Exhaust-gas treatment apparatus and exhaust-gas treatment method
a technology of exhaust gas treatment and treatment apparatus, which is applied in the direction of lighting and heating apparatus, emission prevention, separation processes, etc., can solve the problems of high effluent flow rate, high chemical solution to be used, and difficult use of dissolved salt in desulfurizing effluent, etc., to reduce operating costs, reduce costs, and facilitate construction
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Benefits of technology
Problems solved by technology
Method used
Image
Examples
first embodiment
[0079]A first embodiment according to the present invention will be described below.
[0080]FIG. 1 shows an exhaust-gas treatment apparatus according to this embodiment.
[0081]The exhaust-gas treatment apparatus is disposed in a chimney flue downstream of a boiler 3 provided with a combustion furnace and includes a denitration apparatus 7; an air heater 9; a dry electrostatic precipitator (D-EP) 11; a desulfurization apparatus 13 based on the lime-gypsum method; and a wet electrical dust precipitator (W-EP) 15.
[0082]The boiler 3 is, for example, an oil-fired boiler for combusting heavy oil containing at least 0.5 wt % sulfur content.
[0083]The denitration apparatus 7 removes nitrogen oxides (NOx) contained in the combustion exhaust gas from the boiler 3.
[0084]The air heater 9 performs heat exchange between combustion air supplied to the boiler 3 and combustion exhaust gas. Because of this, the combustion air is heated by the sensible heat of the combustion exhaust gas and supplied to th...
second embodiment
[0123]A second embodiment according to the present invention will be described with reference to FIG. 4. This embodiment differs from the first embodiment in that desulfurizing effluent is subjected to a non-effluent treatment. The other components are the same as those in the first embodiment. Therefore, the same components as those in the first embodiment are denoted with the same reference numerals, and hence, a description thereof will be omitted.
[0124]As shown in FIG. 4, a residue of desulfurizing effluent, excluding the desulfurizing effluent that is supplied from the desulfurization apparatus 13 and introduced into the two-fluid nozzle 35 (refer to FIG. 2), is sprayed upstream of the dry electrostatic precipitator 11 via a flow channel 60. The moisture content of the desulfurizing effluent that has been sprayed upstream of the dry electrostatic precipitator 11 is evaporated by sensible heat of the combustion exhaust gas flowing through the chimney flue, and consequently, dry ...
third embodiment
[0125]A third embodiment according to the present invention will be described with reference to FIG. 5. This embodiment differs from the first embodiment in that a heat exchanger for heat exchange of combustion exhaust gas is added. The other components are the same as those in the first embodiment. Therefore, the same components as those in the first embodiment are denoted with the same reference numerals, and hence, a description thereof will be omitted. This embodiment is also applicable to the second embodiment.
[0126]As shown in FIG. 5, a heat exchanger (gas-gas heater (GGH)) 62 that performs heat exchange between the combustion exhaust gas from the dry electrostatic precipitator 11 to the desulfurization apparatus 13 and the combustion exhaust gas before being released to the atmosphere downstream of the wet electrical dust precipitator 15 is provided. Although the heat exchanger 62 is indicated at two locations in the figure, it does not mean that two separate heat exchangers ...
PUM
| Property | Measurement | Unit |
|---|---|---|
| exit temperature | aaaaa | aaaaa |
| exit temperature | aaaaa | aaaaa |
| diameter | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 


