Process for converting unsaturated C.sub.4 hydrocarbons into normal butane
AssigneeStone & Webster Engineering Corp.
InventorsJacob N. Rubin, Frederick B. Seufert
Life of this patent
Estimating the term…
Abstract
Unsaturated C.sub.4 hydrocarbons are converted into normal butane by introducing an unsaturated C.sub.4 hydrocarbon stream into a hydrogenation zone to convert it into a stream of normal butane and isobutane. Normal butane is recovered from a separation zone while isobutane is directed to an isomerization zone wherein a portion of the isobutane is converted into normal butane. The stream from the isomerization zone is returned to the separation zone to recover the normal butane produced in the isomerization reaction. The normal butane produced by the process is subsequently utilized in a cracking zone to produce ethylene.
Claims36
A process of converting unsaturated C.sub.4 hydrocarbons into normal butane which comprises:
- a. passing a stream consisting essentially of unsaturated C.sub.4 hydrocarbons in contact with hydrogen in a hydrogenation zone to react said hydrogen and said unsaturated C.sub.4 hydrocarbons to form a stream of normal butane and isobutane;
- b. discharging said normal butane and isobutane stream from said hydrogenation zone and introducing said discharged normal butane and isobutane stream into a separation zone to separate said normal butane from said isobutane;
- c. discharging and recovering said normal butane from said separation zone;
- d. passing said isobutane from said separation zone into an isomerization zone to convert a portion of said isobutane into normal butane so that a stream of normal butane and isobutane is produced;
- and
- e. thereafter returning said stream of normal butane and isobutane produced in said isomerization zone into said separation zone to separate and recover the normal butane produced in said isomerization zone.
In a process for the production of ethylene by the pyrolytic cracking of hydrocarbons in a cracking zone to produce a process stream of cracked gases, introducing said process stream of cracked gases into a rapid cooling zone to cool said gases, passing said cooled process stream of cracked gases into a quench prefractionation and compression zone to further cool and compress said gases and remove heavy hydrocarbons, passing said process stream of compressed cracked gases through a demethanization zone wherein methane is removed from said process stream and a stream of hydrogen is generated, thereafter, directing said process stream of compressed cracked gases through a recovery zone wherein ethylene is recovered and a stream of butene raffinate is formed, the improvement comprising the steps of:
- a. introducing said stream of butene raffinate into a hydrogenation zone wherein said butene raffinate is passed in contact with said stream of hydrogen generated in said demethanization zone at temperatures of about 200.degree. to about 450.degree. F. and a pressure of about 100 to about 500 psig to form a stream consisting essentially of normal butane and isobutane;
- b. discharging said stream of normal butane and isobutane from said hydrogenation zone and introducing said discharged normal butane and isobutane stream into a separation zone to separate said normal butane from said isobutane in a separation tower which is operated at overhead temperatures of from about 100.degree. to about 200.degree. F. and overhead pressures of from about 55 to about 240 psig;
- c. discharging said normal butane from said separation zone and introducing said normal butane from said separation zone into said cracking zone as a feedback for the production of ethylene;
- d. passing said isobutane from said separation zone into an isomerization zone wherein a portion of said isobutane is converted into normal butane in the presence of an isomerization catalyst to form a stream of normal butane and isobutane;
- and
- e. thereafter, returning said stream of normal butane and isobutane produced in said isomerization zone into said separation zone to separate the normal butane produced in said isomerization zone.
Dependencies are inferred from the claim text.