COMBUSTION FLUE GAS SOx TREATMENT VIA DRY SORBENT INJECTION
Combustion flue gas containing SO X is treated to remove SO X using a dry particulate sorbent injection procedure in which a sodium-based sorbent precursor is calcined immediately prior to its introduction into the flue gas stream, to activate the sorbent for reaction with SO X . The sorbent precursor is a NaHCO 3 -containing compound, and trona is preferred as the sorbent precursor.
1 . A process for desulfurizing a combustion flue gas stream which comprises (i) injecting a calcined particulate sodium-based sorbent having a mean particle size smaller than about 75 μm into a combustion flue gas stream containing SO X , the flue gas stream having a temperature of about 200° F. to about 1100° F., to desulfurize the flue gas,
the sorbent being derived from a sorbent precursor selected from the group consisting of trona, sodium sesquicarbonate, nahcolite, sodium bicarbonate, wegscheiderite and combinations of these, and
the sorbent being prepared for injection and reaction with SO X by subjecting the sorbent precursor, immediately prior to its injection into the flue gas stream, to a calcination step by calcining the sorbent precursor to decompose at least a portion of its sodium bicarbonate content and thereby activate the sorbent precursor for reaction with SO X , and (ii) collecting the injected sorbent downstream of the injection point in a solids collection device.
2 . The process of claim 1 wherein the SO X comprises a sulfur oxide selected from the group consisting of SO 2 and SO 3 and mixtures thereof
3 . The process of claim 1 wherein the sorbent has a mean particle size smaller than about 50 μm.
4 . The process of claim 1 wherein the sorbent has a mean particle size smaller than about 40 μm.
5 . The process of claim 1 wherein the sorbent precursor is calcined by heating the sorbent precursor to a temperature of about 175° F. to about 500° F.
6 . The process of claim 1 wherein the sorbent precursor is calcined by heating the sorbent precursor to a temperature of about 200° F. to about 400° F.
7 . The process of claim 1 wherein the sorbent precursor is calcined to decompose at least about 25 wt % of its initial sodium bicarbonate content.
8 . The process of claim 1 wherein the sorbent precursor is calcined to decompose at least about 80 wt % of its initial sodium bicarbonate content.
9 . The process of claim 1 wherein the calcination step is carried out by contacting the sorbent precursor with combustion gas from burning of natural gas with air.
10 . The process of claim 1 wherein the calcination step is carried out by contacting the sorbent precursor with a side stream of hot combustion flue gas.
11 . The process of claim 10 wherein the side stream of combustion flue gas comprises combustion flue gas diverted from the hot side or cool side of an economizer or from the hot-side of an air preheater.
12 . The process of claim 1 wherein the flue gas stream at the calcined sorbent injection point has a temperature of about 250° F. to about 900° F.
13 . The process of claim 1 wherein the calcined sorbent is injected into the flue gas stream downstream of an air preheater into the cool-side flue gas stream.
14 . The process of claim 1 wherein the solids collection device is selected from the group consisting of bag filtration devices, electrostatic precipitators, and wet scrubbers.
15 . A process for desulfurizing a combustion flue gas stream which comprises (i) injecting a calcined particulate sodium-based sorbent into a combustion flue gas stream containing SO X , the flue gas stream having a temperature of about 200° F. to about 1100° F., to desulfurize the flue gas,
the sorbent being derived from a sorbent precursor selected from the group consisting of trona, sodium sesquicarbonate, nahcolite, sodium bicarbonate, wegscheiderite and combinations of these, and
the sorbent being prepared for injection and reaction with SO X
by milling a coarsely-sized sorbent precursor to provide a milled particulate sorbent precursor having a mean particle size smaller than about 75 μm and
by subjecting the milled sorbent precursor, immediately prior to its injection into the flue gas stream, to a calcination step by calcining the sorbent precursor to decompose at least a portion of its sodium bicarbonate content and thereby activate the sorbent precursor for reaction with So X , and
(ii) collecting the injected sorbent downstream of the injection point in a solids collection device.
16 . The process of claim 15 wherein the milled sorbent precursor has a mean particle size smaller than about 50 μm.
17 . The process of claim 15 wherein the milled sorbent precursor has a mean particle size smaller than about 40 μm.
18 . The process of claim 15 wherein the coarsely-sized sorbent precursor has a mean particle size in the range of about 75 μm to about 2 mm.
19 . The process of claim 15 wherein the coarsely-sized sorbent precursor has a mean particle size greater than about 50 μm and the milled sorbent precursor has a mean particle size smaller than about 40 μm.