Method of removing sulfur oxides and nitrogen oxides by dry process

Claim 2

In a method of removing sulfur and nitrogen oxides by a dry process comprising passing a waste gas containing sulfur and nitrogen oxides through a moving bed or beds formed of a carbonaceous adsorbent in a direction transverse thereto to remove the sulfur oxides and adding ammonia to remove the nitrogen oxides, the improvement which comprises passing the waste gas containing sulfur and nitrogen oxides through n number of moving beds each formed of carbonaceous materials moving downward in a piston flow in such a manner that the waste gas is allowed to flow upward, said waste gas being directed through each of the moving beds in a transverse direction and in an opposite direction to the movement of the waste gas in the next adjacent moving bed, so that the waste gas alternately crosses and criss-crosses each moving bed successively from the lowest to the highest moving bed, said moving beds being arranged vertically and in series, wherein n is an integer of at least 2, said waste gas being passed through a first moving bed, mixed with ammonia outside the bed and then fed to a second moving bed, said process being repeated successively through the series of n moving beds until the waste gas exits from the n-th moving bed, while the carbonaceous material is transported from the n-th to the first moving bed.

Claim 3

The method of removing sulfur oxides and nitrogen oxides as claimed in claim 1, wherein ammonia is further added to the waste gas before entering the first moving bed.

Claim 4

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the ammonia is added in the form of ammonia gas alone or diluted with another gas.

Claim 5

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the moving bed is held at a temperature of from room temperature to 180° C.

Claim 6

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the carbonaceous adsorbent least one member selected from the group consisting of activated carbons, activated cokes, and semi-cokes.

Claim 7

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the ammonia is added to the waste gas leaving the first moving bed in an NH 3 /(SO 2 +NO x ) mol ratio of 0.1 to 1.4.

Claim 8

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the carbonaceous adsorbent leaving the n-th moving bed is regenerated and circulated to the first moving bed.

Claim 9

The method of removing sulfur and nitrogen oxides as claimed in claim 7, wherein the regeneration is carried out by heating.

Claim 10

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the waste gas leaving the n-th moving bed is treated by the carbonaceous adsorbent used mainly for removal of sulfur oxides to remove unreacted ammonia.

Claim 11

In a dry method of removing sulfur and nitrogen oxides by a dry process comprising passing a waste gas containing sulfur and nitrogen oxides through a moving bed or beds formed of a carbonaceous adsorbent in a direction transverse thereto to remove the sulfur oxides and adding ammonia to remove the nitrogen oxides, the improvement which comprises passing the waste gas containing sulfur and nitrogen oxides through n number of moving beds each formed of carbonaceous materials moving downward in a piston flow in such a manner that the waste gas is allowed to flow upward, said waste gas being directed through each of the moving beds in a transverse direction and in an opposite direction to the movement of the waste gas in the next adjacent moving bed so that the waste gas alternately crosses the criss-crosses each moving bed successively, from the lowest to the highest moving bed, said moving beds being arranged vertically and in series, wherein n is an integer of at least 2, said waste gas being passed through a first moving bed and then fed to a second moving bed, while ammonia is added directly to each of the moving beds, said process being repeated successively through the series of n moving beds until the waste gas exits from the n-th moving bed, while the carbonaceous material is transported from the n-th to the first moving bed.

Claim 12

In a dry method of removing sulfur and nitrogen oxides by a dry process comprising passing a waste gas containing sulfur and nitrogen oxides through a moving bed or beds formed of a carbonaceous adsorbent in a direction transverse thereto to remove the sulfur oxides and adding ammonia to remove the nitrogen oxides, the improvement which comprises passing the waste gas containing sulfur and nitrogen oxides through n number of moving beds each formed of carbonaceous materials moving downward in a piston flow in such a manner that the waste gas is allowed to flow upward, said waste gas being directed through each of the moving beds in a transverse direction and in an opposite direction to the movement of the waste gas in the next adjacent moving bed so that the waste gas alternately crosses the criss-crosses each moving bed successively, from the lowest to the highest moving bed, said moving beds being arranged vertically and in series, wherein n is an integer of at least 2, said waste gas being passed through a first moving bed and then fed to a second moving bed, while ammonia is added directly to each of the moving beds, said process being repeated successively through the series of n moving beds until the waste gas exits from the n-th moving bed, while the carbonaceous material is transported from the n-th to the first moving bed.

Claim 13

The method of removing sulfur oxides and nitrogen oxides as claimed in claim 1, wherein ammonia is further added to the waste gas before entering the first moving bed.

Claim 14

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the ammonia is added in the form of ammonia gas alone or diluted with another gas.

Claim 15

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the moving bed is held at a temperature of from room temperature to 180° C.

Claim 16

The method of removing sulfur and nitrogen oxides as claimed in claim 1, wherein the carbonaceous adsorbent least one member selected from the group consisting of activated carbons, activated cokes and semi-cokes.