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DE1105171B - Process for the production of uniform polymers - Google Patents

Process for the production of uniform polymers

Info

Publication number
DE1105171B
DE1105171B DEB52880A DEB0052880A DE1105171B DE 1105171 B DE1105171 B DE 1105171B DE B52880 A DEB52880 A DE B52880A DE B0052880 A DEB0052880 A DE B0052880A DE 1105171 B DE1105171 B DE 1105171B
Authority
DE
Germany
Prior art keywords
production
fractions
suspension
uniform
uniform polymers
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.)
Pending
Application number
DEB52880A
Other languages
German (de)
Inventor
Dr Erich Umlauf
Dr Erich Schwartz
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.)
BASF SE
Original Assignee
BASF SE
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 BASF SE filed Critical BASF SE
Priority to DEB52880A priority Critical patent/DE1105171B/en
Publication of DE1105171B publication Critical patent/DE1105171B/en
Pending 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
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/12Powdering or granulating
    • 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
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene
    • C08J2323/06Polyethene

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

Verfahren zur Herstellung polymereinheitlicher Polymerisate Es ist wohl bekannt, die verschiedenartigsten, pulverförmigen oder körnigen Stoffe mit unterschiedlicher Teilchengröße durch Sieben oder andere mechanische Verfahren in Fraktionen mit einheitlicher Teilchengröße zu zerlegen. Hierdurch wird das Ahtrennen von Fraktionen mit sehr kleinen oder sehr groben Teilchen bezweckt, weil diese bei der mechanischen Verarbeitung derartiger Stoffe stören können. Process for the production of uniform polymers It is well known, the most diverse, powdery or granular substances with different particle sizes by sieving or other mechanical processes in To break down fractions with uniform particle size. This will cause the disconnection intended for fractions with very small or very coarse particles, because these at can interfere with the mechanical processing of such substances.

Andererseits ist es bekanntlich technisch nicht möglich, makromolekulare Verbindungen mit völlig gleich großen Molekülen herzustellen. Polymerisationsprodukte setzen sich vielmehr aus Molekülen verschiedener Größe zusammen, deren Verteilung im allgemeinen durch eine Verteilungskurve dargestellt werden kann. Es sind deshalb bereits häufig Maßnahmen vorgeschlagen worden, um die Polymereinheitl ichkeit von Polymerisationsprodukten zu verbessern. So kann man die die Polymerisation beeinflussenden Faktoren konstant halten oder die Polymerisate durch fraktioniertes Lösen oder Fällen aus ihrer Lösung zerlegen. On the other hand, it is known that it is technically not possible to use macromolecular Making compounds with molecules of exactly the same size. Polymerization products rather, they are composed of molecules of different sizes, their distribution can generally be represented by a distribution curve. It is therefore Measures have often been proposed to improve the polymer uniformity of To improve polymerization products. So you can influence the polymerization Keeping factors constant or the polymers by fractional dissolving or precipitating disassemble from their solution.

Der vorliegenden Erfindung liegt die Erkenntnis zugrunde, daß die Größe von Teilchen von in Suspension hergestelltem Polyäthylen in einem bestimmten Zusammenhang mit dem Molekulargewicht steht. The present invention is based on the knowledge that the Size of particles of polyethylene produced in suspension in a given It is related to the molecular weight.

Um aus in Suspension hergestelltem Polyäthylen polymereinheitliche Stoffe zu erhalten, wird vorgeschlagen, die suspendierten oder vom Suspensionsmittel getrennten Polymerisatteilchen mechanisch in Fraktionen gleicher oder ähnlicher Teilchengröße zu zerlegen. Die Teilchen können beispielsweise durch Sedimentations-oder Flotationsverfahren fraktioniert werden. To polymer uniform from polyethylene made in suspension To obtain substances, it is suggested that the suspended or from the suspending agent separate polymer particles mechanically in fractions of the same or similar Particle size decompose. The particles can, for example, by sedimentation or Flotation processes are fractionated.

Auch wenn man die vom Suspensionsmittel getrennten Polymerisatteilchen in einem heißen Luft-oder Stickstoffstrom, beispielsweise in einem Schwebetrockner, trocknet, so ist die Korngrößenverteilung die gleiche wie in wäßriger Suspension. Durch Verwendung geeigneter Sichter, z. B. Zentrifugalabscheider oder Windsichter, kann die Trennung in Fraktionen verschiedener Teilchen größe und damit verschiedenen Polymerisationsgrades in technisch einfacher Weise erfolgen. Even if you have the polymer particles separated from the suspension medium in a hot air or nitrogen stream, for example in a flotation dryer, dries, so is the grain size distribution the same as in aqueous suspension. By using suitable classifiers, e.g. B. centrifugal separator or air separator, the separation into fractions of different particle size and thus different Degree of polymerization take place in a technically simple manner.

Beispiel 1 Ein in bekannter Weise in Suspension hergestelltes Polyäthylen wird nach dem Waschen und Trocknen mit Hilfe eines Schwingsiehes mit verschiedenen Siebeinsätzen in Siebfraktionen zerlegt. Die Ergebnisse sind in der folgenden Tabelle 1 wiedergegeben: Tabelle 1 Frak- Menge Korngrößen Intrinsic- Schmelzpunkt tion in 0/0 | in Mikron Viskosität in o C 1 7 ) >600 2,16 127 2 16 400 bis 600 1,75 126,5 3 10 200 bis 400 1,57 126,0bis 1265 4 67 75 bis 200 1,39 123,5 bis 125 Beispiel 2 Ein in üblicher Weise in Suspension hergestelltes Polyäthylen wird mit Hilfe eines Schwingsiebes mit verschiedenen genormten Siebeinsätzen 1 Minute gesiebt. Danach werden die erhaltenen sechs Fraktionen (1 bis 6), jede für sich, nochmals 5 Minuten gesiebt.EXAMPLE 1 A polyethylene produced in suspension in a known manner is broken down into sieve fractions after washing and drying with the aid of a vibrating sieve with various sieve inserts. The results are shown in Table 1 below: Table 1 Fraction quantity, grain sizes, intrinsic melting point tion in 0/0 | in micron viscosity in oC 1 7)> 600 2.16 127 2 16 400 to 600 1.75 126.5 3 10 200 to 400 1.57 126.0 to 1265 4 67 75 to 200 1.39 123.5 to 125 Example 2 A polyethylene produced in suspension in the usual way is sieved for 1 minute with the aid of a vibrating sieve with various standardized sieve inserts. The six fractions obtained (1 to 6) are then sieved for another 5 minutes, each for itself.

Hierbei erhält man aus jeder Fraktion noch je eine Fraktion (la bis 6a). Die Korngrößen der verschiedenen Fraktionen sowie deren Intrinsic-Viskosität sind in der folgenden Tabelle 2 angegeben.In this case, one more fraction is obtained from each fraction (la to 6a). The grain sizes of the various fractions and their intrinsic viscosity are given in Table 2 below.

Tabelle 2 Gewichts- Fraktions- Korngrößen prozent der Intrisic-Viskosität Nr in Mikron Einwaage 1 3,30 >600 5,91 1 a 35,03 400 bis 600 3,07 2 36,50 400 bis 600 2,92 2a 14,38 300 bis 400 2,84 3 4,52 300 bis 400 2,73 3a 2,37 200 bis 300 2,77 4 1,85 200 bis 300 2,68 4a 0,60 150 bis 200 2,69 5 0,60 150 bis 200 2,60 5a 0,29 120 bis 150 2,60 6 0,29 120 bis 150 2,55 6a 0,27 <120 2,74 Table 2 Weight Fractional grain sizes percent of intrisic viscosity No. in microns Initial weight 1 3.30> 600 5.91 1 a 35.03 400 to 600 3.07 2 36.50 400 to 600 2.92 2a 14.38 300 to 400 2.84 3 4.52 300 to 400 2.73 3a 2.37 200 to 300 2.77 4 1.85 200 to 300 2.68 4a 0.60 150 to 200 2.69 5 0.60 150 to 200 2.60 5a 0.29 120 to 150 2.60 6 0.29 120 to 150 2.55 6a 0.27 <120 2.74

Claims (1)

PATENTANSPRUCH: Verfahren zur Herstellung polymereinheitlicher Stoffe aus in Suspension hergestelltem Polyäthy- len, dadurch gekennzeichnet, daß die suspendierten oder vom Suspensionsmittel getrennten polymerisatteilchen mechanisch in Fraktionen mit gleicher oder ähnlicher Teilchengröße zerlegt werden.PATENT CLAIM: Process for the production of uniform polymer materials made of polyethylene produced in suspension len, characterized in that the suspended or polymer particles separated mechanically from the suspension medium into fractions are broken down with the same or similar particle size.
DEB52880A 1955-11-18 1955-11-18 Process for the production of uniform polymers Pending DE1105171B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEB52880A DE1105171B (en) 1955-11-18 1955-11-18 Process for the production of uniform polymers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEB52880A DE1105171B (en) 1955-11-18 1955-11-18 Process for the production of uniform polymers

Publications (1)

Publication Number Publication Date
DE1105171B true DE1105171B (en) 1961-04-20

Family

ID=6970060

Family Applications (1)

Application Number Title Priority Date Filing Date
DEB52880A Pending DE1105171B (en) 1955-11-18 1955-11-18 Process for the production of uniform polymers

Country Status (1)

Country Link
DE (1) DE1105171B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1795396A1 (en) * 1968-09-26 1972-01-05 Basf Ag Process for removing volatile components from finely divided olefin polymers
FR2186486A1 (en) * 1971-11-26 1974-01-11 Snam Progetti

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1795396A1 (en) * 1968-09-26 1972-01-05 Basf Ag Process for removing volatile components from finely divided olefin polymers
FR2186486A1 (en) * 1971-11-26 1974-01-11 Snam Progetti

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