HRSG for fluidized gasification
An HRSG for fluidized bed gasification comprises a high temperature evaporator ( 200 ), a superheater ( 300 ), a low temperature evaporator ( 400 ), and an economizer ( 500 ) connected in series. The superheater ( 300 ), the low temperature evaporator ( 400 ) and the economizer ( 500 ) have a water-tube structure, and the high temperature evaporator ( 200 ) has a fire-tube structure. The HRSG of the present invention allows efficient heat recovery from the raw syngas of a fluidized bed coal gasifier, while avoids or reduces the corrosion of and damage to the components of the HRSG caused by high-speed ash particles in the syngas.
1. A heat recovery steam generator (HRSG) for fluidized bed gasification,
wherein the HRSG comprises from top to bottom a raw syngas inlet, a high temperature evaporator, a superheater, a low temperature evaporator and an economizer connected vertically in series,
wherein each of the superheater, the low temperature evaporator and the economizer comprises a water-tube structure, and the high temperature evaporator comprises a fire-tube structure;
wherein the high temperature evaporator comprises a fire tube assembly encased in a shell, wherein the fire tube assembly is connected with the shell through an upper tube sheet and a lower tube sheet, and wherein the fire tube assembly and the shell are arranged coaxially along a first axis;
wherein the superheater, the low temperature evaporator and the economizer are arranged coaxially along a second axis perpendicular to the ground; and
wherein the first axis is inclined and forms an angle of about 5-10 degrees in relation to the second axis.
2. The HRSG for fluidized bed gasification according to claim 1 , further comprising a steel container enclosing the high temperature evaporator, the superheater, the low temperature evaporator and the economizer to form a combined structure.
3. The HRSG for fluidized bed gasification according to claim 1 , wherein the upper and lower tube sheets are dish shaped in their periphery.
4. The HRSG for fluidized bed gasification according to claim 3 , wherein each of the superheater, the low temperature evaporator and the economizer comprises a shell and a horizontal coil tube assembly installed in the shell, and at least one operation space which is located in the shell next to the horizontal coil tube assembly.
5. The HRSG according to claim 4 , wherein the shell and the horizontal coil tube assembly of the economizer are made of alloy steel.
6. A method for recovering heat from hot raw syngas under pressure exiting a fluidized bed coal gasifier, comprising feeding the hot raw syngas into the raw syngas inlet of an HRSG according to claim 1 , wherein the speed of the raw syngas entering the high temperature evaporator is controlled to a speed of about 15 m/s to about 30 m/s.
7. The method according to claim 6 , wherein the speed of the raw syngas is further controlled to exit the high temperature evaporator at a speed of about 2 m/s to about 8 m/s.