Thermal device and method for increasing temperature of clean boiler smoke obtained by wet desulphurization

Abstract

The invention discloses a thermal device and method for increasing temperature of clean boiler smoke obtained by wet desulphurization. The thermal device comprises a boiler body, a tail smoke treatment device and a clean smoke heating device, wherein the tail smoke treatment device comprises a dust remover and a wet desulphurization device; clean smoke is obtained after the boiler smoke passes through the wet desulphurization device; the clean smoke is heated by the clean smoke heating device and then discharged into a chimney. The method comprises the following steps: adjusting the amount of smoke entering a bypass smoke channel by virtue of a bypass smoke channel adjusting baffle; heating cold air in an air heater by hot smoke in the bypass smoke channel; feeding the obtained high-temperature hot air into a clean smoke channel behind the wet desulphurization device; mixing the high-temperature hot air with the clean smoke by a mixer; and increasing the mixed smoke temperature to over an acid dew point and discharging the mixed smoke by virtue of the chimney. According to the thermal device and method for increasing temperature of the clean boiler smoke obtained by wet desulphurization, the hot smoke energy is transferred to the clean smoke by taking hot air as a heat medium; the corrosion to the chimney is reduced; the smoke diffusion range is widened so as to prevent gypsum rain from generating at the periphery of a power plant.

Description

technical field [0001] The invention relates to a thermal device and method for increasing the temperature of boiler wet desulfurization net flue gas. Background technique [0002] Installing wet desulfurization devices on coal-fired boilers to purify acid gases in flue gas is a relatively mature technology, which has been widely promoted and applied in thermal power plants. After wet desulfurization, the clean flue gas carries a little water droplets and is in a saturated state , SO3 gas that is not captured by the desulfurization system is easily dissolved in saturated wet flue gas to form sulfuric acid, which corrodes the flue and chimney behind the desulfurization. In order to solve this problem, conventional methods use steam to heat the clean flue gas, set up a small oil gun for heating and a flue gas-flue gas heat exchanger (GGH). , leading to corrosion of the heat exchanger and failure; heating with a small oil gun requires the oil gun to be arranged in the clean fl...

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Problems solved by technology

In order to solve this problem, conventional methods use steam to heat the clean flue gas, set up a small oil gun for heating and a flue gas-flue gas heat exchanger (GGH). , leading to corrosion of the heat exchanger and failure; heating with a small oil gun requires the oil gun to be arranged in the clean flue, which not only consumes high-quality fuel, but also corrodes the small oil gun and ignition system with wet flue gas, and the reliability is not high; adopting GGH , using the original flue gas to heat the clean flue gas, due to the small heat transfer temperature difference, the area of ​​the rotary heating surface is large, and the flue gas after desulfurization carries a certain amount of powder such as gypsum, which leads to the blockage of the corrugated plate of the heat exchanger, GGH The running resistance is too large, affecting the normal operation of the unit

[0003] In order to improve the reliability of unit operation, GGH is canceled when designing the desulfurization system of most power plants, and the wet flue gas after desulfurization is directly discharged into the wet chimney. Necessary anti-corrosion measures are taken during design to prevent corrosion of the flue and chimney after desulfurization; In the power plant where GGH has been installed, in order to

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