Preparing method of carbon monoxide, and preparing method of carbonyl chloride by using carbon monoxide
A technology of carbon monoxide and a manufacturing method, applied in directions such as carbon monoxide and phosgene, can solve the problems of inability to remove, poor production efficiency, shortened life of solid catalyst, etc., to avoid the reduction of production volume, suppress the increase of pressure drop, and have excellent industrial effects Effect
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Embodiment 1
[0031] The coke used was coke obtained by pulverizing commercially available coke with a nickel content of 500 ppm by weight and an average particle diameter of 50 mm so that the average particle diameter becomes smaller than 25 mm, and then soaking the coke in 1 mol / L hydrochloric acid. Coke obtained by washing with water after 24 hours in the aqueous solution. The pH of the washed water was 6. The coke was dried at 120° C. for 24 hours in a rotary kiln. At this time, the water content of the coke was 0.3% by weight, and the nickel content was 100 ppm by weight.
[0032] Carbon monoxide is produced by blowing a mixed gas of oxygen and carbon dioxide into a carbon monoxide production furnace filled with the coke. The obtained CO (nickel compound content: 10 volume ppm) was brought into contact with activated alumina added with metal oxides such as chromium (Cr), and after convective contact with caustic soda aqueous solution, cooled to 5°C using a heat exchanger, and then al...
Embodiment 2
[0035] CO was produced in the same manner as in Example 1, except that coke with a Ni content of 100 wtppm used in Example 1 and a commercially available coke with a Ni content of 500 wtppm were mixed at a ratio of 2:1. The purity of the obtained CO was 98.5% by volume, the dew point of CO was below -45°C, the concentration of nickel compounds in CO was 0.02 ppm by volume, and the concentration of sulfur compounds in CO was below 0.2 ppm by volume. 100 t of phosgene was produced using this CO, and as a result, the gas pressure drop from the mixer inlet to the phosgene reaction tank outlet increased by 0.05 kPa compared to when the phosgene production started.
Embodiment 3
[0037] CO was produced in the same manner as in Example 1, except that coke with a Ni content of 100 wtppm used in Example 1 and a commercially available coke with a Ni content of 500 wtppm were mixed at a ratio of 1:1. The purity of the obtained CO was 98.5% by volume, the dew point of CO was -45°C or lower, the nickel compound concentration in CO was 0.04 volume ppm, and the sulfur compound concentration in CO was 0.2 volume ppm or less. 100 t of phosgene was produced using this CO, and as a result, the gas pressure drop from the inlet of the mixer to the outlet of the phosgene reaction tank increased by 0.3 kPa compared to when the production of phosgene was started.
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