CN102002000A - Method for producing 5,5-dimethyl hydantoin - Google Patents

Method for producing 5,5-dimethyl hydantoin Download PDF

Info

Publication number
CN102002000A
CN102002000A CN 201010548808 CN201010548808A CN102002000A CN 102002000 A CN102002000 A CN 102002000A CN 201010548808 CN201010548808 CN 201010548808 CN 201010548808 A CN201010548808 A CN 201010548808A CN 102002000 A CN102002000 A CN 102002000A
Authority
CN
China
Prior art keywords
parts
dimethyl hydantion
heated
stir
minutes
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 201010548808
Other languages
Chinese (zh)
Other versions
CN102002000B (en
Inventor
李本明
宋昊原
孔繁龙
李莹莹
李楠楠
李丹丹
李婷
Original Assignee
DAQING WELL SOURCE OILFIELD TECHNOLOGY DEVELOPMENT 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 DAQING WELL SOURCE OILFIELD TECHNOLOGY DEVELOPMENT Co Ltd filed Critical DAQING WELL SOURCE OILFIELD TECHNOLOGY DEVELOPMENT Co Ltd
Priority to CN2010105488085A priority Critical patent/CN102002000B/en
Publication of CN102002000A publication Critical patent/CN102002000A/en
Application granted granted Critical
Publication of CN102002000B publication Critical patent/CN102002000B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a method for producing 5,5-dimethyl hydantoin which is prepared from the following substances in parts by weight according to the steps as follows: adding water to ammonium bicarbonate and acetone cyanohydrin, stirring until the ammonium bicarbonate and the acetone cyanohydrin are fully dissolved, and sealing up while heating up to 10 DEG C; introducing ammonia to the mixture, heating slowly to 50-65 DEG C, stirring, heating up to 75-85 DEG C after keeping temperature constant for 1-2 hours, introducing air for 30-50 minutes, and filtering after cooling to a room temperature, thus obtaining crude dimethyl hydantoin and a mother liquid; and putting the crude dimethyl hydantoin into the mixture of water and the mother liquid while stirring, adding active carbon after heating up to 80-98 DEG C, decolouring, removing the active carbon by filtration, recooling, crystallizing, filtering centrifugally, and drying, thus obtaining the finished product of dimethyl hydantoin. The method has the advantages of simple technological reaction, low reaction temperature, short reaction time, less side reaction and high yield reaching 85%, and is easy to control; the raw material of ammonium bicarbonate applicable to the method belongs to chemical fertilizers, and is easy to obtain; and the filtrate produced by the technology can be used repeatedly, and no three wastes are discharged.

Description

5, the production method of 5-dimethyl hydantion
Technical field
The present invention relates to a kind of 5, the production method of 5-dimethyl hydantion.
Background technology
5, the 5-dimethyl hydantion has another name called 5,5-T10 (to call DMH in the following text).
DMH is a kind of important organic synthesis intermediate of having many uses, and is the heterogeneous ring compound with certain rigid backbone.Can prepare a series of valuable derivatives by substitution reaction.As: C5H6Br2N2O2, two chlordantoins etc. is widely used in production fields such as organic synthesis, medicine, plastics, food, makeup, agricultural chemicals.
DMH abroad twentieth century seventies suitability for industrialized production just, the production equipment of producing thousands of tons of per year is all had in the U.S., Britain and Switzerland.Also there is production in Japan, but scale has only 600 tons of annual outputs.
China just begins to carry out the research of this respect the beginning of the nineties, and has realized suitability for industrialized production, is mainly used in the production of DMH derivative sterilizing agent.Research unit is by Hubei University, Institutes Of Technology Of Taiyuan, Shenyang Chemical Engineering Inst etc.There is Quzhou County, Hebei province synthetic glass factory (produce 100 tons of devices per year, built up in 1989) in factory, Hengshui Prefecture, Hebei province chemical industry pilot plant (producing 2000 tons of devices, nineteen ninety-fives per year builds up).In recent years, flourish along with the fine chemistry industry industry, acetone cyanohydrin output increase progressively increase in demand with DMH, built up a collection of production DMH factory at home, its synthesis technique generally adopts the cyclisation method, mainly contains interrupter method and continuous processing two lines.As in the patent No. being 200610038040.0 open source literature, a kind of preparation 5 is also disclosed, the production method of 5-dimethyl hydantion but yield be low, be not easy to control.
Summary of the invention
The present invention is intended to overcome the deficiencies in the prior art, developed a kind of 5, the production method of 5-dimethyl hydantion.
Of the present invention 5, the production method of 5-dimethyl hydantion is made by weight as follows by following material:
A, 500~700 parts in 600~800 parts in bicarbonate of ammonia, acetone cyanohydrin is added water stir fully dissolving, airtight when being heated to 10 ℃;
B, in the material that makes through a step, feed 30~50 parts of ammonias again, slowly heat to 50~65 ℃, constant temperature 1~2 hour, and stir;
C, will be heated to 75~85 ℃ through the material of b step system, air inducing 30~50 minutes is cooled to the room temperature after-filtration again, promptly makes dimethyl hydantion crude product and mother liquor;
D, will render in the mother liquor mixture of 150~300 parts water and 700~900 parts through 950~1150 parts of dimethyl hydantion crude products that the c step makes, stir while throwing in, add 3~8 parts of activated carbon after being heated to 80~98 ℃, decoloured 20~40 minutes, remove by filter activated carbon, crystallisation by cooling, centrifuging, oven dry more promptly makes the dimethyl hydantion finished product.
The market of DMH can be considered from purposes two aspects of water quality stabilizer and DMH derivative.China is the very not abundant country of a water resources, and in process water, the consumption of water coolant ranks first.Generally account for more than 60%.Therefore, recycling of water coolant is one of important channel of water saving.At this moment need add various medicaments such as inhibiter in the recirculated water.DMH can be directly used in the anti-stick mud agent of cooling water system.In addition, the multiple derivative of DMH can be done the sterilant of recirculated cooling water.
From the purposes aspect of DMH derivative, be mainly used in the engineering of water treatment sterilization, algae removal, deodorization and swimming sterilizing sterilization etc.Increasing rapidly at halogen glycolylurea series product consumption aspect U.S.'s swimming sterilizing sterilization.In addition, according to the demand of water treatment and entertainment industry, U.S. Zuo Long company produces in several reagent combinations of killing acquired immune deficiency syndrome (AIDS), also contains the halogenated hydantoin derivative.
Of the present invention 5, the production method technological reaction of 5-dimethyl hydantion is simple, temperature of reaction is low, the time is short, be easy to control, and side reaction is few, and yield can reach 85%; The raw material bicarbonate of ammonia that this method was suitable for belongs to fertilizer type, raw material is easy to get; The filtrate that is produced in this technology can recycle, and does not have the discharging of " three wastes ".
Embodiment
Embodiment 1
Of the present invention 5, the production method of 5-dimethyl hydantion is by following material, makes as follows by weight:
A, 500~700 parts in 600~800 parts in bicarbonate of ammonia, acetone cyanohydrin is added water stir fully dissolving, airtight when being heated to 10 ℃;
B, in the material that makes through a step, feed 30~50 parts of ammonias again, slowly heat to 50~65 ℃, constant temperature 1~2 hour, and stir;
C, will be heated to 75~85 ℃ through the material of b step system, air inducing 30~50 minutes is cooled to the room temperature after-filtration again, promptly makes dimethyl hydantion crude product and mother liquor;
D, will render in 150~300 parts of water and 700~900 parts of mother liquor mixtures through 950~1150 parts of dimethyl hydantion crude products that the c step makes, stir while throwing in, add 3~8 parts of activated carbon after being heated to 80~98 ℃, decoloured 20~40 minutes, remove by filter activated carbon, crystallisation by cooling, centrifuging, oven dry more promptly makes the dimethyl hydantion finished product.
Embodiment 2
Of the present invention 5, the production method of 5-dimethyl hydantion is by following material, makes as follows by weight:
A, 600 parts in 700 parts in bicarbonate of ammonia, acetone cyanohydrin is added water stir fully dissolving, airtight when being heated to 10 ℃;
B, in the material that makes through a step, feed 40 parts of ammonias again, slowly heat to 60 ℃, constant temperature 2 hours, and stir;
C, will be heated to 80 ℃ through the material of b step system, air inducing 40 minutes is cooled to the room temperature after-filtration again, promptly makes dimethyl hydantion crude product and mother liquor;
D, will render in the mixture of 800 parts in 200 parts in water and mother liquor through 1050 parts of dimethyl hydantion crude products that the c step makes, stir while throwing in, add 5 parts of activated carbon after being heated to 95 ℃, decoloured 30 minutes, remove by filter activated carbon, crystallisation by cooling, centrifuging, oven dry more promptly makes the dimethyl hydantion finished product.
Embodiment 3
Of the present invention 5, the production method of 5-dimethyl hydantion is by following material, makes as follows by weight:
A, 500 parts in 600 parts in bicarbonate of ammonia, acetone cyanohydrin is added water stir fully dissolving, airtight when being heated to 10 ℃;
B, in the material that makes through a step, feed 30 parts of ammonias again, slowly heat to 50 ℃, constant temperature 1.5 hours, and stir;
C, will be heated to 75 ℃ through the material of b step system, air inducing 30 minutes is cooled to the room temperature after-filtration again, promptly makes dimethyl hydantion crude product and mother liquor;
D, will render in the mixture of 700 parts in 150 parts in water and mother liquor through 950 parts of dimethyl hydantion crude products that the c step makes, stir while throwing in, add 3 parts of activated carbon after being heated to 90 ℃, decoloured 20 minutes, remove by filter activated carbon, crystallisation by cooling, centrifuging, oven dry more promptly makes the dimethyl hydantion finished product.
Embodiment 4
Of the present invention 5, the production method of 5-dimethyl hydantion is by following material, makes as follows by weight:
A, 700 parts in 800 parts in bicarbonate of ammonia, acetone cyanohydrin is added water stir fully dissolving, airtight when being heated to 10 ℃;
B, in the material that makes through a step, feed 50 parts of ammonias again, slowly heat to 65 ℃, constant temperature 2 hours, and stir;
C, will be heated to 85 ℃ through the material of b step system, air inducing 50 minutes is cooled to the room temperature after-filtration again, promptly makes dimethyl hydantion crude product and mother liquor;
D, will render in the mixture of 300 parts of water and 900 parts of mother liquors through 1150 parts of dimethyl hydantion crude products that the c step makes, stir while throwing in, add 8 parts of activated carbon after being heated to 95 ℃, decoloured 40 minutes, remove by filter activated carbon, crystallisation by cooling, centrifuging, oven dry more promptly makes the dimethyl hydantion finished product.

Claims (2)

1.5 the production method of 5-dimethyl hydantion is by following material, makes as follows by weight:
A, 500~700 parts in 600~800 parts in bicarbonate of ammonia, acetone cyanohydrin is added water stir fully dissolving, airtight when being heated to 10 ℃;
B, in the material that makes through a step, feed 30~50 parts of ammonias again, slowly heat to 50~65 ℃, constant temperature 1~2 hour, and stir;
C, will be heated to 75~85 ℃ through the material of b step system, air inducing 30~50 minutes is cooled to the room temperature after-filtration again, promptly makes dimethyl hydantion crude product and mother liquor;
D, will render in the mixture of 150~300 parts of water and 700~900 parts of mother liquors through 950~1150 parts of dimethyl hydantion crude products that the c step makes, stir while throwing in, add 3~8 parts of activated carbon after being heated to 80~98 ℃, decoloured 20~40 minutes, remove by filter activated carbon, crystallisation by cooling, centrifuging, oven dry more promptly makes the dimethyl hydantion finished product.
2. as claimed in claim 15, the production method of 5-dimethyl hydantion is by following material, makes as follows by weight:
A, 600 parts in 700 parts in bicarbonate of ammonia, acetone cyanohydrin is added water stir fully dissolving, airtight when being heated to 10 ℃;
B, in the material that makes through a step, feed 40 parts of ammonias again, slowly heat to 60 ℃, constant temperature 2 hours, and stir;
C, will be heated to 80 ℃ through the material of b step system, air inducing 40 minutes is cooled to the room temperature after-filtration again, promptly makes dimethyl hydantion crude product and mother liquor;
D, will render in the mixture of 200 parts of water and 800 parts of mother liquors through 1050 parts of dimethyl hydantion crude products that the c step makes, stir while throwing in, add 5 parts of activated carbon after being heated to 95 ℃, decoloured 30 minutes, remove by filter activated carbon, crystallisation by cooling, centrifuging, oven dry more promptly makes the dimethyl hydantion finished product.
CN2010105488085A 2010-11-18 2010-11-18 Method for producing 5,5-dimethyl hydantoin Expired - Fee Related CN102002000B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010105488085A CN102002000B (en) 2010-11-18 2010-11-18 Method for producing 5,5-dimethyl hydantoin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010105488085A CN102002000B (en) 2010-11-18 2010-11-18 Method for producing 5,5-dimethyl hydantoin

Publications (2)

Publication Number Publication Date
CN102002000A true CN102002000A (en) 2011-04-06
CN102002000B CN102002000B (en) 2012-07-25

Family

ID=43809735

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010105488085A Expired - Fee Related CN102002000B (en) 2010-11-18 2010-11-18 Method for producing 5,5-dimethyl hydantoin

Country Status (1)

Country Link
CN (1) CN102002000B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104557721A (en) * 2014-12-30 2015-04-29 沈阳化工研究院有限公司 Method for producing 5,5-dimethylhydantoin
CN108148000A (en) * 2018-03-20 2018-06-12 河北鑫淘源环保科技有限公司 A kind of preparation method of 5,5 Dimethyl Hydan
CN115703743A (en) * 2021-11-16 2023-02-17 吉林市吉化江城油脂化工有限责任公司 Crystallization method of 5, 5-dimethylhydantoin
CN115703744A (en) * 2021-11-16 2023-02-17 吉林市吉化江城油脂化工有限责任公司 Preparation method of 5,5-dimethylhydantoin

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1356321A (en) * 2001-12-06 2002-07-03 天津大学 Process for preparing 5,5-dimethyl-2,4-imidazolinedione by intermittent presurizing method
CN1803775A (en) * 2006-01-23 2006-07-19 周新基 Method for preparing 5,5-dimethylhydantion

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1356321A (en) * 2001-12-06 2002-07-03 天津大学 Process for preparing 5,5-dimethyl-2,4-imidazolinedione by intermittent presurizing method
CN1803775A (en) * 2006-01-23 2006-07-19 周新基 Method for preparing 5,5-dimethylhydantion

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
《南京化工学院学报》 19950430 崔群等 改进Bucherer-Berg"s法合成乙内酰脲 125-129 1-2 第17卷, 第2期 2 *
《山东化工》 20001231 王笑海 等 DMH的合成及应用 19-21,15 1-2 第29卷, 第4期 2 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104557721A (en) * 2014-12-30 2015-04-29 沈阳化工研究院有限公司 Method for producing 5,5-dimethylhydantoin
CN108148000A (en) * 2018-03-20 2018-06-12 河北鑫淘源环保科技有限公司 A kind of preparation method of 5,5 Dimethyl Hydan
CN115703743A (en) * 2021-11-16 2023-02-17 吉林市吉化江城油脂化工有限责任公司 Crystallization method of 5, 5-dimethylhydantoin
CN115703744A (en) * 2021-11-16 2023-02-17 吉林市吉化江城油脂化工有限责任公司 Preparation method of 5,5-dimethylhydantoin
CN115703743B (en) * 2021-11-16 2024-05-10 吉林市吉化江城油脂化工有限责任公司 Crystallization method of 5, 5-dimethyl hydantoin

Also Published As

Publication number Publication date
CN102002000B (en) 2012-07-25

Similar Documents

Publication Publication Date Title
CN104473120B (en) A kind of production technology of monosodium glutamate
CN102002000B (en) Method for producing 5,5-dimethyl hydantoin
CN107474088B (en) Extraction process for industrial mass production of spinosad
CN107337618B (en) Production method for simultaneously improving purity and yield of metformin hydrochloride
CN103923140A (en) Preparation method of acetylisovaleryltylosin tartrate
CN108484475A (en) The production method of pesticide intermediate 1,2,3,6- tetrahydric phthalimides
CN103804172B (en) A kind of method improving organic acid production quality
CN103113440B (en) Preparation method of erythromycin thiocyanate
CN105061289B (en) A kind of method for preparing pharmaceutical grade L tryptophans
CN106008554A (en) Preparation method and product of ceftriaxone sodium sterile powder
CN103524389A (en) Method for preparing pesticide methomyl
CN103374046A (en) Method for preparing D-glucosamine hydrochloride
CN111517972A (en) Preparation method of environment-friendly betaine
CN104892554B (en) The preparation method of a kind of gibberic acid GA3
CN106946816A (en) A kind of preparation method of chloro terramycin
CN108484505B (en) Preparation method of 2-methylimidazole
CN112591784A (en) Safe and energy-saving chemical agent production process
CN109836344B (en) Method for producing glycine by organic solvent
CN107043343B (en) Preparation method of L-pyroglutamic acid
CN102530902B (en) Industrialized continuous potassium dihydrogen phosphate production method
CN102020576A (en) High-purity glutamic acid and preparation method thereof
CN104447958B (en) The method of enramycin is extracted from fermentation liquid
CN108640851A (en) A kind of high purity N ,-(trityl)The method of purification of altheine
CN110642723A (en) Synthesis method of p-nitro-o-toluidine
CN111848433B (en) Process for preparing 4-aminophenylacetamide

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
ASS Succession or assignment of patent right

Owner name: ZHU LINING

Free format text: FORMER OWNER: DAQING JINGJINGYUAN OILFIELD TECHNOLOGY DEVELOPMENT CO., LTD.

Effective date: 20120524

C41 Transfer of patent application or patent right or utility model
C53 Correction of patent for invention or patent application
CB03 Change of inventor or designer information

Inventor after: Ma Zhenyu

Inventor after: Wang Jie

Inventor after: Ma Lin

Inventor after: Zhu Lining

Inventor before: Li Benming

Inventor before: Song Haoyuan

Inventor before: Kong Fanlong

Inventor before: Li Yingying

Inventor before: Li Nannan

Inventor before: Li Dandan

Inventor before: Li Ting

COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 163853 DAQING, HEILONGJIANG PROVINCE TO: 163000 DAQING, HEILONGJIANG PROVINCE

Free format text: CORRECT: INVENTOR; FROM: LI BENMING SONG HAOYUAN KONG FANLONG LI YINGYING LI NANNAN LI DANDAN LI TING TO: MA ZHENYU WANG JIE MA LIN ZHU LINING

TA01 Transfer of patent application right

Effective date of registration: 20120524

Address after: 163000 Heilongjiang province Daqing City Longfeng District Dragon Road East leader A-30 Door No. 2 Room 301

Applicant after: Zhu Lining

Address before: 163853 Heilongjiang city in Daqing province north of Honggang District Zhuang Yuanfeng Road Venture

Applicant before: Daqing Well Source Oilfield Technology Development Co., Ltd.

C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Application publication date: 20110406

Assignee: Daqing Jingcheng Chemical Co., Ltd.

Assignor: Zhu Lining

Contract record no.: 2015990000239

Denomination of invention: Preparation of N,N,N',N',-tetraacetyl-3,5,3',5'-tetrabromo(chloro)-4,4'-diaminodiphenyl methane

Granted publication date: 20120725

License type: Exclusive License

Record date: 20150427

LICC Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model
EC01 Cancellation of recordation of patent licensing contract

Assignee: Daqing Jingcheng Chemical Co., Ltd.

Assignor: Zhu Lining

Contract record no.: 2015990000239

Date of cancellation: 20160612

LICC Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120725

Termination date: 20171118