Heat exchanger and double distillation column

Claim 2

A heat exchanger for indirectly exchanging heat between first and second fluids and for use with a sump, said heat exchanger comprising: a plurality of first passages for receiving at least a liquid phase of a froth of a first fluid; a plurality of second passages for receiving a second fluid; said first and second passages alternating with one an other in a heat transfer relationship to allow said liquid phase of said froth to partially vaporize and thereby to form a vapor phase of said froth through indirect heat exchange with said second fluid; said first passages being open at a bottom region of said heat exchanger to discharge at least a liquid resulting from a remaining part of said liquid phase, not vaporized through said indirect heat exchange, to said sump; inlet and outlet means for introducing and discharging said second fluid to and from said second passages; a reservoir located above said first and second passages for receiving said first fluid and for containing said froth; and orifice means for providing flow communication between said reservoir and said first passage so that at least part of said vapor phase of said froth flows through said orifices to said reservoir and interacts with said first fluid to form said froth; each of said orifices having a weep point at which said at least said liquid phase of said froth weeps into said second passages through said orifices, thereby to automatically replenish said first passages with said liquid phase of said froth.

Claim 3

The heat exchanger of claim 1, wherein said orifice means comprises a distributor tray having a plurality of transversely oriented slots and legs supporting said distributor tray above said first and second passages.

Claim 4

The heat exchanger of claim 1, wherein said first and second passages contain corrugated fin material.

Claim 5

The heat exchanger of claim 1, wherein: said orifice means comprises a distributor tray having a plurality of transversely oriented slots and legs supporting said distributor tray above said first and second passages; said legs overlie said fast passages; said first and second passages contain corrugated fin material; and said legs rest on said corrugated fin material.

Claim 6

The heat exchanger of claim 1 or claim 4, wherein said inlet means is located above said outlet means.

Claim 7

The heat exchanger of claim 1, further comprising a skirt depending from said bottom region of said heat exchanger to project into a level of said liquid located within said sump.

Claim 8

The heat exchanger of claim 6 wherein said skirt has a plurality of apertures configured such that a greater proportion of said vaporized liquid is discharged from said orifices as said level of said liquid rises within said sump.

Claim 9

The heat exchanger of claim 1 wherein said fast and second passages are defined between a plurality of vertically oriented, parallel plates.

Claim 10

A double distillation column for rectifying a mixture containing higher and lower boiling components, said double distillation column comprising: a higher pressure column and a lower pressure column; a sump to collect a columns bottom liquid enriched in said higher boiling components; said higher pressure column having a tower overhead region for collecting a vapor tower overhead enriched in said lower boiling components; and at least one condenser/reboiler located within said bottom region of said lower pressure distillation column to condense said vapor tower overhead against vaporizing a reboiler feed, said at least one condenser/reboiler comprising: a plurality of first passages for receiving at least a liquid phase of a froth composed of said reboiler feed; a plurality of second passages for receiving said vapor tower overhead; said first and second passages alternating with one an other in a heat transfer relationship to allow said liquid phase to partially vaporize and thereby to form a vapor phase of said froth through indirect heat exchange with vapor tower overhead; said first passages being open at a bottom region of said heat exchanger to discharge at least said liquid column bottoms, composed of a remaining part of said liquid phase not vaporized through said indirect heat exchange, to said sump; inlet and outlet means for introducing said vapor tower overhead into said second passages and for discharging condensed vapor tower overhead from said second passages, respectively; a reservoir located above said first and second passages for receiving said reboiler feed and for containing said froth; and orifice means having orifices for providing flow communication between said reservoir and said first passages so that at least part of said vapor phase of said froth flows through said orifices to said reservoir and interacts with said reboiler feed to form said froth; each of said orifices having a weep point at which said at least said liquid phase of said froth weeps into said first passages through said orifices, thereby to automatically replenish said first passages with said liquid phase of said froth.

Claim 11

A double distillation column for rectifying a mixture containing higher and lower boiling components, said double distillation column comprising: a higher pressure column and a lower pressure column; a sump to collect a columns bottom liquid enriched in said higher boiling components; said higher pressure column having a tower overhead region for collecting a vapor tower overhead enriched in said lower boiling components; and at least one condenser/reboiler located within said bottom region of said lower pressure distillation column to condense said vapor tower overhead against vaporizing a reboiler feed, said at least one condenser/reboiler comprising: a plurality of first passages for receiving at least a liquid phase of a froth composed of said reboiler feed; a plurality of second passages for receiving said vapor tower overhead; said first and second passages alternating with one an other in a heat transfer relationship to allow said liquid phase to partially vaporize and thereby to form a vapor phase of said froth through indirect heat exchange with vapor tower overhead; said first passages being open at a bottom region of said heat exchanger to discharge at least said liquid column bottoms, composed of a remaining part of said liquid phase not vaporized through said indirect heat exchange, to said sump; inlet and outlet means for introducing said vapor tower overhead into said second passages and for discharging condensed vapor tower overhead from said second passages, respectively; a reservoir located above said first and second passages for receiving said reboiler feed and for containing said froth; and orifice means having orifices for providing flow communication between said reservoir and said first passages so that at least part of said vapor phase of said froth flows through said orifices to said reservoir and interacts with said reboiler feed to form said froth; each of said orifices having a weep point at which said at least said liquid phase of said froth weeps into said first passages through said orifices, thereby to automatically replenish said first passages with said liquid phase of said froth.

Claim 12

The double distillation column of claim 9, wherein said orifice means comprises a distributor tray having a plurality of transversely oriented slots and legs supporting said distributor tray above said first and second passages.

Claim 13

The double distillation column of claim 10, wherein: said first and second passages contain corrugated fin material; and said legs rest on said corrugated fin material.

Claim 14

The double distillation column of claim 11, wherein said inlet means is located above said outlet means.

Claim 15

The double distillation column of claim 9, wherein; said sump is located within said lower pressure column; and said condenser/reboiler is positioned within said lower pressure column with its said bottom region located within said sump.

Claim 16

The double distillation column of claim 9, wherein: said sump is located within said lower pressure column; said condenser/reboiler is positioned within said lower pressure column; and said condenser/reboiler also has a skirt depending from said bottom region of said condenser/reboiler to project into a level of said liquid column bottoms located within said sump.

Claim 17

The double distillation column of claim 14 wherein said skirt has a plurality of apertures configured such that a greater proportion of said vapor phase is discharged from said orifices as said level of said liquid rises within said sump.

Claim 18

The double distillation column of claim 9, wherein said first and second passages are defined between a plurality of vertically oriented, parallel plates.