초록 ▼

A continuous distillation apparatus and method, the apparatus including separate stripping and rectifying sections in tandem, each of which are segregated into a plurality of vapor/liquid contact stages. The rectifying section is operated at a higher temperature than the stripping section by compres

A continuous distillation apparatus and method, the apparatus including separate stripping and rectifying sections in tandem, each of which are segregated into a plurality of vapor/liquid contact stages. The rectifying section is operated at a higher temperature than the stripping section by compressing vapor from the stripping section prior to introducing the vapor into the rectifying section. Thermal energy is conserved during the distillation process by transferring thermal energy from the rectifying section to the stripping section with a plurality of heat pipes.

대표청구항 ▼

A distillation apparatus comprising: a vertical column; a longitudinal divider completely segregating the column into a stripping section and a rectifying section, the divider allowing each of the stripping section and the rectifying section to be maintained at different pressures; and a plurality o

A distillation apparatus comprising: a vertical column; a longitudinal divider completely segregating the column into a stripping section and a rectifying section, the divider allowing each of the stripping section and the rectifying section to be maintained at different pressures; and a plurality of heat pipes transecting the divider and extending between the stripping section and the rectifying section for transferring thermal energy from the rectifying section to the stripping section. A method for improving thermodynamic efficiency during the continuous distillation of multicomponent fluid mixtures comprising: vertically orienting a closed vessel; segregating the vessel with a longitudinal divider into a stripping section and a parallel rectifying section, the divider accommodating maintaining different pressures in the stripping section and the rectifying section; forming a plurality of vapor/liquid contact stages in each of the stripping section and the rectifying section; mounting a plurality of heat pipes between the stripping section and the rectifying section thereby thermally interconnecting at least some of the vapor/liquid contact stages of the stripping section with at least some of the vapor/liquid contact stages of the rectifying section with the plurality of heat pipes; introducing a multicomponent fluid mixture into the stripping section adjacent the upper end of the stripping section as a feed stream; separating vapor from the multicomponent fluid mixture in the stripping section during passage through the vapor/liquid contact stages, said vapor representing a lower boiling point fraction of the feed stream; operating the rectifying section at a first pressure and at a higher temperature than the stripping section by removing said vapor from the stripping section and compressing said vapor to a second pressure prior to introducing said vapor into the rectifying section; condensing vapor from the rectifying section and recycling a portion of the condensed vapor as a reflux liquid into the rectifying section; and transferring thermal energy from the rectifying section to the stripping section with the plurality of heat pipes thereby conserving energy during the continuous distillation of said feed stream.