CN1184150A - Two fermenting combination, triple filtration and saccharification process - Google Patents

Two fermenting combination, triple filtration and saccharification process Download PDF

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Publication number
CN1184150A
CN1184150A CN96122278A CN96122278A CN1184150A CN 1184150 A CN1184150 A CN 1184150A CN 96122278 A CN96122278 A CN 96122278A CN 96122278 A CN96122278 A CN 96122278A CN 1184150 A CN1184150 A CN 1184150A
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China
Prior art keywords
saccharification
fermenting
combination
filtration
mash
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Pending
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CN96122278A
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Chinese (zh)
Inventor
谢俊发
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Individual
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Individual
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Priority to CN96122278A priority Critical patent/CN1184150A/en
Publication of CN1184150A publication Critical patent/CN1184150A/en
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  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Abstract

The present invention is one kind of beer production process. Unlike available beer production process, which has only once filtration and thus is incomplete in filtration and inadequate in enzymolysis, the said beer production process has triple filtrations, no formaldehyde and other additive added, and thus raised product yield and quality.

Description

Two fermenting combination, triple filtration and saccharification process
The present invention is a kind of process for beer production, promptly a kind of two fermenting combination, triple filtration and saccharification process.
At present, in the production process that beer spills, need use gelatinization and Mashing process, promptly Fructus Hordei Germinatus be dropped in the saccharification groove and carry out saccharification, other auxiliary materials be dropped in adjunce coppers carry out gelatinization, the mash of gelatinization be joined filter after mixing in the saccharification groove again.This technology mash concentration is big, and enzymolysis is incomplete, and difficulty in filtration is big.In addition, when feeding intake, add formaldehyde, gypsum etc., experiment showed, what effect above-mentioned additive does not have.
It is abundant to the objective of the invention is to develop a kind of enzymolysis, easy filtering Mashing process.
Above-mentioned purpose is realized by following scheme: earlier the Fructus Hordei Germinatus of powder essence is dropped into the saccharification groove, auxiliary material is dropped into adjunce copper, add portion water after carrying out after the saccharification groove heats up crossing leaching juice the first time, after heating up again, insulation carries out crossing the second time leaching juice, and then after the mash in the mash of adjunce copper and the saccharification groove mixed, filter for the third time again.Add lactic acid and transfer unified system wine water ph value.Before secondary get juice and in the saccharification groove, carry out, after once at filter vat.
In said process, need not add additives such as formaldehyde, hydrochloric acid, gypsum.Also do not influence technological effect.
Adopt above-mentioned technology, reduced the concentration of mash effectively, make enzymolysis more abundant, and help filtering, can obviously improve the yield and the quality of beer.
Introduce a kind of embodiment below in conjunction with accompanying drawing:
Fig. 1 is former process flow sheet.
Fig. 2 is the schema of present embodiment.
As seen from the figure, former technology is for once crossed leaching juice, and technology of the present invention had leaching juice three times.Because during preceding filter for twice, do not add the gelatinization mash, thereby concentration is very low, specific filtration resistance is easier to, and filters more complete.Get juice to three times and be added to together, heat again, after getting juice, all add part system wine water at every turn, can make enzymolysis process carry out more fully.Thereby can significantly improve product yield and quality.
Technology by Fig. 2 introduction is that 35-40 ℃ of saccharification groove blanking temperature is warming up to 52-55 ℃ again, once gets juice.Be warmed up to 65 ℃ again, carry out secondary and get juice.Simultaneously, the adjunce copper blanking is warmed up to 65-70 ℃ of insulation again to 40 ℃ of insulations, is warmed up to boiling again, then mash is added the saccharification groove, filters for the third time after the insulation.Three times filtered juice is carried out enzymolysis process.Leaching filtration the back boils the intensification of wheat juice fully.

Claims (2)

1, a kind of process for beer production two fermenting combination, triple filtration and saccharification process, it is characterized in that: earlier Fructus Hordei Germinatus is dropped into the saccharification groove, auxiliary material is dropped into adjunce copper, after heating up, the saccharification groove carries out crossing the first time leaching juice, after heating up again, carry out crossing the second time leaching juice, and then the mash of adjunce copper with after the mash of saccharification groove mixes, filter for the third time again.
2, two fermenting combination, triple filtration and saccharification process according to claim 1.It is characterized in that: in said process, do not add formaldehyde, gypsum.
CN96122278A 1996-12-03 1996-12-03 Two fermenting combination, triple filtration and saccharification process Pending CN1184150A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN96122278A CN1184150A (en) 1996-12-03 1996-12-03 Two fermenting combination, triple filtration and saccharification process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN96122278A CN1184150A (en) 1996-12-03 1996-12-03 Two fermenting combination, triple filtration and saccharification process

Publications (1)

Publication Number Publication Date
CN1184150A true CN1184150A (en) 1998-06-10

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN96122278A Pending CN1184150A (en) 1996-12-03 1996-12-03 Two fermenting combination, triple filtration and saccharification process

Country Status (1)

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CN (1) CN1184150A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101490238B (en) * 2006-05-19 2013-08-14 喜力供应链有限公司 Method of producing mash extract and apparatus for carrying out such method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101490238B (en) * 2006-05-19 2013-08-14 喜力供应链有限公司 Method of producing mash extract and apparatus for carrying out such method

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