Polymers of olefinically unsaturated monomers and solutions of these polymers

• US 5,298,554 A
• Filed: 06/26/1991
• Issued: 03/29/1994
• Est. Priority Date: 06/29/1990
• Status: Expired due to Term

• Current Assignee: BASF AG (BASF SE)
• Original Assignee: BASF AG (BASF SE)
• Inventors: Auchter, Gerhard, Rehmer, Gerd, Barwich, Juergen
• Primary Examiner(s): Schofer, Joseph L.
• Assistant Examiner(s): Weber, Tom
• Application Number:
  US07/721,836
• Time in Patent Office: 1,007 Days
• Field of Search: 526/317.1, 526/88, 524/725, 524/751, 524/765, 524/770, 524/773
• US Class Current: 524/725
• CPC Class Codes: C08F 2/06 Organic solvent

Abstract

Abstract of the Disclosure: Polymers of olefinically unsaturated monomers and solutions of these polymers are obtainable by a process in which the olefinically unsaturated monomers are polymerized in the presence of a free radical initiator in solution under polymerization conditions which are otherwise predetermined, in such a way that the solvent and/or a liquid part of one or more reactants of the polymerization batch are initially taken and heated to the polymerization temperature, and some or the total amount of the monomers to be polymerized is fed continuously to the agitated initially taken part of the polymerization batch via one or more feeds, with maintenance or initiation of the polymerization, in such a way that the outlet orifice of the one or more feeds is located below the surface of the initially taken liquid part of the polymerization batch.

Claims

1. A process for preparing a polymer of olefinically unsaturated monomers or a solution of the polymer consisting essentially of:

separately taking at least a portion of solvent;

or at least a portion of solvent and at least a portion of at least one olefinically unsaturated monomer selected from the group consisting of unsaturated esters of 3 to 24 carbon atoms of monoolefinically unsaturated carboxylic acids, α

,β

-monoolefinically unsaturated C_3-6 mono- or dicarboxylic acids, acrylamide, methacrylamide, tetrahydrofururylacrylamide, tetrahydrofurfurylmethacrylamide, diacetoneacrylamide, hydroxyalkyl(meth)acrylates, 2-ketobutyl(meth)acrylamide, N-vinylformamide, N-vinylpyrrolidone, 2-methylene-1,3-dioxepan, 2-methylene-1,3-dioxolane, N-methyl-2-methyleneoxazolidine, 2-methylene-1,3-thiolene, (meth)acrolein, acetoacetoxyethyl acrylate, ethylene, propylene, isobutylene, butadiene, isoprene, vinyl methyl ether, vinyl isobutyl ether, vinylpyridine, β

-aminoethyl vinyl ether, aminopentyl vinyl ether, tert-butylaminoethyl methacrylate, a vinylaromatic vinylcaprolactam, tetrahydrofurfur-2-yl(meth)acrylate, vinyl esters of C_1-18 alkanecarboxylic acids and monoethylenically unsaturated acetophenone or benzophenone derivatives to be solution polymerized; and

optionally at least a portion of the polymerization initiator employed in the polymerization reaction, and placing the taken liquid material in a polymerization vessel;

heating the liquid components of the solution polymerization medium in the vessel to a predetermined polymerization temperature; and

continuously feeding any remaining solvent, a portion or all of the monomer and any radical initiator via one or more feedlines to said polymerization vessel in such a way that the orifice outlets of the feedlines are below the surface of agitated liquid polymerization medium which is agitated by an anchor stirrer, bar-stirrer, paddle stirrer, finger stirrer, grid stirrer, gyratory stirrer, crossbeam stirrer, scoop stirrer, propeller stirrer or impeller stirrer in the vessel and polymerizing the at least one monomer under said predetermined conditions in said polymerization medium.

2. The process of claim 1, wherein the initiators to be added to the polymerization medium in the polymerization vessel are introduced through outlet orifice(s) of one or more initiator feedlines located below the surface of the polymerization medium.

3. The process of claim 1, wherein the polymerization reaction is conducted at a temperature of from 20°

to 150°

C. at a pressure ranging from 0.1 to 100 bar.

4. The process of claim 1, wherein the amount of solvent employed ranges from 1 to 200% by weight based on the total amount of monomer polymerized.

5. The process of claim 1, wherein the amount of initiator employed ranges from 0.1 to 10% by weight based on the weight of monomer.

6. The process of claim 1, wherein said solvent is an alcohol, ketone, nitrile, tetrahydrofuran, ethyl acetate or mixtures thereof.

7. The process of claim 1, wherein said initiator is an azo or peroxide initiator.