Tetrahydrofuran is used a lot in the process of pharmaceutical synthesis, polyurethane and some electronic materials. Its recovery difficulties are completely different from those of conventional aromatic hydrocarbon solvents: miscible with water, low boiling point, and easy to generate peroxides. These three characteristics determine that its recovery route cannot simply copy the practice of condensation and re-stratification, and the condensate treatment and storage links should be considered separately.
One is miscible with water. The condensate cannot be separated by static stratification, and the recovered mixture is often an aqueous mixture, which needs to be purified by distillation according to the subsequent process or directly enter the corresponding process for reuse. Second, the boiling point is low and the volatilization at normal temperature is fast. If the collection link is not sealed properly, the gas source concentration will be diluted by ambient air, and the scale of the device will be forced to enlarge. Third, the storage link should pay attention to the problem of peroxide, long-term storage or exposure to air after the risk, storage and treatment methods should be implemented according to the process requirements of the user.
Differences from conventional solvent recovery
| Comparison item | Tetrahydrofuran | Common solvents (such as toluene, ethyl acetate) |
|---|---|---|
| water-soluble | mutual solubility with water | Most are insoluble in water or have limited solubility |
| Condensate separation | Cannot be stratified by standing still. | Allow it to stand until the layers separate. |
| Boiling Point Level | Low, fast volatilization | Moderate or low |
| Storage Concerns | Storage conditions shall be controlled according to process requirements | Routine Closed Storage |
The degree of containment of the collection system is more worthy of investment than the condensation temperature level, because the scale of the equipment will be significantly enlarged after the gas source is diluted, and the unit recovery income will decrease. Condensate outlet temperature and condensate volume to keep continuous records, used to determine the state of the heat transfer surface. The storage time of the intermediate tank shall be controlled according to the process requirements to avoid long-term accumulation. The sampling analysis suggests a fixed frequency, and the change of water content will affect the choice of reuse mode.
Confirm the gas source composition, concentration fluctuation range, exhaust temperature, water content and the quality requirements of the reuse process, and then determine the recovery route and condensate treatment method. These data are clear, the scheme is not prone to the problem of disconnection between front-end recycling and back-end recycling.