Recovery of hydrogen

Claim 2

In a process for hydrogenating a hydrocarbon feed at a hydrogenation pressure of at least 1000 psig wherein a hydrogenation effluent comprising a liquid portion and a gaseous portion is recovered from the hydrogenation, said gaseous portion containing unreacted hydrogen and impurities, the improvement comprising: (a) reducing the pressure of said gaseous portion from a hydrogenation pressure of at least 1000 psig to a lower pressure which is at least 200 psi less than the hydrogenation pressure and which is not in excess of 1500 psig to provide a gas containing hydrogen and impurities at a reduced pressure; (b) removing impurities from gas from step (a) to provide a hydrogen gas containing at least 70%, by volume, of hydrogen; and (c) increasing the pressure of hydrogen gas from step (b) to an elevated pressure which is at least 1000 psig and which is at least 200 psi greater than the lower pressure for use in a hydrogenation process.

Claim 3

The process of claim 1 wherein the gaseous portion and liquid portion are in admixture with each other prior to and subsequent to reducing the pressure, and the gaseous portion is separated from the liquid portion prior to removing impurities from the gaseous portion.

Claim 4

The process claim 1 wherein the gaseous portion and liquid portion are separated from each other prior to reducing the pressure of the gaseous portion.

Claim 5

The process of claim 3 and further comprising: reducing the pressure of the separated liquid portion to a pressure corresponding to the reduced pressure for the gaseous portion to release a further gaseous portion containing hydrogen therefrom; and recovering and combining the further gaseous portion with the gaseous portion to remove impurities from both the gaseous portion and the further gaseous portion at the reduced pressure.

Claim 6

In a process for hydrogenating a hydrocarbon feed at a hydrogenation pressure of at least 1000 psig, wherein a gas containing unreacted hydrogen and impurities is recovered at the hydrogenation pressure, the improvement comprising: (a) reducing the pressure of the gas in at least one stage to a reduced pressure of no greater than 800 psig; (b) removing impurities from gas from step (a) to produce a hydrogen gas containing at least 70%, by volume, of hydrogen; and (c) increasing the pressure of hydrogen gas from step (b) to a pressure of at least 1000 psig for use in a hydrogenation process.

Claim 7

In a process for hydrogenating a hydrocarbon feed at a hydrogenation pressure of at least 1000 psig, wherein a gas containing unreacted hydrogen and impurities is recovered at the hydrogenation pressure, the improvement comprising: (a) reducing the pressure of the gas in at least one stage to a reduced pressure of no greater than 800 psig; (b) removing impurities from gas from step (a) to produce a hydrogen gas containing at least 70%, by volume, of hydrogen; and (c) increasing the pressure of hydrogen gas from step (b) to a pressure of at least 1000 psig for use in a hydrogenation process.

Claim 8

The process of claim 5 wherein the reduced pressure is a pressure of from 150 to 600 psig.

Claim 9

The process of claim 6 wherein hydrogen gas contains at least 90%, by volume, of hydrogen.

Claim 10

The process of claim 7 wherein the hydrocarbon feed contains at least 25%, by volume, of material boiling above 950° F.

Claim 11

The process of claim 7 wherein the pressure of the hydrogen gas is increased to the hydrogenation pressure and the hydrogen gas at the hydrogenation pressure is recycled to the hydrogenation.

Claim 12

The process of claim 5 and further comprising: recovering a liquid effluent from the hydrogenation; reducing the pressure of the liquid effluent in at least one stage to a pressure essentially identical to the lower pressure of said gas; recovering additional gas containing hydrogen and impurities from said liquid effluent at said lower pressure; and combining said additional gas with said gas to remove impurities from both the gas and additional gas at the lower pressure.

Claim 13

The process of claim 10 wherein the pressure of the gas and the liquid effluent are reduced as a combined stream of the gas and liquid effluent.

Claim 14

The process of claim 10 wherein the gas and liquid effluent from the hydrogenation are separated from each other prior to reducing the pressure.

Claim 15

The process of claim 12 wherein the hydrogen gas contains at least 90%, by volume, of hydrogen.

Claim 16

The process of claim 13 wherein the lower pressure is a pressure of from 150 to 600 psig.

Claim 17

The process of claim 14 wherein the hydrocarbon feed contains at least 25%, by volume, of material boiling above 950° F.

Claim 18

The process of claim 15 wherein the pressure of the hydrogen gas is increased to the hydrogenation pressure and the hydrogen gas at the hydrogenation pressure is recycled to the hydrogenation.

Claim 19

The process of claim 16 wherein the hydrogenation pressure is from 1800 to 3000 psig.

Claim 20

The process of claim 17 wherein the hydrocarbon feed is hydrogenated in an ebullated bed and said hydrocarbon feed contains at least 25%, by volume, of material boiling above 950° F.

Claim 21

The process of claim 16 wherein additional gas is stripped from the liquid effluent at the lower pressure.

Claim 22

In a process for hydrogenating a hydrocarbon feed with hydrogen gas at a hydrogenation pressure of at least 1000 psig wherein a hydrogenation effluent comprising a liquid portion and a gaseous portion is recovered from the hydrogenating, said gaseous portion and said liquid portion containing unreacted hydrogen, the improvement comprising: (a) reducing the pressure of said gaseous portion from a hydrogenation pressure of at least 1000 psig to a reduced pressure which is at least 200 psi less than the hydrogenating pressure and which is not in excess of 1500 psig to provide a gas containing hydrogen and impurities at a reduced pressure; (b) reducing the pressure of the liquid portion from a hydrogenating pressure of at least 1000 psig to a reduced pressure which is at least 200 psi less than the hydrogenating pressure and which is not in excess of 1500 psig to recover from the liquid portion a further gas containing hydrogen and impurities at a reduced pressure; (c) removing impurities from gas from step (a) and further gas recovered from step (b) to provide a hydrogen gas containing at least 70%, by volume, of hydrogen; (d) increasing the pressure of hydrogen gas from step (c) to the hydrogenation pressure; and (e) employing gas from step (d) in the process for hydrogenating a hydrocarbon feed.

Claim 23

In a process for hydrogenating a hydrocarbon feed with hydrogen gas at a hydrogenation pressure of at least 1000 psig wherein a hydrogenation effluent comprising a liquid portion and a gaseous portion is recovered from the hydrogenating, said gaseous portion and said liquid portion containing unreacted hydrogen, the improvement comprising: (a) reducing the pressure of said gaseous portion from a hydrogenation pressure of at least 1000 psig to a reduced pressure which is at least 200 psi less than the hydrogenating pressure and which is not in excess of 1500 psig to provide a gas containing hydrogen and impurities at a reduced pressure; (b) reducing the pressure of the liquid portion from a hydrogenating pressure of at least 1000 psig to a reduced pressure which is at least 200 psi less than the hydrogenating pressure and which is not in excess of 1500 psig to recover from the liquid portion a further gas containing hydrogen and impurities at a reduced pressure; (c) removing impurities from gas from step (a) and further gas recovered from step (b) to provide a hydrogen gas containing at least 70%, by volume, of hydrogen; (d) increasing the pressure of hydrogen gas from step (c) to the hydrogenation pressure; and (e) employing gas from step (d) in the process for hydrogenating a hydrocarbon feed.

Claim 24

The process of claim 20 wherein the reduced pressure in steps (a) and (b) is no greater than 800 psig.

Claim 25

The process of claim 21 wherein in step (c) the impurities are removed to provide a hydrogen gas containing at least 90%, by volume, of hydrogen.

Claim 26

The process of claim 22 wherein the hydrogen gas from step (c) contains at least 99%, by volume, of hydrogen.

Claim 27

The process of claim 22 wherein the hydrogenating of hydrocarbon is effected in an expanded bed at a temperature of from 650° F. to 900° F., said hydrocarbon feed having at least 25% by volume, of material boiling above 950° F.

Claim 28

The process of claim 24 wherein the hydrocarbon feed is a tar sand bitumen.

Claim 29

The process of claim 25 wherein the reduced pressure is from 150 to 600 psig.

Claim 30

The process of claim 24 wherein the ratio of hydrogen introduced into the hydrogenating to hydrogen consumed in the hydrogenating is no greater than 2.

Claim 31

The process of claim 24 wherein impurities in step (c) are removed by pressure swing adsorption.