A kind of method that utilizes yellow phosphorus tail gas to prepare ethylene glycol and recover iodine
A yellow phosphorus tail gas, ethylene glycol technology, applied in the carbon dioxide reduction method preparation, iodine, carbon monoxide and other directions, can solve the problems such as no report on the iodine recovery process, improve the recovery rate and the output of iodine, and reduce the recovery cost and cost reduced effect
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Embodiment 1
[0023] Such as figure 1 , the yellow phosphorus tail gas from the yellow phosphorus production workshop is sent to the PSA device, and the carbon dioxide in the yellow phosphorus tail gas is removed through the pressure swing adsorption to obtain the decarbonated waste gas, and then the decarbonated waste gas is sent to another PSA device , and then through the effect of pressure swing adsorption, the carbon monoxide in the decarbonation waste gas is removed to obtain pure carbon monoxide and decarbonization waste gas. After the pure carbon monoxide gas is compressed by a compressor, it is sent to the ethylene glycol production workshop; After the carbon monoxide exhaust gas is treated, its flow rate is controlled at 1dm 3 / min is sent into the iodine absorption tank in the iodine recovery workshop, and the temperature in the iodine absorption tank is controlled to be 60°C. The iodine absorption tank is equipped with a mass percentage concentration of 1% strong oxidant, wherei...
Embodiment 2
[0025] Such as figure 1 , the yellow phosphorus tail gas from the yellow phosphorus production workshop is sent to the PSA device, and the carbon dioxide in the yellow phosphorus tail gas is removed through the pressure swing adsorption to obtain the decarbonated waste gas, and then the decarbonated waste gas is sent to another PSA device , and then through the effect of pressure swing adsorption, the carbon monoxide in the decarbonation waste gas is removed to obtain pure carbon monoxide and decarbonization waste gas. After the pure carbon monoxide gas is compressed by a compressor, it is sent to the ethylene glycol production workshop; After the carbon monoxide exhaust gas is treated, its flow rate is controlled at 500dm 3 / min is sent in the iodine absorption tank in the iodine recovery workshop, and the temperature in the iodine absorption tank is controlled to be 80°C, and the mass percentage concentration is 70% strong oxidant is housed in the iodine absorption tank, whe...
Embodiment 3
[0027] Such as figure 1 , the yellow phosphorus tail gas from the yellow phosphorus production workshop is sent to the PSA device, and the carbon dioxide in the yellow phosphorus tail gas is removed through the pressure swing adsorption to obtain the decarbonated waste gas, and then the decarbonated waste gas is sent to another PSA device , and then through the effect of pressure swing adsorption, the carbon monoxide in the decarbonation waste gas is removed to obtain pure carbon monoxide and decarbonization waste gas. After the pure carbon monoxide gas is compressed by a compressor, it is sent to the ethylene glycol production workshop; After the carbon monoxide exhaust gas is treated, its flow rate is controlled at 400dm 3 / min is sent in the iodine absorption tank in the iodine recovery workshop, and the temperature in the iodine absorption tank is controlled to be 70°C, and the mass percentage concentration is equipped with a 60% strong oxidant in the iodine absorption tan...
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