CN206298571U - A kind of alcoholic system waste heat retracting device - Google Patents
A kind of alcoholic system waste heat retracting device Download PDFInfo
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- CN206298571U CN206298571U CN201621390372.0U CN201621390372U CN206298571U CN 206298571 U CN206298571 U CN 206298571U CN 201621390372 U CN201621390372 U CN 201621390372U CN 206298571 U CN206298571 U CN 206298571U
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Abstract
A kind of alcoholic system waste heat retracting device, it is related to a kind of waste-heat recovery device.The utility model causes the problem of energy dissipation and environmental pollution to solve directly to discharge high-temperature steam during existing alcoholic.Waste-heat recovery device includes Boiler Steam connecting tube, injecting type unit, alcoholic steam inlet duct, alcoholic steam outleting pipe, case tube heat exchanger, plate type heat exchanger, sour water delivery pipe, softened water connecting tube, water collect tank, hot water return pipe and water-break pipe, alcoholic steam outleting pipe is sequentially passed through case tube heat exchanger and plate type heat exchanger by elder generation after, softened water connecting tube passes through plate type heat exchanger, hot water return pipe passes through case tube heat exchanger, the other end of hot water return pipe to be connected with the water inlet end of injecting type unit.The waste heat recovery that the utility model is used for during alcoholic.
Description
Technical field
The utility model is related to a kind of alcoholic system waste heat retracting device.
Background technology
Sorghum is the primary raw material of Chinese alcoholic.Several famous brands of wine having won fame both at home and abroad are to be cooked major ingredient or cooked seasoning with sorghum to make mostly
System is formed.What is brewageed with sorghum is Spirit, is typically also called white wine or liquor.China is to manufacture Spirit with sorghum earliest
Country.Sorghum-brewed wine is the effect of the enzyme produced by Institute of Micro-biology, the Starch Conversion in seed is then produced alcohol for sugar
Process.Microorganism is mainly by means of mould and saccharomycete.Whole wine brewing process, environment and process conditions should all be adapted to institute
With the metabolic characteristic of microorganism, promote their energetic, effects big, starch is fully decomposed into sugar, then convert the sugars into alcohol.
Therefore in the state of whole alcoholic workshop needs to keep certain high temperature constant pressure, produced typically by coal-fired steam boiler at this stage
Substantial amounts of steam is given birth to meet the environmental condition during alcoholic.At the same time, substantial amounts of high temperature can be distilled out during alcoholic
Steam, existing alcoholic process generally directly discharges high-temperature steam, causes the waste of energy, and loss is also result in the energy.
Utility model content
The utility model causes energy dissipation and environment to solve directly to discharge high-temperature steam during existing alcoholic
The problem of pollution, and then propose a kind of alcoholic system waste heat retracting device.
The utility model is adopted the technical scheme that to solve above-mentioned technical problem：
A kind of alcoholic system waste heat retracting device include Boiler Steam connecting tube, injecting type unit, alcoholic steam inlet duct,
Alcoholic steam outleting pipe, case tube heat exchanger, plate type heat exchanger, sour water delivery pipe, softened water connecting tube, water collect tank, hot water backwater
Pipe and water-break pipe, one end of Boiler Steam connecting tube are connected with boiler steam room, the other end and the injection of Boiler Steam connecting tube
The inlet end connection of formula unit, the outlet side of injecting type unit is connected with one end of alcoholic steam inlet duct, alcoholic steam inlet
The other end of pipe is connected with the inlet end in alcoholic workshop, and the outlet side in alcoholic workshop is connected with one end of alcoholic steam outleting pipe,
Alcoholic steam outleting pipe is sequentially passed through case tube heat exchanger and plate type heat exchanger by elder generation after, the other end of alcoholic steam outleting pipe with
Sour water delivery pipe is connected, and is connected between one end of softened water connecting tube and water treatment vehicle, and softened water connecting tube passes through plate type heat exchanger,
The other end of softened water connecting tube is connected with boiler soft water case and water collect tank respectively, the water side of water collect tank and hot water return pipe
One end connection, hot water return pipe passes through case tube heat exchanger, the other end of hot water return pipe to connect with the water inlet end of injecting type unit
Connect, the water side of injecting type unit is connected with one end of water-break pipe, and the other end of water-break pipe is connected with water collect tank.
The beneficial effect that the utility model is included compared with prior art is：
1st, apparatus of the present invention by case tube heat exchanger and board-like can change the high temperature heat produced during alcoholic respectively
Hot device carries out secondary recovery utilization, and the waste heat that will be reclaimed is recycled in whole alcoholic system, realizes the recycling of waste heat,
The loss of heat is effectively prevent, the rate of recovery of heat energy can reach more than 80%.The pollution to environment is effectively reduced simultaneously.
2nd, low-grade steam ejection is dropped using spraying system, has both recycled waste heat, be reduced working steam pot
The consumption of stove moisturizing reduces the energy consumption of boiler.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model, and the direction of wherein arrow represents the flowing side of gas or liquid
To.
Specific embodiment
Specific embodiment one：Present embodiment is illustrated with reference to Fig. 1, a kind of alcoholic system waste heat described in present embodiment is returned
Receiving apparatus include that Boiler Steam connecting tube 1, injecting type unit 2, alcoholic steam inlet duct 3, alcoholic steam outleting pipe 4, package are changed
Hot device 5, plate type heat exchanger 7, sour water delivery pipe 8, softened water connecting tube 9, water collect tank 11, hot water return pipe 12 and water-break pipe 13,
One end of Boiler Steam connecting tube 1 is connected with boiler steam room 15, the other end and the injecting type unit 2 of Boiler Steam connecting tube 1
Inlet end connection, the outlet side of injecting type unit 2 is connected with one end of alcoholic steam inlet duct 3, alcoholic steam inlet duct 3
The other end is connected with the inlet end in alcoholic workshop 16, and the outlet side in alcoholic workshop 16 is connected with one end of alcoholic steam outleting pipe 4,
Alcoholic steam outleting pipe 4 is sequentially passed through case tube heat exchanger 5 and plate type heat exchanger 7 by elder generation after, alcoholic steam outleting pipe 4 it is another
End is connected with sour water delivery pipe 8, and 17 connection between one end of softened water connecting tube 9 and water treatment vehicle, softened water connecting tube 9 passes through plate
Formula heat exchanger 7, the other end of softened water connecting tube 9 is connected with boiler soft water case 18 and water collect tank 11 respectively, water collect tank 11
Water side is connected with one end of hot water return pipe 12, hot water return pipe 12 pass through case tube heat exchanger 5, hot water return pipe 12 it is another
End is connected with the water inlet end of injecting type unit 2, and the water side of injecting type unit 2 is connected with one end of water-break pipe 13, water-break pipe 13
The other end be connected with water collect tank 11.
A kind of exhaust heat recovering method of alcoholic system waste heat retracting device comprises the following steps：
Step one：Steam alcoholic：The pressure that will be produced in boiler steam room 15 first steams for the steam of 0.8MPa through boiler
Vapour connecting tube 1 is drawn and is entered into injecting type unit 2, is the steaming of 0.4MPa by forming pressure after the injection of injecting type unit 2
Vapour enters into alcoholic workshop 16 and carries out alcoholic through alcoholic steam inlet duct 3, and 94 DEG C of high-temperature steams are discharged in alcoholic workshop 16；
Step 2：Waste heat is once reclaimed：94 DEG C of high-temperature steams of the discharge of alcoholic workshop 16 enter into alcoholic steam outleting pipe 4
In, alcoholic steam outleting pipe 4 passes through case tube heat exchanger 5, case tube heat exchanger 5 to steam 94 DEG C of high temperature in alcoholic steam outleting pipe 4
Vapour carries out first time waste heat recovery, and the 94 DEG C of high-temperature steam heat releases liquefaction in alcoholic steam outleting pipe 4 is changed into 90 DEG C of condensed waters；
Step 3：Waste heat secondary recovery：Alcoholic steam outleting pipe 4 passes through plate type heat exchanger 7, and plate type heat exchanger 7 is to alcoholic
90 DEG C of condensed waters in steam outleting pipe 4 carry out second waste heat recovery, 90 DEG C of condensed water heat releases in alcoholic steam outleting pipe 4
It is changed into 10 DEG C of condensed waters, is discharged via sour water delivery pipe 8；
Step 4：Softened water heating recovery：Softened water connecting tube 9 is entered into by the 8 DEG C of softened waters reclaimed between water treatment vehicle
In, softened water connecting tube 9 is changed into 30 DEG C of softened waters, 30 through 7,8 DEG C of softened waters of plate type heat exchanger by the heat absorption of plate type heat exchanger 7
DEG C softened water is partly into softening water tank 18, and another part is entered into water collect tank 11 and stored；
Step 5：Steam Water Sproading：Steam in injecting type unit 2, which part can be liquefied as 30 DEG C of steam water, 30 DEG C
Steam water is entered into water collect tank 11 via water-break pipe 13 and stored；
Step 6：Hot water is counter to be steamed：The 30 DEG C of softened waters and 30 DEG C of steam water stored in water collect tank 11 enter into hot water backwater
In pipe 12, hot water return pipe 12 absorbs heat through 5,30 DEG C of softened waters of case tube heat exchanger and 30 DEG C of steam water by case tube heat exchanger 5
It is changed into 40 DEG C of high-temperature-hot-waters, 40 DEG C of high-temperature-hot-waters are entered into injecting type unit 2, anti-steaming is again by injecting type unit 2
The steam injection of 0.4MPa.
Specific embodiment two：Present embodiment is illustrated with reference to Fig. 1, a kind of alcoholic system waste heat described in present embodiment is returned
Receiving apparatus also include electric butterfly valve 19, and electric butterfly valve 19 is arranged in parallel with injecting type unit 2.Undocumented skill in present embodiment
Art feature is identical with specific embodiment one.
It is so designed that and the other end of Boiler Steam connecting tube 1 is connected with one end of electric butterfly valve 19, alcoholic steam inlet
One end of pipe 3 is connected with the other end of electric butterfly valve 19.
Specific embodiment three：Present embodiment is illustrated with reference to Fig. 1, on alcoholic steam outleting pipe 4 described in present embodiment
Condensate water circulatory pump 6 is provided with, condensate water circulatory pump 6 is arranged between case tube heat exchanger 5 and plate type heat exchanger 7.Present embodiment
In undocumented technical characteristic it is identical with specific embodiment one or two.
Specific embodiment four：Present embodiment is illustrated with reference to Fig. 1, hot water return pipe 12 is provided with described in present embodiment
Primer pump 10, primer pump 10 is arranged between water collect tank 11 and case tube heat exchanger 5.Undocumented technical characteristic in present embodiment
It is identical with specific embodiment three.
Specific embodiment five：Present embodiment is illustrated with reference to Fig. 1, water-break pipe 13 is provided with water-break described in present embodiment
Pump 14.Undocumented technical characteristic is identical with specific embodiment four in present embodiment.
It is so designed that square hole 1-1 is passed through in order to the vertical reinforcement on metope, because reinforcement location has certain deviation,
The length of square hole 1-1 is 70mm in present embodiment, and width is 70mm.
Specific embodiment six：Present embodiment, the heat exchange of case tube heat exchanger 5 described in present embodiment are illustrated with reference to Fig. 1
Area is 60m2, the heat exchange area of plate type heat exchanger 7 is 10m2.Undocumented technical characteristic and specific implementation in present embodiment
Mode one, two, four or five are identical.
The shape of mortar pin groove 9 is so designed that, prevents from sticking up mortar when sliding block 3 is withdrawn from upwards.
Claims (6)
1. a kind of alcoholic system waste heat retracting device, it is characterised in that：A kind of alcoholic system waste heat retracting device includes pot
Stove steam connection tube (1), injecting type unit (2), alcoholic steam inlet duct (3), alcoholic steam outleting pipe (4), case tube heat exchanger
(5), plate type heat exchanger (7), sour water delivery pipe (8), softened water connecting tube (9), water collect tank (11), hot water return pipe (12) and move back
Water pipe (13), one end of Boiler Steam connecting tube (1) is connected with boiler steam room (15), Boiler Steam connecting tube (1) it is another
End is connected with the inlet end of injecting type unit (2), the outlet side of injecting type unit (2) and one end of alcoholic steam inlet duct (3)
Connection, the other end of alcoholic steam inlet duct (3) is connected with the inlet end of alcoholic workshop (16), the outlet side of alcoholic workshop (16)
One end with alcoholic steam outleting pipe (4) is connected, and alcoholic steam outleting pipe (4) is sequentially passed through case tube heat exchanger (5) by elder generation after
With plate type heat exchanger (7), the other end of alcoholic steam outleting pipe (4) is connected with sour water delivery pipe (8), softened water connecting tube (9)
One end and water treatment vehicle between (17) connection, softened water connecting tube (9) through plate type heat exchanger (7), softened water connecting tube (9)
The other end is connected with boiler soft water case (18) and water collect tank (11) respectively, the water side of water collect tank (11) and hot water return pipe
(12) one end connection, hot water return pipe (12) is through case tube heat exchanger (5), the other end and injecting type of hot water return pipe (12)
The water inlet end connection of unit (2), the water side of injecting type unit (2) is connected with one end of water-break pipe (13), water-break pipe (13)
The other end is connected with water collect tank (11).
2. a kind of alcoholic system waste heat retracting device according to claim 1, it is characterised in that：More than a kind of alcoholic system
Heat reclamation device also includes electric butterfly valve (19), and electric butterfly valve (19) is arranged in parallel with injecting type unit (2).
3. a kind of alcoholic system waste heat retracting device according to claim 1 or claim 2, it is characterised in that：The alcoholic steam goes out
Tracheae (4) is provided with condensate water circulatory pump (6), and condensate water circulatory pump (6) is arranged on case tube heat exchanger (5) and plate type heat exchanger
(7) between.
4. a kind of alcoholic system waste heat retracting device according to claim 3, it is characterised in that：The hot water return pipe (12)
Primer pump (10) is provided with, primer pump (10) is arranged between water collect tank (11) and case tube heat exchanger (5).
5. a kind of alcoholic system waste heat retracting device according to claim 4, it is characterised in that：Set on the water-break pipe (13)
There is water-break pump (14).
6. a kind of alcoholic system waste heat retracting device according to claim 1,2,4 or 5, it is characterised in that：The package is changed
The heat exchange area of hot device (5) is 60m2, the heat exchange area of plate type heat exchanger (7) is 10m2。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621390372.0U CN206298571U (en) | 2016-12-16 | 2016-12-16 | A kind of alcoholic system waste heat retracting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621390372.0U CN206298571U (en) | 2016-12-16 | 2016-12-16 | A kind of alcoholic system waste heat retracting device |
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| Publication Number | Publication Date |
|---|---|
| CN206298571U true CN206298571U (en) | 2017-07-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201621390372.0U Active CN206298571U (en) | 2016-12-16 | 2016-12-16 | A kind of alcoholic system waste heat retracting device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106520499A (en) * | 2016-12-16 | 2017-03-22 | 哈尔滨工大金涛科技股份有限公司 | Waste heat recovery device and waste heat recovery method thereof of wine making system |
| CN108841557A (en) * | 2018-08-23 | 2018-11-20 | 四川万家福酒业有限公司 | The heating wine retort bottom pot system of recyclable waste heat |
-
2016
- 2016-12-16 CN CN201621390372.0U patent/CN206298571U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106520499A (en) * | 2016-12-16 | 2017-03-22 | 哈尔滨工大金涛科技股份有限公司 | Waste heat recovery device and waste heat recovery method thereof of wine making system |
| CN108841557A (en) * | 2018-08-23 | 2018-11-20 | 四川万家福酒业有限公司 | The heating wine retort bottom pot system of recyclable waste heat |
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