Patent GB-770818-A (GB)
Title: Improvements in the production of acetylene by incomplete combustion of hydrocarbons
IPC: C07C2/78
Filed: 1955-06-10
Abstract: In a process for the production of acetylene by incomplete combustion of hydrocarbons with oxygen in which the hydrocarbons and oxygen are separately preheated and the preheated gases are supplied to a mixing chamber, and the mixture then enters a reaction chamber in which a reaction with the formation of flame takes place and the reaction product is rapidly cooled, the preheated gases are mixed in a mixing chamber, the surface of the walls of which consist of a non-scaling metal, while maintaining the gradient of the gas speed at the walls above a minimum of 20, preferably 40, centimetres per second per centimetre, and in the same direction as the mean speed of the gas. The wall material may consist of alloys of iron with 5 to 25 per cent of chromium, 0.5 to 2.0 per cent of aluminium, and 0.4 to 3.0 per cent of silicon.  In an example, 2000 cubic metres of natural gas and 1200 cubic metres of oxygen each preheated to 650 DEG  C. were mixed in the apparatus of Specification 672,446, the surface of the mixing section being made from an iron alloy with 6.5 per cent chromium, 1.5 per cent of silicon, 0.5 per cent of aluminium and 0.15 per cent of carbon.  The angle of aperture of the conical extension is so selected that the gas speed gradient is at least 150 centimetres per second per centimetre.  The gaseous reaction products are cooled by the injection of water and contain, by volume, 8.8 per cent acetylene, 6 per cent methane, 0.2 per cent ethylene, 25 per cent carbon dioxide, 56.4 per cent hydrogen and 0.2 per cent of oxygen. An alternative alloy for the inner part of the mixing chamber consists of 23 per cent aluminium and 0.15 per cent of carbon, the remainder being iron.ALSO:Hydrogen and acetylene are obtained by the incomplete combustion of hydrocarbons with oxygen by a process in which the hydrocarbons and oxygen are separately preheated and supplied to a mixing chamber, the mixture then entering a reaction chamber in which a reaction with the formation of flame takes place and the reaction product is rapidly cooled, the preheated gases being mixed in a mixing chamber the walls of which consist of a non-scaling metal while maintaining the gradient of the gas speed at the walls above a minimum of 20, preferably 40 centimetres per second per centimetre, and in the same direction as the mean speed of the gas. The wall material may consist of alloys of iron with 5-25 per cent of chromium, 0.5 to 2.0 per cent of aluminium, and 0.4 to 3.0 per cent of silicon.  In an example, 2,000 cubic metres of natural gas, and 1,200 cubic metres of oxygen each preheated to 650 DEG C. were mixed in the apparatus of Specification 672,446 the surface of the mixing section being made from an iron alloy with 6.5 per cent chromium, 1.5 per cent of silicon, 0.5 per cent of aluminium and 0.15 per cent of carbon.  The angle of aperture of the conical extension is so selected that the gas speed gradient is at least 150 centimetres per second per centimetre.  The gaseous reaction products are cooled by the injection of water and contain, by volume, 56.4 per cent hydrogen, 8.8 per cent acetylene, 6 per cent methane, 0.2 per cent ethylene, 25 per cent carbon dioxide and 0.2 per cent of oxygen.