CN204918549U - Equipment of starch raffinate production alcohol - Google Patents
Equipment of starch raffinate production alcohol Download PDFInfo
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- CN204918549U CN204918549U CN201520587494.8U CN201520587494U CN204918549U CN 204918549 U CN204918549 U CN 204918549U CN 201520587494 U CN201520587494 U CN 201520587494U CN 204918549 U CN204918549 U CN 204918549U
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- tank
- yeast
- tower
- alcohol
- distiller
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Abstract
The utility model is suitable for a technical field is made to alcohol, provides an equipment of starch raffinate production alcohol, including batching jar, liquefaction jar, saccharification jar, boiling pan, fermentation cylinder, distillation column, storage tank, big distiller's yeast jar, little distiller's yeast jar, the boiling pan with between the saccharification jar the saccharification jar with between the fermentation cylinder the fermentation cylinder with between the distillation column big distiller's yeast jar with all be equipped with wide runner plate heat exchanger between the fermentation cylinder and in the distillation column, the distillation column is the combination of seven tower differential pressure distillation columns. Therefore, the utility model discloses a new broadening runner plate heat exchanger collects process's waste heat, changes seven tower differential pressures into by the distillation of three towers and distills, has not only practiced thrift the energy, and special super grade is brought up to by ordinary level to consumption alcohol's quality in addition.
Description
Technical field
The utility model relates to alcohol technology for making field, particularly relates to the equipment that a kind of starch raffinate produces alcohol.
Background technology
When utilizing the isolated starch waste liquor of wheat deep processing starch separation workshop section for raw material production alcohol, its processing method adopted generally comprises liquefaction, saccharification, fermentation, distillation, the processing steps such as liquid waste disposal, need in liquefying with α-amylase mix and blend after, feeding tank of precooking heats up, send into the intensification of boiling post afterwards and be heated to 100 DEG C, in boiling post, be liquefied as liquefaction wake up, then the ferment that will liquefy sends into vapour liquid separator, vapor-liquid separation, exhaust steam sends into refrigerating unit, cooled water condensation, it is be admitted to saccharifying tank after 60 DEG C to carry out saccharification that liquefaction ferment cools, high-temperature steam directly cools, cause the loss of amount of heat, liquefaction ferment temperature is cooled to 60 DEG C by 100 DEG C, cause a large amount of calorific losss equally, cause a large amount of energy dissipations.
In still-process, adopt three tower air distillations, the quality of output edible ethanol is regular grade, and the performance of enterprises cannot ensure, still-process also has the loss of amount of heat simultaneously.
How the heat recuperation of the heat of the high-temperature steam after starchy material boiling and α-amylase can be recycled, how to improve product quality, thus reach reduction Alcohol Production cost, energy-saving and emission-reduction, improve enterprise competitiveness, be also a difficult problem concerning industry technology personnel.
In summary, obviously there is inconvenience and defect in actual use in prior art, so be necessary to be improved.
Utility model content
For above-mentioned defect, the purpose of this utility model is to provide a kind of starch raffinate to produce the equipment of alcohol, and it can improve the quality of edible ethanol, and save energy.
To achieve these goals, the utility model provides a kind of starch raffinate to produce the equipment of alcohol, comprise material-compound tank, liquefied pot, steam cooker, saccharifying tank, fermentor tank, distillation tower, storage tank, large distiller's yeast tank, little distiller's yeast tank, described liquefied pot connects described material-compound tank, described steam cooker connects described liquefied pot, described saccharifying tank connects described steam cooker, described fermentor tank connects described saccharifying tank, described distillation tower connects described fermentor tank, described storage tank connects described distillation tower, described fermentor tank also connects described large distiller's yeast tank, described little distiller's yeast tank connects described large distiller's yeast tank, between described steam cooker and described saccharifying tank, between described saccharifying tank and described fermentor tank, between described fermentor tank and described distillation tower, between described large distiller's yeast tank and described fermentor tank and be equipped with wide-runner plate heat exchanger in distillation tower, described distillation tower is seven tower differential distillation tower combinations.
Produce the equipment of alcohol according to starch raffinate of the present utility model, described liquefied pot is also provided with high-voltage intelligent injector.
Produce the equipment of alcohol according to starch raffinate of the present utility model, described distillation tower is seven tower differential distillation towers, comprises topping still, water wash column, rectifying tower, methanol column, potato spirit tower.
Produce the equipment of alcohol according to starch raffinate of the present utility model, described fermentor tank also connects carbon dioxide recovering apparatus.
The utility model is by the waste heat of newly-increased wide-runner plate heat exchanger collection process process, seven tower differential distillations are changed into by five column distillations, not only save the energy, and the quality of edible ethanol brings up to special top grade by regular grade, by transformation high-voltage intelligent injector, improve starch waste liquor liquefaction effect.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
See Fig. 1, the utility model provides the equipment that a kind of starch raffinate produces alcohol.Comprise material-compound tank 1, liquefied pot 2, steam cooker 3, saccharifying tank 4, fermentor tank 5, distillation tower 6, storage tank 7, large distiller's yeast tank 8, little distiller's yeast tank 9, liquefied pot 2 connects material-compound tank 1, steam cooker 3 connects liquefied pot 2, saccharifying tank 4 connects steam cooker 3, fermentor tank connects saccharifying tank 4, and distillation tower 6 connects fermentor tank 5, and storage tank 7 connects distillation tower 6, fermentor tank 5 also connects large distiller's yeast tank 8, and little distiller's yeast tank 9 connects large distiller's yeast tank 8.
Wide-runner plate heat exchanger 10 is equipped with between distiller's yeast tank 8 and fermentor tank 5 and in distillation tower 6 between steam cooker 3 and saccharifying tank 4, between saccharifying tank 4 and fermentor tank 5, between fermentor tank 5 and distillation tower 6, greatly, reclaim the waste heat of liquefied fermented glutinous rice, converted mash, karusen, yeast wash respectively, for the heating of processing wastewater and starch slurry.
Preferably, starch raffinate of the present utility model produces the equipment of alcohol, and liquefied pot is provided with high-voltage intelligent injector 11 and substitutes original jet apparatus, to improve the liquefaction effect of starch waste liquor.
Further, starch raffinate of the present utility model produces the equipment of alcohol, and seven tower differential distillation towers are made up of equipment such as topping still, water wash column, rectifying tower, methanol column, potato spirit tower, reboiler, condenser, vacuum pumps.Rectifying tower and topping still form one group of differential distillation system, and water wash column and methanol column form one group of differential distillation system, and potato spirit tower is normal-temperature distilled.This technique, by each tower and supporting heat-exchange equipment, impurities removal system are combined, makes interchanger play common effect, when achieving save energy, produces high-quality alcohol.
Better, starch raffinate of the present utility model produces the equipment of alcohol, and fermentor tank 5 also connects carbon dioxide recovering apparatus 12.
In sum, the utility model is by the waste heat of newly-increased wide-runner plate heat exchanger collection process process, seven tower differential distillations are changed into by five column distillations, not only save the energy, and the quality of edible ethanol brings up to special top grade by regular grade, by transformation high-voltage intelligent injector, improve starch waste liquor liquefaction effect.
Certainly; the utility model also can have other various embodiments; when not deviating from the utility model spirit and essence thereof; those of ordinary skill in the art are when making various corresponding change and distortion according to the utility model, but these change accordingly and are out of shape the protection domain that all should belong to the claim appended by the utility model.
Claims (4)
1. the equipment of a starch raffinate production alcohol, it is characterized in that, comprise material-compound tank, liquefied pot, steam cooker, saccharifying tank, fermentor tank, distillation tower, storage tank, large distiller's yeast tank, little distiller's yeast tank, described liquefied pot connects described material-compound tank, described steam cooker connects described liquefied pot, described saccharifying tank connects described steam cooker, described fermentor tank connects described saccharifying tank, described distillation tower connects described fermentor tank, described storage tank connects described distillation tower, described fermentor tank also connects described large distiller's yeast tank, described little distiller's yeast tank connects described large distiller's yeast tank, between described steam cooker and described saccharifying tank, between described saccharifying tank and described fermentor tank, between described fermentor tank and described distillation tower, between described large distiller's yeast tank and described fermentor tank and be equipped with wide-runner plate heat exchanger in distillation tower, described distillation tower is seven tower differential distillation tower combinations.
2. starch raffinate according to claim 1 produces the equipment of alcohol, and it is characterized in that, described liquefied pot is also provided with high-voltage intelligent injector.
3. starch raffinate according to claim 2 produces the equipment of alcohol, and it is characterized in that, described seven tower differential distillation towers comprise topping still, water wash column, rectifying tower, methanol column, potato spirit tower.
4. starch raffinate according to claim 3 produces the equipment of alcohol, and it is characterized in that, described fermentor tank also connects carbon dioxide recovering apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520587494.8U CN204918549U (en) | 2015-08-06 | 2015-08-06 | Equipment of starch raffinate production alcohol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520587494.8U CN204918549U (en) | 2015-08-06 | 2015-08-06 | Equipment of starch raffinate production alcohol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204918549U true CN204918549U (en) | 2015-12-30 |
Family
ID=54967695
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520587494.8U Expired - Fee Related CN204918549U (en) | 2015-08-06 | 2015-08-06 | Equipment of starch raffinate production alcohol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204918549U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108823050A (en) * | 2018-05-24 | 2018-11-16 | 杭州正久机械制造有限公司 | A kind of brewing system of vodka and GIN wine |
-
2015
- 2015-08-06 CN CN201520587494.8U patent/CN204918549U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108823050A (en) * | 2018-05-24 | 2018-11-16 | 杭州正久机械制造有限公司 | A kind of brewing system of vodka and GIN wine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180328 Address after: 262100 Xin'an South Road, Anqiu, Anqiu, Shandong Patentee after: TTCA Co., Ltd. Address before: 262100 east side of north section of Wenchan Road, Anqiu City, Weifang, Shandong Patentee before: SHANDONG QUFENG FOOD TECH CO., LTD. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151230 Termination date: 20190806 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |