PATENTS

      50.  ------.  [ATWELL, H. V.]  (The Texas Co.).  Control of Catalytic Conversions.  United States Patent 2,438,029, Mar. 16, 1948: appl. Filed May 3, 1944, Serial No. 533,900; 3 claims (Cl. 23-1).  Chem. Abs., vol. 42, 1948, p. 4334.

Reactions promoted by finely divided catalyst, specifically the hydrogenation of CO on Co, are controlled by recycling and heating or cooling the liquids in the reactor.  Catalyst is retained in the reactor by setting out in an enlarged section at the top of the reactor.  For example, a stream comprising 1 mol. CO:2 mol, H2 preheated to 365°-380° F. is brought into contact with catalyst suspended in a hydrocarbon fraction b 450°-600° F.  For the production of hydrocarbons, recycling is adjusted to maintain the reactor between 380° and 420° F.: for oxygenated products, a higher temperature is desirable.