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U.S. Department of Energy
Office of Scientific and Technical Information

Process design guidelines vary widely

Journal Article · · Oil Gas J.; (United States)
OSTI ID:5921779
There are guidelines and procedures for the design and cost evaluation of various H/sub 2/S-scavenging processes for checking the technical merits of a bid, and the identification of essential process parameters during the bid preparation. The following general guidelines apply to the design of the formaldehyde-methanol, metallic oxide, and caustic-based scavengers. The sour gas must enter the contractor at or preferably above its hydrocarbon dew point. Special attention must be paid to the gas line between the inlet separator and the contactor. Insulation, heat tracing, or even gas preheating (about 5/sup 0/F. greater than the hydrocarbon dewpoint) should be evaluated. While foaming does not apply with the iron sponge process, the presence of liquid hydrocarbons should also be avoided. With iron sponge units or other metallic oxide-based scavengers, installation of a strainer downstream of the contactor is recommended. The H/sub 2/S-removal efficiency of the various processes is not affected by the operating pressure or the gas CO/sub 2/ concentration. However, when the CO/sub 2/-over H/sub 2/S ratio exceeds 10,000, the solvent supplier's technical group should be consulted. Checking the gas for the presence of waxes and asphaltenes which may plug or foul the system is recommended. Stress relief of the absorbers is recommended.
Research Organization:
9901729
OSTI ID:
5921779
Journal Information:
Oil Gas J.; (United States), Journal Name: Oil Gas J.; (United States) Vol. 87:8; ISSN OIGJA
Country of Publication:
United States
Language:
English