GB858626A - Production of 2,3-dihydropyran - Google Patents
Production of 2,3-dihydropyranInfo
- Publication number
- GB858626A GB858626A GB35270/59A GB3527059A GB858626A GB 858626 A GB858626 A GB 858626A GB 35270/59 A GB35270/59 A GB 35270/59A GB 3527059 A GB3527059 A GB 3527059A GB 858626 A GB858626 A GB 858626A
- Authority
- GB
- United Kingdom
- Prior art keywords
- dihydropyran
- recycled
- weight
- carrier gas
- tetrahydrofurfuryl alcohol
- 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
- C07D—HETEROCYCLIC COMPOUNDS
- C07D309/00—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings
- C07D309/16—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member
- C07D309/18—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member containing only hydrogen and carbon atoms in addition to the ring hetero atom
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
Abstract
2.3-Dihydropyran is produced by contacting tetrahydrofurfuryl alcohol in the vapour phase at a temperature of 250-350 DEG C. with a catalyst comprising from 85 to 95% by weight of titanium dioxide and from 15% to 5% by weight of aluminium oxide. In a preferred method of carrying out the process the tetahydro furfuryl alcohol is vaporised in a vaporisation zone, entrained in a carrier gas and passed to the reaction zone; the product vapours are condensed, the carrier gas is recycled and dihydropyran is separated from unreacted tetrahydrofurfuryl alcohol, which is recycled. The preferred carrier gases are nitrogen and hydrogen.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US858626XA | 1953-10-28 | 1953-10-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB858626A true GB858626A (en) | 1961-01-11 |
Family
ID=22194457
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB35270/59A Expired GB858626A (en) | 1953-10-28 | 1959-10-19 | Production of 2,3-dihydropyran |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB858626A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0691337A1 (en) * | 1994-07-07 | 1996-01-10 | Basf Aktiengesellschaft | Process for the preparation of 3,4-dihydro-2H-pyran |
WO2002012219A1 (en) * | 2000-08-03 | 2002-02-14 | Basf Aktiengesellschaft | Method for producing 3,4-dihydro-2h-pyran |
-
1959
- 1959-10-19 GB GB35270/59A patent/GB858626A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0691337A1 (en) * | 1994-07-07 | 1996-01-10 | Basf Aktiengesellschaft | Process for the preparation of 3,4-dihydro-2H-pyran |
WO2002012219A1 (en) * | 2000-08-03 | 2002-02-14 | Basf Aktiengesellschaft | Method for producing 3,4-dihydro-2h-pyran |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB799876A (en) | Method of preparing pure silicon | |
US2756241A (en) | Ethylene oxide recovery | |
GB848924A (en) | Production of aliphatic nitriles from olefins | |
US2771473A (en) | Ethylene oxide recovery | |
GB858626A (en) | Production of 2,3-dihydropyran | |
US2416156A (en) | Production of hydrogen peroxide | |
US2492983A (en) | Methanol production | |
US3240790A (en) | Catalytic process for the preparation of 2, 3-dihydropyran from tetrahydrofurfuryl alcohol | |
ES388223A1 (en) | Process for recovering heat from gas mixtures obtained by the thermal cracking of hydrocarbons | |
US2325398A (en) | Process for the production of conjugated poly-olefins | |
US2678298A (en) | Extractive distillation of hydrazine with a glycol | |
GB915179A (en) | Process for producing titanium oxychloride with or without titanium dioxide | |
US2951878A (en) | Chlorinated olefins and method for producing same | |
GB791634A (en) | Process for the production of ethylene and its gaseous homologues | |
US3240791A (en) | Preparation of 2, 3-dihydropyran from tetrahydrofurfuryl alcohol | |
US2451712A (en) | Acrolein and ethylene by pyrolysis of dihydropyran | |
GB696489A (en) | Improvements in the manufacture of an alkyl nitrate | |
GB816973A (en) | Process for synthesis of pyridine and 3-picoline | |
US2710883A (en) | Succinaldehyde manufacture | |
GB769773A (en) | Improvements in the production of vinyl chloride from acetylene and hydrogen chloride | |
GB1328304A (en) | Process for the manufacture of carbon disulphide with recovery of sulphur | |
US2209699A (en) | Process for converting alcohol to | |
SU642282A1 (en) | Method of obtaining metallyl choride and dimethylvinylchloride | |
GB846511A (en) | Process for the treatment of gaseous mixtures of carbon dioxide and ammonia | |
GB975325A (en) | Concentrating nitric acid |