GB625570A - - Google Patents
Info
- Publication number
- GB625570A GB625570A GB625570DA GB625570A GB 625570 A GB625570 A GB 625570A GB 625570D A GB625570D A GB 625570DA GB 625570 A GB625570 A GB 625570A
- Authority
- GB
- United Kingdom
- Prior art keywords
- xylene
- xylenes
- cooled
- fraction
- overhead
- 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.)
- Active
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
- C07C15/02—Monocyclic hydrocarbons
- C07C15/067—C8H10 hydrocarbons
- C07C15/08—Xylenes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2729—Changing the branching point of an open chain or the point of substitution on a ring
- C07C5/2732—Catalytic processes
- C07C5/2735—Catalytic processes with metal oxides
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2729—Changing the branching point of an open chain or the point of substitution on a ring
- C07C5/2732—Catalytic processes
- C07C5/274—Catalytic processes with inorganic acids; with salts or anhydrides of acids
- C07C5/2748—Acids of halogen; Salts thereof
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2729—Changing the branching point of an open chain or the point of substitution on a ring
- C07C5/2732—Catalytic processes
- C07C5/274—Catalytic processes with inorganic acids; with salts or anhydrides of acids
- C07C5/2748—Acids of halogen; Salts thereof
- C07C5/2751—Metal halides; Complexes thereof with organic compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/005—Processes comprising at least two steps in series
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
625,570. Distilling and crystallizing xylene. ANGLO-IRANIAN OIL CO., Ltd., BIRCH, S. F., FIDLER, F. A., and HARESNAPE, J. N. April 12, 1946, No. 11295. [Class 32] [Also in Group IV (b)] p-Xylene is obtained from an aromatic hydrocarbon mixture derived from coal tar or petroleum and boiling within 135-150‹ C. by separating by fractional distillation and/or low temperature filtration a fraction enriched in p-xylene, and a fraction enriched in o- and/or m-xylene, subjecting at least part of the latter to catalytic isomerization to convert part of the o- and/or m-xylene to p-xylene, and recovering p-xylene by fractional distillation and/or low temperature filtration. The aromatic fraction may be fractionated to give an overhead boiling up to 137‹ or 138‹ C. containing the ethyl benzene, a 138-139.5‹ C. fraction containing p-xylene and a residue of mainly o- and m-xylenes. The intermediate fraction is cooled to 0‹ to - 50‹ C. to crystallize p-xylene, and the residue passed with the o- and m-xylenes to the isomerization. Alternatively, ethyl benzene may be separated, the remaining xylenes cooled to - 40‹ to - 50‹ C. to crystallize p-xylene, and the mother liquors passed to the isomerization or an overhead containing ethyl benzene, p- and m-xylenes, an intermediate cut rich in m-xylene, and a residue containing o-xylene may be separated, the overhead cooled to crystallize p-xylene and the mother liquors fractionated to give ethyl benzene overhead, an intermediate containing m- and p-xylenes, and a residue concentrated in m-xylene, the intermediate cut being cooled to separate pxylene and the mother liquors fed with the first intermediate cut to the isomerization.
Publications (1)
Publication Number | Publication Date |
---|---|
GB625570A true GB625570A (en) |
Family
ID=1749681
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB625570D Active GB625570A (en) |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB625570A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2879313A (en) * | 1953-09-17 | 1959-03-24 | Union Oil Co | Process for converting a xylene feed mixture to para-xylene and styrene |
US2959626A (en) * | 1957-07-15 | 1960-11-08 | Cosden Petroleum Corp | Process for the production of styrenegrade ethyl benzene |
-
0
- GB GB625570D patent/GB625570A/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2879313A (en) * | 1953-09-17 | 1959-03-24 | Union Oil Co | Process for converting a xylene feed mixture to para-xylene and styrene |
US2959626A (en) * | 1957-07-15 | 1960-11-08 | Cosden Petroleum Corp | Process for the production of styrenegrade ethyl benzene |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101553454B1 (en) | Method and apparatus for obtaining aromatics from diverse feedstock | |
US7371912B2 (en) | Process for making xylene isomer using a deheptanizer with a side draw recycle | |
JP5876883B2 (en) | Method for producing para-xylene | |
KR101501049B1 (en) | Energy-efficient process for para-xylene production | |
TWI622572B (en) | Processes and systems for obtaining aromatics from catalytic cracking hydrocarbons | |
KR101048568B1 (en) | Production method of para-xylene | |
US20120108868A1 (en) | Process for the Production of Paraxylene | |
US5877385A (en) | Process including extractive distillation and/or dehydrogenation to produce styrene from petroleum feedstock including ethyl-benzene/xylene mixtures | |
US2532276A (en) | Production and recovery of para-xylene | |
US9289745B1 (en) | Liquid phase isomerization process | |
JP2014501700A (en) | Process for the production of purified xylene isomers | |
TW201710225A (en) | Processes and apparatuses for toluene methylation in an aromatics complex | |
GB1572014A (en) | Combination toluene transalkylation and xylene separation process | |
US20120108867A1 (en) | Process for the Production of Purified Xylene Isomers | |
US20150051430A1 (en) | Process and Apparatus for the Production of Paraxylene | |
US20200095181A1 (en) | Removal of feed treatment units in aromatics complex designs | |
KR20170131486A (en) | A process and apparatus for separating a stream to provide a transalkylation feed stream in an aromatic complex | |
JP7320066B2 (en) | Process for producing phenol and xylene | |
TWI808166B (en) | Process and device for the inverted separation of aromatics | |
GB625570A (en) | ||
US20160031772A1 (en) | Process for Recovering Paraxylene from at Least Two Feedstreams Containing Xylene Isomers | |
GB1198592A (en) | Method of Separating Xylene Isomers. | |
US5942656A (en) | Process for separating linear alpha olefins from 2-branched and/or 3-branched alpha olefins | |
US11242302B2 (en) | Method for producing paraxylene using a simulated moving-bed step, and a step of fractionating two fractions in a two-section column | |
US10954176B2 (en) | Process for producing para-xylene using a step in a simulated moving bed and a step of fractionation via a three-fraction column |