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Method for preparing polyacrylate-2-acrylamide-2-methyl propane sulfonic acid

A technology of methylpropanesulfonic acid and acrylamide, which is applied in the field of preparation of organic polymers, can solve problems such as long reaction time, harsh reaction conditions, and slow reaction rate, and achieve high equipment utilization efficiency, fast polymerization reaction speed, and improved Effects on Calcium Tolerance

Inactive Publication Date: 2010-06-30
娄底市裕德科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Domestic patent document CN1654369A discloses a method for preparing water scale inhibitors using acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid, etc. as monomers, but this initiation system needs to generate free radicals to initiate polymerization at a higher temperature , the reaction rate is relatively slow
Domestic patent document CN1235818C discloses ternary copolymerization with 2-acrylamide-2-methylpropanesulfonic acid as comonomer, but the initial temperature of the polymerization reaction is high, consumes energy, and needs to add initiator while reacting And monomer, complex process, long reaction time, low equipment efficiency
Existing method for preparing the binary or multiple low molecular weight copolymers of acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid mainly includes following several kinds: adopt isopropanol as molecular weight regulator (for example U.S. Patent US4301266,1981, BASF A.-G.Muenster, A.and Rohmann, M), this method needs high temperature (greater than 120 ℃) ​​high pressure in the reaction process, the reaction condition is harsh, and needs to distill out excess isopropanol in the later operation, this process Energy-consuming and cumbersome procedures; using metal salts (such as Cu 2+ ) as an initiating system (such as U.S. Patent US4314044, 1982, Rohm and Haas Co, Hughes, K.A, Kine, B.B. and Swift, G.), the reaction conditions of this process also need to meet higher temperature (greater than 90 ° C), and need It is completed in the case of continuous feeding, which consumes energy and is cumbersome, while Cu 2+ easy to cause environmental pollution

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] In the reactor, add water 65kg, start agitator, then add successively the ethanolic solution of sodium sulfite 2.5kg, L-ascorbic acid 0.055kg, dodecanethiol (wherein dodecanethiol 0.55kg, ethanol 1.1kg), acrylic acid 30kg, 1.2kg of 2-acrylamide-2-methylpropanesulfonic acid and 0.6kg of ammonium persulfate; start the polymerization reaction when the initial temperature reaches 35°C, and obtain polyacrylic acid-2-acrylamide-2- Methylpropanesulfonic acid, its viscosity average molecular weight is slightly less than 50000, and the conversion rate reaches 96%.

Embodiment 2

[0023] In the reactor, add water 60kg, start agitator, then add successively the ethanolic solution of sodium sulfite 3.0kg, L-ascorbic acid 2kg, acrylic acid 30kg, dodecanethiol (wherein dodecanethiol 2.8kg, ethanol 5kg), 2- Acrylamide-2-methylpropanesulfonic acid 5kg, potassium persulfate 2kg; start the polymerization reaction when the initial temperature reaches 45°C, and obtain polyacrylic acid-2-acrylamide-2-methylpropane after two hours of reaction Sulfonic acid, its viscosity average molecular weight is about 1200, and the conversion rate reaches 96%.

Embodiment 3

[0025] In the reactor, add water 50kg, start agitator, then add successively the ethanolic solution of sodium sulfite 0.2kg, L-ascorbic acid 0.5kg, dodecanethiol (wherein dodecanethiol 1.2kg, ethanol 3.5kg), acrylic acid 25kg, 2-acrylamide-2-methylpropanesulfonic acid 10kg, ammonium persulfate 1.2kg; start the polymerization reaction when the initial temperature reaches 50 ° C, and obtain polyacrylic acid-2-acrylamide-2- Methylpropanesulfonic acid, its viscosity average molecular weight is about 10,000, and the conversion rate reaches 96%.

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Abstract

The invention discloses a method for preparing polyacrylic acid-2-acrylamide-2-methyl propanesulfonic acid. The method mainly comprises the following steps: 5 to 30 mass percent of crylic acid, 1 to 15 mass percent of 2-acrylamide-2-methyl propanesulfonic acid, 0.5 to 6 mass percent of persulfate, 0.2 to 3 mass percent of sodium sulfite, 0.05 to 3 mass percent of L-ascorbic acid, 0.5 to 9 mass percent of ethanol, 0.5 to 3 mass percent of dodecyl mercaptan and 50 to 85 mass percent of water are mixed to have polymerization reaction for not less than one hour at a temperature of between 35 and60 DEG C to obtain the polyacrylic acid-2-acrylamide-2-methyl propanesulfonic acid. The method has the advantages the polyacrylic acid-2-acrylamide-2-methyl propanesulfonic acid with low molecular weight is synthesized once, has low starting reaction temperature, less energy consumption, rapid reaction speed, high utilization efficiency of equipment, a simple process and convenient operation.

Description

technical field [0001] The invention relates to a preparation method of an organic polymer, in particular to a method for preparing an organic polymer by using carbon-carbon unsaturated bonds and inorganic ingredients as raw materials. Background technique [0002] At present, domestic related literatures have reported the method of compound production of scale inhibitor, scale remover or corrosion inhibitor by using low molecular weight polyacrylic acid-2-acrylamide-2-methylpropanesulfonic acid as one of the components, but no The invention relates to a preparation method of low-molecular-weight polyacrylic acid-2-acrylamide-2-methylpropanesulfonic acid initiated at low temperature and fed at one time. The preparation methods that have been used in the prior art mostly carry out polymerization at a relatively high initial temperature, and generally adopt the method of feeding multiple times or gradually adding monomers and initiators when carrying out the polymerization to ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F220/06C08F4/40C08F2/38C08F220/58
Inventor 王韬
Owner 娄底市裕德科技有限公司
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