GB863812A - An apparatus for purifying crude benzene - Google Patents
An apparatus for purifying crude benzeneInfo
- Publication number
- GB863812A GB863812A GB11894/57A GB1189457A GB863812A GB 863812 A GB863812 A GB 863812A GB 11894/57 A GB11894/57 A GB 11894/57A GB 1189457 A GB1189457 A GB 1189457A GB 863812 A GB863812 A GB 863812A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reactor
- hydrogen
- gas
- chamber
- catalyst
- 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
- C07C7/00—Purification; Separation; Use of additives
- C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
- C07C7/163—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation
Abstract
<PICT:0863812/IV (b)/1> In the refining of crude benzene with hydrogen-containing gas in the presence of a catalyst which is a metal of Group 5, 6 or 8 or oxide thereof wherein unconsumed hydrogen is recycled the removal of nitric oxide and carbon monoxide if present from the make-up hydrogen-containing gas is effected in a conduit-like chamber arranged axially with and inside the reactor and filled with a further quantity of said catalyst and constructed in such a manner that the working pressure in the chamber may be different from that in the reactor, and the fresh gas is passed through the chamber, preferably at 10-16 atmospheres, and then brought to hydrofining pressure before being combined with recycle gas. Fresh hydrogen-containing gas enters by line 11, is partially compressed in the multistage compressor 12, heated and mixed with steam if carbon monoxide is present in the device 14, passed through the catalyst chamber 7 disposed within the reactor 1 and therefore heated by heat exchange with the reactants therein which are introduced at 310-320 DEG C. and are further heated in the reactor to 350-360 DEG C. The effluent may be cooled in the cooler 16 and is further compressed to 40-50 atmospheres before being mixed with recycle gas and vapourised impure benzene entering by line 4 at 310-320 DEG C. By performing the prior purification of the gas at a lower pressure than the hydrofining, the formation of polymerisation products by nitric oxide present (which is also removed by the purification) is prevented. Specification 844,380 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE863812X | 1956-04-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB863812A true GB863812A (en) | 1961-03-29 |
Family
ID=6801579
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB11894/57A Expired GB863812A (en) | 1956-04-18 | 1957-04-11 | An apparatus for purifying crude benzene |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB863812A (en) |
-
1957
- 1957-04-11 GB GB11894/57A patent/GB863812A/en not_active Expired
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