DE919666C - Process for the production of synthetic resin exchangers bearing carbonic acid groups on a phenolic basis - Google Patents
Process for the production of synthetic resin exchangers bearing carbonic acid groups on a phenolic basisInfo
- Publication number
- DE919666C DE919666C DEF11773D DEF0011773D DE919666C DE 919666 C DE919666 C DE 919666C DE F11773 D DEF11773 D DE F11773D DE F0011773 D DEF0011773 D DE F0011773D DE 919666 C DE919666 C DE 919666C
- Authority
- DE
- Germany
- Prior art keywords
- carbonic acid
- basis
- synthetic resin
- production
- acid groups
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G8/00—Condensation polymers of aldehydes or ketones with phenols only
- C08G8/28—Chemically modified polycondensates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/08—Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/16—Organic material
- B01J39/18—Macromolecular compounds
- B01J39/19—Macromolecular compounds obtained otherwise than by reactions only involving unsaturated carbon-to-carbon bonds
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
(WiGBl. S. 175)(WiGBl. P. 175)
AUSGEGEBEN AM 2. NOVEMBER 1954ISSUED NOVEMBER 2, 1954
F ιΐγγ3IV c 139 cF ιΐγγ3IV c 139 c
(Ges. v. 15. 7. 51)(Ges. V. July 15, 51)
Es ist bekannt, daß Carbonsäuregruppen tragende Kunstharzgele als Kationenaustauscher Verwendung finden.It is known that synthetic resin gels carrying carboxylic acid groups are used as cation exchangers Find.
Es wurde nun gefunden, daß man überraschenderweise derartige Produkte in besonders einfacher und vorteilhafter Weise herstellen kann, wenn man Phenolaldehydharze vorzugsweise in Form von Gallerten bei erhöhter Temperatur mit Kohlensäure und bzw. oder Kohlensäure abgebenden Stoffen, z. B. Bicarbonaten, behandelt. Je nach Art des Ausgangsmaterials, der Temperatur, des Drucks und der Behandlungszeit treten dabei wechselnde Mengen von Carbonsäuregruppen in das Harzmolekül ein, so daß man auf diese Weise Austauschermaterialien mit ausreichender Kapazität leicht gewinnen kann. Die Harzgrundkörper können auf der Grundlage von ein- oder mehrwertigen Phenolen hergestellt sein, d. h. sie können an sich kationenaktiver oder inaktiver Natur sein. Auch geeignete Substitutionsprodukte der phenolischen Ausgangsmaterialien können bei der Herstellung des Grundkörpers verwendet werden. Die zu behandelnden Harzgrundkörper werden den gewählten Reaktionsbedingungen entsprechend angewendet, d. h. es ist gegebenenfalls zweckmäßig, sie mit Alkali zu beladen. It has now been found that, surprisingly, such products can be obtained in a particularly simple manner and can advantageously be prepared if phenol aldehyde resins are preferably used in the form of Jellied at elevated temperature with carbonic acid and / or substances emitting carbonic acid, z. B. bicarbonates treated. Depending on the type of starting material, the temperature, the pressure and During the treatment time, varying amounts of carboxylic acid groups enter the resin molecule so that exchange materials with sufficient capacity can easily be obtained in this way can. The resin base can be based on monohydric or polyhydric phenols be manufactured, d. H. they can be cation-active or inactive in nature. Also suitable Substitution products of the phenolic starting materials can be used in the manufacture of the base body be used. The resin base bodies to be treated are used in accordance with the selected reaction conditions, d. H. it is it may be useful to load them with alkali.
Eine Lösung aus 440 Teilen Resorcin und 10 Teilen Ätznatron in 400 Teilen Wasser wird bei 200 CA solution of 440 parts of resorcinol and 10 parts of caustic soda in 400 parts of water at 20 0 C
unter Kühlung mit 520 Teilen 3ö°/oigem Formalin in der Weise versetzt, daß man eine Reaktionstemperatur von ioo° C erreicht. Nach 2stündigem Stehen der so erhaltenen Harzgallerte wird das Produkt auf eine Korngröße von etwa 0,5 bis 2 cm 0 zerkleinert und mit 2000 Teilen Wasser, 440 Teilen Natriumbicarbonat und 500 Teilen Kohlensäure im Autoklav während 5 Stunden erhitzt. Hält man bei dieser Arbeitsweise die Temperatur auf no0 C, so erhält man ein kationenaustauschendes Harz, welches als Wasserstoffionenaustauscher eine Volumenleistung von 0,24'1Vo Ca O aufweist. Steigert man die Temperatur auf 1300 C, so weist das erhaltene Produkt eine Kapazität von o,30fl/oCaO auf, während man bei 1500C ein Material mit einer Volumenkapazität von r,o8°/o CaO erhält.520 parts of 30% formalin are added while cooling in such a way that a reaction temperature of 100 ° C. is reached. After the resin jelly thus obtained has stood for 2 hours, the product is comminuted to a particle size of about 0.5 to 2 cm and heated with 2000 parts of water, 440 parts of sodium bicarbonate and 500 parts of carbonic acid in an autoclave for 5 hours. If the temperature is kept at 0 ° C. in this procedure, a cation-exchanging resin is obtained which, as a hydrogen ion exchanger, has a volume performance of 0.24% 1 % by volume of CaO. The temperature is increased to 130 0 C, so the obtained product has a capacity of o, 30 fl / oCaO, while a material is obtained with a volume capacity of r, o8 ° / o CaO at 150 0 C.
Claims (1)
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEF11773D DE919666C (en) | 1941-10-29 | 1941-10-29 | Process for the production of synthetic resin exchangers bearing carbonic acid groups on a phenolic basis |
NL107566A NL59524C (en) | 1941-10-29 | 1942-09-03 | |
FR886704D FR886704A (en) | 1941-10-29 | 1942-10-09 | Manufacturing process of synthetic resin exchangers on a phenolic basis, carrying groups of carboxylic acids |
BE447562D BE447562A (en) | 1941-10-29 | 1942-10-15 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEF11773D DE919666C (en) | 1941-10-29 | 1941-10-29 | Process for the production of synthetic resin exchangers bearing carbonic acid groups on a phenolic basis |
Publications (1)
Publication Number | Publication Date |
---|---|
DE919666C true DE919666C (en) | 1954-11-02 |
Family
ID=7086833
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEF11773D Expired DE919666C (en) | 1941-10-29 | 1941-10-29 | Process for the production of synthetic resin exchangers bearing carbonic acid groups on a phenolic basis |
Country Status (4)
Country | Link |
---|---|
BE (1) | BE447562A (en) |
DE (1) | DE919666C (en) |
FR (1) | FR886704A (en) |
NL (1) | NL59524C (en) |
-
1941
- 1941-10-29 DE DEF11773D patent/DE919666C/en not_active Expired
-
1942
- 1942-09-03 NL NL107566A patent/NL59524C/xx active
- 1942-10-09 FR FR886704D patent/FR886704A/en not_active Expired
- 1942-10-15 BE BE447562D patent/BE447562A/fr unknown
Also Published As
Publication number | Publication date |
---|---|
FR886704A (en) | 1943-10-22 |
BE447562A (en) | 1942-11-30 |
NL59524C (en) | 1947-06-16 |
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