US 6,096,115 AGranted

Pressure swing adsorption process and system utilizing two product storage tanks

AssigneeAir Products and Chemicals, Inc.

InventorsWilliam Thomas Kleinberg, Mark Robert Pillarella, Douglas Paul Dee

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Abstract

Pressure swing adsorption process and system for separating gas mixtures comprising at least one more strongly adsorbable component and at least one less strongly adsorbable component. The process includes storing gas enriched in one of the components in a first storage tank and a second storage tank which are arranged in series. Final product gas is provided from the second storage tank while gas for purge, rinse, and/or repressurization is provided from the first storage tank.

Claims22

Dependent claims

A pressure swing adsorption process for the separation of a pressurized feed gas containing at least one more strongly adsorbable component and at least one less strongly adsorbable component to recover a final product gas enriched in one of the components, which process comprises:

(1) the steps of
(1a) introducing the pressurized feed gas into a feed inlet end of an adsorber vessel containing a solid adsorbent which preferentially adsorbs the more strongly adsorbable component, and withdrawing from an outlet end of the adsorber vessel an adsorber effluent gas enriched in the less strongly adsorbable component;
(1b) depressurizing the adsorber vessel by withdrawing therefrom a gas stream enriched in the more strongly adsorbable component until the pressure therein reaches a minimum adsorber pressure;
(1c) repressurizing the adsorber vessel from the minimum adsorber pressure to the feed pressure by introducing repressurization gas into the adsorber vessel;
and
(1d) repeating steps (1a) through (1c) in a cyclic manner;
(2) when the final product gas is a gas enriched in the less strongly adsorbable component, the additional steps of
(2a) storing adsorber effluent gas in a first gas storage tank, withdrawing stored adsorber effluent from the first gas storage tank and storing the resulting withdrawn gas in a second gas storage tank;
(2b) introducing gas from the first gas storage tank into the outlet end of the adsorber vessel while simultaneously withdrawing gas from the feed inlet end of the adsorber vessel;
and
(2c) withdrawing the final product gas from the second gas storage tank during at least steps (1b) and (1c);
and
(3) when the final product gas is a gas enriched in the more strongly adsorbable component, the additional steps of
(3a) introducing a rinse gas enriched in the more strongly adsorbable component from a first gas storage tank into the feed inlet end of the adsorber vessel while simultaneously withdrawing gas from the outlet end of the adsorber vessel;
(3b) during step (1b), storing the gas stream enriched in the more strongly adsorbable component in the first storage tank, withdrawing stored gas from the first gas storage tank and storing the resulting withdrawn gas in a second storage tank;
and
(3c) withdrawing the final product gas from the second gas storage tank during at least steps (1a), (1b), and (1c).

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(a) introducing the pressurized feed gas into a feed end of an adsorber vessel containing a solid adsorbent which preferentially adsorbs the more strongly adsorbable component, withdrawing from a product end of the adsorber vessel an adsorber effluent gas enriched in the less strongly adsorbable component, introducing adsorber effluent gas into a first gas storage tank, withdrawing stored adsorber effluent from the first gas storage tank and storing the resulting withdrawn gas in a second gas storage tank;
and withdrawing a final product gas from the second gas storage tank;
(b) terminating introduction of the pressurized feed gas into the adsorber vessel and depressurizing the adsorber vessel by withdrawing gas therefrom until the pressure therein reaches a minimum adsorber pressure, while continuing to withdraw a final product gas from the second gas storage tank;
(c) repressurizing the adsorber vessel from the minimum adsorber pressure by introducing repressurization gas into the adsorber vessel, wherein at least a portion of the repressurization gas is provided from the first gas storage tank while the final product gas continues to be withdrawn from the second gas storage tank;
and
(d) repeating steps (a) through (c) in a cyclic manner.

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A pressure swing adsorption system for the separation of a feed gas containing at least one more strongly adsorbable component and at least one less strongly adsorbable component which comprises:

(a) an adsorber vessel containing a solid adsorbent which preferentially adsorbs the more strongly adsorbable component, wherein the vessel has a feed end and a product end;
(b) blower, valve, and piping means for (1) introducing the feed gas into the feed end of the adsorber vessel and (2) withdrawing gas from the feed end of the adsorber vessel;
(c) piping means for withdrawing an adsorber effluent gas enriched in the less strongly adsorbable component from the product end of the adsorber vessel;
(d) a first gas storage tank for holding adsorber effluent gas withdrawn from the product end of the adsorber vessel and a second gas storage tank for holding stored adsorber effluent gas withdrawn from the first gas storage tank;
(e) piping and valve means for introducing adsorber effluent gas into the first gas storage tank and for transferring adsorber effluent gas from the first gas storage tank into the adsorber vessel;
(f) valve means to isolate the first and second gas storage tanks from the adsorber vessel;
(g) piping and valve means for controlling gas flow from the first gas storage tank to the second gas storage tank;
and
(h) piping and valve means for withdrawing stored adsorber effluent gas from the second gas storage tank as a final product gas enriched in the less strongly adsorbable component.

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Dependencies are inferred from the claim text.

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Abstract

(1) the steps of
(1a) introducing the pressurized feed gas into a feed inlet end of an adsorber vessel containing a solid adsorbent which preferentially adsorbs the more strongly adsorbable component, and withdrawing from an outlet end of the adsorber vessel an adsorber effluent gas enriched in the less strongly adsorbable component;
(1b) depressurizing the adsorber vessel by withdrawing therefrom a gas stream enriched in the more strongly adsorbable component until the pressure therein reaches a minimum adsorber pressure;
(1c) repressurizing the adsorber vessel from the minimum adsorber pressure to the feed pressure by introducing repressurization gas into the adsorber vessel;
and
(1d) repeating steps (1a) through (1c) in a cyclic manner;
(2) when the final product gas is a gas enriched in the less strongly adsorbable component, the additional steps of
(2a) storing adsorber effluent gas in a first gas storage tank, withdrawing stored adsorber effluent from the first gas storage tank and storing the resulting withdrawn gas in a second gas storage tank;
(2b) introducing gas from the first gas storage tank into the outlet end of the adsorber vessel while simultaneously withdrawing gas from the feed inlet end of the adsorber vessel;
and
(2c) withdrawing the final product gas from the second gas storage tank during at least steps (1b) and (1c);
and
(3) when the final product gas is a gas enriched in the more strongly adsorbable component, the additional steps of
(3a) introducing a rinse gas enriched in the more strongly adsorbable component from a first gas storage tank into the feed inlet end of the adsorber vessel while simultaneously withdrawing gas from the outlet end of the adsorber vessel;
(3b) during step (1b), storing the gas stream enriched in the more strongly adsorbable component in the first storage tank, withdrawing stored gas from the first gas storage tank and storing the resulting withdrawn gas in a second storage tank;
and
(3c) withdrawing the final product gas from the second gas storage tank during at least steps (1a), (1b), and (1c).

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