Abstract The present invention relates to a continuous type catalyst regeneration process for continuously heating and regenerating a degraded catalyst from a denitration apparatus and recycling the regenerated catalyst to the denitration apparatus for repeated use thereof. In accordance with the present invention, a degraded catalyst is intermittently and by predetermined amounts charged into a heating furnace through a first damper mechanism in a gas-sealed state while the surface level of a catalyst held in the heating furnace is maintained lower than the outlet of catalyst regenerating gas and is therein subjected to heat-treatment at a temperature of 400°-650° C. with catalyst-regenerating gas introduced into the heating furnace. Thus regenerated catalyst is intermittently and by predetermined amounts discharged from the heating furnace toward a second damper mechanism through a catalyst delivery mechanism and recycled to the denitration apparatus.
A process for continuously regenerating a degraded catalyst from an apparatus for removing nitrogen oxides from an exhaust gas comprising: charging said degraded catalyst from said apparatus into a heating furnace in a gas-sealed state intermittently by predetermined amounts while the surface level of the catalyst held in the heating furnace is maintained lower than the outlet of catalyst regenerating gas; subjecting said degraded catalyst to heat treatment at a regeneration temperature of 400°-650° C. with catalyst regenerating gas introduced into the heating furnace, wherein said predetermined amounts of the catalyst to be charged into the heating furnace are such that the charged catalyst can be heated to said regeneration temperature within 10 minutes; discharging thus regenerated catalyst from the heating furnace in the gas-sealed state intermittently by predetermined amounts; and recycling said regenerated catalyst to said apparatus.
Claim 2
Dependent Claim
138 words
A process for continuously regenerating a degraded catalyst from an apparatus for removing nitrogen oxides from an exhaust gas comprising: charging said degraded catalyst from said apparatus into a heating furnace in a gas-sealed state intermittently by predetermined amounts while the surface level of the catalyst held in the heating furnace is maintained lower than the outlet of catalyst regenerating gas; subjecting said degraded catalyst to heat treatment at a regeneration temperature of 400°-650° C. with catalyst regenerating gas introduced into the heating furnace, wherein said predetermined amounts of the catalyst to be charged into the heating furnace are such that the charged catalyst can be heated to said regeneration temperature within 10 minutes; discharging thus regenerated catalyst from the heating furnace in the gas-sealed state intermittently by predetermined amounts; and recycling said regenerated catalyst to said apparatus.
Claim 3
Dependent Claim
25 words
The process of claim 1 wherein said removal of said nitrogen oxides from said exhaust gas is carried out at a temperature of 180°-250° C.
Claim 4
Dependent Claim
10 words
The process of claim 1, said catalyst essentially comprising alumina.
Claim 5
Dependent Claim
19 words
The process of claim 3 wherein the regeneration temperature of said catalyst is in the range of 500°-650° C.
Claim 6
Dependent Claim
10 words
The process of claim 1, said catalyst essentially comprising titania.
Claim 7
Dependent Claim
19 words
The process of claim 5 wherein the regeneration temperature of said catalyst is in the range of 400°-600° C.