How should the air volume of a Venturi scrubber be matched to the required amount of water for scrubbing?
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How should the air volume of a venturi scrubber be matched to the required amount of water for washing? I would like to know the calculation methods used in the design of venturi scrubbers.
I have also been thinking about this issue, but I haven’t found an answer.
I think 1.5 L per standard cubic meter of dry gas would be more appropriate
The liquid-to-gas ratio is 0.5–1.0; there is a calculation example in \"Fundamentals of Coal Chemical Engineering Design\".
Does the temperature of water affect the cleaning effect? ?
The impact should be minimal; this is the water from the scrubber tower, and its temperature doesn’t change much.
Our factory has excess low-temperature hot water, at 95 degrees Celsius. We are considering using this 95-degree hot water as the washing water for the Curi scrubber. We wonder whether this temperature will have an impact on the cleaning efficiency ?
The main function of the venturi is to wet the raw gas, thereby enabling more effective dust removal in the scrubber tower. The temperature there is relatively low, but it should still be sufficient for use; however, the venturi requires a certain pressure on the water, so pressurization is necessary
Is 95 degrees still relatively low? ? What temperature of water is generally used in your Venturi scrubbers? ? There’s no problem with water pressure; we have pressure-boosting equipment.