CN100448987C - Alpha-acetyl lactate dehydrogenase dry powder and its preparation process - Google Patents

Alpha-acetyl lactate dehydrogenase dry powder and its preparation process Download PDF

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Publication number
CN100448987C
CN100448987C CNB2004100609872A CN200410060987A CN100448987C CN 100448987 C CN100448987 C CN 100448987C CN B2004100609872 A CNB2004100609872 A CN B2004100609872A CN 200410060987 A CN200410060987 A CN 200410060987A CN 100448987 C CN100448987 C CN 100448987C
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China
Prior art keywords
alpha
spray
enzyme
acetolactate decarboxylase
dry powder
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Expired - Fee Related
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CNB2004100609872A
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Chinese (zh)
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CN1624121A (en
Inventor
赵文报
蒙健宗
黄日波
王青艳
韦函忠
周志鹏
蒙丽萍
马少敏
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BANGERKE BIOLOGICAL TECHNOLOGY Co Ltd NANNING
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BANGERKE BIOLOGICAL TECHNOLOGY Co Ltd NANNING
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Abstract

The present invention discloses spray-drying alpha-acetolactate decarboxylase and a preparation method thereof, the spray-drying alpha-acetolactate decarboxylase belongs to a food additive biological product of an enzyme preparation and comprises liquid alpha-acetolactate decarboxylase and a spray-drying protective agent, wherein the spray-drying protective agent is composed of trehalose dihydrate, xanthan, sodium alginate, dextrine, etc., and is prepared by a corresponding spray-drying technology. The enzyme has high stability and can be effectively saved for 1 to 2 years at dry places at normal temperature.

Description

Alpha-acetolactate decarboxylase dry powder and preparation method thereof
Technical field
The food that the present invention relates to a kind of zymin adds biological products, is specifically related to a kind of alpha-acetolactate decarboxylase dry powder and preparation method thereof.
Background technology
(ALDC EC4.1.1.5) has obtained the widespread use of beer production producer to alpha-acetolactate decarboxylase as the auxiliary agent of beer slaking.In the brewage process, α-acetylactis forms di-acetyl through non-oxydasis decarboxylation, when the content of di-acetyl surpasses 0.15mg/kg, has a strong impact on the taste of beer.Traditional method of removing di-acetyl is a low-temperature storage beer, and the diacetyl reductase that allows yeast itself produce makes di-acetyl finally be reduced into 2,3 butyleneglycols, and this process generally needed for 3~6 weeks the beer maturing process, and what have reaches 3 months.This enzyme is applied in the beer production, and it can change into acetoin with α-acetylactis direct oxidation decarboxylation, without this intermediate product of di-acetyl, thereby can make fermentation period shorten 3~4 times, and usage ratio of equipment improves 40%.Not only can shorten the production cycle of beer greatly, and make finished beer not produce di-acetyl rise phenomenon in storage process, constant product quality reduces production costs.At present, this enzyme is liquid dosage form, and stability is not good enough, needs the transportation of cryopreservation and van cooler, and the stability of enzyme is manufacturer and uses the problem that producer all very pays close attention to.
By retrieval, find some and extract and produce the scientific and technical literature of alpha-acetolactate decarboxylase, but do not see the research report that alpha-acetolactate decarboxylase dry powder is arranged from bacterial classification.The alpha-acetolactate decarboxylase of manufacturer's production both at home and abroad is liquid dosage form at present, and thermostability is relatively poor, is difficult for storage and transport.
Summary of the invention
The object of the present invention is to provide a kind of Heat stability is good, be convenient to alpha-acetolactate decarboxylase dry powder of storage and transport and preparation method thereof.
The following surface technology scheme of the present invention realizes:
The preparation method of alpha-acetolactate decarboxylase dry powder comprises that earlier enzyme being produced bacterium Lactococcus lactis (Lactococcus lactis) or subtilis (Bacillus subtilis) or weak oxide acetobacter (Acetobacter pasteurianus) or bacillus brevis (Bacillus brevis) or Bacillus licheniformis (Bacillus licheniformis) inoculates according to a conventional method and ferment; obtain behind the leavened prod centrifugal; getting supernatant concentration is 10-30% to containing amount of solid; obtain concentrating enzyme liquid; in concentrated enzyme liquid, add protective material then; add protectant amount for concentrating the 1-30% of enzyme liquid total amount; stir; protective material is dissolved in fully concentrates in the enzyme liquid; through behind the homogeneous; in inlet temperature is 150-2002; temperature of outgoing air is 60-90 ℃; cyclone separating tower pressure reduction is 0.7 * 100KPa; feed rate be spray on the Highspeedcentrifugingandsprayingdrier of 30-50 ml/min dried; promptly get the dried enzyme powder of flaxen spray, be packaged to be product again.This product is contained in and places dry place in the plastics bag, can effectively preserve 1-2 under the condition of normal temperature (25 ℃).
Above-described protectant composition and parts by weight are as follows: 0.5~20 part of trehalose, and 0.01~0.5 part of xanthan gum, 1~20 part in dextrin, 0.2~2.0 part of sodium alginate,
Dextrin wherein can be cycloheptaamylose or maltodextrin, or cycloheptaamylose and maltodextrin are with arbitrary proportion blended mixture.
The alpha-acetolactate decarboxylase dry powder for preparing with the present invention should detect its enzyme activity and water content, technical indicator: enzyme activity 〉=10000u/g, moisture content≤5%.
The active character that alpha-acetolactate decarboxylase adding protective material of the present invention is made behind the dry powder does not change; identical with liquid enzyme; but the transportation and use more convenient; as long as add distilled water or pure water dilution, greatly facilitate the user like this before using, the past is because alpha-acetolactate decarboxylase is liquid; must be kept in 0-10 ℃ the freezer; and adopt the low temperature transportation, if run into the enzyme activity reduction in transit of weather temperature height, influenced the quality of enzyme.
Embodiment
Embodiment one
1. by following set of dispense system protective material enzyme liquor: (w/v)
Concentrate 100 milliliters of enzyme liquid
Protective material 10 grams, wherein:
5 parts of trehaloses
0.08 part of xanthan gum
25 parts of maltodextrins
0.42 part of sodium alginate
2. each component of protective material is joined in the enzyme liquid, it is back standby to be stirred to dissolving fully.
3. be 30~40MPa in operating pressure, working flow be carry out on 1 liter/minute the high pressure homogenizer after the second homogenate standby.
4. be 150 ℃ in inlet temperature, temperature of outgoing air is 90 ℃, and cyclone separating tower pressure reduction is 0.7 * 100KPa, and feed rate is to spray driedly on the Highspeedcentrifugingandsprayingdrier of 30 ml/min, promptly gets the dried enzyme powder of flaxen spray.
5. detect its enzyme activity and water content, enzyme activity is answered 〉=10000u/g, and moisture content answers≤5%.
6. packing places dry place, and normal temperature is preserved down.
Embodiment two
1. by following set of dispense system protective material enzyme liquor: (w/v)
Concentrate 100 milliliters of enzyme liquid
Protective material 1 gram, wherein:
20 parts of trehaloses
0.12 part of xanthan gum
10 parts of cycloheptaamyloses
2.0 parts of sodium alginates
2. each component of protective material is joined in the enzyme liquid, it is back standby to be stirred to dissolving fully.
3. be 30~40MPa in operating pressure, working flow be carry out on 1 liter/minute the high pressure homogenizer behind homogeneous standby.
4. be 160 ℃ in inlet temperature, temperature of outgoing air is 80 ℃, and cyclone separating tower pressure reduction is 0.7 * 100KPa, and feed rate is to spray driedly on the Highspeedcentrifugingandsprayingdrier of 40 ml/min, promptly gets the dried enzyme powder of flaxen spray.
5. detect its enzyme activity and water content, enzyme activity is answered 〉=10000u/g, and moisture content answers≤5%.
6. packing places dry place, and normal temperature is preserved down.
Embodiment three
1. by following set of dispense system protective material enzyme liquor: (w/v)
Concentrate 100 milliliters of enzyme liquid
Protective material 30 grams, wherein:
15 parts of trehaloses
0.15 part of xanthan gum
15 parts of maltodextrins
0.35 part of sodium alginate
2. each component of protective material is joined in the enzyme liquid, it is back standby to be stirred to dissolving fully.
3. be 30~40MPa in operating pressure, working flow be carry out on 1 liter/minute the high pressure homogenizer after the second homogenate standby.
4. be 170 ℃ in inlet temperature, temperature of outgoing air is 80 ℃, and cyclone separating tower pressure reduction is 0.7 * 100KPa, and feed rate is to spray driedly on the Highspeedcentrifugingandsprayingdrier of 50 ml/min, promptly gets the dried enzyme powder of flaxen spray.
5. detect its enzyme activity power and water content, enzyme activity power is answered 〉=10000u/g, and moisture content answers≤5%.
6. packing places dry place, and normal temperature is preserved down.
Embodiment four
1. by following set of dispense system protective material enzyme liquor: (w/v)
Concentrate 100 milliliters of enzyme liquid
Protective material 25 grams, wherein:
25 parts of trehaloses
0.05 part of xanthan gum
5 parts of cycloheptaamyloses
0.45 part of sodium alginate
2. each component of protective material is joined in the enzyme liquid, it is back standby to be stirred to dissolving fully.
3. be 30~40MPa in operating pressure, working flow be carry out on 1 liter/minute the high pressure homogenizer after the second homogenate standby.
4. be 200 ℃ in inlet temperature, temperature of outgoing air is 70 ℃, and cyclone separating tower pressure reduction is 0.7 * 100KPa, and feed rate is to spray driedly on the Highspeedcentrifugingandsprayingdrier of 50 ml/min, promptly gets the dried enzyme powder of flaxen spray.
5. detect its enzyme activity and water content, enzyme activity is answered 〉=10000u/g, and moisture content answers≤5%.
6. packing places dry place, and normal temperature is preserved down.
The foregoing description has provided preferred operations condition of the present invention, but technology contents of the present invention is not subjected to the limitation of embodiment.It is as follows to spray dried enzyme powder acceleration thermal stability test result:
50 ℃ 7 days, front and back enzyme activity rate of descent≤1%.
50 ℃ 14 days, front and back enzyme activity rate of descent≤2%.
The dry place of normal temperature (25 ℃) 24 months, enzyme activity rate of descent≤5%.

Claims (4)

1, a kind of preparation method of alpha-acetolactate decarboxylase dry powder, comprise the process that bacterial classification is inoculated according to a conventional method and fermented, it is characterized in that: after obtaining leavened prod, earlier centrifugal, getting supernatant concentration is 10-30% to containing amount of solid, obtain concentrating enzyme liquid, in concentrated enzyme liquid, add protective material then, add protectant amount for concentrating the 1-30% of enzyme liquid total amount, stir, protective material is dissolved in fully concentrates in the enzyme liquid, through behind the homogeneous, on spray-drier, spray driedly, obtain the dried enzyme powder of flaxen spray;
Described protectant composition and parts by weight are as follows: 0.5~20 part of trehalose, 0.01~0.5 part of xanthan gum, 1~20 part in dextrin, 0.2~2.0 part of sodium alginate.
2, the preparation method of alpha-acetolactate decarboxylase dry powder according to claim 1 is characterized in that: the dextrin in the protective material is cycloheptaamylose or maltodextrin, or cycloheptaamylose and maltodextrin are with arbitrary proportion blended mixture.
3, the preparation method of alpha-acetolactate decarboxylase dry powder according to claim 1, it is characterized in that: spray-dired inlet temperature is 150-200 ℃, temperature of outgoing air is 60-90 ℃, and cyclone separating tower pressure reduction is 0.7 * 100KPa, and feed rate is the 30-50 ml/min.
4, the preparation method of alpha-acetolactate decarboxylase dry powder according to claim 1 is characterized in that: in the alpha-acetolactate decarboxylase power-product for preparing, and its enzyme activity 〉=10000u/g, moisture content≤5%.
CNB2004100609872A 2004-10-18 2004-10-18 Alpha-acetyl lactate dehydrogenase dry powder and its preparation process Expired - Fee Related CN100448987C (en)

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CN100448987C true CN100448987C (en) 2009-01-07

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016191169A1 (en) * 2015-05-22 2016-12-01 Dupont Nutrition Biosciences Aps Acetolactate decarboxylase
CN110669752A (en) * 2019-11-12 2020-01-10 河北省微生物研究所 Preparation method of hexokinase spray-dried powder

Non-Patent Citations (6)

* Cited by examiner, † Cited by third party
Title
A-乙酰乳酸脱羧酶的3种固定化方法的比较. 钱斯日古楞.大连轻工业学院学报,第21卷第4期. 2002
A-乙酰乳酸脱羧酶的3种固定化方法的比较. 钱斯日古楞.大连轻工业学院学报,第21卷第4期. 2002 *
a-乙酰乳酸脱羧酶的研究进展及其应用前景. 张博润等.微生物学通报,第24卷第4期. 1997
a-乙酰乳酸脱羧酶的研究进展及其应用前景. 张博润等.微生物学通报,第24卷第4期. 1997 *
磁性淀粉微球固定化乙酰乳酸脱羧酶及应用. 邱广亮等.广州化工,第28卷第4期. 2000
磁性淀粉微球固定化乙酰乳酸脱羧酶及应用. 邱广亮等.广州化工,第28卷第4期. 2000 *

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