초록 ▼

A process for producing liquid and, optionally, gaseous products from gaseous reactants includes feeding, at a low level, gaseous reactants into a slurry bed, allowing the gaseous reactants to react as they pass upwardly through the slurry bed, withdrawing any gaseous product and unreacted gaseous r

A process for producing liquid and, optionally, gaseous products from gaseous reactants includes feeding, at a low level, gaseous reactants into a slurry bed, allowing the gaseous reactants to react as they pass upwardly through the slurry bed, withdrawing any gaseous product and unreacted gaseous reactants from a head space above the slurry bed and withdrawing liquid product and/or slurry bed to maintain the slurry bed at a desired level. The process further includes passing boiler water, as a first heat transfer fluid, in indirect heat exchange relationship through the slurry bed to remove heat from the slurry bed, allowing the heated boiler water to flash and separate to form pressurised steam, controlling the pressure of the steam to be substantially constant, and passing a second heat transfer fluid in indirect heat exchange relationship through the slurry bed to remove heat from the slurry bed.

대표청구항 ▼

1. A process for producing liquid and, optionally gaseous products from gaseous reactants, which process includesfeeding, at a low level, gaseous reactants into a slurry bed of solid particles suspended in a suspension liquid; allowing the gaseous reactants to react as they pass upwardly through the

1. A process for producing liquid and, optionally gaseous products from gaseous reactants, which process includesfeeding, at a low level, gaseous reactants into a slurry bed of solid particles suspended in a suspension liquid; allowing the gaseous reactants to react as they pass upwardly through the slurry bed, thereby to form liquid and, optionally, gaseous products; withdrawing any gaseous product and unreacted gaseous reactants from a head space above the slurry bed; withdrawing liquid product and/or slurry from the slurry bed to maintain the slurry bed at a desired level; passing boiler water, as a first heat transfer fluid, in indirect heat exchange relationship through the slurry bed to remove heat from the slurry bed; allowing the heated boiler water to flash and separate to form pressurised steam; controlling the pressure of the steam to be substantially constant; and passing a second heat transfer fluid in indirect heat exchange relationship through the slurry bed to remove heat from the slurry bed, wherein the average temperature of the second heat transfer fluid in indirect heat exchange relationship with the slurry bed being lower than the average temperature of the boiler water in indirect heat exchange relationship with the slurry bed. 2. A process as claimed in claim 1, in which the first heat transfer fluid, which is boiler water, removes at least 50% of the total heat removed from the slurry bed by the first and second heat transfer fluids.3. A process as claimed in claim 1, which includes cooling the second heat transfer fluid and returning it for heat exchange duty to the slurry bed, the second heat transfer fluid thus being cycled continuously through the slurry bed, in a substantially closed system.4. A process as claimed in claim 1, which includes controlling the temperature of the slurry bed by controlling an operating temperature of the second heat transfer fluid passing in indirect heat exchange relationship through the slurry bed.5. A process as claimed in claim 1, in which the second heat transfer fluid is water, the process including pumping the water to a pressure sufficient substantially to prevent evaporation of the water to form steam at the operating temperature and pressure of the water.6. A process as claimed in claim 1, in which the second heat transfer fluid is water, the process including allowing steam to be formed by the water.7. A process as claimed in claim 1, which includes selectively increasing a heat transfer surface area between the second heat transfer fluid and the slurry bed, and decreasing a heat transfer surface area between the first heat transfer fluid and the slurry bed, in order to increase the total heat removal rate achieved by the first and second heat transfer fluids, and/or selectively decreasing a heat transfer surface area between the second heat transfer fluid and the slurry bed, and increasing a heat transfer surface area between the first heat transfer fluid and the slurry bed in order to decrease the total heat removal rate achieved by the first and second heat transfer fluids.8. A process as claimed in claim 7, which includes switching heat transfer surface area in contact with the first heat transfer fluid and the slurry bed to be in contact with the second heat transfer fluid and the slurry bed, and/or vice versa.