Isothermal conversion process of high-concentration carbon monoxide and system thereof
A technology of carbon monoxide and isothermal conversion, which is applied in the field of temperature conversion process and its system, can solve the problems affecting the stability of catalyst service life, high bed hot spot temperature, and catalyst bed overtemperature, so as to save equipment investment and operating cost, Reduce system resistance and improve system stability
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Embodiment 1
[0051] Such as Figure 4 As shown, the temperature of the feed gas from a pulverized coal gasification unit (chilling process) is 208°C, the pressure is 3.7MpaG, and the volume content of carbon monoxide on a dry basis is 71.2%. The feed gas first passes through the feed gas separator 1 to separate the entrained moisture. Then pass through the feed gas filter 2 to remove dust and toxic substances harmful to the catalyst, and the filtered feed gas enters the shell side of the air-cooled shift reactor 3 and is preheated to 260°C before entering the 1# water-cooled shift reactor 4 (this implementation In the example, a floating head type water-cooled shift reactor) is used for the shift reaction, and the reaction temperature is controlled at 270°C. The medium-pressure boiler feed water enters the 1# water-cooled shift reactor 4 at the lower part, and passes through the by-product medium-pressure steam in the medium-pressure steam drum 5 (Pressure is 4.2MpaG, temperature is 255 ℃)...
Embodiment 2
[0055] Such as Figure 5 As shown, the temperature of the feed gas from a coal-water slurry gasification unit is 215°C, the pressure is 4.1MpaG, and the volume content of carbon monoxide on a dry basis is 47.6%. The raw material gas first passes through the raw material gas separator 1 to separate the entrained moisture, and then passes through the raw gas filter 2 to remove dust and toxic substances harmful to the catalyst. The filtered raw gas enters the shell side of the air-cooled shift reactor 3 and is preheated to 260 After entering the 1# water-cooled shift reactor 4 (in this embodiment, a plate-type water-cooled shift reactor) for the shift reaction, the reaction temperature is controlled to be 270° C., and the medium-pressure boiler feed water enters the 1# water-cooled shift reactor 4 at the lower part. In the medium-pressure steam drum 5, the reaction heat of the shift reaction is removed by producing medium-pressure steam (with a pressure of 4.2MpaG and a temperatu...
Embodiment 3
[0059] Such as Figure 6 As shown, the temperature of raw gas from a pulverized coal gasification unit (waste boiler process) is 170°C, the pressure is 3.7MPaG, and the volume content of carbon monoxide on a dry basis is 64.1%. The raw material gas first passes through the raw material gas separator 1 to separate the entrained moisture, and then passes through the raw gas filter 2 to remove dust and toxic substances harmful to the catalyst. The filtered raw gas enters the shell side of the air-cooled shift reactor 3 and is preheated to 200 After entering the 1# water-cooled shift reactor 4 (in this embodiment, a floating head type water-cooled shift reactor) for the shift reaction, the reaction temperature is controlled to be 270°C, and the medium-pressure boiler feed water enters the 1# water-cooled shift reactor 4 at the lower part , in the medium-pressure steam drum 5, the heat of reaction of the shift reaction is removed by by-product medium-pressure steam (the pressure is...
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