초록 ▼

A gas-separation membrane module assembly and a gas-separation process using the assembly. The assembly includes sets of manifolds, between which are mounted arrays of membrane modules, the manifolds and membrane modules forming a stack within a pressure vessel or housing. The stacked, manifolded ar

A gas-separation membrane module assembly and a gas-separation process using the assembly. The assembly includes sets of manifolds, between which are mounted arrays of membrane modules, the manifolds and membrane modules forming a stack within a pressure vessel or housing. The stacked, manifolded arrangement enables many membrane elements to be fed in parallel with the gas to be treated.

대표청구항 ▼

1. A gas separation assembly, comprising: (a) a housing comprising first and second ends and a cylindrical shell connecting the ends, at least one of the ends being a removable head;(b) a set of at least 10 gas separation membrane elements, each element being equipped to accept a feed gas from withi

1. A gas separation assembly, comprising: (a) a housing comprising first and second ends and a cylindrical shell connecting the ends, at least one of the ends being a removable head;(b) a set of at least 10 gas separation membrane elements, each element being equipped to accept a feed gas from within the housing, and to discharge a permeate gas at a permeate end and a residue gas at a residue end;(c) a stack of alternating permeate and residue gas-collection manifolds, the stack being aligned lengthwise within the shell, the manifolds being spaced apart with a sub-set of the membrane elements mounted between sequential manifolds, each membrane element within the subset being (i) aligned with its permeate end adjacent to the permeate manifold and its residue end adjacent to the residue manifold, and (ii) connected in gas-transferring relationship to the manifolds such that the permeate gas may enter only the permeate manifold and the residue gas may enter only the residue manifold;(d) a permeate collector element aligned lengthwise within the shell, passing through the residue and permeate manifolds, and being connected in gas-transferring relationship to the manifolds such that permeate gas from the permeate gas-collection manifolds may enter the permeate collector element but residue gas from the residue gas-collection manifolds may not enter the permeate collector element;(e) a residue collector element aligned lengthwise within the shell, passing through the residue and permeate manifolds, and being connected in gas-transferring relationship to the manifolds such that residue gas from the residue gas-collection manifolds may enter the residue collector element but permeate gas from the permeate gas-collection manifolds may not enter the residue collector element;(f) a feed inlet in the housing adapted to introduce a feed gas stream into the housing;(g) a permeate outlet in the housing adapted to enable permeate gas from the permeate collector element to be withdrawn from the housing;(h) a residue outlet in the housing adapted to enable residue gas from the residue collector element to be withdrawn from the housing. 2. A gas separation assembly, comprising: (a) a housing comprising first and second ends and a cylindrical shell connecting the ends, at least one of the ends being a removable head;(b) a set of at least 10 gas separation membrane elements, each element being equipped to accept a feed gas at a feed end, and to discharge a permeate gas at a permeate end and a residue gas into the housing;(c) a stack of alternating feed and permeate manifolds, the stack being aligned lengthwise within the shell, the manifolds being spaced apart with a sub-set of the membrane elements mounted between sequential manifolds, each membrane element within the subset being (i) aligned with its permeate end adjacent to the permeate manifold and its feed end adjacent to the feed manifold, and (ii) connected in gas-transferring relationship to the manifolds such that the permeate gas may enter only the permeate manifold and the feed gas may exit only the feed manifold;(d) a permeate collector element aligned lengthwise within the shell, passing through the feed and permeate manifolds, and being connected in gas-transferring relationship to the manifolds such that permeate gas from the permeate manifolds may enter the permeate collector element but feed gas from the feed manifolds may not enter the permeate collector element;(e) a feed distribution element aligned lengthwise within the shell, passing through the feed and permeate manifolds, and being connected in gas-transferring relationship to the manifolds such that feed gas from the feed distribution element may enter the feed manifolds but permeate gas from the permeate manifolds may not enter the feed distribution element;(f) a residue outlet in the housing adapted to enable residue gas to be withdrawn from the housing;(g) a permeate outlet in the housing adapted to enable permeate gas from the permeate collector element to be withdrawn from the housing;(h) a feed inlet in the housing adapted to enable feed gas to be introduced through the feed distribution element to the feed manifolds. 3. The assembly of claim 1 or claim 2, wherein the stack includes at least two permeate manifolds and two residue manifolds. 4. The assembly of claim 1 or claim 2, wherein the membrane elements are spiral-wound modules. 5. The assembly of claim 1 or claim 2, wherein the membrane elements are hollow-fiber modules. 6. The assembly of claim 1 or claim 2, wherein the housing has a length and a diameter, having dimensions in a ratio of length:diameter of between 3 and 8. 7. A gas separation process using the assembly of claim 1 or claim 2 and comprising the following steps: (a) feeding a mixed gas stream comprising at least a first component and a second component to the feed inlet;(b) providing a driving force for transmembrane permeation;(c) withdrawing from the residue outlet a residue stream depleted in the first component compared with the mixed gas stream;(d) withdrawing from the permeate outlet a permeate stream enriched in the first component compared with the mixed gas stream. 8. The process of claim 7, wherein the mixed gas stream comprises a hydrocarbon. 9. The process of claim 7, wherein the mixed gas stream comprises natural gas. 10. The process of claim 7, wherein the mixed gas stream comprises a refinery off-gas stream. 11. The process of claim 7, wherein the mixed gas stream comprises a petrochemical process stream.