Enhanced reaction system and process for preparing acetic acid through methanol carbonylation
A technology of methanol carbonylation and carbonylation reaction, which is applied in the preparation of carboxylic acid by carbon monoxide reaction, chemical/physical/physicochemical fixed reactor, separation/purification of carboxylic acid compounds, etc., which can solve the problem that carbon monoxide and methanol cannot be fully mixed , system reaction efficiency reduction and other issues, to achieve the effect of saving production resources, reducing production costs and improving operating efficiency
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Embodiment 1
[0050] Fill a sufficient amount of methanol and a corresponding catalyst into the methanol storage tank 12, connect the carbon monoxide feed pipe 11 to a gas source containing 200L of carbon monoxide, start the system, set the system temperature to 170°C, and set the pressure to 2MPa. Methanol and the catalyst are transported to the interior of the reaction kettle 3, and at the same time, carbon monoxide is transported to the interior of the micro interface generator 2 through the carbon monoxide feed pipeline 11;
[0051] The micro-interface generator 2 breaks carbon monoxide into micro-bubbles of micron size, and releases the micro-bubbles into the reactor 3, so that the carbon monoxide fully contacts with methanol in the state of micro-bubbles, and the carbonylation reaction takes place.
[0052] The carbonylation reaction product is sent to the flash column 4 , the light component rectification column 51 and the heavy component rectification column 52 in sequence, and final...
Embodiment 2
[0054] Fill a sufficient amount of methanol and a corresponding proportion of catalyst into the methanol storage tank 12, connect the carbon monoxide feed pipe 11 to a gas source containing 200L of carbon monoxide, start the system, set the system temperature to 175°C, and set the pressure to 3MPa. Methanol and the catalyst are transported to the interior of the reaction kettle 3, and at the same time, carbon monoxide is transported to the interior of the micro interface generator 2 through the carbon monoxide feed pipeline 11;
[0055] The micro-interface generator 2 breaks carbon monoxide into micro-bubbles of micron size, and releases the micro-bubbles into the reactor 3, so that the carbon monoxide fully contacts with methanol in the state of micro-bubbles, and the carbonylation reaction takes place.
[0056] The carbonylation reaction product is sent to the flash column 4 , the light component rectification column 51 and the heavy component rectification column 52 in seque...
Embodiment 3
[0058] Fill a sufficient amount of methanol and a corresponding proportion of catalyst into the methanol storage tank 12, connect the carbon monoxide feed pipe 11 to a gas source containing 200L of carbon monoxide, start the system, set the system temperature to 180°C, and set the pressure to 4MPa. Methanol and the catalyst are transported to the interior of the reaction kettle 3, and at the same time, carbon monoxide is transported to the interior of the micro interface generator 2 through the carbon monoxide feed pipeline 11;
[0059] The micro-interface generator 2 breaks carbon monoxide into micro-bubbles of micron size, and releases the micro-bubbles into the reactor 3, so that the carbon monoxide fully contacts with methanol in the state of micro-bubbles, and the carbonylation reaction takes place.
[0060] The carbonylation reaction product is sent to the flash column 4 , the light component rectification column 51 and the heavy component rectification column 52 in seque...
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