GB659981A - A process for refining synthetic alcohols - Google Patents
A process for refining synthetic alcoholsInfo
- Publication number
- GB659981A GB659981A GB27600/49A GB2760049A GB659981A GB 659981 A GB659981 A GB 659981A GB 27600/49 A GB27600/49 A GB 27600/49A GB 2760049 A GB2760049 A GB 2760049A GB 659981 A GB659981 A GB 659981A
- Authority
- GB
- United Kingdom
- Prior art keywords
- nickel
- per cent
- silicate
- precipitated
- carrier
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/88—Separation; Purification; Use of additives, e.g. for stabilisation by treatment giving rise to a chemical modification of at least one compound
- C07C29/90—Separation; Purification; Use of additives, e.g. for stabilisation by treatment giving rise to a chemical modification of at least one compound using hydrogen only
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
The refining of synthetic alcohols by hydrogenation is carried out in the presence of a stationary catalyst containing at least 25 per cent, preferably at least 35 per cent, of nickel (by weight), calculated as metallic nickel on a carrier, in the preparation of which the nickel has been partially precipitated in the form of a silicate. The following materials can be used as carriers: sintered kieselguhr, aluminium oxide, magnesium silicate, magnesium carbonate, barium sulphate, pumice stone, kaolin, activated carbon and particularly natural or artificial aluminium oxides; metallic carriers such as aluminium and acid-treated or non-acid-treated clay. The nickel may be precipitated, in the presence of the carrier, from a solution by using an alkaline agent such as sodium hydroxide or carbonate in the presence of a soluble silicate in order to precipitate the nickel partly in the form of a silicate. It is also possible to p precipitate the nickel first, to separate and dry the precipitate and mix it with the carrier. The mixture can be pressed into pellets, cylinders, rings or other suitable bodies. Before or after being compressed into suitably shaped lumps the nickel can be liberated from its compound as an oxide which is subsequently reduced. Preferably 20 to 60 per cent of the nickel is precipitated as silicate. The temperature and pressure at which the refining is carried out depends on the type of initial material. The catalyst can be regenerated by oxidation treatment, for example with a mixture of air and steam, and then reduced. In the example a C9 alcohol obtained by the oxo-reaction is refined by hydrogenation in the presence of a catalyst consisting of 40 per cent Ni, 11.2 per cent SiO2 and 48 per cent Al2O3.ALSO:In the refining of synthetic alcohols by catalytic hydrogenation the catalyst consists of at least 25 per cent of nickel by weight calculated as metallic nickel on a carrier, part of the nickel having been precipitated as a silicate. The following materials may be used as carriers: sintered kieselguhr, aluminium oxide, magnesium silicate, magnesium carbonate, barium sulphate, pumice stone, kaolin, activated carbon and particularly natural or artificial aluminium oxides, metallic carriers such as aluminium, and acid-treated or non-acid-treated clay. The nickel may be precipitated in the presence of the carrier from a solution by using an alkaline agent such as sodium hydroxide or carbonate in addition to a soluble silicate so that the nickel is precipitated partly as silicate. It is also possible to precipitate the nickel first, to separate and dry the precipitate and mix it with the carrier. The mixture can be pressed into pellets, cylinders, rings or other suitable bodies. Before or after being compressed into suitably shaped lumps the nickel can be liberated from its compound as an oxide which is subsequently reduced. Preferably 20 to 60 per cent of the nickel is precipitated as silicate. The catalyst may be regenerated by oxidation, for example with a mixture of air and steam and then reduced. In the example a C9 alcohol obtained by the OXO-reaction is refined by hydrogenation in the presence of a catalyst consisting of 40 per cent Ni, 11.2 per cent SiO2 and 48.8 per cent Al2O3. p
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NL659981X | 1948-12-17 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB659981A true GB659981A (en) | 1951-10-31 |
Family
ID=19795362
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB27600/49A Expired GB659981A (en) | 1948-12-17 | 1949-10-27 | A process for refining synthetic alcohols |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB659981A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1221619B (en) * | 1961-03-13 | 1966-07-28 | Shell Int Research | Process for purifying ketone compounds |
| DE1270539B (en) * | 1964-11-09 | 1968-06-20 | Ethyl Corp | Process for the purification of primary alcohols produced by the hydrolysis of aluminum alkoxides |
| US5888923A (en) * | 1996-04-15 | 1999-03-30 | Dairen Chemical Corporation | Modified Raney nickel catalyst and a process for preparing diols by using the same |
| CN111215107A (en) * | 2018-11-26 | 2020-06-02 | 中国科学院大连化学物理研究所 | Catalyst for preparing alcohol by aldehyde hydrogenation with high selectivity and preparation method thereof |
-
1949
- 1949-10-27 GB GB27600/49A patent/GB659981A/en not_active Expired
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1221619B (en) * | 1961-03-13 | 1966-07-28 | Shell Int Research | Process for purifying ketone compounds |
| DE1270539B (en) * | 1964-11-09 | 1968-06-20 | Ethyl Corp | Process for the purification of primary alcohols produced by the hydrolysis of aluminum alkoxides |
| DE1270539C2 (en) * | 1964-11-09 | 1973-05-10 | Ethyl Corp | Process for the purification of primary alcohols produced by the hydrolysis of aluminum alkoxides |
| US5888923A (en) * | 1996-04-15 | 1999-03-30 | Dairen Chemical Corporation | Modified Raney nickel catalyst and a process for preparing diols by using the same |
| CN111215107A (en) * | 2018-11-26 | 2020-06-02 | 中国科学院大连化学物理研究所 | Catalyst for preparing alcohol by aldehyde hydrogenation with high selectivity and preparation method thereof |
| CN111215107B (en) * | 2018-11-26 | 2023-05-16 | 中国科学院大连化学物理研究所 | Catalyst for preparing alcohols by aldehyde hydrogenation with high selectivity and preparation method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2456072A (en) | Conversion of hydrocarbons in the presence of a catalyst and calcium oxide together with steam and/or carbon dioxide | |
| US2551580A (en) | Acid-treated clay catalyst for cracking hydrocarbons | |
| GB659981A (en) | A process for refining synthetic alcohols | |
| US2457719A (en) | Preparation of extruded iron oxide catalysts | |
| US3175021A (en) | Production of 2-methyl-2-pentene | |
| US2147780A (en) | Production of hydrogen | |
| GB899653A (en) | Improvements relating to the hydrogenation of gasolines | |
| US2340698A (en) | Catalytic cracking | |
| US2760939A (en) | Silica-magnesia catalyst having improved regeneration characteristics | |
| GB520829A (en) | Manufacture of sintered calcium oxide | |
| GB1328455A (en) | Catalysts and their use for dehydrogenating saturated hydrocarbons | |
| GB953877A (en) | Catalysts and their use in a hydrocarbon steam reforming process | |
| GB611987A (en) | Improvements in and relating to catalysts | |
| US2393080A (en) | Charge preparation | |
| GB731917A (en) | Manufacture of 2-ethyl-hexanal-(1) and 2-ethyl-hexanol-(1) | |
| US2485927A (en) | Catalytic dehydrogenation of hydrocarbons | |
| GB999255A (en) | Novel unsaturated alcohols and a process for the preparation thereof | |
| US2213131A (en) | Purification of masses containing calcium hydroxide | |
| GB939213A (en) | Method of making a nickel-magnesium hydrocarbon-steam reforming catalyst | |
| ES300055A1 (en) | Improvements in or relating to steam reforming catalysts | |
| GB1109306A (en) | Process for preparing catalysts | |
| GB397295A (en) | Improvements in and relating to catalysts | |
| GB518392A (en) | Process for the hydrogenation of octenes | |
| US2738361A (en) | Preparation of iron catalysts for carbon monoxide hydrogenation | |
| GB1118939A (en) | Catalytic cracking of gaseous and/or vaporisable hydrocarbons containing two to thirty carbon atoms |