CN107652196A - A kind of removal technique of the glycine zine crystallization water - Google Patents

A kind of removal technique of the glycine zine crystallization water Download PDF

Info

Publication number
CN107652196A
CN107652196A CN201710984610.3A CN201710984610A CN107652196A CN 107652196 A CN107652196 A CN 107652196A CN 201710984610 A CN201710984610 A CN 201710984610A CN 107652196 A CN107652196 A CN 107652196A
Authority
CN
China
Prior art keywords
glycine
znso
crystal
crystallization water
glycine zine
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
Application number
CN201710984610.3A
Other languages
Chinese (zh)
Inventor
田录
贾瑞莲
王佳亮
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.)
CHANGNING DEBANG BIOTECHNOLOGY Co.,Ltd.
Original Assignee
Hengyang Debang Xinjin Biotechnology Co Ltd
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 Hengyang Debang Xinjin Biotechnology Co Ltd filed Critical Hengyang Debang Xinjin Biotechnology Co Ltd
Priority to CN201710984610.3A priority Critical patent/CN107652196A/en
Publication of CN107652196A publication Critical patent/CN107652196A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/14Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing already amino and carboxyl groups or derivatives thereof
    • C07C227/18Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing already amino and carboxyl groups or derivatives thereof by reactions involving amino or carboxyl groups, e.g. hydrolysis of esters or amides, by formation of halides, salts or esters
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/38Separation; Purification; Stabilisation; Use of additives
    • C07C227/40Separation; Purification
    • C07C227/42Crystallisation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention belongs to chemical technology field, and in particular to a kind of removal technique of the glycine zine crystallization water, its step comprise the following steps:A certain amount of water, ZnSO are weighed by weight4.H2O, glycine and neopelex, ZnSO is added after first heating the water to 50 65 DEG C4.H2O, stirring make ZnSO4.H2O adds glycine after fully dissolving, then system is reacted under certain conditions the regular hour, then is charged with neopelex, is stirred continuously to cooling and separates out crystal, finally dries crystal.The present invention by being produced in glycine zine during add neopelex and reach good dehydrating effect, and the technology investment is low, obtained product safety, has very big promotional value.

Description

A kind of removal technique of the glycine zine crystallization water
Technical field
The invention belongs to chemical technology field, and in particular to a kind of removal technique of the glycine zine crystallization water.
Background technology
Glycine zine is the additive of feed microelement, just gradually replaces zinc sulfate, the standard of glycine zine be zinc >= 21%, total glycine amount >=23%, water≤10%.Basic zinc carbonate or zinc sulfate and glycine generation chela can be used by producing glycine zine Compound.Use ZnSO4·H2The glycine zine of O synthesis contains the 15-16% crystallization water, does not reach standard.Generally removing the crystallization water has Several method:First, drying temperature is improved in process of production to more than 120 DEG C, but more than more than 80 DEG C glycine zines can divide Solution, the method do not apply to glycine zine;Another method is vacuum drying, but this method is invested, and is unfavorable for promoting;Also one Kind of method is that product is dissolved in ethanol azeotropic dehydration, but changes method and do not allow in cost secure context, investing.Therefore need to grind Study carefully that a kind of dehydrating effect is good, the removal technique of low, product safety the glycine zine crystallization water of investment.
The content of the invention
It is an object of the present invention in view of the above-mentioned problems, a kind of dehydrating effect of offer is good, invests low, product safety The glycine zine crystallization water removal technique.
To reach above-mentioned purpose, the technical solution adopted in the present invention is:
A kind of removal technique of the glycine zine crystallization water, comprises the following steps:
By 100:60:24:1-2.5 weight part ratio is fetched water respectively, ZnSO4.H2O, glycine and neopelex, first Water is placed in a vessel in heating to 50-65 DEG C, is then charged with ZnSO4.H2O, stirring make ZnSO4.H2O is completely dissolved After add glycine, this is system 1, system 1 is stopped heating after reacting 30-40min under conditions of 50-65 DEG C, obtains body It is 2, system 2 is carried out to be concentrated to give system 3;Then toward adding neopelex in system 3, and it is stirred continuously to body It is that 3 coolings separate out crystal, then filters to take its crystal, finally dry crystal, produce the glycine zine for removing the crystallization water.
In the present invention, further instruction, a kind of removal technique of the glycine zine crystallization water, including following step Suddenly:
By 100:60:24:1.8-2 weight part ratio is fetched water respectively, ZnSO4.H2O, glycine and neopelex, first Water is placed in a vessel in heating to 55-60 DEG C, is then charged with ZnSO4.H2O, stirring make ZnSO4.H2O is completely dissolved After add glycine, this is system 1, system 1 is stopped heating after reacting 34-37min under conditions of 55-60 DEG C, obtains body It is 2, system 2 is carried out to be concentrated to give system 3;Then toward adding neopelex in system 3, and it is stirred continuously to body It is that 3 coolings separate out crystal, then filters to take its crystal, finally dry crystal, produce the glycine zine for removing the crystallization water.
In the present invention, further instruction, the volume of system 3 are the 45-55% of the system 2.
In the present invention, further instruction, the crystal baking step, its drying condition are 55-65 DEG C, drying time For 3.5-4.5h.
In the present invention, further instruction, the volume of system 3 are the 48-52% of the system 2.
In the present invention, further instruction, the crystal baking step, its drying condition are 58-62 DEG C, drying time For 3.8-4.2h.
The present invention has the advantage that compared with prior art:
1. the present invention by being produced in glycine zine during add auxiliary agent reach good dehydrating effect.Added in the present invention Auxiliary agent be neopelex, a neopelex molecule part is polarity, and a part is nonpolar, polarity Part is close with the zinc of glycine zine, and nonpolar moiety molecular chain length, can effectively prevent water from generating the crystallization water with glycine zine, So as to reduce moisture content.
2. glycine zine removal crystallization water technology investment of the present invention is low, and product safety.The auxiliary agent dodecane added Base benzene sulfonic acid sodium salt is cheap, reduces cost of investment.Neopelex contains part and glycine zine cocrystallization, but Less than 1 percent, other indexs of glycine zine are not influenceed, obtained glycine zine product safety.The present invention removes glycine The product safety that zinc crystallization water effect is good, investment is low and obtains, has very big promotional value.
Embodiment
The invention provides a kind of removal technique of the glycine zine crystallization water is provided, to make the purpose of the present invention, technical side Case and effect are clearer, clear and definite, and the present invention is described in more detail below.It is it should be appreciated that described herein specific real Example is applied only to explain the present invention, is not intended to limit the present invention.
Embodiment 1
A kind of removal technique of glycine zine crystallization water provided by the invention is as follows:
A kind of removal technique of the glycine zine crystallization water, comprises the following steps:
By 100:60:24:1 weight part ratio is fetched water respectively, ZnSO4.H2O, glycine and neopelex, first by water A vessel in heating is placed in 50 DEG C, is then charged with ZnSO4.H2O, stirring make ZnSO4.H2O adds sweet after being completely dissolved Propylhomoserin, this is system 1, system 1 is stopped heating after reacting 30min under conditions of 50 DEG C, obtains system 2, system 2 is concentrated To the 45% of original volume, system 3 is obtained;Then toward adding neopelex in system 3, and it is stirred continuously cold to system 3 But crystal is separated out, then filters to take its crystal, drying 3.5h is carried out under conditions of crystal finally is placed in into 55 DEG C, produces removal knot The glycine zine of brilliant water.
Embodiment 2
A kind of removal technique of glycine zine crystallization water provided by the invention is as follows:
A kind of removal technique of the glycine zine crystallization water, comprises the following steps:
By 100:60:24:1.8 weight part ratio is fetched water respectively, ZnSO4.H2O, glycine and neopelex, first will Water is placed in a vessel in heating to 55 DEG C, is then charged with ZnSO4.H2O, stirring make ZnSO4.H2O is added after being completely dissolved Glycine, this is system 1, system 1 is stopped heating after reacting 34min under conditions of 55 DEG C, obtains system 2, and system 2 is dense The 48% of original volume is reduced to, obtains system 3;Then toward adding neopelex in system 3, and it is stirred continuously to system 3 Cooling separates out crystal, then filters to take its crystal, carries out drying 3.8h under conditions of crystal finally is placed in into 58 DEG C, produce removal The glycine zine of the crystallization water.
Embodiment 3
A kind of removal technique of glycine zine crystallization water provided by the invention is as follows:
A kind of removal technique of the glycine zine crystallization water, comprises the following steps:
By 100:60:24:2 weight part ratio is fetched water respectively, ZnSO4.H2O, glycine and neopelex, first by water A vessel in heating is placed in 60 DEG C, is then charged with ZnSO4.H2O, stirring make ZnSO4.H2O adds sweet after being completely dissolved Propylhomoserin, this is system 1, system 1 is stopped heating after reacting 37min under conditions of 60 DEG C, obtains system 2, system 2 is concentrated To the 52% of original volume, system 3 is obtained;Then toward adding neopelex in system 3, and it is stirred continuously cold to system 3 But crystal is separated out, then filters to take its crystal, drying 4.2h is carried out under conditions of crystal finally is placed in into 62 DEG C, produces removal knot The glycine zine of brilliant water.
Embodiment 4
A kind of removal technique of glycine zine crystallization water provided by the invention is as follows:
A kind of removal technique of the glycine zine crystallization water, comprises the following steps:
By 100:60:24:2.5 weight part ratio is fetched water respectively, ZnSO4.H2O, glycine and neopelex, first will Water is placed in a vessel in heating to 65 DEG C, is then charged with ZnSO4.H2O, stirring make ZnSO4.H2O is added after being completely dissolved Glycine, this is system 1, system 1 is stopped heating after reacting 40min under conditions of 65 DEG C, obtains system 2, and system 2 is dense The 55% of original volume is reduced to, obtains system 3;Then toward adding neopelex in system 3, and it is stirred continuously to system 3 Cooling separates out crystal, then filters to take its crystal, carries out drying 4.5h under conditions of crystal finally is placed in into 65 DEG C, produce removal The glycine zine of the crystallization water.
Water content in the glycine zine that detection above example 1-4 is obtained respectively, and be recorded in table, it is as a result as follows:
Embodiment Embodiment 1 Embodiment 2 Embodiment 3 Embodiment 4
Water content 12.05% 9.85% 1.5% 0.36%
As seen from the above table, the present invention can effectively remove the crystallization water in glycine zine, and its effect is with neopelex Addition and become.The glycine zine that above example 2-4 is obtained meets the standard of water≤10%.
Described above is the detailed description for the present invention preferably possible embodiments, but embodiment is not limited to this hair Bright patent claim, the equal change completed or modification change under the technical spirit suggested by all present invention, all should belong to Cover the scope of the claims in the present invention.

Claims (6)

1. a kind of removal technique of the glycine zine crystallization water, it is characterised in that comprise the following steps:
By 100:60:24:1-2.5 weight part ratio is fetched water respectively, ZnSO4.H2O, glycine and neopelex, first Water is placed in a vessel in heating to 50-65 DEG C, is then charged with ZnSO4.H2O, stirring make ZnSO4.H2O is completely dissolved After add glycine, this is system 1, system 1 is stopped heating after reacting 30-40min under conditions of 50-65 DEG C, obtains body It is 2, system 2 is carried out to be concentrated to give system 3;Then toward adding neopelex in system 3, and it is stirred continuously to body It is that 3 coolings separate out crystal, then filters to take its crystal, finally dry crystal, produce the glycine zine for removing the crystallization water.
2. the removal technique of a kind of glycine zine crystallization water according to claim 1, it is characterised in that including following step Suddenly:
By 100:60:24:1.8-2 weight part ratio is fetched water respectively, ZnSO4.H2O, glycine and neopelex, first Water is placed in a vessel in heating to 55-60 DEG C, is then charged with ZnSO4.H2O, stirring make ZnSO4.H2O is completely dissolved After add glycine, this is system 1, system 1 is stopped heating after reacting 34-37min under conditions of 55-60 DEG C, obtains body It is 2, system 2 is carried out to be concentrated to give system 3;Then toward adding neopelex in system 3, and it is stirred continuously to body It is that 3 coolings separate out crystal, then filters to take its crystal, finally dry crystal, produce the glycine zine for removing the crystallization water.
A kind of 3. removal technique of glycine zine crystallization water according to claim 1, it is characterised in that:The body of system 3 Product is the 45-55% of the system 2.
A kind of 4. removal technique of glycine zine crystallization water according to claim 1, it is characterised in that:The crystal drying Step, its drying condition are 55-65 DEG C, drying time 3.5-4.5h.
A kind of 5. removal technique of glycine zine crystallization water according to claim 2, it is characterised in that:The body of system 3 Product is the 48-52% of the system 2.
A kind of 6. removal technique of glycine zine crystallization water according to claim 2, it is characterised in that:The crystal drying Step, its drying condition are 58-62 DEG C, drying time 3.8-4.2h.
CN201710984610.3A 2017-10-20 2017-10-20 A kind of removal technique of the glycine zine crystallization water Pending CN107652196A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710984610.3A CN107652196A (en) 2017-10-20 2017-10-20 A kind of removal technique of the glycine zine crystallization water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710984610.3A CN107652196A (en) 2017-10-20 2017-10-20 A kind of removal technique of the glycine zine crystallization water

Publications (1)

Publication Number Publication Date
CN107652196A true CN107652196A (en) 2018-02-02

Family

ID=61117840

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710984610.3A Pending CN107652196A (en) 2017-10-20 2017-10-20 A kind of removal technique of the glycine zine crystallization water

Country Status (1)

Country Link
CN (1) CN107652196A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111662198A (en) * 2020-06-08 2020-09-15 四川爱隆植物营养科技有限公司 Preparation method of zinc glycinate chelate

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103922954A (en) * 2014-04-02 2014-07-16 哈尔滨德邦鼎立生物科技有限公司 Method for preparing glycine zinc chelate
CN106187796A (en) * 2016-07-08 2016-12-07 仲恺农业工程学院 A kind of preparation method of zinc-glycine complex

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103922954A (en) * 2014-04-02 2014-07-16 哈尔滨德邦鼎立生物科技有限公司 Method for preparing glycine zinc chelate
CN106187796A (en) * 2016-07-08 2016-12-07 仲恺农业工程学院 A kind of preparation method of zinc-glycine complex

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111662198A (en) * 2020-06-08 2020-09-15 四川爱隆植物营养科技有限公司 Preparation method of zinc glycinate chelate

Similar Documents

Publication Publication Date Title
CN101486669B (en) Method for synthesizing taurine
EP3029762B1 (en) Method for synthesizing nano-lithium iron phosphate without water of crystallization in aqueous phase at normal pressure
CN105271413B (en) A kind of method for extracting tungsten from phosphotungstic acid/phosphotungstate solution
CN101348299A (en) Glyphosate synthesized mother liquor processing method
CN104098461A (en) Purifying method of [beta]-hydroxyl-[beta]-methylbutyric acid
CN106745099A (en) A kind of method that utilization lithium phosphate prepares lithium carbonate
CN111086977A (en) Method for preparing MCP and MDCP (Madin-Darby Canine phosphate) by using raffinate acid
CN107652196A (en) A kind of removal technique of the glycine zine crystallization water
CN110668489A (en) Method for preparing zinc sulfate monohydrate from zinc-containing waste residue
CN107176907A (en) A kind of method for extracting malic acid/malate
CN103319387B (en) A kind of preparation method of thiophenol compound antioxidant product
CN107324375A (en) A kind of preparation method of basic zinc chloride
CN102275954A (en) Method for purifying potassium iodide and use thereof
CN104387255A (en) Preparation method of calcium formate
CN106350419B (en) Utilize the method for the wine brewing yellow water production compound Wine blending liquid of lactic acid
CN107445878B (en) Lutein crystal and its preparation process
CN115403018A (en) Method for preparing iron phosphate by using high-impurity phosphoric acid and method for preparing anode material
CN110938020B (en) Preparation process of lauroyl arginine ethyl ester hydrochloride
CN103274432A (en) Method for comprehensively utilizing hydrazine hydrate by-product sodium carbonate decahydrate through urea method
CN107698466A (en) A kind of preparation method of N methyl Ns ' nitroguanidine
CN106430282A (en) Preparation method of basic copper sulfate
US2217786A (en) Expander for storage batteries
CN103626235B (en) Method for preparing high-purity manganese sulfate by recrystallizing
CN108217739A (en) It is a kind of to prepare the method for manganese sulfate and its product obtained with troilite
CN111977683A (en) Preparation method of zinc sulfate monohydrate

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right

Effective date of registration: 20201016

Address after: 421500 68 Bridge Road, Shuikou Town, Changning City, Hengyang, Hunan

Applicant after: CHANGNING DEBANG BIOTECHNOLOGY Co.,Ltd.

Address before: 421000, Hunan, Hengyang province Shigu pine Development Zone, Jin Yuan Road, No. 13 south side

Applicant before: HENGYANG DEBANG XINJIN BIOTECHNOLOGY Co.,Ltd.

TA01 Transfer of patent application right
RJ01 Rejection of invention patent application after publication

Application publication date: 20180202

RJ01 Rejection of invention patent application after publication