HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH CONTACTORS

Abstract

The present invention addresses to a high-pressure vessel for packaging hollow fiber type membranes with application in the field of separation process with contactors with membranes aiming at a compact device/piece of equipment configured for the packaging of hollow fiber type bundles that can be used for various fluid separation processes such as liquid-liquid, liquid-gas and gas-gas, capable of working at high-pressures, enabling adequate hydrodynamic conditions and easily scalable. It is called a module the general piece of equipment, consisting of the vessel (A or C), object of the present invention, and the membranes packed inside the vessel. This piece of equipment consists of a vessel inside which the membranes are placed (14), and two heads attached at the ends (B or D). Each head has two connection points, thus allowing this device to be used with membrane contactors-type separation systems, such as “classical” permeation systems (liquid-liquid, gas-gas, pervaporation).

Claims

1- A HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH MEMBRANE CONTACTORS, characterized in that it comprises an eccentric threaded hole (10) for connecting the first line (9), a part of the head, channels/annular housings (5) for a sealing ring, a screw seat for a flange, holes (4) for passing stream in contact with the shell (external part) of the membranes, a central threaded hole (11) for connecting the second line (line B), a cavity/channel (4) for accessing the holes, head body, region with roughness, part of the vessel, internal part of the vessel where the hollow fiber type membranes (14) are packed, a hole (head) for the passage of stream in contact with the shell (external part) of the membranes, internal cavity of the head, vessel body.

2- THE HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH MEMBRANE CONTACTORS according to claim 1, characterized in that the heads are designed with threaded (B) or flange type (D) connections.

3- THE HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH MEMBRANE CONTACTORS according to claim 2, characterized in that the threaded configuration is suitable for the preparation of modules with internal gluing section up to 1″ (inch) (2.54 cm) in diameter (1).

4- THE HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH MEMBRANE CONTACTORS according to claim 2, characterized in that the flange-type configuration is suitable for the preparation of modules with an internal gluing section greater than 1″ (inch) (2.54 cm) in diameter (1).

5- THE HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH MEMBRANE CONTACTORS according to claim 3, characterized in that the threaded configuration has two annular channels (5) that allow the housing of two rubber sealing rings at each end.

6- THE HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH PROCESS WITH MEMBRANE CONTACTORS according to claim 3, characterized in that the flange-type configuration has four annular channels (5) located in the vessel body and one in the head (D) that allow the housing of the rubber sealing rings at each end.

7- THE HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH MEMBRANE CONTACTORS according to claim 1, characterized in that the rubber sealing rings are of the “O-ring” or gasket type on each end.

8- THE HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH MEMBRANE CONTACTORS according to claim 1, characterized in that the vessel is used for liquid-liquid, liquid-gas and gas-gas type of separation.

9- THE HIGH-PRESSURE VESSEL FOR PACKAGING HOLLOW FIBER TYPE MEMBRANES FOR THE SEPARATION PROCESS WITH MEMBRANE CONTACTORS according to claim 8, characterized in that the vessel is used to remove CO.sub.2 from a stream of natural gas or liquid-liquid type for membrane distillation processes or direct osmosis permeation/power generation.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0007] The present invention will be described in more detail below, with reference to the attached figures that, in a schematic way and not limiting the inventive scope, represent examples of its embodiment. In the drawings, there are:

[0008] FIG. 1 illustrating the complete device/piece of equipment with the A-B threaded configuration.

[0009] FIG. 2 illustrating the side view of the body of vessel A.

[0010] FIG. 3 illustrating the cross/longitudinal section A-A of the ends of the vessel body.

[0011] FIG. 4 illustrating the longitudinal side view of the threaded head B.

[0012] FIG. 5 illustrating the cross/longitudinal section B-B of the threaded type head.

[0013] FIG. 6 illustrating the complete device/piece of equipment with the C-D flange type configuration.

[0014] FIG. 7 illustrating the longitudinal side view of vessel body C.

[0015] FIG. 8 illustrating the cross/longitudinal section C-C of the ends of the vessel body.

[0016] FIG. 9 illustrating the side view of the flange head D.

[0017] FIG. 10 illustrating the cross/longitudinal section D-D of the flange-type head.

DETAILED DESCRIPTION OF THE INVENTION

[0018] The present invention refers to a device/piece of equipment that allows the packaging of the type of polymeric hollow fibers/capillaries used in membrane separation processes. It is called module, the general piece of equipment, consisting of the vessel, object of the present invention, and the membranes packed inside the vessel. This piece of equipment consists of a vessel inside which the membranes are placed, and two heads attached at the ends. Each head has two connection points, thus allowing the use of this device with membrane contactors-type separation systems, such as “classic” permeation systems (liquid-liquid, gas-gas, pervaporation). This invention presents two types of configuration according to the present invention and illustrated according to FIGS. 1 to 10.

[0019] FIGS. 1 to 5 represent the vessel with the threaded type configuration. FIG. 1 represents the vessel (A) and the heads (B) presenting threaded connections. FIG. 2 shows the side view of the vessel body (A). FIG. 3 shows the cross/longitudinal section of the ends of the vessel body, where it presents two annular channels (5) that allow the accommodation of two rubber sealing rings of the “O-rings” or gasket type at each end. When threaded/joined to the vessel, the head (B) compresses the sealing rings, ensuring strength at high-pressures. FIG. 4 shows a section B-B of the side view of the head. FIG. 5 represents the cross/longitudinal section B-B of the head, where the eccentric connection (10) corresponds to the outlet/inlet (9) of the line circulating through the shell of the hollow fiber membranes, while the central connection (11) corresponds to the outlet/inlet of the line/stream circulating through the lumen of hollow fiber membranes. The volume of glue inserted into the module must be previously determined so as not to close the holes (4) for accessing the stream circulating through the membrane shell (14). This configuration is suitable for modules having an internal section (1) up to 1″ (inch) (2.54 cm) in diameter (1).

[0020] FIGS. 6 to 10 represent the vessel with the flange-type configuration. As can be seen in FIG. 6, the ends of the vessel (C) as well as the heads were designed with flange-type connections (D). FIG. 7 shows the side view (C) of the vessel body. FIG. 8 represents the cross/longitudinal section C-C of the ends of the vessel body with four annular grooves (5) located in the vessel body and one in the head allowing the accommodation of O-ring or gasket type sealing rings at each end. FIG. 9 shows the side view (D) of the flange-type head. FIG. 10 represents the cross/longitudinal section D-D of the flange-type head, where the eccentric connection (10) corresponds to the outlet/inlet of the line/stream circulating through the lumen of the hollow fiber membranes, while the central connection (11) corresponds to outlet/inlet of the line/stream circulating through the lumen of hollow fiber membranes. The volume of glue inserted into the module must be previously determined so as not to close the holes (4) for the stream/line to access circulating through the shell of the membranes. This configuration is suitable for modules having an internal section (1) greater than 1″ (inch) (2.54 cm) in diameter (8).

[0021] The housing body (2), the head thread (3), the detail of the thread (6), the internal channel of the head corresponding to the circulation of the line/stream passing through the shell of the membranes (7), the part (8), cylinder head body (12), flange bolt hole (13) are also shown in FIGS. 1 to 10.