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 solventsInfo
- 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
Links
- 238000005660 chlorination reaction Methods 0.000 title claims description 10
- 229920000915 polyvinyl chloride Polymers 0.000 title claims description 7
- 239000004800 polyvinyl chloride Substances 0.000 title claims description 7
- 238000000034 method Methods 0.000 title claims description 6
- 239000002904 solvent Substances 0.000 title claims description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 13
- 239000000460 chlorine Substances 0.000 claims description 13
- 229910052801 chlorine Inorganic materials 0.000 claims description 13
- 239000007787 solid Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000003958 fumigation Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/18—Introducing halogen atoms or halogen-containing groups
- C08F8/20—Halogenation
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.
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)
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)
| 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 |
-
1959
- 1959-10-05 DE DEV17356A patent/DE1110873B/en active Pending
Cited By (2)
| 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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