[go: up one dir, main page]

CN105669948A - Energy-saving production process of epicholorohydrin-dimethylamine polymer - Google Patents

Energy-saving production process of epicholorohydrin-dimethylamine polymer Download PDF

Info

Publication number
CN105669948A
CN105669948A CN201610015954.9A CN201610015954A CN105669948A CN 105669948 A CN105669948 A CN 105669948A CN 201610015954 A CN201610015954 A CN 201610015954A CN 105669948 A CN105669948 A CN 105669948A
Authority
CN
China
Prior art keywords
epoxychloropropane
reaction
dimethylamine
energy
epicholorohydrin
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
CN201610015954.9A
Other languages
Chinese (zh)
Inventor
李绍通
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.)
Luoyang Hemeng Technology Co Ltd
Original Assignee
Luoyang Hemeng Technology 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 Luoyang Hemeng Technology Co Ltd filed Critical Luoyang Hemeng Technology Co Ltd
Priority to CN201610015954.9A priority Critical patent/CN105669948A/en
Publication of CN105669948A publication Critical patent/CN105669948A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/02Polycondensates containing more than one epoxy group per molecule
    • C08G59/10Polycondensates containing more than one epoxy group per molecule of polyamines with epihalohydrins or precursors thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Epoxy Resins (AREA)

Abstract

The invention relates to an energy-saving production process of an epicholorohydrin-dimethylamine polymer. The energy-saving production process of the epicholorohydrin-dimethylamine polymer includes: in an airtight stirring reactor, conducting negative pressure feeding on a dimethylamine aqueous solution, and performing low temperature cooling charging on epicholorohydrin; and at the later stage of reaction, using reaction waste heat to perform heat preservation so as to complete the reaction. The energy-saving production process of the epicholorohydrin-dimethylamine polymer provided by the invention optimizes production steps, solves the production hidden dangers, utilizes reaction waste heat to complete synthesis reaction, reduces reaction time, and saves energy.

Description

Epoxychloropropane dimethylamine copolymer energy-saving processing technique
Technical field
The present invention relates to epoxychloropropane dimethylamine copolymer energy-saving processing technique, belong to chemical technology field.
Background technology
Epoxychloropropane dimethylamine copolymer is white to light tan solid, has high-hygroscopicity. Endothermic transition point 32-39 DEG C, heat decomposition temperature 200 DEG C, for important strong cationic polyelectrolytes, linear homopolymer, good water solubility, can mix with arbitrary proportion with water, nonpoisonous and tasteless, stable in properties, pH value is insensitive, there is anti-chlorine Degradation. Additionally, also have the characteristic such as high temperature high voltage resistant and resistance to high speed shear.
US3738945 manufacture method: with dimethylamine and epoxychloropropane for raw material, polymerisation in solution is carried out for solvent with water, its reaction is as follows: equipped with condenser, mechanical agitator, thermometer, in the flask of charging hopper and pH electrode, add 92.5g epoxychloropropane, in charging hopper, add 112.5g dimethylamine agueous solution (40%) simultaneously, start stirring and the time more than 1 hour of the dimethylamine agueous solution in funnel is slowly added in epoxychloropropane, temperature maintains 20 ~ 30 DEG C, then, it is warming up to 50 DEG C, reaction 6h, can obtain including the clear solution of 67% polymer solids.
Though above-mentioned technique is Laboratory Production technique, but commercial production is generally along using this technology, there is the leakage of dimethylamine agueous solution adition process, there is security hidden trouble, and wastes the energy.
Summary of the invention
It is desirable to provide epoxychloropropane dimethylamine copolymer energy-saving processing technique, the method can solve traditional handicraft and there is security hidden trouble, waste energy problem.
Technical scheme is as follows:
1. epoxychloropropane dimethylamine copolymer energy-saving processing technique, it is characterised in that: dimethylamine agueous solution negative pressure charging adds in airtight stirred reactor; Epoxychloropropane feeds in raw material in low-temperature cooling media cool cycles; Epoxychloropropane feeds in raw material the later stage, stops circulating water; Reaction later-stage utilization residual heat of reaction has been incubated reaction.
2. epoxychloropropane dimethylamine copolymer energy-saving processing technique according to claim 1, it is characterised in that: dimethylamine agueous solution negative pressure charging is at gauge pressure about-0.09MPa, is all sucked in airtight stirred reactor by raw material dimethylamine agueous solution.
3. epoxychloropropane dimethylamine copolymer energy-saving processing technique according to claim 1, it is characterized in that: it is that temperature of charge is slowly added in the reactor of stirring when opening lower than the cooling medium circulation system of 45 DEG C, stirred reactor in stirred reactor that epoxychloropropane adds, and carries out copolyreaction with dimethylamine agueous solution.
4. epoxychloropropane dimethylamine copolymer energy-saving processing technique according to claim 1, it is characterised in that: when the addition of epoxychloropropane completes about 80%, close the cooling medium circulation system of stirred reactor and discharge cooling medium in cooler; Then the addition speed improving epoxychloropropane makes reaction temperature be gradually increasing, until epoxychloropropane all adds fashionable reaction temperature at 60-80 DEG C, utilizes residual heat insulation stirring reaction 3-6 hour.
The method have the benefit that
1. in airtight stirred reactor, the charging of dimethylamine agueous solution negative pressure avoids dimethylamine leakage, it is prevented that the dimethylamine leakage harm to operator's health;
2. utilize residual heat of reaction to carry out insulation reaction, eliminate reaction later stage heating step, utilize residual heat of reaction to complete synthetic reaction, decrease the response time, saved the energy.
Detailed description of the invention
Embodiment
In the rustless steel stirred autoclave of 2000L jacketed and interior cooling coil, utilize water ring vacuum pump that reacting kettle inner pressure is evacuated to-0.09MPa, close vacuum pump; Then vacuum state sucks 40% dimethylamine agueous solution 584 kilograms; Opening reacting kettle jacketing and the recirculated water of interior cooling coil, start reactor agitator, be slowly added to the epoxychloropropane of gross weight 480 kilograms with dosing pump, in control reactor, temperature of charge is lower than 45 DEG C; When epoxychloropropane adds about 80%, close the cooling circulating water of reactor and discharge cooler internal recycle water, then improving epoxychloropropane addition and add speed, making reaction temperature be gradually increasing, after making epoxychloropropane all add, reaction temperature is maintained at 65-70 DEG C; Finally, utilize residual heat of reaction insulation reaction 4 hours, obtain the epoxychloropropane dimethylamine copolymer solution that 1060 kilograms of solid contents are 68%.

Claims (4)

1. epoxychloropropane dimethylamine copolymer energy-saving processing technique, it is characterised in that: dimethylamine agueous solution negative pressure charging adds in airtight stirred reactor; Epoxychloropropane feeds in raw material in low-temperature cooling media cool cycles; Epoxychloropropane feeds in raw material the later stage, stops circulating water; Reaction later-stage utilization residual heat of reaction has been incubated reaction.
2. epoxychloropropane dimethylamine copolymer energy-saving processing technique according to claim 1, it is characterised in that: dimethylamine agueous solution negative pressure charging is at gauge pressure about-0.09MPa, is all sucked in airtight stirred reactor by raw material dimethylamine agueous solution.
3. epoxychloropropane dimethylamine copolymer energy-saving processing technique according to claim 1, it is characterized in that: it is that temperature of charge is slowly added in the reactor of stirring when opening lower than the cooling medium circulation system of 45 DEG C, stirred reactor in stirred reactor that epoxychloropropane adds, and carries out copolyreaction with dimethylamine agueous solution.
4. epoxychloropropane dimethylamine copolymer energy-saving processing technique according to claim 1, it is characterised in that: when the addition of epoxychloropropane completes about 80%, close the cooling medium circulation system of stirred reactor and discharge cooling medium in cooler; Then the addition speed improving epoxychloropropane makes reaction temperature be gradually increasing, until epoxychloropropane all adds fashionable reaction temperature at 60-80 DEG C, utilizes residual heat insulation stirring reaction 3-6 hour.
CN201610015954.9A 2016-01-12 2016-01-12 Energy-saving production process of epicholorohydrin-dimethylamine polymer Pending CN105669948A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610015954.9A CN105669948A (en) 2016-01-12 2016-01-12 Energy-saving production process of epicholorohydrin-dimethylamine polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610015954.9A CN105669948A (en) 2016-01-12 2016-01-12 Energy-saving production process of epicholorohydrin-dimethylamine polymer

Publications (1)

Publication Number Publication Date
CN105669948A true CN105669948A (en) 2016-06-15

Family

ID=56299927

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610015954.9A Pending CN105669948A (en) 2016-01-12 2016-01-12 Energy-saving production process of epicholorohydrin-dimethylamine polymer

Country Status (1)

Country Link
CN (1) CN105669948A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3738945A (en) * 1972-02-04 1973-06-12 H Panzer Polyquaternary flocculants
CN204116935U (en) * 2014-10-22 2015-01-21 江苏富淼科技股份有限公司 A kind of automatic control system of producing for poly-Hydroxypropyldimonium Chloride

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3738945A (en) * 1972-02-04 1973-06-12 H Panzer Polyquaternary flocculants
CN204116935U (en) * 2014-10-22 2015-01-21 江苏富淼科技股份有限公司 A kind of automatic control system of producing for poly-Hydroxypropyldimonium Chloride

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
于国彬: ""粘土稳定剂环氧氯丙烷——二甲胺共聚物合成的研究"", 《化学工程与装备》 *

Similar Documents

Publication Publication Date Title
CN102086271B (en) Preparation method of high-transparent high heat resistance liquid calcium-zinc heat stabilizer
CN104829838B (en) A kind of preparation method of hydroxy-end capped poly- fluorosilicone
CN105585704A (en) Bio-polyether ester elastomer and preparation method therefor
CN103933880A (en) Preparation method of high-throughput hydrophilic modified polypropylene hollow fiber membrane
CN102659878A (en) Method for synthesizing tilmicosin and tilmicosin phosphate through using tylosin broth
CN105175732A (en) A kind of silicon boron polymer and its preparation method and application
CN102604347A (en) Preparation method of chitosan modified polylactic acid material by gamma-ray irradiation
CN104211657A (en) Refining method of rubber vulcanizing accelerant M
CN105669948A (en) Energy-saving production process of epicholorohydrin-dimethylamine polymer
CN104500874A (en) Steel belt and reinforced polyvinyl chloride helical bellow and production method thereof
CN105837615B (en) A kind of low pressure, two-component solvent, dual catalyst synthesizing silane coupler Si-75 method
CN109503840A (en) Full-automatic continuous production line for 107 silicone rubber
CN104726168A (en) Lithium-zinc compound lubricant and preparation method thereof
CN106831537A (en) Permanent violet RL intermediate condensate synthesis techniques
CN103467682B (en) Process for circularly producing thermoplastic barium sulfate phenolic resin by precipitation method
CN109251251B (en) A kind of processing method of composite modified starch-based degradable material
CN107793378A (en) A kind of novel method for synthesizing of glycerin triglycidyl ether
CN104710613B (en) Solvothermal preparation method of semi-aromatic polyamide
CN105801728B (en) Molten terminator of polyvinyl chloride resin oil and preparation method thereof
CN107903221B (en) Preparation method of TBSI
CN110089783A (en) Silicone bra cup and its production technology
CN112679638A (en) Hydrosolvent polyacrylic resin and preparation method thereof
CN112391038A (en) Anti-static solid tire
CN109776867A (en) A kind of biopack
CN105237768A (en) Continuous silicon oil production line

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20160615