CN108017551B - Method for recovering dimethylethanolamine from hydrazine reaction solution - Google Patents

Method for recovering dimethylethanolamine from hydrazine reaction solution Download PDF

Info

Publication number
CN108017551B
CN108017551B CN201711354893.XA CN201711354893A CN108017551B CN 108017551 B CN108017551 B CN 108017551B CN 201711354893 A CN201711354893 A CN 201711354893A CN 108017551 B CN108017551 B CN 108017551B
Authority
CN
China
Prior art keywords
dimethylethanolamine
benzene
reaction solution
recovering
hydrazine
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.)
Active
Application number
CN201711354893.XA
Other languages
Chinese (zh)
Other versions
CN108017551A (en
Inventor
陈骏
周龙达
杨常桥
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.)
Shanghai Shisi Chemical Product Co ltd
Original Assignee
Shanghai Shisi Chemical Product 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 Shanghai Shisi Chemical Product Co ltd filed Critical Shanghai Shisi Chemical Product Co ltd
Priority to CN201711354893.XA priority Critical patent/CN108017551B/en
Publication of CN108017551A publication Critical patent/CN108017551A/en
Application granted granted Critical
Publication of CN108017551B publication Critical patent/CN108017551B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/10Separation; Purification; Stabilisation; Use of additives

Abstract

The invention discloses a method for recovering dimethylethanolamine from hydrazine reaction liquid, which is characterized in that benzene is added into the hydrazine reaction liquid to extract dimethylethanolamine, then the benzene and dimethylethanolamine are separated by adopting a method of combining distillation and rectification, and the high-purity dimethylethanolamine is recovered. The invention adopts benzene extraction, simple distillation and rectification to effectively recover the dimethylethanolamine in the hydrazine reaction mother liquor, and has low energy consumption in the recovery process, high purity of the recovered dimethylethanolamine and no influence on the hydrazine synthesis reaction due to repeated use.

Description

Method for recovering dimethylethanolamine from hydrazine reaction solution
Technical Field
The invention belongs to the field of fine chemical engineering, and particularly relates to a method for recovering dimethylethanolamine from a hydrazine reaction solution.
Background
In the conventional organic solvent purification process, a distillation method, particularly a rectification method is mainly adopted for removing water, and the method of collecting fractions by controlling the reflux ratio and the top temperature control improves the content of the organic solvent and reduces the water in the organic solvent. Some solvents also have been treated by adding a water absorbent (e.g., solid sodium hydroxide or concentrated sulfuric acid) to remove traces of water from the organic solvent, and some solvents (e.g., benzene) have been dehydrated in an azeotropic form. However, these methods are only suitable for removing a trace amount of water from a high-concentration organic solvent, or for recovering a solvent from a relatively single solution and containing a very small amount of water, and for recovering a dimethylethanolamine solvent from a mother liquor containing more than 10% of water in a hydrazinization reaction, these methods cannot be used.
For the recovery of dimethylethanolamine solvent from the mother liquor of the hydrazidation reaction, many attempts have been made for a long time by using various methods, but the results are not satisfactory. Dimethyl ethanolamine is recovered by chloroform solvent, NaOH is added to adjust the pH value, the production operation is not complicated, and the raw material cost is increased. Secondly, hydrazine hydrate in the hydrazine reaction mother liquor is dissolved in the trichloromethane, and the hydrazine hydrate is high in safety risk when the trichloromethane and the dimethylethanolamine are separated by high-temperature rectification, so that the hydrazine hydrate is not beneficial to safe production operation.
Disclosure of Invention
The invention aims to solve the technical problem of providing a method for recovering dimethylethanolamine from a hydrazine reaction solution aiming at the difficult problem of recovering dimethylethanolamine solvent from the existing hydrazine reaction mother solution.
The technical problem to be solved by the invention can be realized by the following technical scheme:
a method for recovering dimethylethanolamine from hydrazine reaction liquid is characterized in that benzene is added into the hydrazine reaction liquid to extract dimethylethanolamine, then the benzene and dimethylethanolamine are separated by adopting a method of combining distillation and rectification, and the dimethylethanolamine with high purity is recovered.
The method comprises the following specific steps: adding an extractant benzene into the hydrazine reaction solution, heating to 55-65 ℃, stirring, preserving heat for 0.5 hour, standing and then splitting phases; distilling the upper organic phase; the organic phase is distilled under normal pressure to 125-130 ℃; rectifying the collected fraction, and collecting the fraction at 130-134 ℃, namely the dimethylethanolamine solvent.
In a preferred embodiment of the invention, the mass ratio of the hydrazine reaction liquid to the extracting agent is 1: 0.8.
In a preferred embodiment of the invention, the resting time is more than 0.5 hour.
The invention adopts benzene extraction, simple distillation and rectification to effectively recover the dimethylethanolamine in the hydrazine reaction mother liquor, and has low energy consumption in the recovery process, high purity of the recovered dimethylethanolamine and no influence on the hydrazine synthesis reaction due to repeated use. The invention has unique advantages, which are mainly embodied as follows: firstly, hydrazine hydrate is insoluble in benzene, and almost no hydrazine hydrate is contained in the extracted benzene solution, so that the risk of rectifying hydrazine hydrate at high temperature does not exist; secondly, NaOH is not needed to adjust the pH value in the benzene extraction, so that the complexity of the operation process is reduced, and the effect of saving raw materials is achieved; thirdly, the dimethylethanolamine extracted from the benzene contains no water-soluble impurities basically, and the dimethylethanolamine obtained after rectification has higher purity and is more favorable for being repeatedly used in hydrazine synthesis reaction; and fourthly, benzene is used as a solvent to be easier to separate in the extraction process. In a word, the production operation is safe, the purity of the recovered dimethylethanolamine is high, and the operation is simple.
For example: the composition of a certain hydrazidation reaction mother liquor is as follows: 42% of dimethylethanolamine; 5% of hydrazine hydrate; dimethylethanolamine hydrochloride 30%; water content is 13 percent; other impurities 10%;
adding an extractant benzene into the mother liquor according to the mass ratio of 1:0.8, heating to 55-65 ℃, stirring, keeping the temperature for about 0.5 hour, standing for about 0.5 hour, and then carrying out phase separation; distilling the upper organic phase; the organic phase is simply distilled to 125-130 ℃ under normal pressure; the collected fraction is rectified again, the fraction at the temperature of 130-134 ℃ is collected, and finally 0.4 ton of dimethylethanolamine solvent can be recovered in each ton of mother liquor.
The content of the recovered dimethylethanolamine is more than 98 percent, the benzene residue is less than 0.8 percent, and the water content is less than 0.5 percent; the remainder being the product of the hydrazinization reaction.
Detailed Description
Example 1
2310Kg of benzene is added into a hydrazine reaction mother liquor, and extraction is carried out twice under the condition of heating to 55.6-57.8 ℃ to obtain an extraction liquid. The extract liquid is simply distilled at the temperature of 128-130 ℃, the fraction at the temperature of 132.2-133.4 ℃ is collected, and then the collected fraction is rectified, and 940Kg of recovered solvent is finally obtained. The quality index of benzene is 0.72 percent; 98.54 percent of dimethylethanolamine; 0.4 percent of water.
Example 2
Adding 1800Kg of benzene into 2300Kg of hydrazine reaction mother liquor, and extracting twice under the condition of heating to 55.5-58.1 ℃ to obtain extract liquor. The extract liquid is simply distilled at the temperature of 128-130 ℃, collected at the temperature of 132.0-133.5 ℃, and then the collected fraction is rectified to finally obtain 920Kg of recovered solvent. The quality index of benzene is 0.72 percent; 98.54 percent of dimethylethanolamine; 0.5 percent of water.
Example 3
2320Kg of benzene is added into a certain hydrazinization reaction mother liquor, and the mixture is extracted twice under the condition of heating to 55.4-57.9 ℃ to obtain extract liquor. The extraction liquid is simply distilled, the fraction is collected at the temperature of 128-130 ℃, then the distillation is carried out, and finally the fraction at the temperature of 132.1-133.5 ℃ is collected to obtain 940Kg of recovered dimethylethanolamine solvent, the quality index of which is 0.668 percent of benzene; 98.82% of dimethylethanolamine; 0.3 percent of water.

Claims (3)

1. A method for recovering dimethylethanolamine from a hydrazine reaction solution is characterized in that benzene is added into the hydrazine reaction solution to extract dimethylethanolamine, then the benzene and the dimethylethanolamine are separated by adopting a method of combining distillation and rectification, and the dimethylethanolamine with high purity is recovered;
the method comprises the following specific steps: adding an extractant benzene into the hydrazine reaction solution, heating to 55-65 ℃, stirring, preserving heat for 0.5 hour, standing and then splitting phases; distilling the upper organic phase; the organic phase is distilled under normal pressure to 125-130 ℃; rectifying the collected fraction, and collecting the fraction at 130-134 ℃, namely the dimethylethanolamine solvent.
2. The method for recovering dimethylethanolamine from a hydrazinization reaction solution according to claim 1, wherein the mass ratio of the hydrazinization reaction solution to the extracting agent is 1: 0.8.
3. The method for recovering dimethylethanolamine from a hydrazinization reaction solution according to claim 1, wherein the standing time is more than 0.5 hour.
CN201711354893.XA 2017-12-15 2017-12-15 Method for recovering dimethylethanolamine from hydrazine reaction solution Active CN108017551B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711354893.XA CN108017551B (en) 2017-12-15 2017-12-15 Method for recovering dimethylethanolamine from hydrazine reaction solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711354893.XA CN108017551B (en) 2017-12-15 2017-12-15 Method for recovering dimethylethanolamine from hydrazine reaction solution

Publications (2)

Publication Number Publication Date
CN108017551A CN108017551A (en) 2018-05-11
CN108017551B true CN108017551B (en) 2020-06-05

Family

ID=62073742

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711354893.XA Active CN108017551B (en) 2017-12-15 2017-12-15 Method for recovering dimethylethanolamine from hydrazine reaction solution

Country Status (1)

Country Link
CN (1) CN108017551B (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101648880A (en) * 2009-08-27 2010-02-17 王宇平 Preparation method of N, N-dimethylethanolamine

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101648880A (en) * 2009-08-27 2010-02-17 王宇平 Preparation method of N, N-dimethylethanolamine

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
二烷基乙醇胺的应用及合成工艺研究进展;王磊等;《安徽科技学院学报》;20170915;第31卷(第5期);88-94 *
水合肼的生产技术及其应用进展;张杰等;《化工中间体》;20061231(第3期);8-12 *

Also Published As

Publication number Publication date
CN108017551A (en) 2018-05-11

Similar Documents

Publication Publication Date Title
CN106674292B (en) A kind of purification processing method of Sucralose water crystallization mother liquor
CN109956983B (en) Method for extracting sucralose-6-ethyl ester
CN103242384B (en) Mother liquor of sucralose extraction process
CN108659061B (en) Purification treatment method of sucralose crystallization mother liquor
CA2043152C (en) Production of citric acid
NO761411L (en)
CN106167458B (en) The method that thioacetic acid is detached from thioacetic acid aqueous solution
CN104130105B (en) The method that in D-4-methylsulfonylphserine serine ethyl ester production, ethanol is recycled
CN106957345B (en) Improve the production method of trichloro-cane-6-ethyl ester yield
CN102050764B (en) Method for purifying sodium hydroxyethyl sulphonate
CN108017551B (en) Method for recovering dimethylethanolamine from hydrazine reaction solution
CN105779123B (en) Cleaning process for decomposing urea-saturated fatty acid methyl ester inclusion compound by choline chloride method
CN107937009B (en) Method for separating phenolic compounds from coal tar and direct coal liquefaction product
CN108609661B (en) Method for preparing iron oxide red, aluminum oxide and gallium by using iron-removing resin eluent
CN102382044A (en) Purification method for 2,3-dimethylpyridine
CN113366006B (en) Method for purifying sucralose-6-ethyl ester
CN104447529B (en) Method for extracting and purifying 3,6-matrigon
CN102382045A (en) Purification of 2,3-dimethyl pyridine
CN113527214A (en) Method for preparing 4, 6-dihydroxypyrimidine
CN102952074A (en) Method of recycling dextromethorphan from crystallization mother liquor
CN102249889B (en) Method for extracting succinic acid from citric acid mother solution
CN101906044B (en) Synthesizing 2,5-dichloronitrobenzene by using santochlor extracted from solid waste chlorobenzene tar
CN105440053B (en) A kind of recovery method of GCLE crystalline mother solutions
CN220656435U (en) Device for recycling pyridine or pyridine derivative in hexachlorocyclo-triphosphazene synthetic waste residues
CN211199070U (en) A recovery unit that is arranged in synthetic acetone waste liquid of cephalosporin

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
GR01 Patent grant
GR01 Patent grant