system, comprising:
Oil burning boiler, the wort copper provided being connected with oil burning boiler by steam suppling tube road, wherein oil burning boiler includes boiler sheet
Body, be set to boiler body one side wall fuel filler and help fuel gas inlet, neighbouring fuel filler to be set to boiler body
Internal flame burner, set on boiler body another end wall exhanst gas outlet and set on the top of boiler body into
The mouth of a river and higher pressure steam outlet；Wort copper provided include: wort copper provided ontology, set on wort copper provided ontology bottom wall height
Press steam inlet and condensation-water drain, set on wort copper provided ontology one side wall wheat juice entrance to be boiled, be set to Wort boiling
The secondary steam outlet for boiling the outlet of wheat juice and the roof set on wort copper provided ontology of another side wall of pot ontology.Wheat
Bud digesting apparatus secondary steam utilizing system further include: the secondary steam outlet with wort copper provided passes through secondary steam discharge pipe
The first tubular heat exchanger and the second tubular heat exchanger that road is connected, wherein the first tubular heat exchanger includes: the first high-temperature steam
Entrance, the first condensation-water drain, cold water inlet and hot water outlet, the first high-temperature steam entrance and secondary steam discharge line
It is connected, cold water inlet is connected by pipeline with cold water source, and hot water outlet is connected by pipeline with the water inlet of oil burning boiler
It connects so that the hot water formed after heat exchange is provided to oil burning boiler；Second tubular heat exchanger includes: the second high-temperature steam entrance, second
Condensation-water drain, cold wheat juice entrance and the outlet of hot wheat juice, the second high-temperature steam entrance are connected with secondary steam discharge line
It connects, cold wheat juice entrance is connected with Mai Zhiyuan to be processed, and hot wheat juice outlet is connected with wheat juice basin.
Preferably, 60%~80% secondary steam for accounting for secondary steam total amount enters the first tubular heat exchanger, Zhan Erci
20%~40% secondary steam of steam total amount enters the second tubular heat exchanger.
Selectively, hot water is equipped between the pipeline of the water inlet of the hot water outlet and oil burning boiler of the first tubular heat exchanger
Basin, hot water basin are equipped with hot water inlet, the first hot water outlet and the second hot water outlet, hot water inlet and the first tubular heat exchanger
Hot water outlet be connected, the first hot water outlet is connected with the water inlet of oil burning boiler.
Selectively, the pipeline between the first hot water outlet of hot water basin and the water inlet of oil burning boiler is equipped with deoxygenation
Device, oxygen-eliminating device include shell, the deoxygenation water inlet being set on shell, deoxidation water out, the carbonated drink point for being set to interior of shell
From device and rotating-film tube, deoxygenation water inlet is connected with by part delivery to deoxygenation with the first hot water outlet of hot water basin
Deoxygenation in device, deoxidation water out be connected with the water inlet of oil burning boiler using will the delivery through deoxidation to oil burning boiler as
Boiler feedwater
It selectively, further include heat exchanger and waste heat boiler, wherein heat exchanger includes: high-temperature flue gas entry, low temperature
Exhanst gas outlet, low temperature heat conducting oil inlet and high-temperature heat-conductive oil export, the exhanst gas outlet phase of high-temperature flue gas entry and oil burning boiler
Connection, low-temperature flue gas outlet are connected with chimney；Waste heat boiler includes: high-temperature heat-conductive oil-in, low temperature conduction oil outlet, hot water
Entrance and steam outlet, high-temperature heat-conductive oil-in are connected with the high-temperature heat-conductive oil export of heat exchanger, low temperature conduction oil
Outlet is connected with the low temperature heat conducting oil inlet of heat exchanger, and hot water inlet is connected with the second hot water outlet of hot water basin,
Steam outlet is connected with the higher pressure steam inlet of wort copper provided.
Preferably, the conduction oil that the utility model is selected can choose alkyl biphenyl ether type conduction oil or mineral oil.
Preferably, oil burning boiler is heavy oil oil burning boiler.
Selectively, the wheat juice exit of boiling of wort copper provided is equipped with detachable sieve to filter out the residue in wheat juice.
It selectively, further comprise vapor collecting apparatus, vapor collecting apparatus includes the high steam with oil burning boiler
Export the first vapor inlet port being connected, the second steam input port for being connected with the steam outlet of waste heat boiler and
The steam outlet being connected with the higher pressure steam inlet of wort copper provided.
It selectively, further comprise condensed water collecting device, condensed water collecting device includes: and the first tubular heat exchanger
The first condensation-water drain be connected the first condensation water input, be connected with the second condensation-water drain of the second tubular heat exchanger
The second logical condensation water input and the condensation water output being connected with the cold water inlet of the first tubular heat exchanger.
Wherein, the temperature of the hot water of the hot water exit of the first tubular heat exchanger is 92~99 degrees Celsius, and the second tubulation changes
The temperature of the hot wheat juice in the hot wheat juice exit of hot device is 85~95 degrees Celsius.
Wherein, the flue-gas temperature of the smoke outlet of oil burning boiler is 220~250 degrees Celsius, the low temperature cigarette of heat exchanger
The flue-gas temperature of gas outlet is 130~160 degrees Celsius.
Wherein, the thermally conductive oil temperature of the high temperature heat conductive oil inlet of waste heat boiler is 150~180 degrees Celsius, waste heat boiler
Low temperature conduction oil outlet at thermally conductive oil temperature be 120~140 degrees Celsius.Hot water temperature at the hot water inlet of waste heat boiler
It is 92~99 degrees Celsius, the steam temperature at the steam outlet of waste heat boiler is 110~130 degrees Celsius.
Preferably, the volume settings for the wheat juice tank that the utility model is selected are 55 cubic metres or more.
Selectively, due to using the inhomogeneities of hot water, the volume settings for the hot water basin that the utility model is selected are
50 cubic metres or more.
Selectively, the volume settings of the first tubular heat exchanger and the second tubular heat exchanger are 155 cubic metres or more.
The beneficial effects of the utility model are: the heat of (1), the secondary steam for making full use of wort copper provided to generate, leads to
It crosses the first tubular heat exchanger and cold water is heated to be about 96 degrees Celsius of hot water using the thermal energy of secondary steam, part hot water is as fuel oil
Boiler feedwater improves the heavy oil combustion efficiency in oil burning boiler, and saving fuel oil while reduces production cost, passes through the second tubulation
Wheat juice is heated to 92 degrees centigrades using the thermal energy of secondary steam by heat exchanger, in case next heating link uses；(2), sharp
With the heat of the high-temperature flue gas of oil burning boiler, after being exchanged heat by heat exchanger and conduction oil, conduction oil heat exchanger with
It is circulated between waste heat boiler, 96 degrees Celsius of hot water that the first tubular heat exchanger of heating generates, generates 120 degrees Celsius of water and steam
Vapour is used for boiling wheat juice；(3), for the high-temperature flue gas of oil burning boiler after heat exchange, temperature is reduced to about 150 degrees Celsius to arrange again
Out, the thermal pollution caused by environment is reduced；(4), the malt digesting apparatus secondary steam utilizing system of the utility model can be used
In a large amount of wheat juice of industrial treatment, later period high repayment is obtained with initial stage lower investment, investment is recycled and is expected to be three months.
Detailed description of the invention
Fig. 1 is the schematic diagram of the malt digesting apparatus secondary steam utilizing system of the utility model.
Fig. 2 is the schematic diagram of another embodiment of the utility model.
Specific embodiment
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning
Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by ginseng
The embodiment for examining attached drawing description is exemplary, it is intended to for explaining the utility model, and should not be understood as to the utility model
Limitation.
Firstly, referring to Fig.1, a kind of non-limiting embodiment according to the present utility model, the secondary steaming of malt digesting apparatus
Vapour includes: oil burning boiler 10, wort copper provided 20, the first tubular heat exchanger 30, the second tubular heat exchanger 40, hot water using system
Basin 50 and wheat juice basin 60.
Wherein, oil burning boiler 10 include: boiler body 101, be set to boiler body 101 one side wall fuel filler
102 and the flame burner of the inside for helping fuel gas inlet 103, neighbouring fuel filler 102 to be set to boiler body 101 (do not show
Out), the exhanst gas outlet 104 set on another end wall of boiler body 101,105 and of water inlet set on the top of boiler body 101
Higher pressure steam outlet 106.
Wort copper provided 20 include: wort copper provided ontology 201, set on wort copper provided ontology 201 bottom wall high pressure
Steam inlet 202 and condensation-water drain 203, set on wort copper provided ontology one side wall wheat juice entrance 204 to be boiled, be set to wheat
Another side wall of juice boiling pot ontology 201 boils wheat juice outlet 205 and the roof set on wort copper provided ontology 201
Secondary steam outlet 206, higher pressure steam inlet 202 passes through the higher pressure steam outlet of steam suppling tube road L1 and oil burning boiler 10
106 are connected.
First tubular heat exchanger 30 and the second tubular heat exchanger 40 are boiled by secondary steam discharge line L2 and wheat juice respectively
The secondary steam outlet 206 of boiling pot 20 is connected.Wherein, the first tubular heat exchanger 30 include: the first high-temperature steam entrance 301,
First condensation-water drain 302, cold water inlet 303 and hot water outlet 304, hot water outlet 304 are connected with hot water basin 50.The
Two tubular heat exchangers 40 include: the second high-temperature steam entrance 401, the second condensation-water drain 402, cold wheat juice entrance 403 and heat
Wheat juice outlet 404, hot wheat juice outlet 404 are connected with wheat juice basin 60.
Hot water basin 50 is equipped with the first hot water outlet 501, the second hot water outlet 502 and hot water inlet 503, hot water inlet
503 are connected with the hot water outlet 304 of the first tubular heat exchanger 30.
It further include oxygen-eliminating device 70, heat exchanger 80 and waste heat boiler 90 as a kind of alternative embodiments.
As shown in Figure 1, oxygen-eliminating device 70 includes shell 701, the deoxygenation water inlet 702 being set on shell, deoxidation water out
703, the steam-water separator (not shown) and rotating-film tube (not shown) being set to inside shell 701, deoxygenation water inlet 702 and heat
First hot water outlet 501 of water basin 50 is connected, thus by deoxygenation in part delivery to oxygen-eliminating device 70, deoxidation water out
703 are connected with the water inlet 105 of oil burning boiler 10, so that the delivery through deoxidation to oil burning boiler 10 be given as boiler
Water supplement.
Heat exchanger 80 include: high-temperature flue gas entry 801, low-temperature flue gas outlet 802, low temperature heat conducting oil inlet 803 and
High-temperature heat-conductive oil export 804, high-temperature flue gas entry 801 are connected with the exhanst gas outlet 104 of oil burning boiler 10, low-temperature flue gas outlet
802 are connected with chimney.Waste heat boiler 90 includes: high-temperature heat-conductive oil-in 901, low temperature conduction oil outlet 902, hot water inlet
903 and steam outlet 904, high-temperature heat-conductive oil-in 901 be connected with the high-temperature heat-conductive oil export 804 of heat exchanger 80,
Low temperature conduction oil outlet 902 is connected with the low temperature heat conducting oil inlet 803 of heat exchanger 80, hot water inlet 903 and hot water basin
50 the second hot water outlet 502 is connected, and steam outlet 904 is connected with the higher pressure steam inlet 202 of wort copper provided 20.
It is collected for the ease of the multichannel of steam, in another alternative embodiments, system is additionally provided with vapor collecting apparatus S
With condensed water collecting device C, as shown in Figure 1, vapor collecting apparatus S includes 106 phase of higher pressure steam outlet with oil burning boiler 10
Connection the first vapor inlet port S1, be connected with the steam outlet 904 of waste heat boiler 90 the second steam input port S2, with
And the steam outlet S3 being connected with the higher pressure steam inlet 202 of wort copper provided 20.Condensed water collecting device C include: with
The the first condensation water input C1 and the second tubulation that first condensation-water drain 302 of the first tubular heat exchanger 30 is connected exchange heat
The second condensation water input C2 and cold with the first tubular heat exchanger 20 that second condensation-water drain 402 of device 40 is connected
Water inlet 303 be connected being recycled again condensed water as cold water supplement condensation water output C3.
As a result, in the non-limiting embodiment, heavy oil burn in oil burning boiler 10 generation high-pressure water vapor from
Higher pressure steam outlet 106 is entered in wort copper provided 20 from higher pressure steam inlet 202 to from wheat by steam suppling tube road L1
Juice basin 60 is boiled by wheat juice entrance 204 to be boiled into wheat juice therein, the condensed water that steam generates after boiling wheat juice
It is discharged by condensation-water drain 203, the wheat juice after boiling is discharged from wheat juice outlet 205 is boiled, the secondary steaming generated in boiling part
Vapour respectively enters the first tubular heat exchanger 30 and secondary series with secondary steam discharge line L2 from 206 discharge of secondary steam outlet
Heat exchange of heat pipe 40.Wherein, 70% secondary steam for accounting for secondary steam total amount enters first row from the first high-temperature steam entrance 301
In heat exchange of heat pipe 30,96 degrees Celsius of hot water is generated by heat exchange, by hot water outlet 304, enters hot water from hot water inlet 503
In basin 50, hot water a part in hot water basin 50 is delivered at the water inlet 105 of oil burning boiler 10, and another part is delivered to
In waste heat boiler 90.And 30% secondary steam for accounting for secondary steam total amount enters secondary series from the second high-temperature steam entrance 401
In heat exchange of heat pipe 40, after 72 degrees Celsius of wheat juice is preheating to 92 degrees Celsius by heat exchange, then it is placed in wheat juice basin 60.And
And first the condensed water that generates of tubular heat exchanger 30 and the second tubular heat exchanger 40 can also be mentioned again by condensed water collecting device C
It supplies and is supplemented at the cold water inlet 303 of the first tubular heat exchanger 30 as cold water, realize the substance circulation and energy of water vapour
The extra quality recycling of circulation.
Meanwhile oil burning boiler 10 generate 240 degrees Celsius of high-temperature flue gas, into heat exchanger 80 with it is therein thermally conductive
Temperature is reduced to about 150 degrees Celsius after oil is exchanged heat, then drains into chimney by low-temperature flue gas outlet 802.In heat exchanger 80
130 degrees Celsius of low temperature conduction oil and flue gas heat exchange after temperature raising be about 160 degrees Celsius, from high-temperature heat-conductive oil export 804
It flows into waste heat boiler 90, after 96 degrees Celsius of the hot water heat exchange in waste heat boiler, generates 120 degrees Celsius of steam and be provided to
In vapor collecting apparatus S, the high steam generated with oil burning boiler 10 realizes the effect that vapour cooking uses jointly, conduction oil by
After 160 degrees Celsius are cooled to 130 degrees Celsius, then entered by the low temperature conduction oil of 902 automatic heat-exchanger 80 of low temperature conduction oil outlet
Mouth 803 is back in heat exchanger 80 to exchange heat again with high-temperature flue gas, realizes the recycling of heat.
As shown in Fig. 2, another embodiment according to the present utility model, except not using heat exchanger 80 and waste heat boiler 90
Outside, remaining construction is roughly the same with Fig. 1 illustrated embodiment.
It will be appreciated that the utility model is not limited to the specific structure be described in detail and shown here and step,
It may be effected by one skilled in the art other modifications and variant in the case where without departing from the spirit and scope of the invention.
Claims (6)
1. a kind of malt digesting apparatus secondary steam utilizing system, comprising: oil burning boiler is supplied with the oil burning boiler by steam
The wort copper provided being connected to pipeline, wherein the oil burning boiler includes boiler body, is set to the one of the boiler body
The flame of the fuel filler of side wall and the inside for helping fuel gas inlet, the neighbouring fuel filler to be set to the boiler body is burnt
Device, set on boiler body another end wall exhanst gas outlet and set on the water inlet and high steam at the top of boiler body
Outlet；The wort copper provided include: wort copper provided ontology, set on the wort copper provided ontology bottom wall high steam
Entrance and condensation-water drain, set on the wort copper provided ontology one side wall wheat juice entrance to be boiled, boil set on the wheat juice
Boil another side wall of pot ontology boil the outlet of wheat juice and the secondary steam of the roof set on the wort copper provided ontology goes out
Mouthful；
It is characterized in that, the malt digesting apparatus secondary steam utilizing system further include: secondary with the wort copper provided
The first tubular heat exchanger and the second tubular heat exchanger that steam (vapor) outlet is connected by secondary steam discharge line,
Wherein, first tubular heat exchanger include: the first high-temperature steam entrance, the first condensation-water drain, cold water inlet and
Hot water outlet, the first high-temperature steam entrance are connected with the secondary steam discharge line, and the cold water inlet passes through pipe
Line is connected with cold water source, and the hot water outlet is connected by pipeline with the water inlet of the oil burning boiler；And
Second tubular heat exchanger includes: the second high-temperature steam entrance, the second condensation-water drain, cold wheat juice entrance, Yi Jire
The outlet of wheat juice, the second high-temperature steam entrance is connected with the secondary steam discharge line, the cold wheat juice entrance and to
Processing Mai Zhiyuan is connected, and the hot wheat juice outlet is connected with wheat juice basin.
2. malt digesting apparatus secondary steam utilizing system as described in claim 1, which is characterized in that first tubulation changes
Hot water basin is equipped between the pipeline of the water inlet of the hot water outlet of hot device and the oil burning boiler, the hot water basin is equipped with heat
Water inlet, the first hot water outlet and the second hot water outlet, the hot water outlet of the hot water inlet and first tubular heat exchanger
It is connected, first hot water outlet is connected with the water inlet of the oil burning boiler.
3. malt digesting apparatus secondary steam utilizing system as claimed in claim 2, which is characterized in that the hot water basin
Pipeline between first hot water outlet and the water inlet of the oil burning boiler is equipped with oxygen-eliminating device, the oxygen-eliminating device include shell,
It the deoxygenation water inlet that is set on the shell, deoxidation water out, the steam-water separator for being set to the interior of shell and rises
Membrane tube, the deoxygenation water inlet are connected with the first hot water outlet of the hot water basin to remove part delivery to described
Deoxygenation in oxygen device, the deoxidation water out are connected with the water inlet of the oil burning boiler.
4. malt digesting apparatus secondary steam utilizing system according to any one of claims 1 to 3, which is characterized in that institute
That states wort copper provided boils wheat juice exit equipped with detachable sieve.
5. malt digesting apparatus secondary steam utilizing system according to any one of claims 1 to 3, which is characterized in that into
One step includes vapor collecting apparatus, and the vapor collecting apparatus includes: to be connected with the higher pressure steam outlet of the oil burning boiler
The first vapor inlet port and the steam outlet that is connected with the higher pressure steam inlet of the wort copper provided.
6. malt digesting apparatus secondary steam utilizing system according to any one of claims 1 to 3, which is characterized in that into
One step includes condensed water collecting device, and the condensed water collecting device includes: the first condensation with first tubular heat exchanger
What water out was connected first condensation water input, be connected with the second condensation-water drain of second tubular heat exchanger the
Two condensation water inputs and the condensation water output being connected with the cold water inlet of first tubular heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821027941.4U CN209010474U (en) | 2018-07-01 | 2018-07-01 | Malt digesting apparatus secondary steam utilizing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821027941.4U CN209010474U (en) | 2018-07-01 | 2018-07-01 | Malt digesting apparatus secondary steam utilizing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209010474U true CN209010474U (en) | 2019-06-21 |
Family
ID=66829207
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821027941.4U Expired - Fee Related CN209010474U (en) | 2018-07-01 | 2018-07-01 | Malt digesting apparatus secondary steam utilizing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209010474U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111876277A (en) * | 2020-07-31 | 2020-11-03 | 广州南沙珠江啤酒有限公司 | Energy-saving wort boiling method and steam recovery equipment |
-
2018
- 2018-07-01 CN CN201821027941.4U patent/CN209010474U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111876277A (en) * | 2020-07-31 | 2020-11-03 | 广州南沙珠江啤酒有限公司 | Energy-saving wort boiling method and steam recovery equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102607014B (en) | Boiler water replenishing system capable of collecting waste heat and condensed water | |
| CN203904327U (en) | White liquor distilling apparatus | |
| CN107120714A (en) | A kind of thermal power plant boiler fume afterheat is used for the whole yearization comprehensive utilization energy conserving system of central heating or heating boiler feed water | |
| CN106123339A (en) | A kind of condensing vacuum boiler | |
| CN105222146A (en) | A kind of flue gas waste heat recovery apparatus | |
| CN205909502U (en) | Boiler of make full use of flue gas waste heat | |
| CN209010474U (en) | Malt digesting apparatus secondary steam utilizing system | |
| CN206019378U (en) | A kind of vapor-water heat exchanger with hydrophobic cooling section | |
| CN102838999A (en) | Low moisture coke cooling and waste heat utilizing device | |
| CN106224932A (en) | There is the boiler waste heat recovery system of vertical lower resistance cooling system | |
| CN209508191U (en) | Malt digesting apparatus afterheat utilizing system | |
| CN205897879U (en) | System is used multipurposely to heating furnace waste heat | |
| CN108087861A (en) | A kind of boiler afterheat combined reclamation method | |
| CN104406144A (en) | Double-medium waste heat boiler | |
| CN207049894U (en) | A kind of inspection-free 0.5T/H condensed type combustion gas steam generator | |
| CN109185849A (en) | Malt digesting apparatus steam utilization system | |
| CN206755307U (en) | Condensing-type low-vacuum cooling circulating water heating installation | |
| CN215723144U (en) | Boiler flue gas waste heat utilization device | |
| CN202793121U (en) | Novel high-efficiency superconductive heat pipe flue smoke residual heat collector | |
| CN208186318U (en) | Thick oil heat-collecting steam boiler device | |
| CN208911479U (en) | A kind of waste-heat recovery device of product equipment for purifying | |
| CN108087852A (en) | A kind of industrial energy-saving steam generator system | |
| CN201412959Y (en) | Heat exchange type energy-saving water heater | |
| CN202083089U (en) | Waste heat utilizing system for boiler | |
| CN102313454A (en) | Waste heat recovery device of calcinator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190621 Termination date: 20210701 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |