CN105669948A - Energy-saving production process of epicholorohydrin-dimethylamine polymer - Google Patents
Energy-saving production process of epicholorohydrin-dimethylamine polymer Download PDFInfo
- 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
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- 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
Links
- 238000004519 manufacturing process Methods 0.000 title abstract description 9
- 229920000642 polymer Polymers 0.000 title abstract description 5
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000006243 chemical reaction Methods 0.000 claims abstract description 27
- 238000001816 cooling Methods 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims abstract description 6
- LRWZZZWJMFNZIK-UHFFFAOYSA-N 2-chloro-3-methyloxirane Chemical compound CC1OC1Cl LRWZZZWJMFNZIK-UHFFFAOYSA-N 0.000 claims description 32
- 238000000034 method Methods 0.000 claims description 17
- 229920001577 copolymer Polymers 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 239000002994 raw material Substances 0.000 claims description 7
- 239000002826 coolant Substances 0.000 claims description 6
- 238000009413 insulation Methods 0.000 claims description 4
- 239000002918 waste heat Substances 0.000 abstract 2
- 239000007864 aqueous solution Substances 0.000 abstract 1
- 238000004321 preservation Methods 0.000 abstract 1
- 230000035484 reaction time Effects 0.000 abstract 1
- 238000003786 synthesis reaction Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920000867 polyelectrolyte Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G59/00—Polycondensates 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
- C08G59/02—Polycondensates containing more than one epoxy group per molecule
- C08G59/10—Polycondensates containing more than one epoxy group per molecule of polyamines with epihalohydrins or precursors thereof
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- 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
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.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201610015954.9A CN105669948A (en) | 2016-01-12 | 2016-01-12 | Energy-saving production process of epicholorohydrin-dimethylamine polymer |
Applications Claiming Priority (1)
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---|---|---|---|
CN201610015954.9A CN105669948A (en) | 2016-01-12 | 2016-01-12 | Energy-saving production process of epicholorohydrin-dimethylamine polymer |
Publications (1)
Publication Number | Publication Date |
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CN105669948A true CN105669948A (en) | 2016-06-15 |
Family
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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 |
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CN (1) | CN105669948A (en) |
Citations (2)
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 |
-
2016
- 2016-01-12 CN CN201610015954.9A patent/CN105669948A/en active Pending
Patent Citations (2)
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)
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》 * |
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Application publication date: 20160615 |