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DE1920464A1 - Poly (methylmethacrylate) rods - Google Patents

Poly (methylmethacrylate) rods

Info

Publication number
DE1920464A1
DE1920464A1 DE19691920464 DE1920464A DE1920464A1 DE 1920464 A1 DE1920464 A1 DE 1920464A1 DE 19691920464 DE19691920464 DE 19691920464 DE 1920464 A DE1920464 A DE 1920464A DE 1920464 A1 DE1920464 A1 DE 1920464A1
Authority
DE
Germany
Prior art keywords
rods
cells
polymerisation
methylmethacrylate
polymerization
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
DE19691920464
Other languages
German (de)
Inventor
Fontana Ion A
Mihailescu Constantin Alex
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.)
MINISTERUL IND USOARE
Original Assignee
MINISTERUL IND USOARE
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 MINISTERUL IND USOARE filed Critical MINISTERUL IND USOARE
Priority to DE19691920464 priority Critical patent/DE1920464A1/en
Publication of DE1920464A1 publication Critical patent/DE1920464A1/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • B29C39/00Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor
    • B29C39/003Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor characterised by the choice of material
    • B29C39/006Monomers or prepolymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/02Polymerisation in bulk
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/02Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/10Esters
    • C08F20/12Esters of monohydric alcohols or phenols
    • C08F20/14Methyl esters, e.g. methyl (meth)acrylate

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)

Abstract

Methylmethacrylate is prepolymerised to 40-50% conversion at 80-90 degrees C, and complete polymerisation in synthetic cells of suitable porosity is then effected in water bath at 18-20 degrees C for 48 hrs. in presence of usual polymerisation initiators and regulators. The polymerisation cells may be of porous polyethylene. A thin film of water forming between the cell walls and the PMMA rods enables the rods to be removed easily. The products are qualitatively superior to those produced in glass cells.

Description

Verfahren' zur Herstellung von Stangen aus Polniethakrylsäuremethylest er Die Erfindung bezieht sich auf ein Verfahren zur Herstellung von Polymethylmethakrylatstangen. Process for the production of rods from poliethakrylic acid methyl ester The invention relates to a method for making polymethyl methacrylate rods.

Es ist ein Verfahren bekannt, mit welchem PolymeWhylmethakrylatstangen durch direktes Polymerisieren des Methylmethakrylats in Glasgefäßen erzeugt werden. Die Glasgefäße sind, obwohl sie mit elastischen Dichtungen versehen sind, zu starr, um leicht den volumetrischen Schrumpfungen des polFmerisierenden Methylmethakrylats zu folgen, was zu Mängeln in der Polymethylmethakrylatmasse führt.There is known a method by which polymer / methyl methacrylate rods by polymerizing the methyl methacrylate directly in glass vessels. The glass vessels, although they are provided with elastic seals, are too rigid, around slightly the volumetric shrinkage of polymerizing methyl methacrylate to follow, which leads to deficiencies in the polymethyl methacrylate composition.

Das erfindungsgemäße Verfahren beseitigt den erwähnten Nachteil dadurch, daß, um Strukturmängel, die oft in der Masse des Polymerisats auftreten, zu beseitigen, das Monomere im Verhältnis von 40 - 50 % und bei einer Temperatur von 80 - 90° a vorpolymerisiert und dann die endgültige PoLymerisation in Zellen aus Kunststoff geeigneter Porosität in Wasserbädern bei einer Temperatur von 18 - 20° C 48 Stunden lang durchgeführt wird, wofür an sich bekannte polymerisationsauslösende und regelnde Zusätze verwendet werden.The method according to the invention eliminates the disadvantage mentioned by that, in order to eliminate structural defects which often occur in the bulk of the polymer, the monomer in the ratio of 40-50% and at a temperature of 80-90 ° a prepolymerized and then final polymerization in plastic cells suitable porosity in water baths at a temperature of 18-20 ° C for 48 hours long carried out becomes what is known per se polymerization initiator and regulatory additives can be used.

Im folgenden wird das erfindungsgemäße Verfahren anhand eines, Ausführungsbeispiels näher erläutert: In einem 3 Ltr.-Glaskolben werden 1,2 1 Methylmethakrylat und 1 bis 2 g Perophor eingeführt und ca.-30 Minuten lang auf 900 C erwärmt. Unter diesen Bedingungen wird das Monomere im Verhältnis von ca. 40 bis 50 % polymerisiert. Dann wird das Gemisch auf 200 C abgekühlt .In the following, the method according to the invention is based on an exemplary embodiment explained in more detail: In a 3 liter glass flask, 1.2 liters of methyl methacrylate and 1 Introduced up to 2 g perophore and heated to 900 ° C. for about 30 minutes. Under these Conditions, the monomer is polymerized in a ratio of approx. 40 to 50%. then the mixture is cooled to 200.degree.

iir die Vollendung der Polymerisation, die in einer Zelle aus Polyäthylen oder Celluloseacetat bei einer Temperatur von ca.for the completion of the polymerization, which takes place in a cell made of polyethylene or cellulose acetate at a temperature of approx.

20° C durchgeführt wird, werden in die Nonomer-Polymermasse 2 bis 5 g Benzoylperoxid und 4 bis 5 ml Dimethyl-anilin als einführende Zusätze und 4 bis 5 g Kobaltnaphtenat als Polymerisationsregler eingetragen.20 ° C is carried out, are in the nonomer polymer composition 2 to 5 g of benzoyl peroxide and 4 to 5 ml of dimethyl aniline as introductory additives and 4 up to 5 g cobalt naphtenate registered as a polymerization regulator.

Die durch die Reaktion zwischen dem Benzoyiperoxid und dem Dimethyl-antlin erzeugte Wärme reicht für die weitere Polymerisierungsreaktion bei der Wassertemperatur des Wasserbade, in welches die Polymerisierungszelle eingeführt wurde, aus.The result of the reaction between the benzoyiperoxide and the dimethyl-antlin The heat generated is sufficient for the further polymerization reaction at the water temperature of the water bath into which the polymerization cell was introduced.

Um ein günstigeres Gleichgewicht zwischen dem Schwinden des Polymethakrylats und der Kontraktion der Masse der Polymerisierungszelle zu erzielen,-wird diese, im Gegensatz zu den üblichen Glaspaltten, aus Kunststoff ausgeführt, wie z.B. aus Polyäthylen, Celluloseacetat etc.To find a more favorable balance between the shrinkage of the polymethacrylate and the contraction of the mass of the polymerisation cell, -will this, In contrast to the usual glass slits, made of plastic, such as Polyethylene, Cellulose acetate etc.

Die Polyäthylenzellen, welche mit der passenden Porosität ausgestattet werden können, sind vorgezogen, so daß das Wasser aus dem Wasserbad durch den Unterdruck infolge der in der Polymethakrylatmasse entstandenen Schwindungen in die Polymerisationszelle eindringen kann.The polyethylene cells, which are equipped with the appropriate porosity are preferred so that the water from the water bath through the negative pressure as a result of the shrinkage in the polymethacrylate mass in the polymerization cell can penetrate.

Das in die Polymerisationszellen eingeführte Vorpolymerisat ist, wie oben erwähnt, bei einer Temperatur von 18 - 200 C im Verlauf von ca. 48 Stunden vollständig polymerisiert. Aufgrund des Wasserfilma, der sich zwischen den inneren Wänden der Zelle und den entstandenen Polymethylmethakrylatstangen ausbildet, können diese leicht aus den Polyeerisationszellen ausgezogen werden.The prepolymer introduced into the polymerization cells is like mentioned above, at a temperature of 18 - 200 C in the course of approx. 48 hours completely polymerized. Because of the film of water between the inner Walls of the cell and the resulting polymethyl methacrylate rods can these can easily be pulled out of the polymerization cells.

Das erfindungsgemäße Verfahren besitzt also den Vorteil, die Qualitätsmängel auszuschliessen, die in der Masse des Polymerisats auftreten, wenn die Polymerisation in Zellen mit Glaswänden erfolgt.The method according to the invention therefore has the advantage of eliminating quality defects exclude that occur in the bulk of the polymer when the polymerization takes place in cells with glass walls.

Claims (1)

Patent anspruch Patent claim Verfahren zur Herstellung von Polymethylmethakrylat stangen, dadurch gekennzeichnet, daß Methylmethairylat in einem Verhältnis vom 40 - 50 % bei einer Temperatur von 80 - 90° C vorpolymerisiert und dann die endgültige Polymerisation in Kunststoffsellen geeigneter Porosität in Wasserbädern bei einer Temperatur von 18 - 200 C 48 Stunden lang durchgeführt wird, wofür an sich bekannte polymerisationsauslösende und regelnde Zusätze verwendet werden.Process for the production of polymethyl methacrylate rods, thereby characterized in that methyl methacrylate in a ratio of 40-50% at a Pre-polymerized at a temperature of 80 - 90 ° C and then the final polymerization in plastic cells of suitable porosity in water baths at a temperature of 18 - 200 C is carried out for 48 hours, for which per se known polymerization initiators and regulatory additives can be used.
DE19691920464 1969-04-22 1969-04-22 Poly (methylmethacrylate) rods Pending DE1920464A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE19691920464 DE1920464A1 (en) 1969-04-22 1969-04-22 Poly (methylmethacrylate) rods

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19691920464 DE1920464A1 (en) 1969-04-22 1969-04-22 Poly (methylmethacrylate) rods

Publications (1)

Publication Number Publication Date
DE1920464A1 true DE1920464A1 (en) 1970-11-12

Family

ID=5731960

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19691920464 Pending DE1920464A1 (en) 1969-04-22 1969-04-22 Poly (methylmethacrylate) rods

Country Status (1)

Country Link
DE (1) DE1920464A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2848906A1 (en) * 1977-11-11 1979-05-17 Asahi Chemical Ind SOLVENT RESISTANT ACRYLIC RESINS AND METHOD FOR MANUFACTURING THEM
DE4336594A1 (en) * 1993-10-27 1994-08-04 Klaus Reiser Expander and esp. exerciser for mouth chewing muscles

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2848906A1 (en) * 1977-11-11 1979-05-17 Asahi Chemical Ind SOLVENT RESISTANT ACRYLIC RESINS AND METHOD FOR MANUFACTURING THEM
DE4336594A1 (en) * 1993-10-27 1994-08-04 Klaus Reiser Expander and esp. exerciser for mouth chewing muscles

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