Process for producing high-purity methane chloride
A technology of monochloromethane and methyl chloride, which is applied in the field of methane chloride production technology, can solve the problems of increasing equipment investment, increasing operating costs, and relatively high requirements for rectification tower materials, and achieves the effect of increasing equipment investment and increasing content
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Embodiment 1
[0022] Methanol and hydrogen chloride react in the gas phase under the condition of 210°C and 0.18MpaG in the presence of activated alumina catalyst to generate monochloromethane and water. The temperature of the gaseous product was quenched by dilute hydrochloric acid and dropped to 50°C. The liquid phase after chilling is 20% dilute hydrochloric acid, and the gas phase passes through the pickling tower, the alkali washing tower and the sulfuric acid drying tower successively, and is compressed and condensed to obtain crude monochloromethane. Absorb the unreacted hydrogen chloride in the reaction gas with chilled dilute hydrochloric acid in the pickling tower, and neutralize the unabsorbed hydrogen chloride in the reaction gas with 10% sodium hydroxide in the alkali washing tower. 22% of the hydrochloric acid out of the pickling tower produces 31% of hydrochloric acid, and about 3-5% of the alkali out of the alkali washing tower enters the exhaust gas scrubbing system to neut...
Embodiment 2
[0025] Methanol and hydrogen chloride react in the gas phase at 300°C and 0.38MpaG in the presence of an activated alumina catalyst to produce methylene chloride and water. The gas phase product was quenched by dilute hydrochloric acid and the temperature was lowered to 80°C. The liquid phase after chilling is 20% dilute hydrochloric acid, and the gas phase passes through the pickling tower, the alkali washing tower and the sulfuric acid drying tower successively, and is compressed and condensed to obtain crude monochloromethane. Absorb the unreacted hydrogen chloride in the reaction gas with chilled dilute hydrochloric acid in the pickling tower, and neutralize the unabsorbed hydrogen chloride in the reaction gas with 10% sodium hydroxide in the alkali washing tower. 22% of the hydrochloric acid out of the pickling tower produces 31% of hydrochloric acid, and about 3-5% of the alkali out of the alkali washing tower enters the exhaust gas scrubbing system to neutralize the aci...
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