Abstract: An apparatus is provided for the condensation of sulphur vapor and for the separation of sulphur droplets from a gas flow, preferably from the reaction gas flow from a Claus catalyst. Such apparatus comprises a vessel, a nest of tubes arranged in the vessel between tube plates, pipe connections at the vessel for the supply and discharge of a coolant flowing around the nest of tubes and an inlet pipe connection and an outlet pipe connection for the gas flow at the vessel, upstream and downstream of the said nest of tubes, respectively. Positioned in the vessel is a sulphur separation unit through which the sulphur-containing gas flows and on the surfaces of which sulphur vapor condenses and/or liquid sulphur collects and agglomerates. Sulphur discharge openings are provided in the bottom of the vessel on both the upstream and downstream sides of the separation unit.

Abstract: A process for continuously gasifying carbonaceous material using fluidizing medium and oxygen-containing gas, under controlled feed rates and certain delivery conditions, and under selective processing conditions to produce a product rich in carbon monoxide and hydrogen is provided. If desired, the product can be produced with increased amounts of methane. Gasification is conducted under pressure in a fluidized bed to produce a gaseous reaction product, and char solids are coproduced. Additional increments of oxygen-containing gas with steam is selectively introduced. The product is passed through a dilute-phase, maintained at certain temperatures, at a certain superficial velocity, and for a certain residence time. The presence of undesirable heavy hydrocarbon by-products is precluded. Char, in removal from the bottom of the bed, is contacted with steam or inert gas to recover sensible heat. Cooled product gas is provided having less than about 4 grains of solid per scf at certain conditions.