Method for treating high-concentration ammonia and nitrogen in coking gas
A high-concentration technology of coking gas, which is applied in combustible gas purification, combustible gas purification/transformation, petroleum industry, etc., can solve problems such as high energy consumption and secondary pollution, and achieve the effect of avoiding secondary pollution and complete desorption
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example 1
[0022] First, the coking gas is desulfurized and then absorbed in the absorption tower with orthophosphoric acid to generate a mixed solution of diammonium hydrogen phosphate and ammonium dihydrogen phosphate; ammonium; then pipe the generated diammonium hydrogen phosphate into the ammonia distillation tower, add 10ppm organic denitrification agent; install Bi-Lu-Y / β-Fe in the ammonia distillation tower 3 o 4 Catalyst; then steam is introduced into the ammonia distillation tower, diammonium hydrogen phosphate is decomposed into ammonium dihydrogen phosphate and ammonia; finally ammonia is reduced to nitrogen under the action of the catalyst, and diammonium hydrogen phosphate is pumped into the absorption tower with a circulating pump top, to reabsorb the ammonia in the pipeline gas.
[0023] By using the method of the invention to treat waste gas with an ammonia nitrogen concentration of 3000 mg / L in a coking gas plant, the nitrogen nitrogen concentration is reduced from 3000...
example 2
[0025] First, the coking gas is desulfurized and then absorbed in the absorption tower with orthophosphoric acid to generate a mixed solution of diammonium hydrogen phosphate and ammonium dihydrogen phosphate; ammonium; then pipe the generated diammonium hydrogen phosphate into the ammonia distillation tower, add 30ppm organic denitrification agent; install Bi-Lu-Y / β-Fe in the ammonia distillation tower 3 o 4 Catalyst; then steam is introduced into the ammonia distillation tower, diammonium hydrogen phosphate is decomposed into ammonium dihydrogen phosphate and ammonia; finally ammonia is reduced to nitrogen under the action of the catalyst, and diammonium hydrogen phosphate is pumped into the absorption tower with a circulating pump top, to reabsorb the ammonia in the pipeline gas.
[0026] Using the method of the invention to treat waste gas with an ammonia nitrogen concentration of 3000 mg / L in a coking gas plant, the ammonia nitrogen concentration is reduced from 4000 mg / ...
example 3
[0028] First, the coking gas is desulfurized and then absorbed in the absorption tower with orthophosphoric acid to generate a mixed solution of diammonium hydrogen phosphate and ammonium dihydrogen phosphate; ammonium; then pipe the generated diammonium hydrogen phosphate into the ammonia distillation tower, add 20ppm organic denitrification agent; install Bi-Lu-Y / β-Fe in the ammonia distillation tower 3 o 4 Catalyst; then steam is introduced into the ammonia distillation tower, diammonium hydrogen phosphate is decomposed into ammonium dihydrogen phosphate and ammonia; finally ammonia is reduced to nitrogen under the action of the catalyst, and diammonium hydrogen phosphate is pumped into the absorption tower with a circulating pump top, to reabsorb the ammonia in the pipeline gas.
[0029] Using the method of the invention to treat waste gas with an ammonia nitrogen concentration of 5000 mg / L in a coking gas plant, the ammonia nitrogen concentration is reduced from 5000 mg / ...
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