US2451743A

US2451743A - Powdered polythene

Info

Publication number: US2451743A
Application number: US547645A
Authority: US
Inventors: Jarrett Kenneth Barry
Original assignee: Imperial Chemical Industries Ltd
Current assignee: Imperial Chemical Industries Ltd
Priority date: 1943-09-17
Filing date: 1944-08-01
Publication date: 1948-10-19
Anticipated expiration: 1965-10-19

Description

Patented Oct. 19, 1948 POWDERED POLYTHENE I Kenneth Barry Jarrett, Welwyn Garden City, England, assignor to Imperial Chemical Industries Limited, a corporation of Great Britain No Drawing. Application August 1, 1944, Serial This invention relates to a new and improved process for the production of polythene powder. In particular, it relates to the production of polythene powder suitable for use in conjunction with a flame-gun for coating surfaces with a covering of polythene. Throughout this specification the term polythene refers to polymers of ethylene which are solid at room temperature. The type of powder most suitable for spraying through a flame-gun consists of particles which are roughly spherical and which will pass through a 36 B. S. S. sieve and yet be retained on a 200 B. S. S. sieve. It should be appreciated. that these limits are by no means critical.

Owing to the tough and rubbery nature of polythene, it has not hitherto been possible to comminute it to a finely divided powder of this type by any of the conventional methods. For,

example, the product obtained by passing any commercial grade of polythene through aBridge Banbury mixer is fibrous in structure and consists essentially of long fibrous particles and is completely unsuitable for use in conjunction with a flame-gun.

According to the present invention we have now found that soft grades of polythene, as hereinafter defined, may be converted to a powdered state suitable for use in conjunction with a flamegun by a process which comprises the steps of treating the said polythene with a quantity of a lower aliphatic alcohol at least suflicient to cause it to become brittle, mechanically disintegrating it whilst avoiding any substantial evaporation of the alcohol and thereafter evaporaing off the alcohol.

By "treating the polythene with alcohol we mean covering the surface of the polythene with a layer of alcohol. For this reason it is preferred to use polythene in the form of flakes or chips, for example, polythene cut in a cutter. A sufficient amount of alcohol to cause all the'poly thene to become brittle is generally 7 /g of the weight of polythene; preferably at" least 10%- should be used in practice. If too small an amount of alcohol is used the yield of polythene which will pass a 36 mesh sieve after a given disintegrating treatment is low and the material produced has, an undesirably high surface area which results in the powder produced having a tendency to catch fire when passed through a flame gun. If it is attempted to work this process with other than soft grades of polythene, the

I yields and quality of powder produced deteriorates with increasing hardness of the polythene. On these considerations we limit the present inven- In Great Britain September 17,

6 Claims. (01. 260-94) vtion to the treatment of soft grades of polythene, i. e., to polythenes having a melt viscosity at 190 C. less than 6,700 poises.

Suitable machines for mechanically disintegrating the embrittled polythene are enclosed machines, for example, those sold under the trade name of Banbury mixers. Machines through which pass large volumes of air when they are in operation are not suitable for disintegrating the brittle polythene.

By lower aliphatic alcohol" as used in this specification we mean any aliphatic alcohol having less than 6 carbon atoms per molecule. The preferred alcohols are methanol and ethanol.

Our invention is illustrated but in no way limited by the following example in which all parts given are by weight.

Example 100 parts of polythene having a melt viscosity of 330 poises at 190 C. were mixed with 10 parts of methylated spirits and the mixture fed into a Bridge Banbury mixer" and mechanically disintegrated for 30 minutes. Cold water was circulated through the casing and rotor of the mixer .to prevent any appreciable rise of temperature in the polythene. The product was spread in layers A2" deep on stainless steel trays and the trays placed in an oven at 30 C. through which a rapid stream of air was circulated. After the powder had become dry it was sieved through a 36 B. S. S. sieve. Approximately 50% of the powder passed through the sieve and was found to be excellent for use in a flame-gun of the type described in British Patent Number 538,203.

The powder which did. not pass through the sieve was reprocessed as described above when a further 50% of the quantity reprocessed was produced in a form suitable for use with a flame- Having now particularly described and ascertained the nature of our said invention and in what manner the same is to be performed, we destate suitable for use in conjunction with a flame gun, which comprises the steps of covering the surface of the said polythene with an aliphatic monohydric alcohol having less than 6 carbon atoms per molecule and thereafter mechanically disintegrating the resultant mixture in an enclosed space and drying the resulting product, the amount of said alcohol being sufflcient to cause the said polythene to become brittle, said quantity being at least 7/z% of the weight of the said polythene.

3. A process whereby soft grades of polythene having a melt viscosity at 190 C. of less than 6,700 poises may be converted to a powdered state suitable for use in conjunction with a flame gun which comprises the steps of covering the surface of the said polythene in the form of flakes with an aliphatic monohydrlc alcohol having from 1 to 2 carbon atoms per molecule, inclusive, and thereafter mechanically disintegrating the resultant mixture in an enclosed space and drying the resulting product, the amount of the said alcohol being sufficient to cause the said polythene to become brittle, said quantity being at least '7 /2% of the weight of the said polythene.

4. A process whereby soft grades of polythene having a melt viscosity at 190 C. of less than 6,700 poises may be converted to a powdered state suitable for use in conjunction with a flame gun which comprises the steps of covering the sur face of the said polythene in the form of chips with an aliphatic monohydric alcohol having from 1 to 2 carbon atoms per molecule, inclusive, and thereafter mechanically disintegrating the resultant mixture in an enclosed space and drying the resulting product, the amount of the said alcohol being sufficient to cause the said polythene to become brittle, said quantity being at least 35% of the weight of the said polythene. 5. A process whereby soft grades of polythene having a melt viscosity at 190 C. of less than 6,700 poises may be converted to a powdered state suitable for use in conjunction with a flame gun which comprises wetting the surface of the said polythene with methanol and thereafter mechanically disintegrating the resultant mixture in an enclosed space and drying the resultin product, the amount of methanol being about 754% to 10% of the weight of the said polythene.

6. A process whereby soft grades of polythene,

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 2,188,465 Perrin Jan. 30, 1940 2,334,195 Hopfl Nov. 16, 1943 2,340,452 Child Feb. 1, 1943 OTHER. REFERENCES Swallow, Endeavor, vol. 3 (Jan., 1944). Pp. 26-31.