Improved butanol recovery process and device
A butanol, propanol technology, applied in separation methods, organic chemistry methods, chemical instruments and methods, etc., can solve problems such as process addition complexity, process limitations and/or costs
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Embodiment 1
[0069] This experimental example comprises an embodiment of the process of the invention comprising three distillation columns and two phase separators, i.e. evaluating figure 1 The top, side and bottom streams of distillation column 110, and the top and bottom streams of column 120. A feed comprising 33% water, 32% methanol, 2% propanol, and 33% butanol is fed to a side inlet of a distillation column, such as column 110, maintained at atmospheric pressure. corresponds to figure 1 The overhead stream of stream 10 contained 4% water, 96% methanol, 0% propanol, 0% butanol, had a temperature of 65°C and a color factor greater than 30. corresponds to figure 1 The side stream of stream 12 contained 91.5% water, 0.8% methanol, 0.9% propanol, and 6.8% butanol and had a temperature of about 92°C. corresponds to figure 1 The bottom stream of stream 17 contained 0.05% water, 0.00% methanol, 0.01% propanol, 99.94% butanol and had a temperature of about 117°C and a color factor gr...
Embodiment 2
[0072] The experimental example includes a second distillation column such as figure 2 Column 210 is an embodiment of the process of the present invention. A feed comprising 36% water, 10% methanol, 7% propanol, and 47% butanol is fed to a side inlet of a distillation column, such as column 210, maintained at atmospheric pressure. corresponds to figure 2 The overhead stream of stream 34 contains 6.4% water, 85.5% methanol, 6.5% propanol and 1.6% butanol and has a temperature of about 66°C. corresponds to figure 2 The bottom stream of stream 36 contained 41.8% water, 0.5% methanol, 4.9% propanol, and 51.0% butanol and had a temperature of about 92°C. The organic portion of the bottom stream, i.e. in the figure 2 After processing in a phase separator such as separator 250, further use figure 2 of distillation columns 220 and 230 or figure 1 The distillation columns 110 and 120 are processed. Use when recovery of methanol is required figure 2 The construction of wi...
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Abstract
Description
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Application Information
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