Coke oven gas desulfuration and deamination combined purifying method and special device thereof
A technology of coke oven gas and special device, which is applied in the direction of combustible gas purification, combustible gas purification/renovation, chemical industry, etc., can solve problems such as uneconomical, reduce alkali consumption, reduce fixed ammonium consumption, and increase alkali consumption. Effect
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Embodiment 1
[0024] A coke oven gas desulfurization and deamination combined purification method, including a desulfurization method and a deamination method, coke oven gas desulfurization adopts a wet catalytic oxidation method, deamination adopts a water washing method; coke oven gas desulfurization is performed by cooling and washing naphthalene, followed by desulfurization After desulfurization, water washing and ammonia distillation are carried out; the ammonia consumed by desulfurization comes from the ammonia produced by gas and ammonia distillation. The cooling and washing of naphthalene includes two stages of oil washing and water cooling, the oil washing includes oil cooling and oil washing of naphthalene, and the water cooling is gas-water direct cooling. The operating temperature of the cooling and washing of naphthalene is controlled below 33-35°C.
Embodiment 2
[0026] Such as figure 1 As shown, it is a special device for the coke oven gas desulfurization and deammonification combined purification method of the present invention. This special device comprises oil-washing naphthalene precooling tower 1, desulfurization tower 2, water-washing ammonia tower 3 and ammonia distillation tower 4 connected successively; The ammonia tower 3 is provided with a circulating rich ammonia water cooler 6, a circulating semi-ammonia rich water cooler 7 and an ammonia stripping water cooler 8; The ammonia vapor condensing cooler 9 is provided with a concentrated ammonia water or a concentrated ammonia vapor pipeline to communicate with the desulfurization tower 2; a lean / rich ammonia water heat exchanger 10 is arranged on the connecting pipeline between the ammonia washing tower 3 and the ammonia distillation tower 4.
[0027]The oil washing naphthalene precooling tower 1 is composed of a standpipe indirect cooler and a direct cooling sprayer; the wa...
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