Patent GB-1416914-A (GB)
Title: Method of cracking a liquid hydrocarbon fuel and apparatus for use therein
IPC: F02B1/04
Filed: 1973-05-29
Abstract: 1416914 Temperature control in catalytic cracker SIEMENS AG 29 May 1973 [13 July 1972] 25604/73 Heading B1F [Also in Divisions C5 and F1] A gas mixture comprising carbon monoxide, carbon dioxide, methane and/or hydrogen which may be supplied to an internal combustion engine or turbine, industrial or domestic burner, or used as a reducing gas in metallurgical processes is produced in a multiple stage catalytic cracking method in which a mixture of a hydrocarbon which is liquid at ambient temperatures and which has been vaporized into a gaseous phase e.g. boiling, evaporation, spraying or mist-forma tion, and an oxygen-containing gas, is subjected to catalytic cracking to produce a gas mixture which is then subjected to at least one further catalytic cracking after admixture with oxygen-containing gas before the or each further catalytic cracking, the amount and/or the composition of the oxygen-containing gas admixed prior to each catalytic cracking being constantly regulated in accordance with the temperature of the catalytic cracking to which the mixture is subjected. The oxygen-containing gas supplied to the first cracking may be air and/or exhaust gas from an i.c. engine, and that supplied before the further cracking may be air. Heat which may be supplied by the gas mixture produced in the final cracking or by exhaust gas from an i.e. engine, may be supplied by heat exchange to the gas mixture between the crackings or to vaporize the hydrocarbon. Additional hydrocarbon may be supplied to the gas mixture produced in the final cracking. The hydrocarbon may be petrol free from antiknock additives. Apparatus for producing the gas mixture comprises a first cracking unit 11 comprising mixing chamber 14 followed by catalyst-containing cracking chamber 22 having temperature measuring means, the unit being followed by at least one further unit 12, 13 with the cracking chamber 22, 23, 24 of one such unit communicating with the mixing chamber 15, 16 of the next unit, heat exchanger means 25, 26 for vaporising a hydrocarbon which is liquid at ambient temperatures e.g. using product gas mixture, and means to supply the vapourised hydrocarbon to the mixing chamber 14, means 19 for supply of oxygen-containing gas to each of the mixing chambers 14, 15, 16 and an outlet 29 from the final cracking chamber 24 for the gas mixture produced and which may be in communication with the combustion chambers of an internal combustion engine, means 36 and associated temperature measuring means 35 for regulating the volume and/ or content of the oxygen-containing gas supplied in dependence upon the temperature obtaining in the next following cracking chamber. Each mixing chamber may be provided with a heat exchanger and at least one mixing chamber may have a firing device 32 for a combustible gas mixture. As shown, a cracking carburettor has one or more tubes 18 formed with outlet openings 17 is/are disposed in each mixing chamber to allow oxygen-containing gas to be introduced over substantially the entire flow cross-section of the mixing chambers. Gas-guiding surfaces 21 e.g. flat walls of tubes 18, are disposed between the outlet openings 17 and the following cracking chamber 22, 23, 24 and serve to increase gradually the free flow cross-section to the cracking chambers of the gas mixtures produced in the mixing chambers. Means disposed after the final cracking chamber supplies liquid hydrocarbon fuel to the gas mixture emitted from that chamber. The oxygencontaining gas supplied to each mixing chamber may be preheated. Each cracking chamber comprises at least one support body 33 e.g. a porous sintered block which may have a pore volume of 20 to 60% and may be provided with a plurality of substantially parallel through passages 34 substantially perpendicular to the largest surface of the blocks and which may have a diameter of 0.1 to 2mm, the catalyst e.g. nickel, platinum, or as described in Specifications 1402207 and 1416913 distributed on surfaces accessible to the gas mixture.