Patent GB-883393-A (GB)
Title: Low temperature cleaning of an impurity-containing gas
IPC: F25J5/00
Filed: 1959-11-26
Abstract: 883,393. Cold separation of gas mixtures. UNION CARBIDE CORPORATION. Nov. 26, 1959 [Dec. 9, 1958], No. 40269/59. Class 8(2). In a process for freeing a compressed gas mixture e.g. air from high boiling point impurities e.g., water vapour and carbon dioxide by condensing them during passage of the air through a reversing path ring 14, Fig. 1, of the on-stream portion 15 of a heat axchanger 13 in countercurrent with a cold separated component e.g., nitrogen discharged from a separating column (not shown) and traversing a non-reversible path 17 and simultaneously evaporating impurities previously condensed in a reversing path 23 of the purge-stream portion 24 of exchanger 13 by passing a reverse flow therethrough of purge gas e.g., oxygen from a line 22 and reversing valve 21, evaporation is assisted by warming the purge oxygen during the early part of the period by a counterflow through a non-reversing path 29 of nitrogen at ambient temperature drawn from the warm end of path 17 through a line 18, a reversing valve 19 and lines 19a, 26 by a blower 27 which discharges through a flow control valve 28, the non-reversing path 29 and a line 30 back to the cold nitrogen supply line 16 ; the temperature of the purge gas stream being reduced to normal towards the end of the period by stopping or reducing the recycle nitrogen stream. Switching of portions 15, 24 of the exchanger 13 during change-over is effected by conventional warm and cold end reversing valves 12, 21. In a modification nitrogen is used as purge gas in that ray 123, Fig. 2, of reversing paths 123, 114 of portions 124, 115 of exchanger 113 not being traversed by incoming air, oxygen product is directed by a valve 138 through that ray 135 of switchable paths 135, 136 thermally associated with the on-stream portion of the exchanger 113, cold nitrogen is directed by a valve 119 from a line 116 through that path ray 117 of non-reversing paths 117, 129 of the on-stream exchanger portions 115, 124 and as purge gas a portion of cold nitrogen is bled from line 116 through a flow control valve 128 and a reversing valve 121 through the pan 123 previously traversed by incoming air and is warmed during the early part of the period by nitrogen withdrawn from the outlet 119a of valve 119 by a blower 127 and discharged through the valve 119 and the non-reversing path 129 of the heat exchanger portion 124 under purge back to the line 116. In a further modification a group of five heat exchangers are used four of them being on-stream and one on purge using oxygen and being warmed by recycle nitrogen. In a further modification the heat exchanger portions comprise cold accumulators 415, 424, Fig. 4, having packing 460, 470 alternately traversed by incoming air and reversely flowing purge nitrogen directed by reversing valves 412, 421 and having embedded therein coils 417, 429 that in the on-stream accumulator ray 415 being traversed by cold product oxygen from a supply line 416 during the first half of an air cleaning period thus providing extra cold and coil 429 in the purge accumulator being traversed by re-cycle oxygen drawn from a line 461 by a blower 427 which discharges through a control valve 463, the coil 429 and a line 430 leading to the line 416. About midway through the period the counterflowing warm recycle oxygen in coil 429, is replaced by a co-current flow of cold oxygen diverted from line 416 through line 430 and the so warmed oxygen is returned through a valve 465 to the blower 427 which delivers it through a line 466, a valve 467 and the coil 417 back to the line 416. Immediately the air and purge nitrogen flows are switched the oxygen continues to pass from the cold to the warm end of coil 429 and start mid-way the oxygen is switched so as to pass from the cold to the warm end of coil 417 and from the warm to the cold end of coil 429.