US2648593A - Removing salts from polyacrylonitrile - Google Patents

Removing salts from polyacrylonitrile Download PDF

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Publication number
US2648593A
US2648593A US319182A US31918252A US2648593A US 2648593 A US2648593 A US 2648593A US 319182 A US319182 A US 319182A US 31918252 A US31918252 A US 31918252A US 2648593 A US2648593 A US 2648593A
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United States
Prior art keywords
salt
per cent
fibers
article
salts
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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.)
Expired - Lifetime
Application number
US319182A
Inventor
George W Stanton
Theodore B Lefferdink
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dow Chemical Co
Original Assignee
Dow Chemical Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to US228759A priority Critical patent/US2648592A/en
Application filed by Dow Chemical Co filed Critical Dow Chemical Co
Priority to US319182A priority patent/US2648593A/en
Priority to FR1082729D priority patent/FR1082729A/en
Priority to DED15083A priority patent/DE1044346B/en
Priority to CH326492D priority patent/CH326492A/en
Priority to NL178428A priority patent/NL81838C/xx
Priority to GB15167/53A priority patent/GB732008A/en
Application granted granted Critical
Publication of US2648593A publication Critical patent/US2648593A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D05SEWING; EMBROIDERING; TUFTING
    • D05BSEWING
    • D05B1/00General types of sewing apparatus or machines without mechanism for lateral movement of the needle or the work or both
    • D05B1/08General types of sewing apparatus or machines without mechanism for lateral movement of the needle or the work or both for making multi-thread seams
    • D05B1/18Seams for protecting or securing edges
    • D05B1/20Overedge seams
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/02Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/18Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polymers of unsaturated nitriles, e.g. polyacrylonitrile, polyvinylidene cyanide
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/28Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/38Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds comprising unsaturated nitriles as the major constituent
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S424/00Drug, bio-affecting and body treating compositions
    • Y10S424/06Chelate

Definitions

  • This invention relates to a method for removing metal salts from polymeric films or filaments composed chiefly of acrylonitrile. It is concerned particularly with such a method for minimizing the salt content of fibers of polyacrylonitrile which have been spun from aqueous saline solutions of the polymer. It is taught by Rein in U. S. 2,140,921 and by Kropa' in U. S. 2,356,767 that polyacrylonitrile is soluble in concentrated aqueous solutions of certain highly hydrated metal salts, such as zinc chloride, and that such solutions can be spun to make fibers. Such fibers have been criticised in numerous patents as being weak, brittle and full of voids. Such brittleness or weakness may be due in some cases to the voids resulting from too rapid extraction of the salt during coagulation of the filamentary extruded product, but in others it is due to the presence of some of the salt in the final spun product.
  • the desired salt removal is effected after the fibers have been coagulated and stretched in the desired manner.
  • the fiber forming process may entail coagulation of the polymer solution as it is extruded into water, acid or dilute brine, followed by cold stretching or hot stretching, or both, with following or intervening treatments of the fiber with water or other coagulants to reduce the salt content to a value usually between 2 and 5 per cent.
  • Such an amount of residual salt is not detrimental during a subsequent drying operation, though the presence of over 5 per cent salt usually causes the fibers to fuse when heated to 125 C. or so during drying. A much lower salt content is required when the fibers are to be used in making woven or knit goods which may be worn in contact with sensitive skins.
  • an agent capable of forming a complex with the metal ion or ions of the salt or salts in the fibers include chelating agents and other metal sequestering agents.
  • the preferred agents include the alkali metal salts of ethylene diamine metal ions which may be present in the fibers, including those of zinc, calcium, magnesium, tin, aluminum, antimony, arsenic, bismuth,. and others.
  • the treatment is carried out while the fibers are still wet from a prior step in the process, as it has been found that dried fibers containing salt lose it very slowly to a solution of one of the complex-forming o'r sequestering agents, as they do to plain water.
  • a solution was prepared consisting of '7 per cent by weight of polyacrylonitrile, having a Staudinger molecular weight'of 76,100,216 per cent zinc chloride, 23.2 per cent calcium chloride and 38.2 per cent water.
  • This solution having a viscosity of 300 poises, lwas extruded through a IOU-hole spinneret, having openings 0.0025 inch in diameter, into water at C.
  • the socoagulated tow of filaments was cold-stretched in air 1.8 times its initial length, and was hotstretched in wet steam 2.4 times its coldstretched length.
  • the low of stretched fiber was washed for 10 seconds with water. Analysis of the product at various stages in the process to this point showed the following values:
  • Zinc chloride Calcium chloride Polymer Water One portion of the tow was dried to l per cent moisture content, and had 2.9 per cent zinc chloride and 1.7 per 1 cent calcium chloride. Another portion of the wet tow was soaked in water for one minute, and, when dried, had 0.35 per cent zinc chloride and 0.22 per cent calcium chloride. When, however, the wet tow was led through a 10 per cent solution in water at pH 8 of the tetrasodium salt of ethylene diamine tetraacetic acid for one minute, the subsequently dried fibers had 0.04 per cent zinc chloride and 0.08 per cent calcium chloride. By way of contrast, if thetow was dried before being exposed to the solution of sequestering or chelating agent, soaking'in such a solution for 18 hours still leftover 1 per cent total salt in the redried fibers.
  • the invention has been illustrated with respect to the treatment of fibers produced by wet spinning of aqueous saline solutions of poly-: acrylonitrile. It is applicable as well to the removal of salts from such other products as films made by extrusion and coagulation of such:
  • T w In a method for making shaped articles by coagulation of an aqueous polyvalent metal salt-containing saline solution of a polymer 0011-. taining at least per cent acrylonitrile inthe polymer molecule, the improvement'which con sists in immersing the article, before it h'asbeen' dried, in an aqueous solution of a Water-soluble alkali metal salt of a polyphosphoric acid as a sequestering agent for'the polyvalent metalions in the salt contained inthe coagulated article, until the salt content is reduced to a negligible value, and then drying the article. 7 g 1 2.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Artificial Filaments (AREA)

Description

Patented Aug. 11, 1953 REMOVING-SALTS FROM POLY-' ACRYLONITRILE George W. Stanton, WalnutCreek, and Theodore B. Lefferdink, Concord, Calif., assignors to The Dow Chemical Company, Midland, Mich., a corporation of Delaware No Drawing. Original application May 28, 1951, Serial No. 228,759. Divided and this application October 27, 1952, Serial No. 319,182
3 Claims.
This invention relates to a method for removing metal salts from polymeric films or filaments composed chiefly of acrylonitrile. It is concerned particularly with such a method for minimizing the salt content of fibers of polyacrylonitrile which have been spun from aqueous saline solutions of the polymer. It is taught by Rein in U. S. 2,140,921 and by Kropa' in U. S. 2,356,767 that polyacrylonitrile is soluble in concentrated aqueous solutions of certain highly hydrated metal salts, such as zinc chloride, and that such solutions can be spun to make fibers. Such fibers have been criticised in numerous patents as being weak, brittle and full of voids. Such brittleness or weakness may be due in some cases to the voids resulting from too rapid extraction of the salt during coagulation of the filamentary extruded product, but in others it is due to the presence of some of the salt in the final spun product.
In a group of applications filed concurrently with the original hereof, on May 28, 1951, by one or both of the present inventors and others. Serial Nos. 228,751 to 228,758 inclusive, it is disclosed that improved spun products can be made from polyacrylonitrile when the latter is first dissolved in an aqueous solution of at least 30 per cent, and usually not over 50 per cent, of a solvent salt and a lesser amount, from 5 to 25 per cent of a non-solvent salt, in proportions such that the aggregate amount of the two salts is at least 55 per cent, by Weight. The solvent salts are those whose anions are at least as high in the following table as their cations, and the non-solvent salts are those whose anions are lower in the table than their cations. To be useful, both types of salts employed must be mutually soluble in water.
While fibers spun from solutions in such mixed salts are superior to those made from solutions in single solvent salts, it is desirable for most purposes that the amount of salt or salts left in the'finished fiber be reduced to a minimum. It has been found that the rate of extraction of the last few percent of salts from the fibers by Water is very slow, and often may be considered impractical for use in a continuous fiber spinning process.
It is the principal object of the present invention to provide a practical and rapid method for reducing the salt content of articles such as films or filaments which have been formed from aqueous saline solutions of the polymer of acrylonitrile or of copolymers of at least 85 per cent acrylonitrile with another monoethylenically unsaturated compound.
TABLE Lyotropic series for polyacrylom'trile Cations in Increasing Order of Effectiveness l Anions in Decreasing Order of Effectiveness In accordance with the present invention, which will be described with reference to polyacrylonitrile fibers, the desired salt removal is effected after the fibers have been coagulated and stretched in the desired manner. The fiber forming process may entail coagulation of the polymer solution as it is extruded into water, acid or dilute brine, followed by cold stretching or hot stretching, or both, with following or intervening treatments of the fiber with water or other coagulants to reduce the salt content to a value usually between 2 and 5 per cent. Such an amount of residual salt is not detrimental during a subsequent drying operation, though the presence of over 5 per cent salt usually causes the fibers to fuse when heated to 125 C. or so during drying. A much lower salt content is required when the fibers are to be used in making woven or knit goods which may be worn in contact with sensitive skins. Hence, after the final wet stretching treatment, and before the fibers are dried, they are conducted through an aqueous solution of an agent capable of forming a complex with the metal ion or ions of the salt or salts in the fibers. Such agents include chelating agents and other metal sequestering agents. The preferred agents include the alkali metal salts of ethylene diamine metal ions which may be present in the fibers, including those of zinc, calcium, magnesium, tin, aluminum, antimony, arsenic, bismuth,. and others. The treatment is carried out while the fibers are still wet from a prior step in the process, as it has been found that dried fibers containing salt lose it very slowly to a solution of one of the complex-forming o'r sequestering agents, as they do to plain water.
The following example illustrates the practice of the invention, but is not tobe construed as limiting: H
A solution was prepared consisting of '7 per cent by weight of polyacrylonitrile, having a Staudinger molecular weight'of 76,100,216 per cent zinc chloride, 23.2 per cent calcium chloride and 38.2 per cent water. This solution, having a viscosity of 300 poises, lwas extruded through a IOU-hole spinneret, having openings 0.0025 inch in diameter, into water at C. The socoagulated tow of filaments was cold-stretched in air 1.8 times its initial length, and was hotstretched in wet steam 2.4 times its coldstretched length. The low of stretched fiber was washed for 10 seconds with water. Analysis of the product at various stages in the process to this point showed the following values:
Zinc chloride Calcium chloride Polymer Water One portion of the tow was dried to l per cent moisture content, and had 2.9 per cent zinc chloride and 1.7 per 1 cent calcium chloride. Another portion of the wet tow was soaked in water for one minute, and, when dried, had 0.35 per cent zinc chloride and 0.22 per cent calcium chloride. When, however, the wet tow was led through a 10 per cent solution in water at pH 8 of the tetrasodium salt of ethylene diamine tetraacetic acid for one minute, the subsequently dried fibers had 0.04 per cent zinc chloride and 0.08 per cent calcium chloride. By way of contrast, if thetow was dried before being exposed to the solution of sequestering or chelating agent, soaking'in such a solution for 18 hours still leftover 1 per cent total salt in the redried fibers.
In other tests, when the coagulated and stretched product was immersed in aqueous solutions of metal complexing agents while the product was still wet from a prior step, in the process, the alkali metal salts of ethylene diamine tetraproduct. Thus, when the treated product has been digested with nitric acid, burned to constant weight, and the ash analyzed photometrically for calcium and colorimetrically with dithiazine for zinc, values as low as nil for both elements have been obtained, and total values for the two are seldom found to exceed 0.2 per cent. The complexing agents have been found to be most effective when their solutions are adjusted to a pH value near 8, as their normally alkaline condition, pH 11 or higher,
tends to discolor the fibers.
The invention has been illustrated with respect to the treatment of fibers produced by wet spinning of aqueous saline solutions of poly-: acrylonitrile. It is applicable as well to the removal of salts from such other products as films made by extrusion and coagulation of such:
saline solutions.
This application is a division of our application Serial No. 228,759, filed May 28, 1951.; -i
We claim: T w '1. In a method for making shaped articles by coagulation of an aqueous polyvalent metal salt-containing saline solution of a polymer 0011-. taining at least per cent acrylonitrile inthe polymer molecule, the improvement'which con sists in immersing the article, before it h'asbeen' dried, in an aqueous solution of a Water-soluble alkali metal salt of a polyphosphoric acid as a sequestering agent for'the polyvalent metalions in the salt contained inthe coagulated article, until the salt content is reduced to a negligible value, and then drying the article. 7 g 1 2. The method as claimed'in claim 1, wherein the shaped'article is a wet-spun fiber of polyacrylonitrile. 3. The method as claimed in claim 1, wherein the solution of said alkali metal salt is, employed at a pH of about 8. GEORGE W. STANTON. s
THEODORE B. LEFFERDINK.
No references cited.

Claims (1)

1. IN A METHOD FOR MAKING SHAPED ARTICLES BY COAGULATION OF AN AQUEOUS POLYVALENT METAL SALT-CONTAINING SALINE SOLUTION OF A POLYMER CONTAINING AT LEAST 85 PER CENT ACRYLONITRILE IN THE POLYMER MOLECULE, THE IMPROVEMENT WHICH CONSISTS IN IMMERSING THE ARTICLE, BEFORE IT HAS BEEN DRIED, IN AN AQUEOUS SOLUTION OF A WATER-SOLUBLE ALKALI METAL SALT OF A POLYPHOSPHORIC ACID AS A SEQUESTERING AGENT FOR THE POLYVALENT METAL IONS IN THE SALT CONTAINED IN THE COAGULATED ARTICLE, UNTIL THE SALT CONTENT IS REDUCED TO A NEGLIGIBLE VALUE, AND THEN DRYING THE ARTICLE.
US319182A 1951-05-28 1952-10-27 Removing salts from polyacrylonitrile Expired - Lifetime US2648593A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
US228759A US2648592A (en) 1951-05-28 1951-05-28 Removing salts from polyacrylonitrile
US319182A US2648593A (en) 1951-05-28 1952-10-27 Removing salts from polyacrylonitrile
FR1082729D FR1082729A (en) 1951-05-28 1953-05-18 Improvements relating to the manufacturing process for shaped articles
DED15083A DE1044346B (en) 1951-05-28 1953-05-18 Process for the production of structures from polyacrylonitrile
CH326492D CH326492A (en) 1951-05-28 1953-05-19 Process for the manufacture of shaped articles such as threads or films from acrylonitrile polymers
NL178428A NL81838C (en) 1951-05-28 1953-05-19
GB15167/53A GB732008A (en) 1951-05-28 1953-06-01 Improvements in or relating to the purification of polyacrylonitrile filaments and films

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US228759A US2648592A (en) 1951-05-28 1951-05-28 Removing salts from polyacrylonitrile
US319182A US2648593A (en) 1951-05-28 1952-10-27 Removing salts from polyacrylonitrile
GB15167/53A GB732008A (en) 1951-05-28 1953-06-01 Improvements in or relating to the purification of polyacrylonitrile filaments and films

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US319182A Expired - Lifetime US2648593A (en) 1951-05-28 1952-10-27 Removing salts from polyacrylonitrile

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DE (1) DE1044346B (en)
FR (1) FR1082729A (en)
GB (1) GB732008A (en)
NL (1) NL81838C (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2878208A (en) * 1956-05-23 1959-03-17 Chemstrand Corp Acrylonitrile polymer composition stabilized with formaldehyde, ethylenediamine tetraacetic acid and sodium salts thereof, and an inorganic acid, and method of making same
US2878200A (en) * 1956-05-23 1959-03-17 Chemstrand Corp Stabilized acrylonitrile polymer composition and method of preparing same
US2878204A (en) * 1956-05-23 1959-03-17 Chemstrand Corp Acrylonitrile polymer composition stabilized with metal formaldehyde sulfoxylate, ethylenediamine tetra-acetic acid and sodium salts thereof, and an inorganic acid, and method of making same
US2904391A (en) * 1956-09-10 1959-09-15 Courtaulds Ltd Production of polyacrylonitrile threads, fibres, filaments and the like
US2916348A (en) * 1956-08-21 1959-12-08 American Cyanamid Co Production of polyacrylonitrile filaments
US3003993A (en) * 1959-10-19 1961-10-10 Eastman Kodak Co Process for color stabilizing acrylonitrile polymers by washing with ethylene diamine tetraacetic acid
US3030235A (en) * 1958-03-13 1962-04-17 American Viscose Corp Discoloration-resistant regenerated cellulose articles
US3079213A (en) * 1958-06-02 1963-02-26 Yardney International Corp Antimicrobial treatment of organic materials and composition therefor
US4228056A (en) * 1969-06-13 1980-10-14 Ceskoslovenska Akademie Ved Shaped articles from insoluble hydrogels and method of manufacturing same

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2879204A (en) * 1956-05-05 1959-03-24 Roussel Uclaf Vitamin b12 recovery process
US2879203A (en) * 1956-05-09 1959-03-24 Roussel Uclaf Recovery of vitamin b12 from diluted solutions
US3057811A (en) * 1958-04-25 1962-10-09 American Cyanamid Co Self-insolubilizing mineral pigment coating compositions for paper comprising a water-soluble anionic polymer adhesive and a water-soluble alum-sequestering agent complex
US3056169A (en) * 1959-09-28 1962-10-02 Du Pont Process of preparing shaped articles of acrylonitrile polymer containing silver insoluble particles
DE1181367B (en) * 1960-06-08 1964-11-12 Toho Rayon Kabushiki Kaisha Process for the production of threads from acrylonitrile polymers or copolymers with at least 85% acrylonitrile by wet spinning
US3154509A (en) * 1960-07-13 1964-10-27 Celanese Corp Solutions of polymers in solvent comprising antimony trichloride and process for preparing same
US3081273A (en) * 1960-07-13 1963-03-12 Celanese Corp Solution of terephthalamide polymer in solvent comprising antimony trichloride and process for preparing same
GB954860A (en) * 1960-09-24 1964-04-08 Toho Rayon Kk Process for the manufacture of polyacrylonitrile fibers
US3415611A (en) * 1965-10-28 1968-12-10 Dow Chemical Co Method of improving heat stability of acrylonitrile polymer fibers
DE3418943A1 (en) * 1984-05-22 1985-11-28 Bayer Ag, 5090 Leverkusen METHOD FOR PRODUCING THREADS AND FIBERS FROM ACRYLNITRILE POLYMERISATS

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425191A (en) * 1944-07-13 1947-08-05 American Cyanamid Co Polymerization of acrylates, methacrylates alone or in mixtures, and products thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2878208A (en) * 1956-05-23 1959-03-17 Chemstrand Corp Acrylonitrile polymer composition stabilized with formaldehyde, ethylenediamine tetraacetic acid and sodium salts thereof, and an inorganic acid, and method of making same
US2878200A (en) * 1956-05-23 1959-03-17 Chemstrand Corp Stabilized acrylonitrile polymer composition and method of preparing same
US2878204A (en) * 1956-05-23 1959-03-17 Chemstrand Corp Acrylonitrile polymer composition stabilized with metal formaldehyde sulfoxylate, ethylenediamine tetra-acetic acid and sodium salts thereof, and an inorganic acid, and method of making same
US2916348A (en) * 1956-08-21 1959-12-08 American Cyanamid Co Production of polyacrylonitrile filaments
US2904391A (en) * 1956-09-10 1959-09-15 Courtaulds Ltd Production of polyacrylonitrile threads, fibres, filaments and the like
US3030235A (en) * 1958-03-13 1962-04-17 American Viscose Corp Discoloration-resistant regenerated cellulose articles
US3079213A (en) * 1958-06-02 1963-02-26 Yardney International Corp Antimicrobial treatment of organic materials and composition therefor
US3003993A (en) * 1959-10-19 1961-10-10 Eastman Kodak Co Process for color stabilizing acrylonitrile polymers by washing with ethylene diamine tetraacetic acid
US4228056A (en) * 1969-06-13 1980-10-14 Ceskoslovenska Akademie Ved Shaped articles from insoluble hydrogels and method of manufacturing same

Also Published As

Publication number Publication date
FR1082729A (en) 1954-12-31
DE1044346B (en) 1958-11-20
CH326492A (en) 1957-12-31
NL81838C (en) 1956-06-15
US2648592A (en) 1953-08-11
GB732008A (en) 1955-06-15

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