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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Publication number
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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US
United States
Prior art keywords
grains
powder
mixture
diameter
coarse
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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
US96616A
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English (en)
Inventor
Halbig Paul
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Individual
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Individual
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Publication of US2553916A publication Critical patent/US2553916A/en
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Classifications

    • 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.

Landscapes

  • 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)
US96616A 1948-06-14 1949-06-01 Mixture for the production of pastes of synthetic material Expired - Lifetime US2553916A (en)

Applications Claiming Priority (1)

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

Publications (1)

Publication Number Publication Date
US2553916A true US2553916A (en) 1951-05-22

Family

ID=4527662

Family Applications (1)

Application Number Title Priority Date Filing Date
US96616A Expired - Lifetime US2553916A (en) 1948-06-14 1949-06-01 Mixture for the production of pastes of synthetic material

Country Status (7)

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

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 (fr) * 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 (de) 1995-11-16 1997-05-22 Roehm Gmbh Plastisole auf der Grundlage von durch Weichmacherzusatz weichgemachte Polymermassen
DE19928352A1 (de) 1999-06-21 2000-12-28 Roehm Gmbh Verbesserte Poly(meth)acrylatptastisole und Verfahren zu ihrer Herstellung

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE737058C (de) * 1936-09-07 1943-07-06 Kulzer & Co Gmbh Verfahren zur Herstellung von Prothesen fuer zahnaerztliche oder andere Zwecke aus polymerisierten organischen Verbindungen
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 (fr) * 1971-11-26 1973-08-25
JPS5613722B2 (fr) * 1971-11-26 1981-03-31
US4657966A (en) * 1983-04-25 1987-04-14 Polysar Limited Carboxylated latex

Also Published As

Publication number Publication date
BE489599A (fr)
GB671045A (en) 1952-04-30
CH272263A (de) 1950-12-15
DE934498C (de) 1955-10-27
NL72985C (fr)
FR987880A (fr) 1951-08-20
NL146908B (nl)

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