DE1667436A1 - Process for the production of fused silica with embedded activated carbon - Google Patents
Process for the production of fused silica with embedded activated carbonInfo
- Publication number
- DE1667436A1 DE1667436A1 DE19681667436 DE1667436A DE1667436A1 DE 1667436 A1 DE1667436 A1 DE 1667436A1 DE 19681667436 DE19681667436 DE 19681667436 DE 1667436 A DE1667436 A DE 1667436A DE 1667436 A1 DE1667436 A1 DE 1667436A1
- Authority
- DE
- Germany
- Prior art keywords
- activated carbon
- production
- hydrosol
- silica gel
- embedded
- 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
Classifications
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Silicon Compounds (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
\0e. (Z-beeltfiiaL /Ctdi\ 0e. (Z-beeltfiiaL / Ctdi
Patentanwalt Anw.-Akte: 75/66Patent attorney application file: 75/66
23. Januar 1968January 23, 1968
PATEITAIM ELD UIGPATEITAIM ELD UIG
Anmelder: Ceskoslovenska akademie ved, Praha 1 Applicant: Ceskoslovenska akademie ved, Praha 1
Verfahren zur Herstellung von Kieselgel mit eingelagerterProcess for the production of silica gel with embedded
AktivkohleActivated carbon
Die Erfindung betrifft ein Verfahren zur Herstellung von Kieselgel mit eingelagerter aktiver Kohle.The invention relates to a method for producing Silica gel with embedded active carbon.
Bekanntlich wird Kieselgel und aktive Kohle oder ihre mechanische Mischung als Adsorbent in verschiedenen Zweigen der Chemie benutzt« Eine besonders hohe Adsorptions-Kapazität wurde bei dem Kieselgel, das eingebaute aktive Kohle enthält, festgestellt. Siehe z.B. H. A. Fells und J. B» Hrt, J. Soc. Chem. Ind. 46, T39 (1927), I. SMIoν, M. Dubinin, S. Toropov, Kolloid, Z. 49, 120 (1929), Z. Z. Vyaockij und I. E. lejmark, Ukrain. Khim, Shur. 22, 485 (1956), B. R. Puri, S. Parkash und D, % Singh, J,-. BgU Has, (India);21B, 158 (1962),It is well known that silica gel and active charcoal or their mechanical mixture is used as an adsorbent in various branches of chemistry. A particularly high adsorption capacity was found with silica gel, which contains built-in active charcoal. See, for example, HA Fells and J. B »Hrt, J. Soc. Chem. Ind. 46, T39 (1927), I. SMIoν, M. Dubinin, S. Toropov, Kolloid, Z. 49, 120 (1929), ZZ Vyaockij and IE lejmark, Ukrain. Khim, Shur. 22, 485 (1956), BR Puri, S. Parkash and D, % Singh, J, -. BgU Has, (India); 21B, 158 (1962),
Ein solcher Stoff wurde jedoch bis jetzt in der Praxis als Adsorbent in verschiedenen Chromatographie-Zweigen noch nicht benutzt, wahrscheinlich deswegen, weil es nicht gelungen ist, ein Kieselgel mit eingelagerter aktiver Kohle zu erzeugen, welches die erforderliche Homogenität besitzt und außerdem vollkommen frei von anorganischen Salzen ist.However, such a substance has heretofore been known in practice as Adsorbent not yet used in various branches of chromatography, probably because it did not succeed is to produce a silica gel with embedded active carbon, which has the required homogeneity and is also completely free of inorganic salts.
φ Die bisher bekannten Verfahren zur Herstellung von Kieselgel mit eingelagerter Aktivkohle bestehen in der Einwirkung der Säuren auf die Mischung des Wasserglases und der-aktiven Kohle oder in der Wirkung des Zinkchlorids auf die mit Wasserglas getränkten Birkensägespäne. Diese Verfahren garantieren das Ausbleiben der störenden Salze in dem Endprodukt jedoch nicht.φ The previously known processes for the production of silica gel with embedded activated charcoal consist in the action of the acids on the mixture of the water glass and the active charcoal or in the effect of zinc chloride on those with water glass soaked birch sawdust. However, these processes do not guarantee that the interfering salts will not be present in the end product.
Die Aufgabe der Erfindung ist es deshalb, die bisher aufgetretenen Mängel bei der Herstellung und im Endprodukt von Kieselgel mit eingelagerter, diffundierter Aktivkohle auszuschalten, . ■ ■ .The object of the invention is therefore to address those that have occurred so far Eliminate deficiencies in the manufacture and in the end product of silica gel with embedded, diffused activated carbon, . ■ ■.
Die Erfindung beim Verfahren zur Herstellung von Kieselgel mit eingelagerter aktiver Kohle besteht darin, in das Hydrosol der Kieselsäure, welches auf ionenaustauschende Art erzeugt wurde,The invention in the method of making silica gel with embedded active charcoal consists in the hydrosol the silica, which was produced in an ion-exchanging manner,
"■■'"" -"■■■■- ' . - " - - 3 —"■■ '" "-" ■■■■ -'. - "- - 3 -
101825/tSS4101825 / tSS4
3 1067436 3 1067436
die aktive Kohle zu diffundieren und nach der Selbst umwandlung des Hydrosols in Hydrogel dieses zu trocknen und bei der Wärme von 105 - 1500C zu aktivieren.diffusing the active charcoal and after self-converting the hydrosol into hydrogel to dry this, and in the heat of 105 - 150 0 C to activate.
Die Umwandlung des Hydrosols in Hydrogel kann erfindungsgemäß durch den Zusatz von bekannten Reagenzien, ζ. B. der Ammoniumsalze, unterstützt werden. Das nach dem erfindungsgemäßen Verfahren hergestellte Kieselgel mit der eingelagerten aktiven Kohle ist sehr rein, homogen, frei von anorganischen Salzen, Es ist deshalb besonders gut in verschiedenen Chemie-Zweigen, vor allem in der Chromatografie verwendbar.The conversion of the hydrosol into hydrogel can according to the invention by the addition of known reagents, ζ. B. the ammonium salts, get supported. The silica gel produced by the process according to the invention with the incorporated active Coal is very pure, homogeneous, free of inorganic salts, It is therefore particularly useful in various branches of chemistry, especially in chromatography.
Das folgende Beispiel erläutert das Herstellungsverfahren gemäß der Erfindung:The following example illustrates the manufacturing process according to the invention:
Die Suspension der Aktivkohle (100 g).in Wasser (T Liter) wird beim intensiven Rühren bei 15-25°C in 60 Liter des Kieselsäure-Hydrosols (dessen Kieselsäuregehalt den 5 kg des Finalproduktes entspricht) gegeben und das Rühren wird eine weitere Stunde fortgesetzt. Die erhaltene Mischung wird dann in bekannter Art,d. h. spontan oder durch Zugabe von anorganischen Salzen, , in Hydrogel verwandelt. Das Hydrogel wird daraufhin bei einer Temperatur von 120 C bis zum Konstantgewicht getrocknet. Das Ergebnis:' 5 kg Kieselgels mit 2 # Aktivkohle in darin diffun- : dierter Form.The suspension of activated carbon (100 g) in water (T liter) is added to 60 liters of the silicic acid hydrosol (the silicic acid content of which corresponds to 5 kg of the final product) while stirring intensively at 15-25 ° C, and stirring is continued for another hour continued. The mixture obtained is then converted into hydrogel in a known manner, ie spontaneously or by adding inorganic salts. The hydrogel is then dried at a temperature of 120 ° C. to constant weight. The result: '5 kg silica gel with 2 # activated carbon therein diffuses: dierter form.
109825/ ISS4 -I-109825 / ISS4 -I-
ORIGINAL INSPECTlDORIGINAL INSPECTlD
Claims (2)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS64767 | 1967-01-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
DE1667436A1 true DE1667436A1 (en) | 1971-06-16 |
Family
ID=5338943
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19681667436 Pending DE1667436A1 (en) | 1967-01-27 | 1968-01-25 | Process for the production of fused silica with embedded activated carbon |
Country Status (8)
Country | Link |
---|---|
AT (1) | AT279560B (en) |
BE (1) | BE709608A (en) |
CH (1) | CH499460A (en) |
DE (1) | DE1667436A1 (en) |
FR (1) | FR1554075A (en) |
GB (1) | GB1188873A (en) |
NL (1) | NL6801237A (en) |
SE (1) | SE344195B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2855251A1 (en) * | 1978-12-21 | 1980-07-03 | Mittex Ag | METHOD AND DEVICE FOR PRODUCING SILICONE GEL |
DE3015439A1 (en) * | 1980-04-22 | 1981-10-29 | Bayer Ag, 5090 Leverkusen | Silica gel-contg. active carbon granulate - quickly disintegrating in aq. system and used for purifying liquids. and esp. fining alcoholic drinks |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1371440A (en) * | 1972-05-31 | 1974-10-23 | Mo G Uni Im Mv Lomonosova | Process for preparing a wide-pore adsorbent for use in chromato graphy |
GB1539735A (en) * | 1975-06-13 | 1979-01-31 | Ici Ltd | Adsorbent material |
GB2118534B (en) * | 1982-04-15 | 1985-10-09 | South African Inventions | Electronically conductive tectosilicates |
IT1197667B (en) * | 1983-06-24 | 1988-12-06 | Enea | STATIONARY PHASES FOR CHROMATOGRAPHY AND PREPARATION PROCEDURE OF THE SAME |
DE4216867A1 (en) * | 1992-05-22 | 1993-11-25 | Solvay Catalysts Gmbh | Sorption of organic compounds from gases |
DE4343358A1 (en) * | 1993-12-18 | 1995-06-22 | Hasso Von Bluecher | Porous adsorbent plate or moulding useful as filter esp. for gas purification |
-
1968
- 1968-01-19 BE BE709608D patent/BE709608A/xx unknown
- 1968-01-19 FR FR1554075D patent/FR1554075A/fr not_active Expired
- 1968-01-24 CH CH105568A patent/CH499460A/en not_active IP Right Cessation
- 1968-01-24 GB GB373268A patent/GB1188873A/en not_active Expired
- 1968-01-25 DE DE19681667436 patent/DE1667436A1/en active Pending
- 1968-01-26 NL NL6801237A patent/NL6801237A/xx unknown
- 1968-01-26 SE SE106568A patent/SE344195B/xx unknown
- 1968-01-26 AT AT00797/68A patent/AT279560B/en not_active IP Right Cessation
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2855251A1 (en) * | 1978-12-21 | 1980-07-03 | Mittex Ag | METHOD AND DEVICE FOR PRODUCING SILICONE GEL |
DE3015439A1 (en) * | 1980-04-22 | 1981-10-29 | Bayer Ag, 5090 Leverkusen | Silica gel-contg. active carbon granulate - quickly disintegrating in aq. system and used for purifying liquids. and esp. fining alcoholic drinks |
Also Published As
Publication number | Publication date |
---|---|
BE709608A (en) | 1968-05-30 |
AT279560B (en) | 1970-03-10 |
CH499460A (en) | 1970-11-30 |
NL6801237A (en) | 1968-07-29 |
SE344195B (en) | 1972-04-04 |
FR1554075A (en) | 1969-01-17 |
GB1188873A (en) | 1970-04-22 |
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