Extraction-rectification recovery method of N, N-dimethylformamide
A technology of dimethylformamide and a recovery method, which is applied in the field of chemical waste solvent treatment and recovery, can solve problems such as clogging of adsorption channels, and achieve the effects of reducing process energy consumption, making the process green, and realizing industrialization.
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Embodiment 1
[0031]The obtained batch of N,N-dimethylformamide wastewater solvent, the concentration of N,N-dimethylformamide in it was determined to be 40%, using a single solvent octanoic acid as the extraction agent, entering from the lower part of the rotary disk extraction tower, The feed flow rate is fixed at 10ml / min, and the waste solvent enters from the upper part of the extraction tower, and the flow rate is set at 20ml / min. Set the rotary speed of the sieve-plate rotary-disk extraction tower to 40 r / min, the extraction temperature to 25° C., and obtain the extraction phase at the top of the extraction tower. The obtained extraction phase is subjected to a rectification operation, which enters from the middle of the rectification tower, and the operating pressure is controlled to be 0.75 atm, and the reflux ratio is set to 0.5. Under these operating conditions, a top fraction at a top temperature of 140.8°C was collected. Then the obtained fractions are further refined through a...
Embodiment 2
[0033] The obtained batch of N,N-dimethylformamide wastewater solvent, the concentration of N,N-dimethylformamide in it was determined to be 30%, using a single solvent octanoic acid as the extraction agent, entering from the lower part of the rotary disk extraction tower, The feed flow rate is fixed at 10ml / min, and the waste solvent enters from the upper part of the extraction tower, and the flow rate is set at 20ml / min. Set the rotary speed of the sieve plate rotary extraction tower to 60r / min, the extraction temperature to 25°C, and obtain the extraction phase at the top of the extraction tower. The obtained extraction phase is subjected to a rectification operation, which enters from the middle of the rectification tower, and the operating pressure is controlled to be 0.75 atm, and the reflux ratio is set to 0.5. Under these operating conditions, a top fraction at a top temperature of 140.8°C was collected. Then the obtained fractions are further refined through a dehydr...
Embodiment 3
[0035] The obtained batch of N,N-dimethylformamide wastewater solvent, the concentration of N,N-dimethylformamide was determined to be 15%, and a single solvent octanoic acid was used as the extraction agent, which entered from the lower part of the rotary extraction tower. The feed flow rate is fixed at 10ml / min, and the waste solvent enters from the upper part of the extraction tower, and the flow rate is set at 20ml / min. Set the rotary speed of the sieve plate rotary extraction tower to 60r / min, the extraction temperature to 25°C, and obtain the extraction phase at the top of the extraction tower. The obtained extraction phase is subjected to a rectification operation, which enters from the middle of the rectification tower, and the operating pressure is controlled to be 0.5 atm, and the reflux ratio is set to 0.5. Under these operating conditions, an overhead fraction was collected at an overhead temperature of 127.2°C. Then the obtained fractions are further refined thro...
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