GB968202A - Improvements in or relating to metal oxide sols and silica sols - Google Patents
Improvements in or relating to metal oxide sols and silica solsInfo
- Publication number
- GB968202A GB968202A GB1164861A GB1164861A GB968202A GB 968202 A GB968202 A GB 968202A GB 1164861 A GB1164861 A GB 1164861A GB 1164861 A GB1164861 A GB 1164861A GB 968202 A GB968202 A GB 968202A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sol
- sols
- aqueous
- formation
- ethyl
- 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
- 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
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
- C01B33/141—Preparation of hydrosols or aqueous dispersions
- C01B33/142—Preparation of hydrosols or aqueous dispersions by acidic treatment of silicates
- C01B33/143—Preparation of hydrosols or aqueous dispersions by acidic treatment of silicates of aqueous solutions of silicates
-
- 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
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/0004—Preparation of sols
- B01J13/0008—Sols of inorganic materials in water
- B01J13/0017—Sols of inorganic materials in water by extraction of ions from aqueous solutions
Abstract
Aqueous sols of polyvalent metals may have a particle size of 0.1-100mm and aqueous silica sols may have a particle size of 0.1-3 mm . Such aqueous sols may be prepared by contacting an aqueous solution of a metal salt or of an alkali metal silicate with a solution of an alkylamine or of an alkyl-phosphoric, -sulphuric or -carboxylic acid respectively in a water-immiscible organic solvent, allowing the phases to separate and removing the aqueous layer containing the sol. The formation of sols of SiO2, Cr2O3 and ThO2 respectively from sodium silicate, CrCl3 or Cr(NO2)3 and Th(NO2)4 solutions employing di-(2-ethyl-hexyl) phosphoric acid, di-tridecylamine and C18-C20 mixed primary amines or di-tridecylamine are exemplified. In each case 5 vol. per cent iso-decanol is present in the organic phase to avoid formation of third phases, and the organic solvent is kerosene. The metals Ni, Fe, Al, Ba, Ca, Cu, Mg and U are also mentioned; they may be present as nitrates, sulphates, phosphates, chlorides or other halides. Organic acids specified contain as alkyl groups, 2-ethyl hexyl, n-octyl, 3,5,5-trimethylhexyl, heptadecyl and 4 - ethyl - 1 - isobutyloctyl. Sulphuric or phosphoric acid may be used to regenerate these acids after sol formation. Bases which may be used may be primary, secondary and tertiary amines and quaternary ammonium compounds, trioctylmonomethylammonium hydroxide, trioctylamine, ditridecylamine and mixed isomers of primary amines of t.-C18H37NH2 to t.-C21H43NH2. After sol-formation the basic material may be regenerated with sodium carbonate. In addition to i-decanol, the alcohols 2-ethyl hexanol, 4-ethyl octanol, capryl alcohol, undecanol, diisobutyl carbonol, tetradecanol and trimethyl nonanol may be used to prevent the formation of a third phase. Organic solvents mentioned are hexane, kerosene, carbon tetrachloride, chloroform, benzene and polar solvents; solvents may be first scrubbed with sodium carbonate solution to avoid contamination. If so desired the sol formation may be carried out at above room temperature, up to 100 DEG C., this resulting in an increase in size of the particles. In a preferred embodiment, the aqueous salt solution and the organic solution are fed into a reaction zone containing a previously prepared seed sol. The aqueous phase may be fed at a constant or a logarithmic rate and the organic phase fed at a constant rate; a quiescent zone in the reaction zone provides for settling out of the phases and the organic phase may be recirculated after regeneration (e.g. by two-stage counter-current contact with sodium carbonate) and washing with water. The size of the particles may thus be built up, and sol thus produced made the seed material in further similar processes. In examples, single-stage processes produce Cr2O3 sols of particle diameter 6.2 and 9 mm and a ThO2 sol of 9.5 mm diameter and in successive stages a ThO2 sol had particle diameter of 9.5, 19.7, 35 and 56 mm . The sols of Specification 924,999 are disclaimed.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US1944960A | 1960-04-04 | 1960-04-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB968202A true GB968202A (en) | 1964-08-26 |
Family
ID=21793284
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1164861A Expired GB968202A (en) | 1960-04-04 | 1961-03-30 | Improvements in or relating to metal oxide sols and silica sols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB968202A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1912252A1 (en) * | 1968-03-12 | 1969-11-27 | Atomic Energy Authority Uk | Process for the production of mixed oxides |
CN113667843A (en) * | 2020-05-13 | 2021-11-19 | 厦门稀土材料研究所 | Method for separating thorium by using eutectic solvent |
-
1961
- 1961-03-30 GB GB1164861A patent/GB968202A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1912252A1 (en) * | 1968-03-12 | 1969-11-27 | Atomic Energy Authority Uk | Process for the production of mixed oxides |
CN113667843A (en) * | 2020-05-13 | 2021-11-19 | 厦门稀土材料研究所 | Method for separating thorium by using eutectic solvent |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS6058171B2 (en) | Method for extracting gallium using substituted hydroxyquinoline and organic compound containing sulfate or sulfonate groups | |
GB867450A (en) | Process for treating aqueous solutions containing oleaginous materials | |
GB968202A (en) | Improvements in or relating to metal oxide sols and silica sols | |
GB1507170A (en) | Method for increasing the lifetime of an extraction medium used for reprocessing spent nuclear fuel and/or breeder materials | |
US3582290A (en) | Metal extraction process | |
US3413082A (en) | Process for recovering zr-values from ores | |
US2449962A (en) | Dicyclohexylammonium nitrite and its preparation | |
GB1113634A (en) | Improvements in or relating to fungicidal compositions | |
US2415971A (en) | Stabilization of organic peroxides | |
US2847471A (en) | Method for purifying tetracycline | |
GB1463742A (en) | Purification of phosophoric acid by means of organic solvents | |
US3192196A (en) | Oxidation of aliphatic hydrazo compounds to the corresponding aliphatic azo compounds | |
US3808309A (en) | Purification of silica by preferential extraction | |
US2982785A (en) | Cesium recovery | |
US2615798A (en) | Extraction of cerium with an organic solvent | |
US2842563A (en) | Purification of 2-t-butylanthraquinone | |
US3095270A (en) | Method of separating silica from zirconium sulphate solutions | |
US2975185A (en) | Piperidinol compounds | |
DE1091994B (en) | Process for separating hydrofluoric acid from gas mixtures | |
US2832783A (en) | Preparation of piperazine adipate | |
RU2575028C1 (en) | Method for extractive separation of molybdenum from radioactive solutions | |
US2751325A (en) | Mercurial diuretic compositions and method of stabilization | |
US2899422A (en) | Purification of chlortetracycline | |
ES261071A1 (en) | Paints | |
US2117619A (en) | Process for the manufacture of ammonium dithiocarbamate |