Distillation with condensation process

Claim 2

A process comprising: (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead fraction having a temperature differential of at least 20° F. between its dew point and its bubble point; (b) condensing a portion of the overhead fraction in a condensation zone having at least one condensation stage, producing a condensation zone effluent comprising vapor and liquid; (c) removing condensation zone effluent from the condensation zone and separating the liquid from the condensation zone effluent to produce a condensation zone effluent vapor, and accumulating said liquid in an accumlation zone; (d) removing a first liquid stream from said accumulation zone, and utilizing said first liquid stream as reflux in said distillation column; (e) removing a second liquid stream from said accumulation zone, and cooling said stream to a temperature of at least 10° F. below the temperature of the liquid in said accumulation zone, and producing a cooled removed liquid; (f) passing condensation zone effluent vapor from step (c) to a contacting zone, and contacting said condensation zone effluent vapor with the cooled removed to condense and absorb components of said vapor in said cooled removed liquid and produce a combined liquid, and collecting the combined liquid in the accumulation zone.

Claim 3

The process of claim 1 wherein the second liquid stream of step (e) is cooled to a temperature of from about 10° F. to about 100° F. below the temperature of the liquid in the accumulation zone.

Claim 4

The process of claim 2 wherein the multi-component liquid is a crude oil.

Claim 5

The process of claim 1 wherein the vapor and liquid in the condensation zone effluent are separated in the accumulation zone.

Claim 6

The process of claim 4 wherein the accumulation zone comprises a first accumulation section and a second accumulation section having vapor communication with the first accumulation section but being separated from said first accumulation section by a barrier which provides limited flow of liquids between the first accumulation section and the second accumulation section, the first accumulation section and the second accumulation section being at different liquid temperatures, and wherein the vapor and liquid from the condensation zone effluent are recovered and separated in the first accumulation section.

Claim 7

A process comprising: (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead fraction having a temperature differential of at least 20° F. between its dew point and its bubble point; (b) condensing of the overhead fraction in a first condensation zone having at least one condensation stage, producing a first condensation zone effluent comprising liquid and vapor, and removing liquid and vapor from said first condensation zone and collecting said liquid and vapor in a first accumulation zone, said accumulation zone comprising at least a first accumulation section and a second accumulation section having vapor communication with the first accumulation section but being separated from said first accumulation section by a barrier for liquid, the first accumulation section and the second accumulation section being at different liquid temperatures; (c) removing a first liquid steam from said first accumulation section, and utilizing said first liquid stream as reflux in said distillation column; (d) passing a vapor stream from the first accumulation zone to a second condensation zone, and condensing a portion of said vapor steam in said second condensation zone and producing a second condensation zone effluent comprising a second vapor and a second liquid; (e) removing second condensation zone effluent from the second condensation zone and separating second liquid from said second condensation zone effluent to produce a second condensation zone effluent vapor, and accumulating second liquid in a third accumulation section is a second accumulation zone, said second accumulation zone comprising said third accumlation section and a fourth accumulation section having vapor communication with the third accumulation section but being separated from said third accumulation section by a barrier which provides limited flow of liquids between the third accumulation section and the fourth accumulation section, the third accumulation section and the fourth accumulation section being at different liquid temperatures, removing a second light stream from said third accumulation section, and cooling said stream to a temperature of at least about 10° F. below the temperature of the liquid accumulation section, and producing a cooled removed liquid; (g) passing second condensation zone effluent vapor from step (e) to a contacting zone, and contacting said second condensation zone effluent vapor with cooled removed liquid to condense and absorb components of said second condensation zone effluent vapor in said cooled removed liquid and produce a combined liquid, and collecting the combined liquid in the fourth accumulation section.

Claim 8

A process comprising: (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead fraction having a temperature differential of at least 20° F. between its dew point and its bubble point; (b) condensing of the overhead fraction in a first condensation zone having at least one condensation stage, producing a first condensation zone effluent comprising liquid and vapor, and removing liquid and vapor from said first condensation zone and collecting said liquid and vapor in a first accumulation zone, said accumulation zone comprising at least a first accumulation section and a second accumulation section having vapor communication with the first accumulation section but being separated from said first accumulation section by a barrier for liquid, the first accumulation section and the second accumulation section being at different liquid temperatures; (c) removing a first liquid steam from said first accumulation section, and utilizing said first liquid stream as reflux in said distillation column; (d) passing a vapor stream from the first accumulation zone to a second condensation zone, and condensing a portion of said vapor steam in said second condensation zone and producing a second condensation zone effluent comprising a second vapor and a second liquid; (e) removing second condensation zone effluent from the second condensation zone and separating second liquid from said second condensation zone effluent to produce a second condensation zone effluent vapor, and accumulating second liquid in a third accumulation section is a second accumulation zone, said second accumulation zone comprising said third accumlation section and a fourth accumulation section having vapor communication with the third accumulation section but being separated from said third accumulation section by a barrier which provides limited flow of liquids between the third accumulation section and the fourth accumulation section, the third accumulation section and the fourth accumulation section being at different liquid temperatures, removing a second light stream from said third accumulation section, and cooling said stream to a temperature of at least about 10° F. below the temperature of the liquid accumulation section, and producing a cooled removed liquid; (g) passing second condensation zone effluent vapor from step (e) to a contacting zone, and contacting said second condensation zone effluent vapor with cooled removed liquid to condense and absorb components of said second condensation zone effluent vapor in said cooled removed liquid and produce a combined liquid, and collecting the combined liquid in the fourth accumulation section.

Claim 9

The process of claim 6 wherein the second liquid stream of step (f) is cooled to a temperature of from about 10° F. below the temperature of the liquid in the third accumulation section.

Claim 10

The process of claim 7 wherein the multi-component liquid is a crude oil.

Claim 11

The process of claim 6 wherein the second vapor and second liquid in the second condensation zone effluent are separated in said third accumulation section of said second accumulation zone.

Claim 12

The process of claim 9 wherein the limited flow of liquids is through an opening in the barrier sized to achieve liquid balance without significant mixing of liquids between the sections.

Claim 13

A process comprising: (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead condensable vapor; (b) condensing a portion of the vapor in a condensation zone, producing a condensation zone effluent comprising vapor and liquid; (c) removing condensation zone effluent from the condensation zone and separating the liquid from the condensation zone effluent to produce a condensation zone effluent vapor, and accumulating said liquid in an accumulation zone; (d) removing a first liquid stream from said accumulation zone, and utilizing said first liquid stream as reflux in said distillation column; (e) removing a second liquid stream said accumulation zone, and cooling said stream to a temperature of at least about 10° F. below the temperature of the liquid in said accumulation zone, and producing a cooled removed liquid; (f) passing condensation zone effluent vapor from step (c) to a contacting zone, and contacting said condensation zone effluent vapor with the cooled removed liquid to condense and absorb components of said condensation zone effluent vapor in said cooled removed liquid and produce a combined liquid, and collecting the combined liquid in the accumulation zone.

Claim 14

A process comprising: (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead condensable vapor; (b) condensing a portion of the vapor in a condensation zone, producing a condensation zone effluent comprising vapor and liquid; (c) removing condensation zone effluent from the condensation zone and separating the liquid from the condensation zone effluent to produce a condensation zone effluent vapor, and accumulating said liquid in an accumulation zone; (d) removing a first liquid stream from said accumulation zone, and utilizing said first liquid stream as reflux in said distillation column; (e) removing a second liquid stream said accumulation zone, and cooling said stream to a temperature of at least about 10° F. below the temperature of the liquid in said accumulation zone, and producing a cooled removed liquid; (f) passing condensation zone effluent vapor from step (c) to a contacting zone, and contacting said condensation zone effluent vapor with the cooled removed liquid to condense and absorb components of said condensation zone effluent vapor in said cooled removed liquid and produce a combined liquid, and collecting the combined liquid in the accumulation zone.

Claim 15

The process of claim 11 wherein the said second liquid stream of step (e) is cooled to a temperature of from about 10° F. below the temperature of the liquid in the accumulation zone.

Claim 16

The process of claim 11 wherein the vapor and liquid in the condensation zone are separated in the accumulation zone.

Claim 17

The process of claim 13 wherein the accumulation zone comprises a first accumulation section and a second accumulation section having vapor communication with the first accumulation section but being separated from said first accumulation section by a barrier which provides limited flow of liquids between the first accumulation section and the second accumulation section, the first accumulation section and the second accumulation section being at different liquid temperatures, and wherein the vapor and liquid from the condensation zone effluent are recovered and separated in the first accumulation section.