Process for distillation and condensation

Claim 2

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead condensable vapor; (b) condensing the bulk of the overhead condensable vapor in a condensation zone, and producing a condensation zone effluent comprising vapor and liquid; (c) passing condensation zone effluent from step (b) to a separation zone, and separating said condensation zone effluent into a major vapor-liquid fraction and a minor first liquid fraction, and passing said major vapor-liquid fraction to an accumulation zone; (d) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (e) separating vapor from the major vapor-liquid fraction, and contacting cooled removed first liquid fraction with said separated vapor in the contacting zone, and producing a second liquid fraction in said contacting zone; and (f) collecting second liquid fraction from step (e) in the accumulation zone.

Claim 3

The method of claim 1 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 reflux liquid is returned to the column from the first accumulation section, and vapor from both accumulation sections is passed to the contacting zone.

Claim 4

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor fraction having a temperature differential of at least 20° F. between its dew point and its bubble point; (b) condensing the bulk of the overhead vapor fraction in a condensation zone, and producing a condensation zone effluent comprising vapor and liquid; (c) passing condensation zone effluent from step (b) to a separation zone, and separating said condensation zone effluent into a major vapor-liquid fraction and a minor first liquid fraction, and passing said major vapor-liquid fraction to an accumulation zone; (d) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (e) separating vapor from the major vapor-liquid fraction, and contacting cooled removed first liquid fraction with said separated vapor in the contacting zone, and producing a second liquid fraction in said contacting zone, and (f) collecting second liquid fraction from step (e) in the accumulation zone.

Claim 5

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor fraction having a temperature differential of at least 20° F. between its dew point and its bubble point; (b) condensing the bulk of the overhead vapor fraction in a condensation zone, and producing a condensation zone effluent comprising vapor and liquid; (c) passing condensation zone effluent from step (b) to a separation zone, and separating said condensation zone effluent into a major vapor-liquid fraction and a minor first liquid fraction, and passing said major vapor-liquid fraction to an accumulation zone; (d) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (e) separating vapor from the major vapor-liquid fraction, and contacting cooled removed first liquid fraction with said separated vapor in the contacting zone, and producing a second liquid fraction in said contacting zone, and (f) collecting second liquid fraction from step (e) in the accumulation zone.

Claim 6

The method of claim 3 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 reflux liquid is returned to the column from the first accumulation section, and vapor from both accumulation sections is passed to the contacting zone.

Claim 7

The method of claim 4 wherein the multi-component liquid is a crude oil.

Claim 8

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead condensable vapor; (b) separating a minor portion of vapor from the overhead condensable vapor; (c) condensing the remaining overhead condensable vapor in a condensation zone, and producing a liquid condensation zone effluent; (d) passing liquid condensation zone effluent from step (c) to a separation zone, and separating a first liquid fraction from said liquid condensation zone effluent, and passing the remaining liquid condensation zone effluent to an accumulation zone; (e) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (f) contacting cooled removed first liquid fraction from step (e) with at least a portion of said minor portion of vapor from step (b) in the contacting zone, and producing a second liquid fraction in said contacting zone; and (g) collecting second liquid fraction from step (f) in the accumulation zone.

Claim 9

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead condensable vapor; (b) separating a minor portion of vapor from the overhead condensable vapor; (c) condensing the remaining overhead condensable vapor in a condensation zone, and producing a liquid condensation zone effluent; (d) passing liquid condensation zone effluent from step (c) to a separation zone, and separating a first liquid fraction from said liquid condensation zone effluent, and passing the remaining liquid condensation zone effluent to an accumulation zone; (e) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (f) contacting cooled removed first liquid fraction from step (e) with at least a portion of said minor portion of vapor from step (b) in the contacting zone, and producing a second liquid fraction in said contacting zone; and (g) collecting second liquid fraction from step (f) in the accumulation zone.

Claim 10

The method of claim 6 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 reflux liquid is returned to the column from the first accumulation section, and vapor from both accumulation sections is passed to the contacting zone.

Claim 11

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor fraction having a temperature differential of at least 20° F. between its dew point and its bubble point; (b) separating a minor portion of vapor from the overhead vapor fraction; (c) condensing the remaining overhead vapor fraction in a condensation zone, and producing a liquid condensation zone effluent; (d) passing liquid condensation zone effluent from step (c) to a separation zone, and separating a first liquid fraction from said liquid condensation zone effluent, and passing the remaining liquid condensation zone effluent to an accumulation zone; (e) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (f) contacting cooled removed first liquid fraction from step (e) with at least a portion of said minor portion of vapor from step (b) in the contacting zone, and producing a second liquid fraction in said contacting zone; and (g) collecting second liquid fraction from step (f) in the accumulation zone.

Claim 12

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor fraction having a temperature differential of at least 20° F. between its dew point and its bubble point; (b) separating a minor portion of vapor from the overhead vapor fraction; (c) condensing the remaining overhead vapor fraction in a condensation zone, and producing a liquid condensation zone effluent; (d) passing liquid condensation zone effluent from step (c) to a separation zone, and separating a first liquid fraction from said liquid condensation zone effluent, and passing the remaining liquid condensation zone effluent to an accumulation zone; (e) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (f) contacting cooled removed first liquid fraction from step (e) with at least a portion of said minor portion of vapor from step (b) in the contacting zone, and producing a second liquid fraction in said contacting zone; and (g) collecting second liquid fraction from step (f) in the accumulation zone.

Claim 13

The method of claim 8 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 reflux liquid is returned to the column from the first accumulation section, and vapor from both accumulation sections is passed to the contacting zone.

Claim 14

The method of claim 9 wherein the multi-component liquid is a crude oil.

Claim 15

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead condensable vapor; (b) separating a minor portion of vapor from said overhead condensable vapor; (c) condensing the bulk of the remaining overhead condensable vapor in a condensation zone, and producing a condensation zone effluent comprising vapor and liquid; (d) passing condensation zone effluent from step (c) to a separation zone, and separating said condensation zone effluent into a major vapor-liquid fraction and a minor first liquid fraction, and passing said major vapor-liquid fraction to an accumulation zone; (e) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (f) separating vapor from the major vapor-liquid fraction; (g) contacting vapor separated from the major vapor-liquid fraction and at least a portion of said minor portion of vapor from step (b) with cooled removed first liquid fraction in the contacting zone, and producing a second liquid fraction; (h) collecting second liquid fraction from step (g) in the accumulation zone.

Claim 16

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead condensable vapor; (b) separating a minor portion of vapor from said overhead condensable vapor; (c) condensing the bulk of the remaining overhead condensable vapor in a condensation zone, and producing a condensation zone effluent comprising vapor and liquid; (d) passing condensation zone effluent from step (c) to a separation zone, and separating said condensation zone effluent into a major vapor-liquid fraction and a minor first liquid fraction, and passing said major vapor-liquid fraction to an accumulation zone; (e) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (f) separating vapor from the major vapor-liquid fraction; (g) contacting vapor separated from the major vapor-liquid fraction and at least a portion of said minor portion of vapor from step (b) with cooled removed first liquid fraction in the contacting zone, and producing a second liquid fraction; (h) collecting second liquid fraction from step (g) in the accumulation zone.

Claim 17

The method of claim 11 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 reflux liquid is returned to the column from the first accumulation section, and vapor from both accumulation sections is passed to the contacting zone.

Claim 18

The method of claim 12 wherein the multi-component liquid is a crude oil.

Claim 19

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor 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, and producing liquid condensate and partially cooled vapor; (c) passing liquid condensate from step (b) to an accumulation zone, and passing partially cooled vapor from step (b) to a second condensation zone having at least one condensation stage; (d) condensing the bulk of said partially cooled vapor in the second condensation zone, and producing a condensation zone effluent comprising vapor and liquid; (e) passing condensation zone effluent from step (c) to a separation zone, and separating said condensation zone effluent into a major vapor-liquid fraction and a minor first liquid fraction, and passing said major vapor-liquid fraction to an accumulation zone; (f) removing said liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (g) separating vapor from the major vapor-liquid fraction, and contacting cooled removed first liquid fraction step (f) with the separated vapor in said contacting zone, and producing a second liquid fraction; and (h) collecting second liquid fraction from step (g) in the accumulation zone.

Claim 20

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor 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, and producing liquid condensate and partially cooled vapor; (c) passing liquid condensate from step (b) to an accumulation zone, and passing partially cooled vapor from step (b) to a second condensation zone having at least one condensation stage; (d) condensing the bulk of said partially cooled vapor in the second condensation zone, and producing a condensation zone effluent comprising vapor and liquid; (e) passing condensation zone effluent from step (c) to a separation zone, and separating said condensation zone effluent into a major vapor-liquid fraction and a minor first liquid fraction, and passing said major vapor-liquid fraction to an accumulation zone; (f) removing said liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (g) separating vapor from the major vapor-liquid fraction, and contacting cooled removed first liquid fraction step (f) with the separated vapor in said contacting zone, and producing a second liquid fraction; and (h) collecting second liquid fraction from step (g) in the accumulation zone.

Claim 21

The method of claim 14 wherein a single accumulation zone is used for steps (c), (e) and (g), and 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 reflux liquid is returned to the column from the first accumulation section, and vapor from both accumulation sections is passed to the contacting zone.

Claim 22

The method of claim 15 wherein the multi-component liquid is a crude oil.

Claim 23

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor 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 first condensation zone having at least one condensation stage, and producing a first condensation zone effluent comprising liquid condensate and partially cooled vapor; (c) separating a minor portion of vapor from said first condensation zone effluent; (d) passing liquid condensate from step (b) to an accumulation zone, and passing remaining partially cooled vapor producing in step (c) to a second condensation zone having at least one condensation stage; (e) condensing remaining partially cooled vapor produced in step (c) in the second condensation zone, and producing a liquid condensation zone effluent; (f) passing liquid condensation zone effluent from step (e) to a separation zone, and separating a first liquid fraction from said liquid condensation zone effluent, and passing remaining liquid condensation zone effluent to an accumulation zone; (g) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (h) contacting cooled removed first liquid fraction from step (g) with at least a portion of said minor portion of partially cooled vapor from step (c) in the contacting zone, and producing a second liquid fraction; and (i) collecting second liquid fraction from step (h) in the accumulation zone of step (f).

Claim 24

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor 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 first condensation zone having at least one condensation stage, and producing a first condensation zone effluent comprising liquid condensate and partially cooled vapor; (c) separating a minor portion of vapor from said first condensation zone effluent; (d) passing liquid condensate from step (b) to an accumulation zone, and passing remaining partially cooled vapor producing in step (c) to a second condensation zone having at least one condensation stage; (e) condensing remaining partially cooled vapor produced in step (c) in the second condensation zone, and producing a liquid condensation zone effluent; (f) passing liquid condensation zone effluent from step (e) to a separation zone, and separating a first liquid fraction from said liquid condensation zone effluent, and passing remaining liquid condensation zone effluent to an accumulation zone; (g) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (h) contacting cooled removed first liquid fraction from step (g) with at least a portion of said minor portion of partially cooled vapor from step (c) in the contacting zone, and producing a second liquid fraction; and (i) collecting second liquid fraction from step (h) in the accumulation zone of step (f).

Claim 25

The method of claim 17 wherein a single accumulation zone is used for steps (d), (f) and (i), and 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 reflux liquid is returned to the column from the first accumulation section, and vapor from both accumulation sections is passed to the contacting zone.

Claim 26

The method of claim 18 wherein the multi-component liquid is a crude oil.

Claim 27

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor 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 first condensation zone having at least one condensation stage, and producing a first condensation zone effluent comprising liquid condensate and partially cooled vapor; (c) separating a minor portion of vapor from said first condensation zone effluent, and passing liquid condensate from step (b) to an accumulation zone; (d) condensing at least the bulk of the remaining partially cooled vapor from step (b) in a second condensation zone, and producing a second condensation zone effluent comprising vapor and liquid; (e) passing second condensation zone effluent from step (d) to a separation zone, and separating a first liquid fraction from said second condensation zone effluent, and passing remaining second condensation zone effluent comprising vapor and liquid to an accumulation zone; (f) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (g) separating vapor from the second condensation zone effluent; (h) contacting vapor separated from the second condensation zone effluent and at least a portion of said minor portion of partially cooled vapor from the first condensation zone effluent with cooled removed first liquid fraction in said contacting zone, and producing a second liquid fraction; and (i) collecting second liquid fraction from step (h) in the accumulation zone.

Claim 28

A process comprising (a) distilling a multi-component liquid in a distillation column under conditions effective to provide an overhead vapor 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 first condensation zone having at least one condensation stage, and producing a first condensation zone effluent comprising liquid condensate and partially cooled vapor; (c) separating a minor portion of vapor from said first condensation zone effluent, and passing liquid condensate from step (b) to an accumulation zone; (d) condensing at least the bulk of the remaining partially cooled vapor from step (b) in a second condensation zone, and producing a second condensation zone effluent comprising vapor and liquid; (e) passing second condensation zone effluent from step (d) to a separation zone, and separating a first liquid fraction from said second condensation zone effluent, and passing remaining second condensation zone effluent comprising vapor and liquid to an accumulation zone; (f) removing said first liquid fraction from said separation zone and cooling the removed first liquid fraction, and passing the cooled removed first liquid fraction to a contacting zone; (g) separating vapor from the second condensation zone effluent; (h) contacting vapor separated from the second condensation zone effluent and at least a portion of said minor portion of partially cooled vapor from the first condensation zone effluent with cooled removed first liquid fraction in said contacting zone, and producing a second liquid fraction; and (i) collecting second liquid fraction from step (h) in the accumulation zone.

Claim 29

The method of claim 20 wherein a single accumulation zone is used for steps (c), (e) and (i), and 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 reflux liquid is returned to the column from the first accumulation section, and vapor from both accumulation sections is passed to the contacting zone.

Claim 30

The method of claim 21 wherein the multi-component liquid is a crude oil.