| 摘要 |
1,091,095. Controlling the olefin concentration in desorbing and/or purging mediums. BRITISH PETROLEUM CO. Ltd. Oct. 20, 1966 [Nov. 4, 1965], No. 46754/65. Heading B1L. In a cyclic process employing molecular sieves to separate straight chain hydrocarbons from branched chain and/or cyclic hydrocarbons, in which process the circulation of desorbing and/or purging medium is effected, and in which process olefins tend to build up in the circulating medium to an equilibrium level, the olefin concentration is controlled by hydrogenating at least a proportion of the olefins. Preferably the purging medium is hydrogen, the desorbing medium is n-pentane, and the hydrogenation is carried out in the presence of a catalyst comprising either nickel supported upon sepiolite or cobalt and molybdenum oxides supported on alumina. The denormalised hydrogen fraction containing n-pentane and hydrogen together with olefins obtained from the purge stage passes from absorbers through line 1 to hydrogen separator 2 and thence to stripper 4 from where the final de-normalised product is removed as bottoms and the npentane and olefins as overhead offtake. The n-pentane and olefins are similarly stripped at 12 from the normal paraffins from the desorption stage. The n-pentane fed to drum 10 from strippers 4 and 12 is recirculated to the absorber, a portion being hydrogenated in reactor 17 and fed into the stripper 2 for removal of any hydrogen present in the hydrogenated n-pentane stream. |
