Process for the polymerization of formaldehyde

• US 3,979,480 A
• Filed: 12/16/1974
• Issued: 09/07/1976
• Est. Priority Date: 12/28/1973
• Status: Expired due to Term

• Current Assignee: Societa Italiana Pentole SpA
• Original Assignee: Societa Italiana Pentole SpA
• Inventors: Colombo, Paolo, Colombo, Daniele, Radici, Pierino
• Primary Examiner(s): Tillman, Murray
• Assistant Examiner(s): Danison, Jr., W. C.
• Application Number:
  US05/533,268
• Time in Patent Office: 631 Days
• Field of Search: 260/857 F
• US Class Current: 528/243
• CPC Class Codes: C08G 2/06 Catalysts Catalysts in general B01J
• CPC Class Codes: C08G 2/08 Polymerisation of formaldehyde

Abstract

Polyformaldehyde is prepared by feeding anhydrous formaldehyde to a reaction medium containing a liquid organic diluent non-solvent for the polyformaldehyde and non-reactive towards the other constituents of the reaction medium, and containing in a dispersed form a copolymer A-B, wherein

A is a polylactonic block of recurring units ##EQU1## B is a polylactamic block of recurring units ##EQU2## wherein PM₁ and PM₂ are linear polymethylene chains having from 2 to 13 and 3 to 13 carbon atoms, respectively.

Claims

1. A method for preparing a polyoxymethylene, comprising the step of supplying anhydrous monomeric formaldehyde to a reaction medium comprising an organic diluent which is a liquid and non-solvent for the polyoxymethylene under the reaction conditions and inert towards the other constituents of the reaction medium, and comprising from 0.001 to 0.5 percent by weight of a catalyst based upon the polyoxymethylene, dispersed in said medium, said catalyst having a molecular weight of from 1,000 to 50,000, containing block A in a proportion of from 1 to 89 weight percent, and consisting of a block copolymer carrying ionic couples on its macromolecular chain, said block copolymer being defined by the general structure A-B in which:

A is a polylactonic block consisting of recurring units;

##EQU5## obtainable from at least one monomeric lactone of the general formula;

##EQU6## B is a polylactam block consisting of recurring units;

##EQU7## obtainable from at least one monomeric lactam of the general formula;

##EQU8## wherein PM₁ and PM₂ are polymethylene chains having from 2 to 13 and 3 to 13 carbon atoms, respctively, non-substituted or having at least one hydrogen atom replaced by a radical selected from the group consisting of alkyl, aryl, alkylaryl and cycloalkyl radicals.

2. The method of claim 1, wherein the said lactone is selected from the group consisting of ε

-caprolactone, δ

-valerolactone, β

-propiolactone, pivalolactone and ω

-enanthiolactone.

3. The method of claim 1, wherein the said lactam is selected from the group consisting of ε

-caprolactam, α

-pyrrolidone, ω

-lauryllactam, α

-piperidone and ω

-enanthiolactam.

4. The method of claim 1, wherein the diluent is selected from the group consisting of ethers, hydrocarbons and chlorinated hydrocarbons.

5. The method of claim 1, wherein the reaction temperature is from -120°

up to the temperature of ebullition of the diluent, said diluent having a temperature of ebullition not exceeding 110°

C.

6. The method of claim 1, wherein the reaction temperature is from -30°

to 70°

C.

7. The method of claim 1, wherein the block copolymer A-B is obtained by catalytic copolymerization of said lactamic and lactonic monomers at a temperature of from -20°

C to 300°

C and during a period of from 2 min to 6 hours, the catalyst employed being in a proportion of from 0.1 to 10 moles for 100 moles lactonic and lactamic monomers and being defined by the general formula;

##STR6## wherein Me is selected from the group consisting of the alkali and alkaline earth metals, Z is 1 or 2 and PM₂ is the said polymethylene chain.

8. The method of claim 6, wherein the block copolymer A-B is obtained by copolymerizing said monomers in a solvent for the forming copolymer A-B.

9. The method of claim 6, wherein the block copolymer A-B is obtained by copolymerizing said monomers in a diluent non-solvent for the forming copolymer A-B.

10. The method of claim 1, wherein the said dispersed catalyst is in the form of particles 1 to 300 microns in size.

11. The method of claim 10, wherein said particles are 1 to 100 microns in size.