US2553916A - Mixture for the production of pastes of synthetic material - Google Patents

Mixture for the production of pastes of synthetic material Download PDF

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US2553916A
US2553916A US96616A US9661649A US2553916A US 2553916 A US2553916 A US 2553916A US 96616 A US96616 A US 96616A US 9661649 A US9661649 A US 9661649A US 2553916 A US2553916 A US 2553916A
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grains
powder
mixture
diameter
coarse
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Halbig Paul
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/18Plasticising macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/005Processes for mixing polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/09Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids
    • C08J3/11Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids from solid polymers

Definitions

  • fluent pastes with as small as possible quantities of liquid as plasticisers can be obtained by using for the production of the paste synthetic material powder containing larger quantities of larger particles of synthetic material and smaller quantities f smaller particles of synthetic materiaLwhilst substantially excluding the intermediate particles of intermediate size.
  • the synthetic material mixture contains a gap in the distribution of particle sizes. i. e. particles of intermediate grain size are substantially absent between the larger and the smaller particle sizes.
  • This special novel particle distribution gives a fluent paste even with relatively small quantities of liquid, whereas the usual mixture of grains, containing grains of intermediate size, gives a non-fluent stiff paste with the same liquid content which cannot readily be worked up.
  • the synthetic material powders according to the invention may consist of particles of sizes less than /1000 mm. up to 0.5 mm. and more. For example 1 part by weight of polymethylmethacrylate pearls with a particle size of 0.250
  • a polyvinyl chloride powder with particles of 9 to 15 microns does not give a suspension with equal parts of dibutylphthalate, but only mixtures of muddyconsistency; if, however, 20 to of the polyvinyl chloride particles of 9 to 15 microns are replaced by particles of 0.4 to 1.5 microns, then a liquid suspension is obtained similar to a painting lacquer. It had hitherto been assumed that good paste-forming powers depended more or less on the degree of polymerisation and on the manner in which the polymer was isolated. This is not, however, of primary importance; according to the present invention pasteforming power is primarily a function of the fineness of the grain composition of the synthetic material powder.
  • the paste is produced by mixing or triturating the powder with the liquid plasticiser at low temperatures for example at room temperature, until a uniform suspension is produced, and the fractions of the powder of different granular sizes can be added to the liquid one after the other or as a mixture.
  • the granular distribution follows the following rules:
  • the powder is produced from two granular sizes, the ratio of the mean particle size of which is 1:6 or more.
  • Granular sizes between these proportions should be kept as small as possible, i. e. there should be as few particles as possible having a granular size of between 1.1 times and 5.9 times the size of the smaller grains.
  • the proportion by weight of larger grains should amount to 0.8 times to 5 times the weight of the smaller grains.
  • each one of the above-mentioned granular sizes requires at least 1.2 parts of liquid for 1.0 part of powder to produce a liquid suspension as do mixtures of (a) with (b) or (c) with (d).
  • a powder for the production of pastes of thermoplastic polymeric material for thermoplastic working up consisting essentially of a mixture of coarse grained and fine grained powder of the polymeric material the coarse grains having a diameter at least six times the diameter of the fine grains, and the ratio of the weight of the coarse grains to the weight of the fine grains being between 8:10 and :15, said powder mixture being substantially devoid of grains sized between the coarse and fine grain sizes.
  • thermoplastic working up consisting of a powdery mixture of coarse and fine grained thermoplastic polymeric material
  • the coarse grains having a diameter at least six times the diameter of the fine grains, and the ratio of the weight of the coarse grains to the weight of the fine grains being between 8:10 and 85:15, said powder mixture being substantially devoid of grains sized between the coarse and fine grain sizes, and a sufiicient quantity of liquid plasticiZer to convert said powder mixture into a fluent paste.
  • thermoplastic polymeric material is a polyvinyl resin.
  • thermoplastic polymeric material is polyvinyl chloride.
  • thermoplastic material is an acrylic resin
  • thermoplastic material is a polym-ethacrylate and said plasticizer is a monomeric methacrylate.
  • a paste according to claim '2 in which the diameter of the coarse grains is less than 0.1 mm.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Paints Or Removers (AREA)

Description

Patented May 22, 1951 MIXTURE FOR, THE PRODUCTION OF PASTES OF SYNTHETIC MATERIAL Paul Halbig, Fribourg, Switzerland No Drawing. Application June 1, 1949, Serial No. 96,616. In Switzerland June 14, 1948 For working up powders of synthetic material in accordance with the thermoplastic principle it is advantageous first to prepare a paste, i. e. a flowing suspension, which can be brought like a lacquer or latex into the desired form, for example by pouring, painting, dipping, injecting, etc., by mixing the powder with a liquid plasticiser, i. e. a liquid which has a plasticising action on the powder in the heat but has no perceptible effect on the latter in the cold. The plasticising or solidifying then subsequently takes place by simple heating with or without pressure, whereby gelatinisation of the mixture takes place. Attempts are made nowadays to apply this method of working to many plastic masses, in particular this method of working is used in working up polyvinyl compounds, such for example as polyvinyl chloride, for the production of coatings on materials and the like. As a rule it is advantageous to bring about the fluent, i. e. liquid to paintable or pourable, condition of the paste with as small a quantity of liquid as possible. It has not hitherto been determined what particular properties of the powder of synthetic material are responsible for the paste-forming capacity. In production, for example, suitable pastes are found simply by practical experiment with softeners. It has now been found that fluent pastes with as small as possible quantities of liquid as plasticisers can be obtained by using for the production of the paste synthetic material powder containing larger quantities of larger particles of synthetic material and smaller quantities f smaller particles of synthetic materiaLwhilst substantially excluding the intermediate particles of intermediate size. Whereas in the mixtures of powders hitherto generally used particles were contained in all intermediate sizes, even if in different quantities, for the present invention it is characteristic that the synthetic material mixture contains a gap in the distribution of particle sizes. i. e. particles of intermediate grain size are substantially absent between the larger and the smaller particle sizes. This special novel particle distribution gives a fluent paste even with relatively small quantities of liquid, whereas the usual mixture of grains, containing grains of intermediate size, gives a non-fluent stiff paste with the same liquid content which cannot readily be worked up. a
The synthetic material powders according to the invention may consist of particles of sizes less than /1000 mm. up to 0.5 mm. and more. For example 1 part by weight of polymethylmethacrylate pearls with a particle size of 0.250
8 Claims. (Cl. 260-342) to 0.300 mm. can ive a readily flowing pourable suspension by simple stirring with 0.4 to 0.5 part by weight of monomeric methacrylate, if at least 15% by weight of the grains of 0.250 to 0.300 mm. diameter are replaced by pearls of only 0.010 to 0.050 mm. diameter. The inventive idea can particularly readily be demonstrated in this range of size. The idea is also applicable, however, to particles with a diameter of a smallness of the order of the length of light waves, for example 0.0005 mm. Thus for example a polyvinyl chloride powder with particles of 9 to 15 microns does not give a suspension with equal parts of dibutylphthalate, but only mixtures of muddyconsistency; if, however, 20 to of the polyvinyl chloride particles of 9 to 15 microns are replaced by particles of 0.4 to 1.5 microns, then a liquid suspension is obtained similar to a painting lacquer. It had hitherto been assumed that good paste-forming powers depended more or less on the degree of polymerisation and on the manner in which the polymer was isolated. This is not, however, of primary importance; according to the present invention pasteforming power is primarily a function of the fineness of the grain composition of the synthetic material powder.
The paste is produced by mixing or triturating the powder with the liquid plasticiser at low temperatures for example at room temperature, until a uniform suspension is produced, and the fractions of the powder of different granular sizes can be added to the liquid one after the other or as a mixture.
Preferably the granular distribution follows the following rules:
1. The powder is produced from two granular sizes, the ratio of the mean particle size of which is 1:6 or more.
2. Granular sizes between these proportions should be kept as small as possible, i. e. there should be as few particles as possible having a granular size of between 1.1 times and 5.9 times the size of the smaller grains.
3. The proportion by weight of larger grains should amount to 0.8 times to 5 times the weight of the smaller grains.
Examples l. Grains of the following sizes:
(a) 0.0005-0.0015 mm. diameter (b) 0002-0008 mm. diameter (c) 0.010-0.020 mm. diameter (d) 0050-0080 mm. diameter are produced from polyvinyl chloride powder,
for example by sieving, elutriating, sifting or by carrying out the polymerisation under particular conditions. Each one of the above-mentioned granular sizes requires at least 1.2 parts of liquid for 1.0 part of powder to produce a liquid suspension as do mixtures of (a) with (b) or (c) with (d).
If, onthe other hand, 1 part of the grains (a) is mixed with 1.4 parts of the grains the intermediate grains (b) being left out, then with 0.5 to 1.0 parts of dibutylphthalate per 1 part of the mixture, easily flowing suspensions are obtained. The same result is obtained by mixing the grains (b) and (d). The paste may be plasticised in known manner by heating to 140 to 180 C.
2. Grains of the following size are obtained by sieving polymethylmethacrylate pearls:
(a) 0.010-0.020 mm. diameter (22) 0.020-.0.0 i0 mm. diameter (c) 0420-0450 mm. diameter (d) 0240-0280 mm. diameter None of the above grains gives a liquid suspension with 0.5 part of monomeric methylmethacrylate per 1 part of pearls. On the other hand if 15 to 50 parts of the grains (:1) or (b) are mixed with 85 to :50 parts of the grains (c) or (d) respectively, then when 1 part of this mixture is triturated with 0.5 part of monomeric methylmethacrylate a paste or liquid suspension is obtained which can be poured, and which solidifies on heating to a glassy body.
I claim:
1. A powder for the production of pastes of thermoplastic polymeric material for thermoplastic working up, the powder consisting essentially of a mixture of coarse grained and fine grained powder of the polymeric material the coarse grains having a diameter at least six times the diameter of the fine grains, and the ratio of the weight of the coarse grains to the weight of the fine grains being between 8:10 and :15, said powder mixture being substantially devoid of grains sized between the coarse and fine grain sizes.
2. A paste for the thermoplastic working up consisting of a powdery mixture of coarse and fine grained thermoplastic polymeric material,
the coarse grains having a diameter at least six times the diameter of the fine grains, and the ratio of the weight of the coarse grains to the weight of the fine grains being between 8:10 and 85:15, said powder mixture being substantially devoid of grains sized between the coarse and fine grain sizes, and a sufiicient quantity of liquid plasticiZer to convert said powder mixture into a fluent paste.
3. A paste according to claim 2, wherein the weight of the plasticizer amounts to between 50 to percent of the weight of said powder mixture.
4. A paste according to claim 2, wherein said thermoplastic polymeric material is a polyvinyl resin.
5. A paste according to claim 2, wherein said thermoplastic polymeric material is polyvinyl chloride.
6. A paste according to claim 2, wherein said thermoplastic material is an acrylic resin.
'7. A paste according to claim 2, wherein said thermoplastic material is a polym-ethacrylate and said plasticizer is a monomeric methacrylate.
'8. A paste according to claim '2, in which the diameter of the coarse grains is less than 0.1 mm.
PAUL HALBIG.
No references cited.

Claims (1)

1. A POWDER FOR THE PRODUCTION OF PASTES OF THERMOPLASTIC POLYMERIC MATERIAL FOR THERMOPLASTIC WORKING UP, THE POWDER CONSISTING ESSENTIALLY OF A MIXTURE OF COARSE GRAINED AND FINE GRAINED POWDER OF THE POLYMERIC MATERIAL, THE COARSE GRAINS HAVING A DIAMETER AT LEAST SIX TIMES THE DIAMETER OF THE FINE GRAINS, AND THE RATIO OF THE WEIGHT OF THE COARSE GRAINS TO THE WEIGHT OF THE FINE GRAINS BEING BETWEEN 8:10 AND 85:15, SAID POWDER MIXTURE BEING SUBSTANTIALLY DEVOID OF GRAINS SIZED BETWEEN THE COARSE AND FINE GRAIN SIZES.
US96616A 1948-06-14 1949-06-01 Mixture for the production of pastes of synthetic material Expired - Lifetime US2553916A (en)

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Application Number Priority Date Filing Date Title
CH671045X 1948-06-14

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US (1) US2553916A (en)
BE (1) BE489599A (en)
CH (1) CH272263A (en)
DE (1) DE934498C (en)
FR (1) FR987880A (en)
GB (1) GB671045A (en)
NL (2) NL146908B (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2674585A (en) * 1951-07-24 1954-04-06 Shell Dev Plastisols of vinyl chloride polymer
US2721859A (en) * 1954-08-16 1955-10-25 Us Rubber Co Spray-drying process for making plastisol grade vinyl chloride polymers
US2729627A (en) * 1952-11-26 1956-01-03 Us Rubber Co Polyvinyl chloride for use in plastisols
US2753287A (en) * 1953-09-18 1956-07-03 Millville Mfg Company Organic dispersion type adhesives, their preparation and application
US2784177A (en) * 1949-07-22 1957-03-05 Distillers Co Yeast Ltd Production of paste-forming polyvinyl chloride
US2843576A (en) * 1953-12-03 1958-07-15 Ethyl Corp Production of vinyl compounds
US3179646A (en) * 1959-09-28 1965-04-20 Dow Chemical Co Polymerization to produce friable aggregates of individual spheres of polyvinyl chloride
JPS4860747A (en) * 1971-11-26 1973-08-25
US4657966A (en) * 1983-04-25 1987-04-14 Polysar Limited Carboxylated latex

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4210567A (en) 1974-11-15 1980-07-01 Teroson G.M.B.H. Plastisol of an acrylate polymer and a plasticizer
US4595590A (en) * 1984-01-17 1986-06-17 Laboratoires Biocodex Method for preventing or treating pseudo-membranous colitis
DE19542746A1 (en) 1995-11-16 1997-05-22 Roehm Gmbh Plastisols based on polymer masses softened by the addition of plasticizers
DE19928352A1 (en) 1999-06-21 2000-12-28 Roehm Gmbh Plastisol use for mould articles, comprises (meth)acrylate (co)polymer(s) with bimodal or multi-modal prim. particle distribution prepared from methyl methacrylate, (meth) acrylate, vinyl monomer and adhesion aiding monomers

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE737058C (en) * 1936-09-07 1943-07-06 Kulzer & Co Gmbh Process for the manufacture of prostheses for dental or other purposes from polymerized organic compounds
GB535612A (en) * 1939-09-07 1941-04-16 Archibald Renfrew Improvements in and relating to the production of pastes from polymerised vinyl chloride

Non-Patent Citations (1)

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

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2784177A (en) * 1949-07-22 1957-03-05 Distillers Co Yeast Ltd Production of paste-forming polyvinyl chloride
US2674585A (en) * 1951-07-24 1954-04-06 Shell Dev Plastisols of vinyl chloride polymer
US2729627A (en) * 1952-11-26 1956-01-03 Us Rubber Co Polyvinyl chloride for use in plastisols
US2753287A (en) * 1953-09-18 1956-07-03 Millville Mfg Company Organic dispersion type adhesives, their preparation and application
US2843576A (en) * 1953-12-03 1958-07-15 Ethyl Corp Production of vinyl compounds
US2721859A (en) * 1954-08-16 1955-10-25 Us Rubber Co Spray-drying process for making plastisol grade vinyl chloride polymers
US3179646A (en) * 1959-09-28 1965-04-20 Dow Chemical Co Polymerization to produce friable aggregates of individual spheres of polyvinyl chloride
JPS4860747A (en) * 1971-11-26 1973-08-25
JPS5613722B2 (en) * 1971-11-26 1981-03-31
US4657966A (en) * 1983-04-25 1987-04-14 Polysar Limited Carboxylated latex

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BE489599A (en)
GB671045A (en) 1952-04-30
CH272263A (en) 1950-12-15
DE934498C (en) 1955-10-27
NL72985C (en)
FR987880A (en) 1951-08-20
NL146908B (en)

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