Calculation of biogas desulfurization tower
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I have been working on a biogas power generation project recently, with a daily gas production of 45,000 cubic meters. The composition of the biogas is unknown; based on available information, the hydrogen sulfide content is assumed to be 7 g/m3, and it drops to 20 mg/m3 after desulfurization. I would like to ask what is the loading amount of the iron oxide desulfurizer? How large should the desulfurization tower be designed? If the tower is too tall, can a series configuration be used?
Such a large volume of biogas makes dry desulfurization unsuitable, as the costs are too high
Using dry desulfurization photocatalysts requires a significant amount of work, and it also involves the issue of handling waste desulfurization agents; the cost of processing these agents is even higher than the price of the desulfurization agents themselves
For such projects, professional manufacturers are still needed to provide detailed solutions.
If the amount of biogas is low, can dry desulfurization be used? How to design it?
This hydrogen sulfide content is a value I chose arbitrarily; the hydrogen sulfide content in biogas produced from livestock and poultry manure is not yet known. I checked some information, and the content varies.
This hydrogen sulfide content is a value I chose arbitrarily; the hydrogen sulfide content in biogas produced from livestock and poultry manure is not yet known. I checked some information, and the content varies.
Use wet flue gas desulfurization in series or with dry method; the dry method is costly. 15324073997