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This present invention relates to a fluid separation module adapted to separate a given fluid mixture into permeate and retentate portions using bundles of hollow fiber membranes. The membranes may be composed of different kinds of membranes depending on the application being used to separate the fl

This present invention relates to a fluid separation module adapted to separate a given fluid mixture into permeate and retentate portions using bundles of hollow fiber membranes. The membranes may be composed of different kinds of membranes depending on the application being used to separate the fluid mixture. The fluid separation module may be used to separate fluid mixtures by a number of different processes, including but not limited to, pervaporation, vapour permeation, membrane distillation (both vacuum membrane distillation and direct contact membrane distillation), ultra filtration, microfiltration, nanofiltration, reverse osmosis, membrane stripping and gas separation. The present invention also provides an internal heat recovery process applied in association with those fluid separation applications where separation takes place by evaporation through the membrane of a large portion of the feed into permeate. Desalination and contaminated water purification by means of vacuum membrane distillation are just two examples where the internal heat recovery process may be applied. In these two examples, large portions of the feed are separated by membranes into a high purity water permeate stream by evaporation through the membranes and into a retentate stream containing a higher concentration of dissolved components than present in the feed. In this process the permeate vapour that is extracted from the fluid separation module is compressed by an external compressor to increase the temperature of the vapour higher than the temperature of the feed entering the separation module. Heat from the permeate vapour at the elevated temperature is transferred back to the incoming feed fluid mixture entering the fluid separation module in a condenser/heat exchange.

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What is claimed is: 1. A fluid separation apparatus comprising: a. a hollow housing defining a separation chamber, having at least one permeate outlet to permit one or more permeate components of a feed fluid mixture to exit the housing; b. at least one feed inlet for feeding the feed fluid mixture

What is claimed is: 1. A fluid separation apparatus comprising: a. a hollow housing defining a separation chamber, having at least one permeate outlet to permit one or more permeate components of a feed fluid mixture to exit the housing; b. at least one feed inlet for feeding the feed fluid mixture into the housing; c. at least one bundle of hollow fiber membranes being supported along its length by at least two telescoping rods, contained within the housing having first and second open ends, the first ends being in fluid communication with a feed inlet, the ends of a bundle of hollow fiber membranes each being secured by a holding member comprising a tube sheet, such that the ends of the hollow fiber membranes are exposed to the feed inlet and retentate outlet, respectively; d. at least one retentate outlet to permit one or more non-permeate components of the feed fluid mixture to exit the housing; and e. the bundle of hollow fiber membranes being enclosed in a sleeve that has openings, the sleeve protecting the physical integrity of the hollow fiber membranes contained within said sleeve but allowing the passage of fluids through the sleeve; whereby the feed fluid mixture passes through the hollow fiber membranes such that the one or more permeate components of the feed fluid mixture migrate across the walls of the membranes to a permeate region defined between the fiber membranes and an interior wall of the housing, and the one or more retentate portions of the feed fluid mixture pass along the length of the membranes to the retentate outlet. 2. The apparatus of claim 1 wherein the housing has two open ends which are sealed by first and second sealing members respectively, each sealing member comprising openings through which the ends of the bundle of membranes is inserted, whereby the ends of the hollow fiber membranes are exposed to a region external to each sealing member. 3. The apparatus of claim 2 wherein each end of the bundle of membranes is secured by a holding member having a threaded portion, and the bundle is secured to each sealing member by threaded members engaging the threaded portions of the holding members. 4. The apparatus of claim 2 wherein one end of the bundle of membranes is secured to a holding member by threaded members engaging threaded portions of the holding member, and the opposite end of the bundle of membranes is secured to the sealing member in a fluid-tight slip fit engagement. 5. The apparatus of claim 2 wherein a first endcap is secured to an inlet end of the housing such that a feed inlet region is defined between the first endcap and the first sealing member. 6. The apparatus of claim 5 wherein a second endcap is secured to an outlet end of the housing such that a retentate outlet region is defined between the second endcap and the second sealing member. 7. The apparatus of claim 6 wherein the first endcap comprises a feed inlet. 8. The apparatus of claim 7 wherein retentate exits the fiber membranes into the retentate outlet region. 9. The apparatus of claim 8 wherein the second endcap comprises a retentate outlet. 10. The apparatus of claim 5 wherein the feed inlet passes through the first endcap and supplies feed fluid mixture directly to the end of at the bundle of hollow fiber membranes in fluid-tight relation. 11. The apparatus of claim 1 wherein the housing has one open end sealed by means of a sealing member containing at least one opening through which a feed inlet passes whereby the feed inlet connects to the ends of at least one bundle of membranes by means of a connecting member, and said sealing member contains at least one opening through which a retentate outlet passes, whereby the retentate outlet connects to the ends of at least one bundle of membranes. 12. The apparatus of claim 11, wherein the two or more bundles of membranes are connected to one another in series. 13. The apparatus of claim 11, wherein the two or more bundles of membranes are connected to one another in parallel. 14. The apparatus of claim 6 wherein two or more bundles of membranes are physically supported by a bearing means against the interior of the housing. 15. The apparatus of claim 11 wherein one or more endcaps is secured to the end of the housing such that a feed inlet region is defined between said endcap and the sealing member, and a retentate outlet region is defined between said endcap and the sealing member, and the feed inlet region and retentate outlet region are physically separate from one another. 16. The apparatus of claim 15, wherein the endcap creating the feed inlet region has at least one opening through which a feed inlet passes and empties feed into said feed inlet region. 17. The apparatus of claim 16, wherein the endcap creating the retentate outlet region has at least one opening through which a retentate outlet passes and permits retentate within the retentate outlet region to exit the housing. 18. The apparatus of claim 1 wherein each rod consists of at least three rod portions, comprising two end rods each having one end fixed into the medial surface of a holding member and a medial rod, whereby opposite ends of the medial rod engage the two end rods in a telescoping relation. 19. The apparatus of claim 1 wherein the sleeve consists of two or more elements that move telescopically in relation to one another. 20. The apparatus of claim 1 wherein permeate traverses the walls of the hollow fiber membranes by means of pervaporation, vapour permeation, membrane distillation including vacuum membrane distillation, direct contact membrane distillation, ultra filtration, microflltration nanofiltration, reverse osmosis, membrane stripping, gas separation or a combination thereof. 21. The apparatus of claim 1 for use in the process of desalination. 22. The apparatus of claim 21 wherein the housing operates under a vacuum conditions with the-permeate side and sub-ambient pressures ranging from about 0.05 psia to about 14.4 psia. 23. The apparatus of claim 22 wherein the housing operates under a vacuum conditions with the permeate side and sub-ambient pressures ranging from about 0.1 psia to about 12.0 psia. 24. The apparatus of claim 22 wherein the hollow fiber membranes are porous. 25. The apparatus of claim 22 wherein the hollow fiber membranes are hydrophobic. 26. A method for separating fresh water from saltwater utilizing the apparatus of claim 1, comprising the steps of: a. heating a saltwater feed entering the fluid separation apparatus; b. separating a permeate of water vapour from the saltwater under vacuum or vacuum-like conditions; c. passing the water vapour through a compressor or blower to increase the temperature of the water vapour; d. passing the heated water vapour through a heat exchanger to heat the saltwater feed and condense the water vapour; and e. collecting the condensed water. 27. The apparatus of claim 26 wherein the hollow fiber membranes are porous. 28. The apparatus of claim 26 wherein the hollow fiber membranes are hydrophobic. 29. A fluid separation apparatus comprising: a hollow housing defining a separation chamber, having at least one permeate outlet to permit one or more permeate components of a feed fluid mixture to exit the housing, the housing having two open ends which are sealed by first and second sealing members respectively, each sealing member comprising openings through which the ends of the bundle of membranes is inserted, whereby the ends of the hollow fiber membranes are exposed to a region external to each sealing member; a first endcap secured to an inlet end of the housing such that a feed inlet region is defined between the first endcap and the first sealing member; a second endcap secured to an outlet end of the housing such that a retentate outlet region is defined between the second endcap and the second sealing member; at least one feed inlet for feeding the feed fluid mixture into the housing; at least one bundle of hollow fiber membranes being supported along its length by at least two telescoping rods, contained within the housing having first and second open ends, the first ends being in fluid communication with the feed inlet; and at least one retentate outlet to permit one or more non-permeate components of the feed fluid mixture to exit the housing; whereby the feed fluid mixture passes through the hollow fiber membranes such that the one or more permeate components of the feed fluid mixture migrate across the walls of the membranes to a permeate region defined between the fiber membranes and an interior wall of the housing, and the one or more retentate portions of the feed fluid mixture pass along the length of the membranes to the retentate outlet and a first heating area is defined in the feed inlet region and a second beating area is defined, in the retentate outlet region the first and second heating areas each providing at least one heating fluid inlet and at least one heating fluid outlet to allow the passage of heated fluid therethrough. 30. The apparatus of claim 10 wherein the ends of the bundles of hollow fiber membranes are interconnected in fluid-tight communication by conduits to create a series of serially connected bundles of hollow fiber membranes through which the feed fluid mixture is conveyed to the retentate outlet. 31. The apparatus of claim 30 wherein the feed fluid mixture is separated into permeate and retentate portions by means of pervaporation, vapour permeation, membrane distillation including vacuum membrane distillation, direct contact membrane distillation, ultra filtration, microfiltration nanofiltration, reverse osmosis, membrane stripping, gas separation or a combination thereof. 32. The apparatus of claim 29 wherein the conduits are disposed within in the first and second heating areas. 33. The apparatus of claim 32 wherein the feed fluid mixture is heated within the conduits by heated fluid passing over said conduits within the first and second heating areas. 34. The apparatus of claim 33 wherein the feed fluid mixture is separated into permeate and retentate portions by means of pervaporation, vapour permeation, membrane distillation including vacuum membrane distillation, direct contact membrane distillation, ultra filtration, microfiltration nanofiltration, reverse osmosis, membrane stripping, gas separation or a combination thereof. 35. The apparatus of claim 34 wherein the feed inlet passes through the first endcap and supplies feed fluid mixture directly to the end of at the bundle of hollow fiber membranes in fluid-tight relation. 36. The apparatus of claim 35 wherein the ends of the bundles of hollow fiber membranes are interconnected in fluid-tight communication by conduits to create a series of serially connected bundles of hollow fiber membranes through which the feed fluid mixture is conveyed to the retentate outlet. 37. The apparatus of claim 36 wherein the conduits are disposed within in the first and second heating areas. 38. A fluid separation apparatus comprising: a. a hollow housing defining a separation chamber, having at least one permeate outlet to permit one or more permeate vapour components of a feed fluid mixture to exit the housing; b. at least one feed inlet for feeding the feed fluid mixture into the housing; c. at least one bundle of hollow fiber membranes being supported along its length by at least two telescoping rods, contained within the housing having first and second open ends, the first ends being in fluid communication with a feed inlet; d. at least one retentate outlet to permit one or more non-permeate components of the feed fluid mixture to exit the fluid separation module; e. at least. one compressor for compressing and heating the one or more permeate vapour components of the feed fluid mixture; and f. at least one heat exchanger within the housing for transferring heat from the compressed permeate to the feed inlet mixture; whereby the feed fluid mixture passes through the hollow fiber membranes such that the one or more permeate components of the feed fluid mixture migrate across the walls of the membranes to a permeate region defined between the fiber membranes and an interior wall of the housing, and the one or more retentate portions of the feed fluid mixture pass along the length of the membranes to the retentate outlet. 39. The apparatus of claim 38 where the heat exchanger includes a condenser for condensing the one or more permeate vapour components; whereby latent heat of vapounzation is transferred from the one or more permeate vapour components to the feed inlet mixture. 40. The apparatus of claim 39 where the condenser includes a pump for removing non-condensable portions of the one or more permeate vapour components of feed fluid mixture whereby a partial-vacuum is maintained in the condenser. 41. The apparatus of claim 37 wherein the feed fluid mixture is heated within the conduits by heated fluid passing over said conduits within the first and second heating areas.