Patent GB-956179-A (GB)
Title: Acetylene recovery process
IPC: C07C7/11
Filed: 1962-03-09
Abstract: Acetylene is recovered from gases containing it by absorption in liquid ammonia followed by stripping and gaseous ammonia is introduced into the stripping zone as stripping gas.  The feed gas, e.g. a pyrolysis gas, is cooled and dried by countercurrent contact with a cold heavy naphtha stream, further cooled and then contacted with heavy naphtha in a two-stage absorption tower to remove acetylene homologues, being contacted with a small amount of naphtha in a lower first stage and then separately contacted with a larger amount in an upper second stage.  The naphtha recovered from the second stage is prestripped to recover acetylene which is recycled and then fully stripped and returned to the absorption; the naphtha from the first stage is stripped and reused.  Residue gas is employed in these stripping stages. Ammonia may be added to each of the absorption stages to prevent freezing. The acetylene-containing gas is now cooled and contacted with liquid ammonia, unabsorbed gas being washed to recover ammonia in two stages, first by contact with a body of water from the second stage, this first stage being cooled by a water-cooled coil, and then in a second stage by contact with water dispersed as a spray or on trays, external cooling being applied as necessary. The acetylene-ammonia solution is partially flashed, gases being washed and then recycled to the feed gas, and then stripped with gaseous ammonia.  The acetylene is water washed in two stages. Stripped ammonia is partially recycled and a bleed stream distilled to purify.  Ammonia solutions are distilled to recover liquid ammonia which is then vaporized and used as stripping gas, the cooling obtained by vaporization being employed in the naphtha absorption stages and the ammonia absorption stage. Specification 555,580 is referred to.ALSO:Acetylene is recovered from gases containing it by absorption in liquid ammonia followed by stripping and gaseous ammonia is introduced into the stripping zone as stripping gas.  The feed gas, e.g. a pyrolysis gas, is cooled and dried by countercurrent contact with a cold heavy naphtha stream, further cooled and then contacted with heavy naphtha in a two-stage absorption tower to remove acetylene homologues, being contacted with a small amount of naphtha in a lower first stage and then separately contacted with a larger amount in an upper second stage.  The naphtha recovered from the second stage is prestripped to recover acetylene which is recycled and then fully stripped and returned to the absorption; the naphtha from the first stage is stripped and reused.  Residue gas is employed in these stripping stages. Ammonia may be added to each of the absorption stages to prevent freezing.  The acetylene-containing gas is now cooled and contacted with liquid ammonia, unabsorbed gas being washed to recover ammonia in two stages, first by contact with a body of water from the second stage, this first stage being cooled by a water-cooled coil, and then in a second stage by contact with water dispersed as a spray or on trays, external cooling being applied as necessary.  The acetylene-ammonia solution is partially flashed, gases being washed and then recycled to the feed gas, and then stripped with gaseous ammonia.  The acetylene is water-washed in two stages.  Stripped ammonia is partially recycled and a bleed stream distilled to purify.  Ammonia solutions are distilled to recover liquid ammonia which is then vaporized and used as stripping gas, the cooling obtained by vaporization being employed in the naphtha absorption stages and the ammonia absorption stage. Specification 955,580 is referred to.