GB1328362A - Dispersion of materials in thermoplastics - Google Patents

Dispersion of materials in thermoplastics

Info

Publication number
GB1328362A
GB1328362A GB1328362DA GB1328362A GB 1328362 A GB1328362 A GB 1328362A GB 1328362D A GB1328362D A GB 1328362DA GB 1328362 A GB1328362 A GB 1328362A
Authority
GB
United Kingdom
Prior art keywords
section
screw
blowing agent
polymer
thermoplastic
Prior art date
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
Application number
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.)
Imperial Chemical Industries Ltd
Original Assignee
Imperial Chemical Industries Ltd
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
Application filed by Imperial Chemical Industries Ltd filed Critical Imperial Chemical Industries Ltd
Priority claimed from GB4944772A external-priority patent/GB1317162A/en
Publication of GB1328362A publication Critical patent/GB1328362A/en
Expired legal-status Critical Current

Links

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
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
    • C08J9/14Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/3442Mixing, kneading or conveying the foamable material

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

1328362 Extruding foam plastics IMPERIAL CHEMICAL INDUSTRIES Ltd 4 Oct 1971 [19 Oct 1970] 49447/70 Heading B5A [Also in Division C3] A foamed thermoplastic polymer is formed in an apparatus comprising a screw extruder provided with two inlet ports, downstream of the melting zone, through which a liquid and a gaseous blowing agent respectively may be injected, the inlet port for the gaseous blowing agent being connected to a constant pressure supply of gaseous blowing agent via a flow restricting device across which a pressure drop of at least 100 p.s.i. can be maintained while the inlet port for the liquid blowing agent is connected to a metering device delivering a given quantity of liquid blowing agent per unit time. The flow restricting device may be a length of capillary tube. The extruder screw may have a section, rotating with the screw and opposite at least the injection port for the liquid blowing agent, wherein the molten thermoplastic is divided into a plurality of streams. This division may be achieved by providing a fluted section in the screw comprising a cylinder having several (at least 3) axial channels formed on its outer surface. It is preferred that the cylinder has a length at least equal to the internal diameter of the extruder barrel, e.g. 3-6 times the diameter. The fluted section may be followed by a turbine section which both shears and further subdivides the mixture. The turbine mixing section preferably comprises a plurality of toothed rotors mounted on the screw to rotate therewith, the teeth of alternate rotors being staggered. After this section there is preferably a further mixing section in which a cylindrical member provided with inlet grooves not extending along the whole length of the member is used. In Fig. 1 a screw rotates in a barrel 1 and the thermoplastic polymer is compressed and melted in a compression section 3 of the screw. The polymer then passes to section 4 of the screw which is fluted having a series of axial grooves (Fig. 2) (not shown) which divides it into a plurality of streams. The first blowing agent is fed in at port 6 and the second injected via a capillary tube 9 at 8. The polymer then passes to turbine mixing section 10 containing a series of spaced toothed rotors (Fig. 3) (not shown) 11, 12, 13, 14 mounted on the screw so that they rotate therewith. The polymer is finally passed through a shearing section 18 consisting of a cylinder 19 provided with axial grooves 20 (Fig. 4) (not shown). The process for forming the foamed polymer is described (see Division C3), the first blowing agent comprising 20-75% by weight of the thermoplastic and the second up to 10% by weight of the thermoplastic. The polymer may be polyethylene.
GB1328362D 1970-10-19 1970-10-19 Dispersion of materials in thermoplastics Expired GB1328362A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB4944772A GB1317162A (en) 1969-07-30 1970-10-19 Material tester and search unit therefor

Publications (1)

Publication Number Publication Date
GB1328362A true GB1328362A (en) 1973-08-30

Family

ID=10452374

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1328362D Expired GB1328362A (en) 1970-10-19 1970-10-19 Dispersion of materials in thermoplastics

Country Status (7)

Country Link
JP (1) JPS5513894B1 (en)
BE (1) BE774164A (en)
CA (1) CA963215A (en)
ES (1) ES396145A1 (en)
FR (1) FR2111694B1 (en)
GB (1) GB1328362A (en)
NL (1) NL7114343A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1092311A (en) * 1975-09-04 1980-12-30 John C. Miller Extrusion of cellular thermoplastic material
FI771008A (en) * 1976-05-10 1977-11-11 Berstorff Gmbh Masch Hermann
JPS5781680U (en) * 1980-11-05 1982-05-20
WO1990012841A1 (en) * 1989-04-24 1990-11-01 Huetzen Hans Wilhelm Polyurethane foam material free of halogenated hydrocarbons and process for producing the same
TR26440A (en) * 1989-10-09 1995-03-15 Hans Wilhelm Huetzen HALOGEN HYDRO CARBONS THAT DO NOT CONTAIN POLYURETHANE FOAM MATERIAL AND A PROCESS FOR THE PRODUCTION OF IT

Also Published As

Publication number Publication date
ES396145A1 (en) 1975-02-16
BE774164A (en) 1972-04-19
DE2152018A1 (en) 1972-05-18
DE2152018B2 (en) 1975-11-06
FR2111694A1 (en) 1972-06-09
JPS5513894B1 (en) 1980-04-12
AU3475771A (en) 1973-05-03
NL7114343A (en) 1972-04-21
FR2111694B1 (en) 1975-07-18
CA963215A (en) 1975-02-25

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee