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DE1110873B - Process for the chlorination of polyvinyl chloride without the use of solvents - Google Patents

Process for the chlorination of polyvinyl chloride without the use of solvents

Info

Publication number
DE1110873B
DE1110873B DEV17356A DEV0017356A DE1110873B DE 1110873 B DE1110873 B DE 1110873B DE V17356 A DEV17356 A DE V17356A DE V0017356 A DEV0017356 A DE V0017356A DE 1110873 B DE1110873 B DE 1110873B
Authority
DE
Germany
Prior art keywords
chlorination
polyvinyl chloride
solvents
chlorine
temperature
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
DEV17356A
Other languages
German (de)
Inventor
Horst Heinrich
Dr Felix Seidel
Walter Singer
Hans Springer
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.)
Filmfabrik Wolfen VEB
Original Assignee
Filmfabrik Wolfen VEB
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 Filmfabrik Wolfen VEB filed Critical Filmfabrik Wolfen VEB
Priority to DEV17356A priority Critical patent/DE1110873B/en
Priority claimed from FR830729A external-priority patent/FR1272026A/en
Publication of DE1110873B publication Critical patent/DE1110873B/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • C08F8/00Chemical modification by after-treatment
    • C08F8/18Introducing halogen atoms or halogen-containing groups
    • C08F8/20Halogenation

Landscapes

  • Chemical & Material Sciences (AREA)
  • General 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

Bekanntlich können die Eigenschaften des durch Polymerisation des monomeren Vinylchlorids erhältlichen Polyvinylchlorids durch Erhöhung seines ursprünglichen Chlorgehaltes von etwa 54 auf ungefähr 64% durch nachträgliche Chlorierung in verschiedener Hinsicht verbessert werden. Diese Nachchlorierung erfolgt bei allen jetzt bekannten technischen Verfahren in geeigneten Flüssigkeiten und erfordert auf umständliche Weise die Isolierung des nachchlorierten Produktes, seine Trocknung und insbesondere die Wiedergewinnung und Aufarbeitung der eingesetzten Flüssigkeiten bzw. Lösungsmittel. Insofern hat es nicht an Versuchen gefehlt, im Zusammenhang mit dieser Nachchlorierung den dafür nötigen großen Aufwand für die einzelnen Phasen dieses Prozesses einzuschränken. Es werden daher Verfahren beschrieben, unter Einsparung an Chemikalien in Suspension zu arbeiten, wobei sogar schließlich als Hauptkomponente Wasser neben geringen Mengen organischer Flüssigkeiten als Quellmittel in Vorschlag gebracht wurde. Bei der Weiterführung dieser prinzipiellen Vereinfachung wurde auf die Verwendung von Flüssigkeiten bei dieser Nachchlorierung verzichtet und die Nachchlorierung des Polyvinylchlorids in großoberflächiger Form bei erhöhter Temperatur mit gasförmigem Chlor beschrieben. Danach soll die Temperatur möglichst hoch gewählt und nur durch die Sintertemperatur des Pulvers begrenzt werden; d. h., man steigert die Reaktionstemperatur von 110 auf 180° C.It is known that the properties of the vinyl chloride can be obtained by polymerizing the monomeric vinyl chloride Polyvinyl chloride by increasing its original chlorine content from about 54 to about 64% can be improved in various ways by subsequent chlorination. This post-chlorination takes place in all now known technical processes in suitable liquids and requires the isolation of the post-chlorinated product, its drying and cumbersome way in particular the recovery and processing of the liquids or solvents used. In this respect there has been no lack of attempts in connection with this post-chlorination to limit the great effort required for the individual phases of this process. It will therefore Process described to work while saving chemicals in suspension, and even finally as the main component water in addition to small amounts of organic liquids as a swelling agent in Proposal was brought. In the continuation of this basic simplification, the The use of liquids in this post-chlorination is dispensed with and the post-chlorination of polyvinyl chloride described in large-surface form at elevated temperature with gaseous chlorine. Thereafter, the temperature should be selected as high as possible and only by the sintering temperature of the Powder limited; d. That is, the reaction temperature is increased from 110 to 180 ° C.

Es wurde nun im Gegensatz zu diesen Angaben, daß die Chloraufnahme des Polyvinylchlorids um 110° C noch gering ist, gefunden, daß sie bereits bei Raumtemperatur erheblich ist; es ist also nicht erforderlich, Temperaturen über 110° C zu wählen. Dies ist von erheblicher technischer Bedeutung. Man kann ferner den Verlauf der Chlorierung bei diesen niedrigeren Temperaturen durch UV-Licht noch beträchtlich beschleunigen.In contrast to this information, it has now been found that the chlorine uptake of the polyvinyl chloride is around 110 ° C is still low, found that it is already considerable at room temperature; so it is not necessary Temperatures above 110 ° C should be selected. This is of considerable technical importance. Man Furthermore, the course of the chlorination at these lower temperatures by UV light can still be considerable accelerate.

Beispielexample

In einem Drehrohr aus Jenaer Geräteglas (Durchmesser 55 mm, Länge der benutzten Strecke 1100 mm, 3Umdr./Min., 3,8 ml Chlor/Sekunde) wird 1,0 kg Verfahren zur ChlorierungIn a rotating tube made of Jena device glass (diameter 55 mm, length of the route used 1100 mm, 3 revs / min., 3.8 ml chlorine / second) 1.0 kg process for chlorination

von Polyvinylchlorid ohne Verwendungof polyvinyl chloride without use

von Lösungsmittelnof solvents

Anmelder:Applicant:

VEB Farbenfabrik Wolfen,
Wolfen (Kr. Bitterfeld)
VEB paint factory Wolfen,
Wolfen (district of Bitterfeld)

Dr. Felix Seidel, Wolfen (Kr. Bitterfeld),
Walter Singer, Berlin-Treptow,
Dr. Felix Seidel, Wolfen (district of Bitterfeld),
Walter Singer, Berlin-Treptow,

Hans Springer, Jeßnitz (Kr. Bitterfeld),Hans Springer, Jeßnitz (district of Bitterfeld),

und Horst Heinrich, Greppin (Kr. Bitterfeld),and Horst Heinrich, Greppin (Kr.Bitterfeld),

sind als Erfinder genannt wordenhave been named as inventors

trockenes Polyvinylchlorid 17,5 Stunden bei 25° C und Einstrahlung von UV-Licht mit Chlor begast. Ohne äußerlich erkennbare Veränderungen ist der ursprüngliche Chlorgehalt von ungefähr 54 auf etwa 64% gestiegen. Nach der beendeten Begasung beträgt der Chlorgehalt des Produktes an der Eintrittsstelle des Chlors 64,65 bzw. 64,31% und an der Austrittsstelle von Chlor und Chlorwasserstoff 65,38 bzw. 65,20%. Wird für denselben Versuch die Temperatur von 75 bis 80° C gewählt, so ist der Chlorgehalt des Produktes an der Eintrittsstelle des Chlors 66,63 bzw. 66,75% und an der Austrittsstelle von Chlor und Chlorwasserstoff 66,98 bzw. 67,35 %.dry polyvinyl chloride fumigated with chlorine for 17.5 hours at 25 ° C and exposure to UV light. Without any externally noticeable changes, the original chlorine content is around 54 increased about 64%. After the end of the fumigation, the chlorine content of the product is at the point of entry of the chlorine 64.65 or 64.31% and at the point of exit of chlorine and hydrogen chloride 65.38 and 65.20%, respectively. If a temperature of 75 to 80 ° C is chosen for the same experiment, the chlorine content is of the product at the point of entry of the chlorine 66.63 or 66.75% and at the point of exit of Chlorine and hydrogen chloride 66.98 and 67.35%, respectively.

Claims (1)

PATENTANSPRUCH:PATENT CLAIM: Verfahren zur Chlorierung von Polyvinylchlorid in fester, großoberflächiger Form ohne Verwendung von Lösungsmitteln durch Behändem mit gasförmigem Chlor, dadurch gekennzeichnet, daß man bei einer Temperatur von unter 100° C, gegebenenfalls unter Einwirkung von UV-Licht, chloriert.Process for the chlorination of polyvinyl chloride in solid, large-surface form without the use of solvents by handling with gaseous chlorine, characterized in that chlorination is carried out at a temperature of below 100 ° C., optionally under the action of UV light.
DEV17356A 1959-10-05 1959-10-05 Process for the chlorination of polyvinyl chloride without the use of solvents Pending DE1110873B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEV17356A DE1110873B (en) 1959-10-05 1959-10-05 Process for the chlorination of polyvinyl chloride without the use of solvents

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEV17356A DE1110873B (en) 1959-10-05 1959-10-05 Process for the chlorination of polyvinyl chloride without the use of solvents
FR830729A FR1272026A (en) 1960-06-22 1960-06-22 Chlorination process of polyvinyl chloride without the use of solvent

Publications (1)

Publication Number Publication Date
DE1110873B true DE1110873B (en) 1961-07-13

Family

ID=26001407

Family Applications (1)

Application Number Title Priority Date Filing Date
DEV17356A Pending DE1110873B (en) 1959-10-05 1959-10-05 Process for the chlorination of polyvinyl chloride without the use of solvents

Country Status (1)

Country Link
DE (1) DE1110873B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1259573B (en) * 1965-08-03 1968-01-25 Toa Gosei Kagaku Kogyo Kabushi Process for the chlorination of dry, powdery polyvinyl chloride
US3510416A (en) * 1968-07-20 1970-05-05 Manifattura Ceramica Pozzi Spa Process for the dry chlorination of polyvinyl chloride in the presence of gaseous hydrogen

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1259573B (en) * 1965-08-03 1968-01-25 Toa Gosei Kagaku Kogyo Kabushi Process for the chlorination of dry, powdery polyvinyl chloride
US3510416A (en) * 1968-07-20 1970-05-05 Manifattura Ceramica Pozzi Spa Process for the dry chlorination of polyvinyl chloride in the presence of gaseous hydrogen

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