Abstract: 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.

Abstract: 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.

Abstract: An apparatus for the separation of fluid mixtures into a permeate and a retentate comprises separation modules each having fluid containment chambers stacked therein. Each fluid containment chamber is defined by a pair of selectively permeable membranes having their active surfaces facing inwardly toward one another, with a gasket sandwiched therebetween in sealing engagement with each membrane. A channelled support plate is positioned adjacent to the outside surface of each membrane. The channels in the support plates fluidly communicate with a housing, thereby allowing negative pressure from the housing to be brought into direct contact with the outside surface of each selectively permeable membrane. The fluid mixture is pumped into each fluid containment chamber at one end and moves across the active surfaces of the membranes toward a retentate receiver positioned at the opposite end. In doing so, permeate is drawn out through both membranes into the channels and the housing.

Abstract: An apparatus for the separation of fluid mixtures into a permeate and a retentate comprises separation modules each having fluid containment chambers stacked therein. Each fluid containment chamber is defined by a pair of selectively permeable membranes having their active surfaces facing inwardly toward one another, with a gasket sandwiched therebetween in sealing engagement with each membrane. A channelled support plate is positioned adjacent to the outside surface of each membrane. The channels in the support plates fluidly communicate with a housing, thereby allowing negative pressure from the housing to be brought into direct contact with the outside surface of each selectively permeable membrane. The fluid mixture is pumped into each fluid containment chamber at one end and moves across the active surfaces of the membranes toward a retentate receiver positioned at the opposite end. In doing so, permeate is drawn out through both membranes into the channels and the housing.