Patent GB-793762-A (GB)
Title: Process and apparatus for separating gas mixtures
IPC: F25J3/04
Filed: 1956-09-21
Abstract: 793,762. Cold separation of gas mixtures. UNION CARBIDE CORPORATION, [formerly UNION CARBIDE & CARBON CORPORATION. Sept. 21, 1956 [Oct. 10, 1955], No. 28974/56. Class 8(2). In a compressed gas mixture, e.g., air separation process wherein the air is cooled and freed from readily condensible impurities in a heat exchanger 16 in countercurrent to returning nitrogen traversing a duct 18 or 20 not being traversed by air and also in countercurrent to returning oxygen flowing continuously through a duct 19, periodic thawing of the low-pressure rectification column 30 to effect removal of traces of solid impurities from the plates 40 thereof and from a body of adsorbent 51 therein is effected by passage therethrough of compressed air having been cleaned and cooled in the exchanger 16 in heat exchange with liquid oxygen from a storage vessel 70 being fed through duct 19 in the same direction as the product oxygen during normal working. Cold air leaving the exchanger 16 is further freed from carbon dioxide in an adsorber 23 before passing through a duct 22 into the high pressure column 29. Oxygen-rich liquid is fed through a duct 46 and an expansion valve 47 to the low pressure column 30, and nitrogen-rich gas from the column 29 traverses a duct 41, a condenser chamber 33b surrounded by the body of adsorbent 51, and the so-condensed liquid is expanded through a valve 45 to act as reflux for the column 30. Thaw-out is effected firstly by passing warm clean air through the low pressure column 30 and secondly by passing warm raw air through the high pressure column 29. The first stage is effected by opening drain valves 84, 85, closing a valve 26a and a valve 72 through which liquid oxygen normally passes to the column 30, opening a valve 81 to allow passage of stored liquid oxygen through the heat exchanger duct 19, isolating the high pressure column 29 by closing a valve 86, diverting clean air from duct 22 by opening a valve 87 in a duct 88 leading to a heater 89 from which warmed clean air at 90C. passes along a duct 92 through an open valve 93 to below the adsorbent 51 and the condenser tubes 33a which are thus freed of solid contaminants ; the resulting contaminated air leaving through a duct 54 and a vent valve 54a. To initiate the second thaw-out stage the column 30 is sealed off by closing valves 54a, 84, 45, 47, 87 and 93. Flow of oxygen from reservoir 70 is stopped by closing valve 81. The valve 86 is re-opened, a drain valve 94 is closed, a normally open compressed air valve 97 is closed and a valve 90 is opened to allow access of raw compressed air to the heater 89 and a normally closed valve 95 is opened to allow part of the warmed air to traverse heat exchanger ducts 18, 20, whilst the remainder of the warmed air traverses duct 92, an open valve 98 in a duct 92a leading to the top of column 29 and through the duct 41, the condenser space 33b and duct 42 leading to the column 29. Cold necessary for restarting rectification is obtained by passing the stored liquid oxygen through the duct 19. In a modification extra cold is provided by expanding in a turbine some of the air leaving the heat exchanger 16.