| 摘要 |
An apparatus and method are disclosed for the recovery of sensible heat from a hot tar-free gas produced in a coal gasification process and in combined-cycle power generation. The recovered heat is utilized to generate a flow of superheated steam which may be used in the gasification plant. The apparatus includes a first boiler and a superheater fabricated from materials susceptible to damage from thermal shock when a flow of the tar-free gas having a temperature in excess of a predetermined safety temperature is introduced to the superheater when it is dry. The first boiler, filled with a flow of saturated water, initially receives the flow of gas. Within the first boiler, the gas indirectly heats the water converting it to a flow of saturated steam and reducing the gas temperature below the safety temperature. The reduced temperature gas is passed to the superheater and the saturated steam is passed to the superheater. The gas heats the saturated steam in the superheater to convert it to superheated steam and the temperature of the gas is further reduced. The gas flows to a second boiler for converting a flow of saturated water to saturated steam and further reducing the gas temperature. The saturated steam from the second boiler is passed to the superheater and the gas flows to an economizer for converting a flow of unsaturated water to saturated water for the boilers and reducing the temperature of the gas to a final temperature. |
