Patent classifications
C07C5/367
Production and Use of 3,4' and 4,4'-Dimethylbiphenyl Isomers
Processes are described for separating 3,4- and 4,4-dimethylbiphenyl from a mixture comprising at least 3,3-, 3,4- and 4,4-dimethylbiphenyl. In the processes, the mixture is cooled to produce a crystallization product comprising at least of the 4,4-dimethylbiphenyl from the feed mixture and a first mother liquor product. The first mother liquor product is distilled to produce a bottoms stream enriched in 4,4-dimethylbiphenyl as compared with the first mother liquor product and an overhead stream deficient in 4,4-dimethylbiphenyl as compared with the first mother liquor product. The overhead stream is then cooled to produce a second crystallization product comprising at least part of the 3,4-dimethylbiphenyl from the overhead stream and a second mother liquor product.
Production and Use of 3,4' and 4,4'-Dimethylbiphenyl Isomers
Processes are described for separating 3,4- and 4,4-dimethylbiphenyl from a mixture comprising at least 3,3-, 3,4- and 4,4-dimethylbiphenyl. In the processes, the mixture is cooled to produce a crystallization product comprising at least of the 4,4-dimethylbiphenyl from the feed mixture and a first mother liquor product. The first mother liquor product is distilled to produce a bottoms stream enriched in 4,4-dimethylbiphenyl as compared with the first mother liquor product and an overhead stream deficient in 4,4-dimethylbiphenyl as compared with the first mother liquor product. The overhead stream is then cooled to produce a second crystallization product comprising at least part of the 3,4-dimethylbiphenyl from the overhead stream and a second mother liquor product.
Production and Use of 3,4' and 4,4'-Dimethylbiphenyl Isomers
Processes are described for separating 3,4- and 4,4-dimethylbiphenyl from a mixture comprising at least 3,3-, 3,4- and 4,4-dimethylbiphenyl. In the processes, the mixture is cooled to produce a crystallization product comprising at least of the 4,4-dimethylbiphenyl from the feed mixture and a first mother liquor product. The first mother liquor product is distilled to produce a bottoms stream enriched in 4,4-dimethylbiphenyl as compared with the first mother liquor product and an overhead stream deficient in 4,4-dimethylbiphenyl as compared with the first mother liquor product. The overhead stream is then cooled to produce a second crystallization product comprising at least part of the 3,4-dimethylbiphenyl from the overhead stream and a second mother liquor product.
METHOD FOR PRODUCING INDENE
The present invention provides a production method for indene, comprising a dehydrogenation step of obtaining a reaction product containing indene by contacting a raw material composition containing indene with a dehydrogenation catalyst, wherein the dehydrogenation catalyst comprises a support containing aluminum, and a group 14 metal element and platinum supported on the support, a content of the platinum in the dehydrogenation catalyst is 0.6 to 2.5% by mass based on a whole amount of the dehydrogenation catalyst, and an atomic ratio of the group 14 metal element to the platinum in the dehydrogenation catalyst is 4.0 to 20.0.
METHOD FOR PRODUCING INDENE
The present invention provides a production method for indene, comprising a dehydrogenation step of obtaining a reaction product containing indene by contacting a raw material composition containing indene with a dehydrogenation catalyst, wherein the dehydrogenation catalyst comprises a support containing aluminum, and a group 14 metal element and platinum supported on the support, a content of the platinum in the dehydrogenation catalyst is 0.6 to 2.5% by mass based on a whole amount of the dehydrogenation catalyst, and an atomic ratio of the group 14 metal element to the platinum in the dehydrogenation catalyst is 4.0 to 20.0.
Liquid hydrogen storage material
Disclosed is a liquid hydrogen storage material, and more particularly, a hydrogen storage material which contains m-phenyltoluene (m=2, 3) and undergoes reversible dehydrogenation/hydrogenation reactions or contains a binary eutectic mixture or a ternary eutectic mixture of m-phenyltoluene (m=2, 3, 4).
Liquid hydrogen storage material
Disclosed is a liquid hydrogen storage material, and more particularly, a hydrogen storage material which contains m-phenyltoluene (m=2, 3) and undergoes reversible dehydrogenation/hydrogenation reactions or contains a binary eutectic mixture or a ternary eutectic mixture of m-phenyltoluene (m=2, 3, 4).
Liquid hydrogen storage material
Disclosed is a liquid hydrogen storage material, and more particularly, a hydrogen storage material which contains m-phenyltoluene (m=2, 3) and undergoes reversible dehydrogenation/hydrogenation reactions or contains a binary eutectic mixture or a ternary eutectic mixture of m-phenyltoluene (m=2, 3, 4).
Systems and processes for maintaining ethylbenzene dehydration catalyst activity
Processes and systems for dehydrogenating ethylbenzene may include mixing a steam stream and an ethylbenzene stream to form a feed mixture. The ethylbenzene/steam feed mixture may then be fed to a dehydrogenation reactor containing an alkali metal promoted catalyst. A liquid, selected from an alkali metal liquid, an alkali metal compound liquid, or a liquid solution comprising an alkali metal, may be injected into a feed stream, such as the steam stream, the ethylbenzene stream, or the ethylbenzene/steam feed mixture. Following injection, the liquid vaporizes and disperses into the feed stream upstream of the dehydrogenation reactor. The liquid may be maintained as a liquid from a point upstream of injection to an injection nozzle. The liquid is dispersed through the injection nozzle, in liquid form, to form droplets of liquid dispersed in the feed stream, which evaporate and/or dissolve into the vaporous feed stream.
Systems and processes for maintaining ethylbenzene dehydration catalyst activity
Processes and systems for dehydrogenating ethylbenzene may include mixing a steam stream and an ethylbenzene stream to form a feed mixture. The ethylbenzene/steam feed mixture may then be fed to a dehydrogenation reactor containing an alkali metal promoted catalyst. A liquid, selected from an alkali metal liquid, an alkali metal compound liquid, or a liquid solution comprising an alkali metal, may be injected into a feed stream, such as the steam stream, the ethylbenzene stream, or the ethylbenzene/steam feed mixture. Following injection, the liquid vaporizes and disperses into the feed stream upstream of the dehydrogenation reactor. The liquid may be maintained as a liquid from a point upstream of injection to an injection nozzle. The liquid is dispersed through the injection nozzle, in liquid form, to form droplets of liquid dispersed in the feed stream, which evaporate and/or dissolve into the vaporous feed stream.