The application discloses a
calcium carbide furnace
tail gas deep purification process. The
calcium carbide furnace
tail gas is firstly subjected to wet desulfurization and dehydrocyanation and TSA treatment, and then sequentially enters a de-
fluorine and de-
hydrocyanation reactor, a
hydrolysis desulfurization reactor, a fine desulfurization reactor, a de-
phosphorus and de-
arsenic reactor, a de-
oxygen reactor and a de-
hydrocarbon reactor. After the treatment process, the HCl content in the gas is less than 0.1 ppm, the HF content is less than 0.1 ppm, the HCN content is less than 0.1 ppm, the total
sulfur content is less than 0.1 ppm, the AsH3 content is less than 5 ppb, the PH3 content is less than 5 ppb, the
oxygen content is less than 10 ppm, and the
unsaturated hydrocarbon content is less than 0.1 ppm, thereby meeting the separation and purification requirements of subsequent processes, and the pressure drop of the whole process is not more than 100 kPa. The process can remove
oxygen and unsaturated hydrocarbons in the gas under low-temperature conditions, thereby reducing the occurrence of side reactions, and has the characteristics of reasonable
process design, high purification precision, low
energy consumption and low operation cost.