초록 ▼

A continuous pressure letdown system connected to a hopper decreases a pressure of a 2-phase (gas and solid) dusty gas stream flowing through the system. The system includes a discharge line for receiving the dusty gas from the hopper, a valve, a cascade nozzle assembly positioned downstream of the

A continuous pressure letdown system connected to a hopper decreases a pressure of a 2-phase (gas and solid) dusty gas stream flowing through the system. The system includes a discharge line for receiving the dusty gas from the hopper, a valve, a cascade nozzle assembly positioned downstream of the discharge line, a purge ring, an inert gas supply connected to the purge ring, an inert gas throttle, and a filter. The valve connects the hopper to the discharge line and controls introduction of the dusty gas stream into the discharge line. The purge ring is connected between the discharge line and the cascade nozzle assembly. The inert gas throttle controls a flow rate of an inert gas into the cascade nozzle assembly. The filter is connected downstream of the cascade nozzle assembly.

대표청구항 ▼

The invention claimed is: 1. A continuous pressure letdown system connected to a hopper for decreasing a pressure of a dusty gas stream flowing through the system, the system comprising: a discharge line for receiving the dusty gas stream from the hopper; a valve connecting the hopper to the discha

The invention claimed is: 1. A continuous pressure letdown system connected to a hopper for decreasing a pressure of a dusty gas stream flowing through the system, the system comprising: a discharge line for receiving the dusty gas stream from the hopper; a valve connecting the hopper to the discharge line for controlling introduction of the dusty gas stream into the discharge line; a cascade nozzle assembly positioned downstream of the discharge line and configured to decrease a pressure of the dusty gas stream over a distance; a purge ring connected in the discharge line upstream of the cascade nozzle assembly; an inert gas supply connected to the purge ring for introducing an inert gas into the cascade nozzle assembly; an inert gas throttle for controlling a flow rate of the inert gas into the cascade nozzle assembly; and a filter connected downstream of the cascade nozzle assembly. 2. The system of claim 1, wherein the discharge line is greater than approximately 200 feet in length. 3. The system of claim 1, wherein the filter is a baghouse. 4. The system of claim 1, wherein the velocity of the dusty gas stream entering the cascade nozzle assembly is between about 70 feet per second and about 200 feet per second. 5. The system of claim 1, wherein the dusty gas stream leaving the cascade nozzle assembly has a void fraction of greater than about 90% by volume. 6. The system of claim 1, wherein the cascade nozzle assembly comprises a plurality of orifices having sequentially increasing throat diameters. 7. The system of claim 6, wherein each of the orifices of the cascade nozzle assembly has an included convergence angle of approximately thirty degrees. 8. A continuous pressure letdown system having a dusty gas stream with solid particulates flowing through the system, wherein the system is connected to a hopper, the system comprising: a discharge line connected to the hopper; a valve for controlling introduction of the dusty gas stream with solid particulates into the discharge line; a cascade nozzle assembly positioned downstream of the discharge line for decreasing a pressure of the dusty gas stream; a purge ring connected between the discharge line and the cascade nozzle assembly; an inert gas supply connected to the purge ring for introducing an inert gas into the cascade nozzle assembly; an inert gas throttle for controlling a flow rate of the inert gas into the cascade nozzle assembly; and a filter connected downstream of the cascade nozzle assembly for separating the solid particulates from the dusty gas stream. 9. The system of claim 8, wherein the inert gas supply is also connected to the hopper. 10. The system of claim 8, wherein the cascade nozzle assembly comprises a plurality of orifices having varying diameters. 11. The system of claim 10, wherein each of the orifices has an included convergence angle of approximately thirty degrees. 12. The system of claim 8, wherein the dusty gas stream leaving the cascade nozzle assembly has a void fraction of between about 98% by volume and about 99% by volume. 13. The system of claim 8, wherein the hopper is connected to at least one of a cyclone or a candle filter of a gasification system. 14. The system of claim 8, wherein the velocity of the dusty gas stream within the cascade nozzle assembly is between about 70 feet per second and about 200 feet per second. 15. A method of continuously decreasing a pressure of a dusty gas stream flowing through a gasification system, the method comprising: passing the dusty gas stream through a length of discharge line; passing the dusty gas stream from the discharge line through a cascade nozzle assembly having a sequentially increasing diameter to incrementally decrease a pressure of the dusty gas stream over a distance; and adjusting flow rate of the dusty gas stream entering the cascade nozzle assembly. 16. The method of claim 15, wherein passing the dusty gas stream through a length of discharge line comprises passing the dusty gas stream through a length of approximately 200 feet. 17. The method of claim 15, wherein adjusting flow rate of the dusty gas stream comprises using a purge ring. 18. The method of claim 15, wherein passing the dusty gas stream from the discharge line through the cascade nozzle assembly having a sequentially increasing diameter comprises alternately decreasing and increasing the diameter of the cascade nozzle assembly. 19. The method of claim 15, wherein passing the dusty gas stream from the discharge line through the cascade nozzle assembly having a sequentially increasing diameter comprises transporting the dusty gas stream through a convergence angle of approximately thirty degrees. 20. The method of claim 15, wherein passing the dusty gas stream through a length of discharge line comprises increasing a void fraction of the dusty gas stream to between about 80% by volume and about 90% by volume.