Treatment method of digesting waste steam produced by soda pulping process
A technology of alkaline pulping and treatment method, which is applied in the direction of pulping waste gas treatment, separation method, chemical instrument and method, etc. effect, the effect of eliminating odor
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Embodiment 1
[0021] The cooking waste steam produced by alkaline pulping is pretreated, that is, the cooking waste steam first flows through the steam-water separator, and after the steam-water is separated, it enters the heat exchanger for heat exchange. After the heat exchange, the cooking waste steam enters the warm water tank and is generated by the heat exchanger. After the condensed water is sprayed, the cooking waste steam enters the desulfurization tower. The flue gas flow rate of the boiler entering the desulfurization tower is 154000 m 3 / h and the spraying amount of lime emulsion with a concentration of 8% is constant, use the valve to control the flow of cooking waste steam into the desulfurization tower, so that the flow of cooking waste steam entering the desulfurization tower is 5086m 3 / h, to make the cooking waste steam mixed with flue gas and lime emulsion. After measurement, the S content in the flue gas discharged from the desulfurization tower is 288.7mg / m 3 , Na con...
Embodiment 2
[0023] The treatment steps of the cooking waste steam are the same as in Example 1, except that the amount of cooking waste steam entering the desulfurization tower is 8650 m 3 / h. After measurement, the S content in the flue gas discharged from the desulfurization tower is 284.2 mg / m 3 , Na content is 83.4 mg / m 3 , K content is 9.3 mg / m 3 .
Embodiment 3
[0025] The treatment steps of the cooking waste steam are the same as in Example 1, except that the amount of cooking waste steam entering the desulfurization tower is 10170 m 3 / h. After measurement, the S content in the flue gas discharged from the desulfurization tower is 279.6 mg / m 3 , Na content is 84.5 mg / m 3 , K content is 9.8 mg / m 3 .
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