CN101293907A - Technique for preparing 5'-inosine acid disodium - Google Patents

Technique for preparing 5'-inosine acid disodium Download PDF

Info

Publication number
CN101293907A
CN101293907A CN 200810028996 CN200810028996A CN101293907A CN 101293907 A CN101293907 A CN 101293907A CN 200810028996 CN200810028996 CN 200810028996 CN 200810028996 A CN200810028996 A CN 200810028996A CN 101293907 A CN101293907 A CN 101293907A
Authority
CN
China
Prior art keywords
saturated
acid disodium
inosine acid
solution
adds
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.)
Granted
Application number
CN 200810028996
Other languages
Chinese (zh)
Other versions
CN101293907B (en
Inventor
张逸伟
刘剑
潘小锋
伍文锋
瞿东方
顾振东
梁健富
宁异真
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ZHAODONG XINGHU BIOTECHNOLOGY Co.,Ltd.
Original Assignee
XINGHU BIOTECH CO Ltd ZHAOQING CITY GUANGDONG PROV
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by XINGHU BIOTECH CO Ltd ZHAOQING CITY GUANGDONG PROV filed Critical XINGHU BIOTECH CO Ltd ZHAOQING CITY GUANGDONG PROV
Priority to CN 200810028996 priority Critical patent/CN101293907B/en
Publication of CN101293907A publication Critical patent/CN101293907A/en
Application granted granted Critical
Publication of CN101293907B publication Critical patent/CN101293907B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Saccharide Compounds (AREA)

Abstract

The invention relates to a production process of 5'-disodium inosinate, particularly to a production process of 5'-disodium inosinate by barium (Ba) precipitation. The production process comprises the steps of: collecting 5'-disodium inosinate water phase, adding certain 5'-disodium inosinate equivalent times of BaCl2 solution (saturated or nearly saturated), adding membrane caustic soda or alkali under stirring to neutralize to pH 7.3-7.6, adding certain 5'-disodium inosinate equivalent times of BaCl2 solution (saturated or nearly saturated), stirring, allowing precipitation, cooling down to below 10DEG C, performing vacuum filtration with a Buchner funnel filter paper to obtain a mother liquid and a barium inosinate (IMPBa) salt, calculating mother liquid loss rate, adding the IMPBa salt into NaSP4 solution (saturated or nearly saturated) with certain equivalent times of 5'-disodium inosinate in the 5'-disodium inosinate water phase, stirring at 60-70DEG C to precipitate inosinate (IMP), performing vacuum filtration with a Buchner funnel filter paper at 60-70DEG C to obtain a BaSO4 precipitate and a filtrate, and calculating 5'-disodium inosinate yield and purity of 5'-disodium inosinate in the filtrate. Compared with the prior art, the inventive production process has the advantages of improved yield and purity of 5'-disodium inosinate, and reduced production cost.

Description

The production technique of 5 '-inosine acid disodium
Technical field
The present invention relates to a kind of 5 '-inosine acid disodium production technique, particularly obtain the production technique of 5 '-inosine acid disodium with the Ba depositing technology.
Background technology
5 '-t-inosinic acid (5 '-IMP) be an intermediate material of biological nucleic acid anabolism system, it is used to multiple field, as food and medicine, and multiple medical field.5 '-t-inosinic acid (5 '-IMP) non-hygroscopic, water-soluble, stabilized aqueous solution.In acidic solution, easily decompose during high temperature, can be decomposed by Phosphoric acid esterase and destroy, be dissolved in ethanol slightly, be dissolved in ether hardly.When JECFA estimated once more in 1993,5 '-inosine acid disodium do not have carcinogenic, teratogenecity, and breeding is not had harm.And it belongs to one of nucleic acid class seasonings, its sodium salt is except that itself has delicate flavour, produce synergy when mixing use with Sodium Glutamate, simultaneously sweet taste, meat flavour there is synergism, salty, sour, bitter taste and raw meat, the smell of burning there is restraining effect, along with improving constantly of living standards of the people, the demand of 5 '-t-inosinic acid sodium salt is increased rapidly, therefore quality is also had higher requirement.As 5 ' of intermediate-t-inosinic acid (5 '-IMP) quality played conclusive effect to the finished product.By direct fermentation produce 5 '-production technique of inosine acid disodium is known in this field, the important key of economic aspect be high density and high yield produce 5 '-inosine acid disodium.Prior art cooling water slowly adds 45%NaOH (w/v) solution, and record PH=10.8 this moment, and temperature is 20.3 ℃.When cooling to-0.5 ℃ again, centrifugation adds 45%NaOH (w/v) solution once more and neutralizes, and neutralization finishes, and this moment, pH value was 7.4, and temperature is 26 ℃, is cooled to 0 ℃ of cooling, and with the crystallization suction filtration, 5 '-the inosine acid disodium crude product.Whole process is consuming time longer, and the solution crystallization is slow, and in addition solution heats up higherly in the exogenously added alkali process, will constantly cool off midway, is unfavorable for the generation of xln, consume simultaneously cold big, the power cost height, the crude product yield is low, solution purity is also not high enough.
Summary of the invention
Purpose of the present invention provides a kind of production technique of 5 '-inosine acid disodium, and it can overcome the deficiencies in the prior art.
The present invention is achieved in that
Get 5 '-the inosine acid disodium water, add 5 '-certain equivalent multiple BaCl of inosine acid disodium equivalents 2Solution (saturated or near saturated), stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, add 5 then '-certain equivalent multiple BaCl of inosine acid disodium equivalents 2Solution (saturated or approaching saturated) stirs precipitation, is cooled to below 10 ℃, with B filter paper vacuum filtration, mother liquor and IMPBa salt, calculate the mother liquor rate of loss, IMPBa salt is added to be equivalent to 5 '-inosine acid disodium aqueous phase 5 '-Na of certain equivalent multiple of inosine acid disodium equivalents 2SO 4Solution (saturated or approaching saturated), IMP is separated out in 60-70 ℃ of stirring, and 60-70 ℃ begins to get BaSO with B filter paper vacuum filtration 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
The present invention compared with prior art, have improve 5 '-yield and the purity of inosine acid disodium crystallization, advantage such as reduce production costs.
Embodiment
Embodiment 1
Get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 300ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 300ml stirs precipitation, normal temperature, and 5 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 60 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, 60 ℃ begin to consider fast 5L/m with B filter paper vacuum filtration 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
Embodiment 2
Get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 300ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 300ml stirs precipitation, and 0 ℃, 5 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 60 ℃ of stirrings, and 20 minutes time, separate out 5 '-inosine acid disodium, 60 ℃ begin with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
Embodiment 3
Get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 300ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 300ml stirs precipitation, is cooled to below 10 ℃, and 40 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, stirring at normal temperature, and 20 minutes time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
Embodiment 4
Get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 300ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 300ml stirs precipitation, is cooled to below 10 ℃, and 40 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 60 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
Embodiment 5
Get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 100ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 100ml stirs precipitation, is cooled to below 4 ℃, and 30 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 70 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
Embodiment 6
Get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 100ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 100ml stirs precipitation, is cooled to below 4 ℃, and 120 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 70 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
Embodiment 7
Get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 200ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 100ml stirs precipitation, is cooled to below 10 ℃, and 120 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 70 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
Obtain in the foregoing description 1~7 5 '-yield of inosine acid disodium and purity with and the rate of loss of water mother liquor, the results are shown in table 1:
Table 1
Figure A20081002899600091
The purity of 5 ' Sodium Inosinate disodium is to measure the present invention BaCl with HPLC 2The precipitator method have obtained desirable result.Compared with prior art, its rate of loss obviously reduces, and yield significantly improves, and its purity also increases under certain condition.In general, the present invention can obtain 5 ' Sodium Inosinate disodium more economically than prior art.

Claims (8)

1, a kind of production technique of 5 '-inosine acid disodium is characterized in that having following steps: get 5 '-the inosine acid disodium water, add 5 '-certain equivalent multiple BaCl of inosine acid disodium equivalents 2Solution (saturated or near saturated), stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, add 5 then '-certain equivalent multiple BaCl of inosine acid disodium equivalents 2Solution (saturated or approaching saturated) stirs precipitation, is cooled to below 10 ℃, with B filter paper vacuum filtration, mother liquor and IMPBa salt, calculate the mother liquor rate of loss, IMPBa salt is added to be equivalent to 5 '-inosine acid disodium aqueous phase 5 '-Na of certain equivalent multiple of inosine acid disodium equivalents 2SO 4Solution (saturated or approaching saturated), IMP is separated out in 60-70 ℃ of stirring, and 60-70 ℃ begins to get BaSO with B filter paper vacuum filtration 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
2, the production technique of a kind of 5 '-inosine acid disodium according to claim 1 is characterized in that having following steps: get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 300ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 300ml stirs precipitation, normal temperature, and 5 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 60 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, 60 ℃ begin to consider fast 5L/m with B filter paper vacuum filtration 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
3, the production technique of a kind of 5 '-inosine acid disodium according to claim 1 is characterized in that having following steps: get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 300ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 300ml stirs precipitation, and 0 ℃, 5 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 60 ℃ of stirrings, and 20 minutes time, separate out 5 '-inosine acid disodium, 60 ℃ begin with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
4, the production technique of a kind of 5 '-inosine acid disodium according to claim 1 is characterized in that having following steps: get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 300ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 300ml stirs precipitation, is cooled to below 10 ℃, and 40 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, stirring at normal temperature, and 20 minutes time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
5, the production technique of a kind of 5 '-inosine acid disodium according to claim 1 is characterized in that having following steps: get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 300ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 300ml stirs precipitation, is cooled to below 10 ℃, and 40 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 60 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
6, the production technique of a kind of 5 '-inosine acid disodium according to claim 1 is characterized in that having following steps: get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 100ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 100ml stirs precipitation, is cooled to below 4 ℃, and 30 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 70 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
7, the production technique of a kind of 5 '-inosine acid disodium according to claim 1 is characterized in that having following steps: get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 100ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 100ml stirs precipitation, is cooled to below 4 ℃, and 120 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 70 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
8, the production technique of a kind of 5 '-inosine acid disodium according to claim 1 is characterized in that having following steps: get 5 '-inosine acid disodium water 200ml, add BaCl 2Solution (saturated or near saturated) 200ml, stir on one side, adding film alkali is neutralized to PH7.3-7.6 on one side, or adds alkali and be neutralized to PH7.3-7.6, adds BaCl 2Solution (saturated or approaching saturated) 100ml stirs precipitation, is cooled to below 10 ℃, and 120 minutes time, with B filter paper vacuum filtration, get mother liquor and IMPBa salt, calculating mother liquor rate of loss adds to Na with IMPBa salt 2SO 4Solution (saturated or near saturated) is to 200ml, 70 ℃ of stirrings, and 3 hours time, separate out 5 '-inosine acid disodium, with B filter paper vacuum filtration, filtering velocity 5L/m 2H gets BaSO 4Precipitation and filtrate, calculate in the filtrate 5 '-inosine acid disodium yield and survey purity.
CN 200810028996 2008-06-24 2008-06-24 Technique for preparing 5'-inosine acid disodium Active CN101293907B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200810028996 CN101293907B (en) 2008-06-24 2008-06-24 Technique for preparing 5'-inosine acid disodium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200810028996 CN101293907B (en) 2008-06-24 2008-06-24 Technique for preparing 5'-inosine acid disodium

Publications (2)

Publication Number Publication Date
CN101293907A true CN101293907A (en) 2008-10-29
CN101293907B CN101293907B (en) 2012-12-12

Family

ID=40064475

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200810028996 Active CN101293907B (en) 2008-06-24 2008-06-24 Technique for preparing 5'-inosine acid disodium

Country Status (1)

Country Link
CN (1) CN101293907B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102199182A (en) * 2011-04-10 2011-09-28 浙江钱江生物化学股份有限公司 One-step extraction method for disodium 5'-inosinate
CN102718823A (en) * 2012-06-26 2012-10-10 华南理工大学 Process method for elution, crystallization and refining of 5'-flavor nucleotide disodium

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4010230B2 (en) * 2002-11-22 2007-11-21 味の素株式会社 Method for producing purine derivative nucleotide disodium crystal and method for removing methanol
CN1243009C (en) * 2003-10-29 2006-02-22 徐昌洪 Technique for preparing 5'nucleotide bi-sodium

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102199182A (en) * 2011-04-10 2011-09-28 浙江钱江生物化学股份有限公司 One-step extraction method for disodium 5'-inosinate
CN102718823A (en) * 2012-06-26 2012-10-10 华南理工大学 Process method for elution, crystallization and refining of 5'-flavor nucleotide disodium
CN102718823B (en) * 2012-06-26 2014-11-12 华南理工大学 Process method for elution, crystallization and refining of 5'-flavor nucleotide disodium

Also Published As

Publication number Publication date
CN101293907B (en) 2012-12-12

Similar Documents

Publication Publication Date Title
CN101591400B (en) Post-extracting method for low-acyl clean-type gellan gum
WO2010074335A1 (en) Method for producing flavor material
CN110818752B (en) Process for producing lactitol
US20140308422A1 (en) Liquid composite high-intensity sweetener and preparation method thereof
CN102898548A (en) Method for preparing inulin
US20230027601A1 (en) Method for manufacturing revaudioside-d-containing crystallized product, and revaudioside-d-containing crystallized product
CN103804439A (en) Synthesis method for neohesperidin dihydrochalcone
CN101293907B (en) Technique for preparing 5'-inosine acid disodium
CN101904483A (en) Method for preparing novel shrimp seasoning
CN101564142A (en) Oyster juice manufacturing method
CN114539333A (en) Cyclic production process of sialic acid
CN103999961B (en) The fixing method of Mulberry-leaf Tea
CN101917872A (en) Method for the production of fermented beverages
CN105237652A (en) Method for preparing polydextrose through dextrose monohydrate
CN104431688A (en) Method for improving erythritol sweetness by co-crystallizing withstevioside
CN103936798B (en) The method for improving the yield of lactose production
US20160302461A1 (en) Process for obtaining a sugar-cane flavoring with a taste based on sugar cane concentrates or on the intermediate honeys and molasses obtained from sugar extraction by the sugar mills, as an additive for high yield sweeteners and the resulting product
CN102106529A (en) Method for producing nutritional flavoring juice by using low-salt salted bittern of preserved vegetables
CN104119408A (en) Method for synthesizing neohesperidin dihydrochalcone from naringin
JP4261429B2 (en) How to improve the taste of food
CN104355989A (en) Method for preparing magnesium malate
CN109608422B (en) Method for synthesizing sodium ascorbate
CN109761798B (en) Preparation method of lactate
JP2006006188A (en) Mineral composition and method for suppressing bitter taste of the same
CN103993107B (en) Method for improving the yield of lactose production

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20211025

Address after: 151100 No. 199, Baxian North Road, Zhaodong City, Suihua City, Heilongjiang Province

Patentee after: ZHAODONG XINGHU BIOTECHNOLOGY Co.,Ltd.

Address before: 526040 No. 67 workers North Road, Duanzhou District, Guangdong, Zhaoqing

Patentee before: Guangdong Zhaoqing Xinghu Biological Technology Co.,Ltd.

TR01 Transfer of patent right