Patent · US Active

Hydrocarbon gas processing

US8919148B2 · kind B2 · utility

28Cited by
73References
12Claims
0Family size

Assignee

Inventors

Key dates

Filing dateSep 8, 2008
Grant dateDec 30, 2014
Priority date
Expiry dateApr 16, 2032

Classification

  • Technology area (CPC F)Mechanical Engineering; Lighting; Heating
  • CPC primaryF25J2290/40
  • WIPO fieldChemical engineering
  • WIPO sectorChemistry

Abstract

A process for the recovery of ethane, ethylene, propane, propylene, and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. The stream is cooled and divided into first and second streams. The first stream is further cooled to condense substantially all of it and is thereafter expanded to the fractionation tower pressure and supplied to the fractionation tower at a first mid-column feed position. The second stream is expanded to the tower pressure and is then supplied to the column at a second mid-column feed position. A vapor distillation stream is withdrawn from the column above the feed point of the second stream and is then directed into heat exchange relation with the tower overhead vapor stream to cool the vapor distillation stream and condense at least a part of it, forming a condensed stream. At least a portion of the condensed stream is directed to the fractionation tower as its top feed. The quantities and temperatures of the feeds to the fractionation tower are effective to maintain the overhead temperature of the fractionation tower at a temperature whereby the major portion of the desired components is recovered.

Source: USPTO / EPO open patent data. Objective bibliographic and citation counts.