Absorption-absorption-absorption vapor recovery process

Claim 2

In a process in which hydrocarbon components are removed from an inlet air-hydrocarbon mixture by passing said inlet air-hydrocarbon mixture through solid adsorbent beds capable of selectively adsorbing hydrocarbon components from said inlet air-hydrocarbon mixture to exhaust substantially hydrocarbon free air, and in which said adsorbent beds are vacuum regenerated to produce a rich air hydrocarbon mixture which is passed to a liquid hydrocarbon absorbent absorber in which a substantial portion of the hydrocarbon components are absorbed from the rich air-hydrocarbon mixture with a liquid hydrocarbon absorbent to produce an absorber overhead gas containing nonabsorbed hydrocarbon components, the improvement comprising: (a) producing a flashed absorbent stream by flashing an effective amount of a liquid having an affinity to absorb hydrocarbon components from the inlet air-hydrocarbon mixture; (b) mixing the absorber overhead gas from the liquid hydrocarbon absorbent absorber with the inlet air-hydrocarbon mixture; (c) passing the combined absorber overhead gas and inlet air-hydrocarbon mixture from step (b) in absorption relationship with the flashed absorbent stream in a flashed hydrocarbon absorbent absorber to produce another absorber overhead gas and to produce an enriched absorber bottom liquid; and (d) passing said other absorber overhead gas from step (c) to the solid adsorbent beds for adsorbing substantially all of the hydrocarbon components in the other absorber overhead gas.

Claim 3

The improvement of claim 1 further comprising: passing the enriched absorber bottom liquid from the flashed hydrocarbon absorbent absorber to a flash vessel to regenerate the flashed absorbent stream and to produce an overhead flash vapor stream; returning the regenerated flashed absorbent stream to the flashed hydrocarbon absorbent absorber; and passing the flash vapor stream from the flash vessel to the liquid hydrocarbon absorbent absorber which receives the rich air-hydrocarbon mixture from the adsorbent beds.

Claim 4

The improvement of claim 2 further comprising: bleeding an incremental part of the flashed absorbent stream at a predetermined rate.

Claim 5

The improvement of claim 3 further comprising: making up the flashed absorbent stream with an amount of the liquid hydrocarbon absorbent as required to maintain a desired system inventory of same.

Claim 6

The improvement of claim 2 wherein a subatmospheric pressure of between about 1.0 to about 5.0 psia is maintained in the flash vessel by a liquid ring vacuum pump.

Claim 7

The improvement of claim 2 wherein the air-hydrocarbon mixture comprises air-gasoline vapors and wherein the liquid hydrocarbon absorbent is gasoline.

Claim 8

The improvement of claim 3 wherein the air-hydrocarbon mixture comprises air-gasoline vapors and wherein the liquid hydrocarbon absorbent is gasoline.

Claim 9

The improvement of claim 4 wherein the air-hydrocarbon mixture comprises air-gasoline vapors and wherein the liquid hydrocarbon absorbent is gasoline.

Claim 10

The improvement of claim 5 wherein the air-hydrocarbon mixture comprises air-gasoline vapors and wherein the liquid hydrocarbon absorbent is gasoline.

Claim 11

A process for recovering hydrocarbon components from an air-hydrocarbon mixture, comprising: (a) flashing a liquid hydrocarbon in a flash vessel which is at subatmospheric pressure to produce a flashed hydrocarbon absorbent; (b) absorbing a portion of the hydrocarbon components from the inlet air-hydrocarbon mixture with the flashed hydrocarbon absorbent in a first absorber to produce a first absorber overhead gas stream containing hydrocarbon components and air, and producing a first absorber bottom liquid; (c) passing the first absorber overhead gas through a solid adsorbent bed capable of selectively adsorbing the hydrocarbon components therefrom so as to leave substantially hydrocarbon free air; (d) venting the substantially hydrocarbon free air to the atmosphere; (e) subjecting the hydrocarbon laden solid adsorbent bed to a vacuum with a liquid ring vacuum pump to desorb the adsorbed hydrocarbon components therefrom so as to produce a rich air-hydrocarbon mixture comprising recovered liquid hydrocarbon and liquid from the liquid ring vacuum pump; (f) separating the liquid from the liquid ring vacuum pump in the rich air-hydrocarbon mixture from the solid adsorbent bed; (g) absorbing substantially all of the hydrocarbon components from the rich air-hydrocarbon mixture with a liquid hydrocarbon absorbent in a second absorber to produce a second absorber overhead gas stream and a recovered liquid hydrocarbon mixed with said liquid hydrocarbon absorbent; (h) combining the second absorber overhead gas stream with the inlet air-hydrocarbon mixture prior to passing same to the first absorber for the absorption step (b) above; (i) passing the first absorber overhead gas from the absorption step (b) above to a second solid adsorbent bed capable of selectively adsorbing the hydrocarbon components therein to leave substantially hydrocarbon free air; (j) venting the substantially hydrocarbon free air of step (i) to the atmosphere; (k) cooling the liquid ring vacuum pump liquid; and (1) recycling said liquid ring vacuum pump liquid for use in the liquid ring vacuum pump.

Claim 12

A process for recovering hydrocarbon components from an air-hydrocarbon mixture, comprising: (a) flashing a liquid hydrocarbon in a flash vessel which is at subatmospheric pressure to produce a flashed hydrocarbon absorbent; (b) absorbing a portion of the hydrocarbon components from the inlet air-hydrocarbon mixture with the flashed hydrocarbon absorbent in a first absorber to produce a first absorber overhead gas stream containing hydrocarbon components and air, and producing a first absorber bottom liquid; (c) passing the first absorber overhead gas through a solid adsorbent bed capable of selectively adsorbing the hydrocarbon components therefrom so as to leave substantially hydrocarbon free air; (d) venting the substantially hydrocarbon free air to the atmosphere; (e) subjecting the hydrocarbon laden solid adsorbent bed to a vacuum with a liquid ring vacuum pump to desorb the adsorbed hydrocarbon components therefrom so as to produce a rich air-hydrocarbon mixture comprising recovered liquid hydrocarbon and liquid from the liquid ring vacuum pump; (f) separating the liquid from the liquid ring vacuum pump in the rich air-hydrocarbon mixture from the solid adsorbent bed; (g) absorbing substantially all of the hydrocarbon components from the rich air-hydrocarbon mixture with a liquid hydrocarbon absorbent in a second absorber to produce a second absorber overhead gas stream and a recovered liquid hydrocarbon mixed with said liquid hydrocarbon absorbent; (h) combining the second absorber overhead gas stream with the inlet air-hydrocarbon mixture prior to passing same to the first absorber for the absorption step (b) above; (i) passing the first absorber overhead gas from the absorption step (b) above to a second solid adsorbent bed capable of selectively adsorbing the hydrocarbon components therein to leave substantially hydrocarbon free air; (j) venting the substantially hydrocarbon free air of step (i) to the atmosphere; (k) cooling the liquid ring vacuum pump liquid; and (1) recycling said liquid ring vacuum pump liquid for use in the liquid ring vacuum pump.

Claim 13

The process of claim 10 further comprising: removing a portion of the flashed hydrocarbon absorbent stream at a predetermined rate; and making up said flashed hydrocarbon absorbent with the liquid hydrocarbon as required to maintain the desired system inventory of same.

Claim 14

The process of claim 11 wherein the first absorber is maintained at slightly above atmospheric pressure.

Claim 15

The process of claim 12 wherein the flash vessel is maintained at a vacuum of about 1.0 to about 5.0 psia.

Claim 16

The process of claim 11 wherein the air-hydrocarbon mixture comprises air-gasoline vapors and wherein the liquid hydrocarbon absorbent used in the second absorber is gasoline.

Claim 17

The process of claim 14 wherein the liquid hydrocarbon used in the flash vessel for producing the flashed hydrocarbon absorbent is gasoline.

Claim 18

A process for removing and recovering gasoline vapors from an air-gasoline vapor mixture, comprising: (a) passing an inlet stream of air-gasoline vapors through a first absorber in liquid-vapor absorption relationship with vacuum flashed liquid gasoline absorbent to produce a first absorber overhead gas containing nonabsorbed hydrocarbon vapors and air, and to produce a first absorber bottom liquid containing recovered hydrocarbon components of the gasoline vapors of the inlet stream of air-gasoline vapors; (b) passing the first absorber overhead gas to a first solid adsorbent bed capable of selectively adsorbing the nonabsorbed hydrocarbon vapors and to leave substantially hydrocarbon free air; (c) passing the first absorber bottom liquid to a flash vessel maintained at subatmospheric pressure to produce an overhead flash vapor and to regenerate the flashed liquid gasoline absorbent; (d) venting the substantially hydrocarbon free air from the first solid adsorbent bed to the atmosphere; (e) passing the first absorber overhead gas to a second solid adsorbent bed of similar capability to the first solid adsorbent bed when said first solid adsorbent bed becomes sufficiently hydrocarbon laden; (f) subjecting the hydrocarbon laden first solid adsorbent bed to a vacuum with a liquid ring vacuum pump to desorb the hydrocarbon components therefrom so as to produce a rich air-hydrocarbon mixture comprising recovered hydrocarbon and liquid from the liquid ring vacuum pump; (g) separating the liquid from the liquid ring vacuum pump from the rich air-hydrocarbon mixture from the first solid adsorbent bed in a separator to produce an air-hydrocarbon effluent stream; (h) cooling the separated liquid ring vacuum pump liquid and recycling same to the liquid ring vacuum pump; (i) passing the air-hydrocarbon effluent stream from the separator and the overhead flash vapor from the flash vessel through a second absorber in absorption relationship with fresh liquid gasoline absorbent from a selected source of same in a sufficiently high L/V ratio to produce a constant composition second absorber overhead gas containing nonabsorbed hydrocarbon vapors and air, and to produce a second absorber bottom liquid; (j) passing the second absorber bottom liquid to a selected destination; (k) passing the second absorber overhead gas to the first absorber to pass therethrough in combination with the inlet stream of air-gasoline vapors of step (a) above; and (l) passing the first absorber overhead gas to the first adsorbent bed when the second solid absorbent bed becomes sufficiently hydrocarbon laden and repeating the above steps alternatingly using the first and second adsorbent beds in an on stream adsorbing mode and in a vacuum regenerating mode.

Claim 19

A process for removing and recovering gasoline vapors from an air-gasoline vapor mixture, comprising: (a) passing an inlet stream of air-gasoline vapors through a first absorber in liquid-vapor absorption relationship with vacuum flashed liquid gasoline absorbent to produce a first absorber overhead gas containing nonabsorbed hydrocarbon vapors and air, and to produce a first absorber bottom liquid containing recovered hydrocarbon components of the gasoline vapors of the inlet stream of air-gasoline vapors; (b) passing the first absorber overhead gas to a first solid adsorbent bed capable of selectively adsorbing the nonabsorbed hydrocarbon vapors and to leave substantially hydrocarbon free air; (c) passing the first absorber bottom liquid to a flash vessel maintained at subatmospheric pressure to produce an overhead flash vapor and to regenerate the flashed liquid gasoline absorbent; (d) venting the substantially hydrocarbon free air from the first solid adsorbent bed to the atmosphere; (e) passing the first absorber overhead gas to a second solid adsorbent bed of similar capability to the first solid adsorbent bed when said first solid adsorbent bed becomes sufficiently hydrocarbon laden; (f) subjecting the hydrocarbon laden first solid adsorbent bed to a vacuum with a liquid ring vacuum pump to desorb the hydrocarbon components therefrom so as to produce a rich air-hydrocarbon mixture comprising recovered hydrocarbon and liquid from the liquid ring vacuum pump; (g) separating the liquid from the liquid ring vacuum pump from the rich air-hydrocarbon mixture from the first solid adsorbent bed in a separator to produce an air-hydrocarbon effluent stream; (h) cooling the separated liquid ring vacuum pump liquid and recycling same to the liquid ring vacuum pump; (i) passing the air-hydrocarbon effluent stream from the separator and the overhead flash vapor from the flash vessel through a second absorber in absorption relationship with fresh liquid gasoline absorbent from a selected source of same in a sufficiently high L/V ratio to produce a constant composition second absorber overhead gas containing nonabsorbed hydrocarbon vapors and air, and to produce a second absorber bottom liquid; (j) passing the second absorber bottom liquid to a selected destination; (k) passing the second absorber overhead gas to the first absorber to pass therethrough in combination with the inlet stream of air-gasoline vapors of step (a) above; and (l) passing the first absorber overhead gas to the first adsorbent bed when the second solid absorbent bed becomes sufficiently hydrocarbon laden and repeating the above steps alternatingly using the first and second adsorbent beds in an on stream adsorbing mode and in a vacuum regenerating mode.

Claim 20

The process of claim 16 further comprising: (m) bleeding a portion of the flashed liquid gasoline absorbent stream at a predetermined rate; and (n) making up the system inventory of flashed liquid gasoline absorbent stream with fresh liquid gasoline as required.

Claim 21

The process of claim 17 wherein the bleeding portion of flashed liquid gasoline absorbent stream is passed to the second absorber vessel and combined with the second absorber bottom liquid for removal to the selected destination.

Claim 22

The process of claim 18 wherein the first and second absorber vessels are maintained at slightly above atmospheric pressure.

Claim 23

The process of claim 19 wherein the flash vessel is maintained at a vacuum of about 1.0 to about 5.0 psia.