CN1136590A - Method for producing micro beer and apparatus - Google Patents
Method for producing micro beer and apparatus Download PDFInfo
- Publication number
- CN1136590A CN1136590A CN 96104977 CN96104977A CN1136590A CN 1136590 A CN1136590 A CN 1136590A CN 96104977 CN96104977 CN 96104977 CN 96104977 A CN96104977 A CN 96104977A CN 1136590 A CN1136590 A CN 1136590A
- Authority
- CN
- China
- Prior art keywords
- tank
- outlet
- import
- wheat juice
- separation
- 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.)
- Pending
Links
- 235000013405 beer Nutrition 0.000 title claims description 26
- 238000004519 manufacturing process Methods 0.000 title description 23
- 238000000034 method Methods 0.000 claims abstract description 28
- 239000002994 raw material Substances 0.000 claims abstract description 17
- 238000009835 boiling Methods 0.000 claims abstract description 16
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910052802 copper Inorganic materials 0.000 claims abstract description 10
- 239000010949 copper Substances 0.000 claims abstract description 10
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 3
- 239000010935 stainless steel Substances 0.000 claims abstract description 3
- 241000209140 Triticum Species 0.000 claims description 20
- 235000021307 Triticum Nutrition 0.000 claims description 20
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims description 18
- 230000008676 import Effects 0.000 claims description 17
- 238000000926 separation method Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 239000002893 slag Substances 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 238000010298 pulverizing process Methods 0.000 claims description 6
- 238000005057 refrigeration Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 239000002826 coolant Substances 0.000 claims description 3
- 238000005516 engineering process Methods 0.000 abstract description 9
- 230000007423 decrease Effects 0.000 abstract 1
- 238000001914 filtration Methods 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000011265 semifinished product Substances 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The invented method adopts the semiproduct as raw material and accomplishes once through the saccharifying separating and boiling process. Said multifunction saccharifying tank possesses of a red copper seal, and a red copper tank body in which a stainless steel internal tank is installed, on the bottom of the tank body there is an outlet, from which the product in the tank is pumped out by the delivery pump and pumped in through the inlet, thus it onducts the continuous circulation and accomplishes the saccharifying, separating and boiling in the course of continuous circulation. Compared with the existing technologies, said method greatly simpifies the productive process, shortens the productive period and decreases the mumber of equipment and the occupied floor area.
Description
The present invention relates to the micro beer manufacturing technology.
Micro beer is to flow into China over the past two years, and be the popular good a kind of novel beer production method of liking, mostly at 50 liters~2000 liters of/day pure fresh beer, its principal feature is the industrial scale of micro beer: view and admire and make exquisite Brewing equipment while method novelty, client can be tasted young beer in the hotel; Its two be the pure fresh beer of field fabrication without all swivel links in centre, guaranteed the real taste of beer, the product of the large-scale brew-house of this point does not have comparable extremely.In view of above-mentioned two principal features, the scene is brewageed mode and is favourably welcome.But its production method of beer that delicious high-quality is good to eat is really not so simple.Existing small-sized equipment for brewing beer such as ZL93244976.X, the production equipment of it and brew-house does not have any difference, need adjunce copper, brew kettle, filter vat, boiling pot, eddy flow groove, heat exchanger, fermentor tank or the like equally, just with these device and device miniaturization, its complex manufacturing technology, loaded down with trivial details, device and equipment are too much, and floor space is big, Production Time is long, thereby and is not suitable for the requirement of general restaurant, hotel, bar, shop field fabrication fresh beer.
Purpose of the present invention promptly is to comprise the problem of aspects such as complex manufacturing technology, equipment is too much, floor space is big, Production Time is long, and a kind of high-grade micro beer making method and device are provided at above-mentioned the deficiencies in the prior art.
In order to make more people can enjoy the pure fresh beer of field fabrication.Our especial manufacture a kind of cost lower, operate easier production unit, use the user of this equipment and my company's raw materials for production, need only just can grasp production technology through simple training, and can produce qualified beer.The appearance of this beer production equipment and technology can greatly promote China's beer culture to popularize to broad masses, and China's beer production is more stepped to a new level.
The objective of the invention is to be achieved through the following technical solutions:
A kind of making method that comprises the high-grade micro beer of saccharification, separation and the boiling part of wheat juice adopts the work in-process raw material, and once finishes saccharification, separation and the boiling part of wheat juice in a multi-functional saccharifying tank.The making processes of said work in-process raw material comprises following two schemes:
Scheme (1), Fructus Hordei Germinatus pulverizing → separation slag crust → pack.
Scheme (2), Fructus Hordei Germinatus pulverizing → separation slag crust, and the interpolation weight ratio is auxiliary material → pack of 20~40%.
Adopt the work in-process raw material, and in a multi-functional saccharifying tank saccharification, separation and the boiling part of once intact wheat juice, said multi-functional saccharifying tank (1), it has the end socket (10) of red copper, the tank body (102) of red copper, and interior jar (104) made from stainless steel are housed in tank body (102), on interior jar (104), electrothermal tube (106) is housed; Charging opening (105) is arranged at the top in tank body (102) and interior jar (104), and outlet (107) is arranged at the bottom, and the opposite side in tank body (102) and interior jar (104) is provided with the import (109) and the outlet (110) of water coolant.Said end socket (101) is
Shape, and the bottom of tank body (102) and interior jar (104) is
Shape.Between multi-functional saccharifying tank (1) and fermentor tank, also be provided with multi-usage frozen water case (2), this multi-usage frozen water case (2) has import (203), the outlet (204) of import (201), outlet (202) and the refrigeration agent of wheat juice, what connect between the import (201) of wheat juice and outlet (202) is a spiral tube, goes out connection one spiral tube between the import (203) of refrigeration agent and outlet (204); CHP (209) is equipped with on the top of frozen water case (2).
The present invention has the following advantages and effect:
1, compared with prior art, the present invention has simplified production technique greatly, reduces number of devices, has shortened fabrication cycle, and the prior art floor space is big, the making wheat juice cycle is long.The present invention uses treated work in-process, only can finish each process of saccharification and loaded down with trivial details work such as wort filtration and Wort boiling in use with an equipment, owing to use treated work in-process raw material, saccharification time shortens greatly, reducing to present 3 hours by original 8 hours can finish, and the skin slag separates the absolute detention forced filtration method that adopts.
2, prior art is because raw material is unprocessed, a large amount of wheat skins need specific equipment to separate when saccharification, the used large equipment of saccharification part at least three (saccharification boiling pot, wort filtration equipment, heat of dissociation coagulum equipment) is because wort filtration adopts deep layer natural filtration method, and the used time increases greatly.
3, the present invention, requires to reduce greatly to operator's state of the art owing to use the work in-process raw material except that reducing saccharifying equipment.
The drawing of accompanying drawing is described as follows:
Fig. 1 a is the structure iron of brew kettle.
Fig. 1 b is the A-A sectional view of Fig. 1 a.
Fig. 2 is multi-usage frozen water box structure figure.
Elaborate below in conjunction with drawings and Examples:
The present invention's difference emphasis compared with prior art is at raw material treatment process and beer The saccharification part that wine is produced.
The production technology of prior art is generally:
Raw material pulverizing → saccharification → filtration → separation → washing trough → Wort boiling → coarse sludge separates → fermentation
Wherein equipment needed thereby is: one of Fructus Hordei Germinatus Special grinder for disintegrating, adjunce copper, brew kettle, At least three four equipment such as boiling pot, filtering separation device and heat exchanger.
Prior art is because raw material is unprocessed, and a large amount of wheat skins need special equipment when saccharification Separate, because wort filtration adopts deep layer natural filtration method, the used time greatly Increase.
Production technology of the present invention is:
Semi-finished product raw material → saccharification, separate, boil → ferment
Wherein saccharification, to separate, boil be to be that wheat juice saccharification boiling separates pot at an equipment Finish in (multi-functional saccharifying tank), therefore greatly simplified technology, reduced and established Standby, whole process only needed to finish in 3~4 hours.
As for the manufacture craft of this products material, before saccharifying, finish in semi-finished product processing factory, and process processing before dispatching from the factory, processing scheme is as follows:
Slag crust → pack is pulverized → separated to scheme 1, fructus hordei germinatus
Above-mentioned Fructus Hordei Germinatus is pulverized all can adopt general disintegrating apparatus, owing to used packed work in-process raw material, except that reducing saccharifying equipment, the requirement of operator's state of the art is reduced greatly.
See also Fig. 1 a, 1b below, multi-functional saccharifying tank 1 of the present invention, have red copper end socket 101, red copper tank body 102 and in tank body 102, be equipped with interior jar 104 that makes with stainless material, on interior jar 104, electrothermal tube 106 is housed, charging opening 105 is arranged at the top at end socket 101 and interior jar 104, outlet 107 is arranged at the bottom, by the transferpump (not shown) goods in the jar is constantly extracted out and constantly circulation in jar is squeezed in import 108.Constantly finish saccharification, boiling and separating in the round-robin process.Be provided with the import 109 and the outlet 110 of water coolant at the opposite side of tank body 102 and interior jar 104.A thermometer 103 also is housed on multi-functional saccharifying tank 1.
See also Fig. 2, the present invention also is provided with multi-usage frozen water case 2 between multi-functional saccharifying tank 1 and fermentor tank, it has the import 203 and the outlet 204 of wheat juice import 201, the outlet 202 of wheat juice and refrigeration agent (fluorine Lyons F22), the bottom of frozen water case 2 also has sewage draining exit 205, CHP 209 is equipped with on top, and it is squeezed into deicing fluid from exporting 207 from import 206 and gets for fermentor tank cooling and controlled temperature.What connected between above-mentioned wheat juice import 201 wheat juice outlet 202 is a spiral tube, also connect a spiral tube in the import 203 of refrigeration agent with between exporting 204, two spiral tubes carry out heat exchange and remain on below 10 ℃ to control the effusive wheat juice of multi-functional saccharifying tank temperature.
Claims (5)
1, a kind of comprising, it is characterized in that: adopt the work in-process raw material, and in a multi-functional saccharifying tank, once finish saccharification, separation and the boiling part of wheat juice the making method of the micro beer of saccharification, separation and the boiling part of wheat juice.
2, the making method of micro beer according to claim 1 is characterized in that: the making processes of said work in-process raw material comprises following two schemes:
Scheme (1), Fructus Hordei Germinatus pulverizing → separation slag crust → pack.
Scheme (2), Fructus Hordei Germinatus pulverizing → separation slag crust, and the interpolation weight ratio is auxiliary material → pack of 20~40%.
3, a kind of saccharification to wheat juice, separation and boiling part are at interior micro beer producing device, it is characterized in that: adopt the work in-process raw material, and in a multi-functional saccharifying tank, once finish saccharification, separation and the boiling part of wheat juice, said multi-functional saccharifying tank (1), it has the end socket (101) of red copper, the tank body (102) of red copper, and interior jar (104) made from stainless steel are housed in tank body (102), on interior jar (104), electrothermal tube (106) is housed; Charging opening (105) is arranged at the top in end socket (101) and interior jar (104), and outlet (107) is arranged at the bottom, and the opposite side in tank body (102) and interior jar (104) is provided with the import (109) and the outlet (110) of water coolant.
5, micro beer producing device according to claim 3, it is characterized in that: between multi-functional saccharifying tank (1) and fermentor tank, also be provided with multi-usage frozen water case (2), this multi-usage frozen water case (2) has import (203), the outlet (204) of import (201), outlet (202) and the refrigeration agent of wheat juice, what connect between the import (201) of wheat juice and outlet (202) is a spiral tube, goes out connection one spiral tube between the import (203) of refrigeration agent and outlet (204); CHP (209) is equipped with on the top of frozen water case (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96104977 CN1136590A (en) | 1996-05-14 | 1996-05-14 | Method for producing micro beer and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96104977 CN1136590A (en) | 1996-05-14 | 1996-05-14 | Method for producing micro beer and apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1136590A true CN1136590A (en) | 1996-11-27 |
Family
ID=5118658
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 96104977 Pending CN1136590A (en) | 1996-05-14 | 1996-05-14 | Method for producing micro beer and apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1136590A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1333061C (en) * | 2003-04-15 | 2007-08-22 | 克朗斯股份公司 | Apparatus and method for brewing beer |
| CN116024057A (en) * | 2023-02-01 | 2023-04-28 | 杭州海顺制药机械有限公司 | Multifunctional wine pot |
-
1996
- 1996-05-14 CN CN 96104977 patent/CN1136590A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1333061C (en) * | 2003-04-15 | 2007-08-22 | 克朗斯股份公司 | Apparatus and method for brewing beer |
| CN116024057A (en) * | 2023-02-01 | 2023-04-28 | 杭州海顺制药机械有限公司 | Multifunctional wine pot |
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| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C01 | Deemed withdrawal of patent application (patent law 1993) | ||
| WD01 | Invention patent application deemed withdrawn after publication |