A kind of ultra-high-purity carbon monoxide preparation device and process
A carbon monoxide and preparation device technology, applied in the direction of carbon monoxide, inorganic chemistry, chemical instruments and methods, etc., can solve the problems of unsatisfactory carbon monoxide gas purity, insufficient resource utilization, high production cost, etc., achieve good industrial application prospects, improve resource Efficiency and ease of operation
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Embodiment 1
[0048] In this embodiment, the ultra-high purity carbon monoxide preparation process and apparatus, such as figure 1 Indicated.
[0049]In this example, the ultra-high purification carbon monoxide preparation device includes a formic acid dehydration reaction device 6, a base washed tower, a low temperature cold trap 12, a deoxidation column 14, an adsorbed drying tower 16, a low temperature rectification tower 18, wherein specifically:
[0050] A formic acid dehydration reaction occurs in the formic acid dehydration reaction, produces a mixture of carbon monoxide, and a formic acid storage tank 2 is also attached to the formate of the formate before the formation of a mixture of carbon monoxide.
[0051] The alkali washed tower is used to remove the acidic impurity components in the mixed gas, the base wasolata includes the first base base washed tower 8 and the second alkali washing tower, which constitutes a two-stage base washing structure. In the two-stage alkali washing stru...
Embodiment 2
[0064] In this embodiment, the method step is the same as that of the first embodiment, and the operation parameters are implemented as follows: the feed speed of the feed pump is 220 kg / h; the second alkali washing tower uses 5.5% NaOH solution; the reaction of the deoxidation column The temperature is -185 ° C, atmospheric pressure; the operating temperature of the adsorption of the drying tower is 6 ° C, atmospheric pressure; the tower of the base washed tower is the stainless steel liner in the plastic, the tower is filled with acid and alkali-resistant plastic Ball Stacking filling; low temperature rectification tower theory level is 90, the top of the tower is 90 kPa (absolute pressure), the tower pressure drop 2.2 kPa, the top operating temperature is -194 ° C, the tower is -188 ° C.
Embodiment 3
[0066] In this embodiment, the method steps are the same as that of the first embodiment, and the operation parameters are implemented as follows: the feed pump conveyed feed speed is 250 kg / h; the second alkali washing tower uses 5.8% NaOH solution; the reaction of the deoxidation column The temperature is -190 ° C, atmospheric pressure; the operating temperature of the suction drying tower is 7 ° C, atmospheric pressure; the tower of the base washed tower is a stainless steel lining polypropylene plastic, and the tower is filled with acid and alkali-resistant plastic θ loop-resistant filler The low temperature rectification tower Theory is 95, the top of the top operation pressure is 85 kPa (absolute pressure), the tower pressure drop 2.5 kPa, the top operating temperature is -193 ° C, the tower is -185 ° C.
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