An integrated device and method for wet desulfurization and denitrification of ship exhaust gas
A technology of desulfurization, denitrification, and wet desulfurization, which is applied to chemical instruments and methods, separation methods, and separation of dispersed particles. Smaller floor area, simplified forced oxidation process, and compact device
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Embodiment 1
[0034] A method for desulfurization and denitrification using the integrated device for wet desulfurization and denitrification of ship waste gas, comprising the following steps:
[0035] (1) Ship exhaust gas (SO 2 Concentration 600ppm, NO x 1100ppm, flow 50000Nm 3 / h) Enter the primary washing and dedusting zone 2 through the exhaust gas inlet 1, and the liquid-gas ratio of the primary washing and dedusting zone 2 is 2L / Nm 3 , Part of the circulating washing liquid is processed by the solid-liquid separator 7, and the concentrated liquid is stored in the sludge tank, and the clear liquid is returned to the first-level circulating pool 5, and the outboard seawater is extracted to replenish water;
[0036] (2) After dedusting, the exhaust gas enters the secondary washing and desulfurization zone 3, and the liquid-gas ratio of the secondary washing and desulfurization zone 3 is controlled to be 4L / Nm 3 , by adding magnesium hydroxide to the secondary circulation tank 8, the p...
Embodiment 2
[0041] A method for desulfurization and denitrification using the integrated device for wet desulfurization and denitrification of ship waste gas, comprising the following steps:
[0042] (1) Ship exhaust gas (SO 2 Concentration 600ppm, NO x 1100ppm, flow 50000Nm 3 / h) Enter the primary washing and dedusting zone 2 through the exhaust gas inlet 1, and the liquid-gas ratio of the primary washing and dedusting zone 2 is 2L / Nm 3 , Part of the circulating washing liquid is processed by the solid-liquid separator 7, and the concentrated liquid is stored in the sludge tank, and the clear liquid is returned to the first-level circulating pool 5, and the outboard seawater is extracted to replenish water;
[0043] (2) After dedusting, the exhaust gas enters the secondary washing and desulfurization zone 3, and the liquid-gas ratio of the secondary washing and desulfurization zone 3 is controlled to be 4L / Nm 3 , by adding magnesium hydroxide to the secondary circulation tank 8, the p...
Embodiment 3
[0048] A method for desulfurization and denitrification using the integrated device for wet desulfurization and denitrification of ship waste gas, comprising the following steps:
[0049] (1) Ship exhaust gas (SO 2 Concentration 600ppm, NO x 1100ppm, flow 50000Nm 3 / h) Enter the primary washing and dedusting zone 2 through the exhaust gas inlet 1, and the liquid-gas ratio of the primary washing and dedusting zone 2 is 2L / Nm 3 , Part of the circulating washing liquid is processed by the solid-liquid separator 7, and the concentrated liquid is stored in the sludge tank, and the clear liquid is returned to the first-level circulating pool 5, and the outboard seawater is extracted to replenish water;
[0050] (2) After dedusting, the exhaust gas enters the secondary washing and desulfurization zone 3, and the liquid-gas ratio of the secondary washing and desulfurization zone 3 is controlled to be 4L / Nm 3 , by adding magnesium hydroxide to the secondary circulation tank 8, the p...
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