A multi-stage flash reversal unit includes a housing; plural stages located inside the housing; an evaporation port that receives a water feed having a first temperature; a condensation port that outputs a concentrated water feed having a second temperature, which is lower than the first temperature; and a cooling unit that cools down the concentrated water feed.

The present disclosure relates to isolating one or more cannabinoids from an input mixture. There is disclosed an apparatus that comprises a mixing vessel, a volatizing unit, and a distillation unit. The mixing vessel combines a first input mixture and a high boiling-point carrier agent to generate a second input mixture. The volatizing unit volatilizes cannabinoids from the second input mixture for separating the mixture into a cannabinoid-containing vapor stream and a residue. The distillation unit receives the cannabinoid-containing vapor stream and separates a first cannabinoid from at least a second cannabinoid. There are also disclosed methods that comprise the steps of combining a first input mixture with a high boiling-point carrier agent to provide a second input mixture, volatilizing the second input mixture into a vapor stream containing one or more cannabinoids and a residue, and separating a first cannabinoid from a second in the distillation unit.

Provide is a distillation tower management system, a distillation tower state analysis method, and a distillation tower management method that are capable of predicting abnormality in distillation towers before the abnormality becomes apparent and capable of taking preventive actions. The distillation tower management system includes a measurement unit 10 that is at least one selected from the group consisting of a pressure measurement unit 11, a temperature measurement unit 12 and a chlorine measurement unit 13, an operation data unit 20 for producing operation data containing measurement data measured with the measurement unit 10, an analysis unit 30 for analyzing the state of a distillation tower 103 from the operation data and producing analysis data regarding the state of the distillation tower 103, and a control unit 40 for producing, based on the analysis data, control data regarding a differential pressure-eliminating agent that is added to the distillation tower 103.

Provide is a distillation tower management system, a distillation tower state analysis method, and a distillation tower management method that are capable of predicting abnormality in distillation towers before the abnormality becomes apparent and capable of taking preventive actions. The distillation tower management system includes a measurement unit 10 that is at least one selected from the group consisting of a pressure measurement unit 11, a temperature measurement unit 12 and a chlorine measurement unit 13, an operation data unit 20 for producing operation data containing measurement data measured with the measurement unit 10, an analysis unit 30 for analyzing the state of a distillation tower 103 from the operation data and producing analysis data regarding the state of the distillation tower 103, and a control unit 40 for producing, based on the analysis data, control data regarding a differential pressure-eliminating agent that is added to the distillation tower 103.

Provided is a method for preparing synthesis gas, and more particularly, a method for preparing synthesis gas including: supplying a pyrolysis fuel oil (PFO) stream including a PFO and a pyrolysis gas oil (PGO) stream including a PGO discharged from a naphtha cracking center (NCC) process to a distillation tower as a feed stream (S10); and supplying a lower discharge stream from the distillation tower to a combustion chamber for a gasification process to obtain synthesis gas (S20), wherein the PGO stream is supplied to an upper end of the distillation tower and the PFO stream is supplied to a lower end of the distillation tower.

An herbal distillation device includes a herb chamber with perforated holes for holding herbs and a closed heated boiling chamber with openings at the side for a steam outlet. The herbal distillation device further includes an electric air-cooled condensation chamber which connects to the boiling chamber.

An herbal distillation device includes a herb chamber with perforated holes for holding herbs and a closed heated boiling chamber with openings at the side for a steam outlet. The herbal distillation device further includes an electric air-cooled condensation chamber which connects to the boiling chamber.

The present disclosure provides a control method for a rectification and purification system of electronic-grade chlorine trifluoride. A rectification device of electronic-grade chlorine trifluoride includes a two-stage cryogenic rectification device including a low-boiling column and a high-boiling column. An extraction agent is arranged in the two-stage cryogenic rectification device for further dissociating associated molecules of hydrogen fluoride and chlorine trifluoride to meet the requirements of electronic-grade chlorine trifluoride. The reflux ratio parameter stability of a vapor-liquid (chlorine trifluoride-hydrogen fluoride) phase equilibrium system can be effectively improved by a column plate temperature control method, thus realizing wide dynamic smooth running under various working conditions. The column plate temperature control method can achieve an effective separation of chlorine trifluoride and various impurity components by deep rectification technology, yielding electronic-grade chlorine trifluoride through purification.

The present disclosure provides a control method for a rectification and purification system of electronic-grade chlorine trifluoride. A rectification device of electronic-grade chlorine trifluoride includes a two-stage cryogenic rectification device including a low-boiling column and a high-boiling column. An extraction agent is arranged in the two-stage cryogenic rectification device for further dissociating associated molecules of hydrogen fluoride and chlorine trifluoride to meet the requirements of electronic-grade chlorine trifluoride. The reflux ratio parameter stability of a vapor-liquid (chlorine trifluoride-hydrogen fluoride) phase equilibrium system can be effectively improved by a column plate temperature control method, thus realizing wide dynamic smooth running under various working conditions. The column plate temperature control method can achieve an effective separation of chlorine trifluoride and various impurity components by deep rectification technology, yielding electronic-grade chlorine trifluoride through purification.

Disclosed are processes and systems for removing water from a polyether polyol that employs a controlled temperature and pressure profile.