Method for recovery of furfural and acetic acid from furfural stripping steam condensate
A technology for stripping steam and condensate, applied in the separation/purification of carboxylic acid compounds, organic chemistry, etc., can solve the problems of being unable to be used as acetic acid extractant, high solubility, loss of extractant, etc., and achieve reduced processing difficulty and improved chemical properties The effect of stability and efficiency improvement
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Embodiment 1
[0025] The concentrations of furfural and acetic acid in furfural stripping steam condensate were 5.2% (wt) and 1.6% (wt), respectively.
[0026] The extractant is a mixed solvent of benzene, ethyl acetate and trichlorethylene, wherein benzene accounts for 40wt%, ethyl acetate accounts for 20wt%, and trichlorethylene accounts for 40wt%.
[0027] The pulse packing extraction tower is filled with wire mesh corrugated packing, the effective height is 5 meters, which is equivalent to 10 theoretical plates, the feed ratio of extraction agent and furfural stripping steam condensate is 3:1, the extraction temperature is 31°C, and the pulse frequency is 2s -1 , after the operation stabilized, the temperatures of the extract phase and the raffinate phase were 36°C and 40°C, respectively.
[0028] The extraction agent regeneration tower is filled with wire mesh corrugated packing, the effective height is 4 meters, which is equivalent to 28 theoretical trays, the feeding position is equi...
Embodiment 2
[0032] It is basically the same as Example 1, but the feed ratio of extractant to furfural stripping steam condensate is 1:1.
Embodiment 3
[0034] It is basically the same as Example 1, but the feed ratio of extractant to furfural stripping steam condensate is 5:1.
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