Flue gas to washing liquid ratio
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In the upper part of the ammonia-based desulfurization absorption section, the current process includes a flue gas washing section and a liquid collection tank for the generated gas. What should be the liquid-to-gas ratio in the washing section? Are there any specific calculation criteria for the liquid collection tank of the anger cap?
Please give it some support; I’m also very interested in this
The value for traditional desulfurization is 10 to 15, while that for traditional heat exchange is around 1 to 1.5. What we do now is to achieve both heat exchange and desulfurization simultaneously, using a liquid-to-gas ratio of 5 to 6.