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A suspension of inorganic particles, a copolymer comprising soft segments and hard segments, and a solvent may be extruded through a spinnerette to produce inorganic/organic composite hollow precursor fibers. The precursor fibers may be sintered. The fibers may be utilized in a gas separation module

A suspension of inorganic particles, a copolymer comprising soft segments and hard segments, and a solvent may be extruded through a spinnerette to produce inorganic/organic composite hollow precursor fibers. The precursor fibers may be sintered. The fibers may be utilized in a gas separation module for separation of a gas mixture or production of syngas. The fibers may be installed in the gas separation module after sintering or they may be sintered after installation.

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1. A composite hollow fiber comprised of inorganic particles bound together with a copolymer comprising soft segments and hard segments. 2. The hollow fiber of claim 1, wherein a weight ratio of inorganic particles to copolymer is in a range of from about 5.0:1.0 to about 12.0:1. 3. The hollow fiber

1. A composite hollow fiber comprised of inorganic particles bound together with a copolymer comprising soft segments and hard segments. 2. The hollow fiber of claim 1, wherein a weight ratio of inorganic particles to copolymer is in a range of from about 5.0:1.0 to about 12.0:1. 3. The hollow fiber of claim 1, wherein an outside diameter of the fiber is in a range from about 100 to 2000 μm and a ratio of the outside-diameter to the inside-diameter is in a range of from about 1.20:1.0 to about 3.0:1.0. 4. The hollow fiber of claim 1, wherein the copolymer is a block copolymer selected from the group consisting of poly(ether)urethane-block-polyurethane, poly(ether)urethane-block-polyurea, poly(ester)urethane-block-polyurethane, and poly(ester)urethane-block-polyurea. 5. The hollow fiber of claim 4, wherein the block copolymer essentially consists of a first block comprising repeating units represented by formula 1a and a second block comprising repeating units represented by formula Ib: wherein each Ri is independently an aliphatic or aromatic radical;each PE is independently a polyether or polyester;each Ra is independently a linear or branched aliphatic radical; andX is O or NH. 6. The hollow fiber of claim 5, wherein each PE is independently a polyether derived from a polyether glycol selected from the group consisting of hydroxyl terminated polyethylene glycol, hydroxyl terminated 1,2-polypropylene glycol, hydroxyl terminated 1,3-polypropylene glycol, and hydroxyl terminated 1,4-polybutylene glycol. 7. The hollow fiber of claim 5, wherein each PE is independently a polyester derived from the reaction of a linear or branched aliphatic diol comprising 2-18 carbon atoms and a linear or branched aliphatic diacid comprising 2-18 carbon atoms. 8. The hollow fiber of claim 5, wherein each Ra is independently derived from at least one linear or branched aliphatic diol selected from the group consisting of ethylene glycol, 1,3-propanediol, 1,2-propanediol, 1,4-butanediol, and 1,6-hexanediol. 9. The hollow fiber of claim 5, wherein each Ra is independently derived from a linear or branched aliphatic diamine selected from the group consisting of 1,2-diaminoethane, 1,4-diaminobutane, 1,5-diaminopentane, 1,5-diaminohexane, and 1,6-diaminohexane. 10. The hollow fiber of claim 5, wherein Ra is derived from a mixture of at least one aliphatic diol and at least one aliphatic diamine. 11. The hollow fiber of claim 5, wherein the soft segments comprise about 50-95 weight % of the copolymer. 12. The hollow fiber of claim 1, wherein the inorganic particles are made of a material selected from the group consisting of an elemental metal, a glass material, a metallic oxide, a zeolite, a perovskite, and mixtures thereof. 13. The hollow fiber of claim 1, wherein the inorganic particles are made of a perovskite. 14. The hollow fiber of claim 13, wherein the inorganic particles are comprised of a perovskite of the formula (Ln1-xAx)w(B1-yB′y)O3-d, wherein: Ln represents one or more elements selected from the group consisting of La, the D block lanthanides, and Y;A represents one or more elements selected from the group consisting of Mg, Ca, Sr, and Ba;B and B′ each represent one or more elements selected from the group consisting of Sc, Ti, V, Cr, Mn, Fe, Co, Ni, Zr, and Ga;0≦x≦1, 0≦y≦1, and 0.95≦w≦1.05; andd is a number that renders the perovskite charge neutral. 15. The hollow fiber of claim 14, wherein the inorganic particles are comprised of a perovskite of the formula La0.8Sr0.2Fe0.7Ga0.3O3-d and d is a number that renders the perovskite charge neutral. 16. The hollow fiber of claim 14, wherein the inorganic particles are comprised of a strontium doped lanthanum iron cobalt oxide perovskite of the composition La(1-x)SrxCo(1-y)FeyO3-d, wherein 0x; andd is a number such that the perovskite is electrically neutral. 24. The hollow fiber of claim 1, wherein 50% by volume of the inorganic particles have a diameter less than 0.7 μm. 25. The hollow fiber of claim 1, wherein the hollow fiber has an elongation at break of 2.0-5.0%. 26. A sintered hollow fiber produced by sintering the hollow fiber of claim 13. 27. The sintered hollow fiber of claim 26, wherein an outside diameter of the sintered fiber is in a range from about 250 to 1500 μm and a ratio of the outside-diameter to the inside-diameter is in a range of from about 1.20:1.0 to about 3.0:1.0. 28. The sintered hollow fiber of claim 26, wherein said fiber is gas-tight. 29. A process for making the composite hollow fiber of claim 1, comprising the steps of: a) preparing a suspension of the inorganic material in particulate form, the copolymer binder, a solvent for said copolymer binder, and optionally one or more additives;b) providing a spinneret adapted and configured to continuously extrude one or more nascent hollow fibers, the spinneret having an inner annular channel disposed concentrically within an outer annular channel;c) feeding a bore fluid through the inner annular channel to form a cylindrical fluid stream positioned concentrically within the fiber;d) feeding the suspension through the outer annular channel so that it surrounds the cylindrical fluid stream to form a nascent hollow fiber;e) passing the nascent hollow fiber from the spinneret through an air gap;f) immersing the nascent hollow fiber in a liquid coagulant to facilitate phase inversion;g) removing the fiber from the coagulant;h) winding the fiber onto a take-up roll;i) washing the fiber to remove residual solvent and optional additives; and(j) drying the fiber to remove volatile material. 30. The process of claim 29, wherein the suspension has a concentration of particulate inorganic material in a range of from about 50 wt. % to about 75 wt. % and a concentration of the copolymer binder in a range of from about 5 wt. % to about 15 wt. %. 31. A gas separation membrane module, comprising: first and second opposed tubesheets;at least one of the sintered hollow fibers of claim 26, said at least one sintered hollow fiber having a first end extending through a hole extending through said first tube sheets and a second end extending through a hole formed in said second tubesheet;a housing enclosing said tubesheets and at least one fiber, said housing having an outlet port and optionally an inlet port;a first end cap engaging with said housing to define a space defined by an outer planar surface of said first tubesheet, an inner surface of said housing, and an inner surface of said first end cap, said first end cap having a inlet port; anda second end cap engaging with said housing to define a space defined by an outer planar surface of said second tubesheet, an inner surface of said housing, and an inner surface of said second end cap, said second end cap having an outlet port. 32. A gas production method, comprising the steps of: providing the gas separation membrane module of claim 31;introducing a first gas to one side of said at least one fiber;withdrawing a second gas from an opposite side of said at least one fiber, wherein the second gas comprises hydrogen or oxygen. 33. The gas production method of claim 32, further comprising the step of methane and steam are introduced to an interior of said at least one fiber via said first end cap inlet port, wherein: the first gas is air;the second gas comprises syngas comprising hydrogen and carbon monoxide;the first gas is introduced to an exterior of said at least one fiber via said housing inlet port; andthe second gas is withdrawn from the module via said second end cap outlet port. 34. The gas production method of claim 32, wherein: the first gas comprises syngas comprising hydrogen and carbon monoxide;the second gas essentially consists of hydrogen;the first gas is introduced to an exterior of said at least one fiber via said housing inlet port;the second gas is withdrawn from said module via said second end cap outlet port; andCO-enriched syngas is withdrawn from said housing outlet port. 35. The gas production method of claim 32, wherein: the first gas is air;the second gas comprises oxygen;the first gas is introduced to an exterior of said at least one fiber via said housing inlet port;the second gas is withdrawn from said module via said second end cap outlet port; andnitrogen-enriched air is withdrawn from said housing outlet port. 36. The gas production method of claim 35, wherein the second gas essentially consists of oxygen. 37. The gas production method of claim 35, further comprising the step of introducing a sweep gas to said opposite side of said at least one fiber via said housing inlet port, wherein: the first gas comprises air and is introduced to an exterior of said at least one fiber via said housing inlet port;the second gas comprises oxygen-enriched sweep gas and is withdrawn from said module via said second end cap outlet port. 38. The gas production method of claim 37, wherein the sweep gas comprises CO2. 39. The gas production method of claim 37, wherein the sweep gas comprises steam. 40. The gas production method of claim 37, wherein the sweep gas comprises CO2 and steam derived from a flue gas.