# US 7,410,580 B2 · Hollow fiber module

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- Number: US 7,410,580 B2
- Document ID: US7410580B2
- Status: Granted
- Kind: B2
- Application number: 10/531,539
- Filed: 2003-10-09
- Published: 2006-03-30
- Granted: 2008-08-12
- Earliest claimed: 2002-10-16
- Assignees: Beko Technologies GmbH
- Inventors: Berthold Koch; Markus Müller; Herbert Schlensker
- Web page: https://patentgrep.com/patent/US7410580B2

## CPC

- B01D 63/06: Tubular membrane modules
- B01D 53/22: by diffusion (manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00)
- B01D 53/268: {by diffusion}
- B01D 63/0232: {using hollow fibers mats as precursor, e.g. wound or pleated mats}
- B01D 63/0233: {forming the bundle}
- B01D 63/025: {Bobbin units}
- B01D 2319/04: Elements in parallel
- B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28)

## Abstract

The invention relates to a hollow fiber separation module comprising an inlet (20) for the gas to be dried, an outlet (22) for dried gas, an access element (26) and a discharge element (28) for circulation gas, and a plurality of hollow fibers which respectively extend from the inlet (29) to the outlet (22) and comprise an inner region which communicates with the inlet (20) on one end of each hollow fiber, and with the outlet (22) on the other end of each hollow fiber. The hollow fibers are wound up in a plurality of layers (40, 42, 44) to form a hollow cylindrical winding. Each layer (40, 42, 44) is inwardly defined by an imaginary cylinder (35, 36, 37) and has a number of hollow fibers which are wound onto the cylinder (35, 36, 37) in a helical manner with an alpha angle of inclination, are located at a distance a from each other, and are arranged on the cylinder in a homogeneously distributed manner. A layer (40) differs from an adjacent layer (e.g. 42) in that the fibers of one of the layers all form a plus alpha winding angle, whereas the fibers of the adjacent layers all form a minus alpha winding angle.

## Claims

### Claim 1

A hollow fiber fluid separation module comprising:
an inlet for an inlet feed flow, an outlet for an exit flow;
an access port for a permeate flow, a discharge port for the permeate flow;
a module axis and a plurality of hollow fibers;
each of the hollow fibers extending from the inlet to the outlet and comprising an interior communicating with the inlet at one end of each hollow fiber and with the outlet at the other end of each hollow fiber, with the hollow fibers wound in multiple layers to form a hollow cylindrical coil;
each layer being defined on its inner side by an imaginary cylinder and having a number of hollow fibers helically wound on the cylinder with a helix angle α;
the hollow fibers being in a clearance relationship with each other and equally spaced on the cylinder, with one layer differing from a neighboring layer by the fact that all the fibers of the one layer are inclined at the wind angle plus α whereas all the fibers of the neighboring layer are at the wind angle minus α; and
each hollow fiber disposed at least once around the circumference of the cylinder and having a tensile strain of at least 10 g to frictionally maintain the fibers around the cylinder and sufficiently hold the fibers against the crosswise disposed fibers lying underneath without noticeably restricting the respective inner cross sections of the fibers even though the fibers are deformed at the respective intersections.

### Claim 2 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein the first, lowermost layer is located on a tube that forms the imaginary cylinder of the layer.

### Claim 3 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein the access port comprises at least one axial bore that is formed in the tube.

### Claim 4 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein the wind angle α ranges between about 15° and about 75°.

### Claim 5 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein the distance (a) between two hollow fibers of one layer ranges between onefold and tenfold the inner radius of the hollow fibers.

### Claim 6 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein all of the fibers have the same length.

### Claim 7 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein all of the fibers are built according to the same design principle.

### Claim 8 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein the tensile strain is selected such that the free inner cross section of the hollow fiber at the intersections is more than 90% of the inner cross section of the hollow fiber outside of the intersections.

### Claim 9 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein the outermost layer of the winding is enclosed by a shell that tightly surrounds the outermost layer and comprises access or exit means for permeate flow.

### Claim 10 (depends on 1)

The hollow fiber fluid separation module as set forth in claim 1, wherein the module is obtained from a preform by cutting the preform along the sectioning planes and that the preform comprises an axially quite long winding and has an axial length that is greater than the length of a plurality of modules.

### Claim 11 (depends on 8)

The hollow fiber fluid separation module as set forth in claim 8, wherein the tensile strain is selected such that the free inner cross section of the hollow fiber at the intersections is more than 95% of the inner cross section of the hollow fiber outside of the intersections.

### Claim 12 (depends on 11)

The hollow fiber fluid separation module as set forth in claim 11, wherein the tensile strain is selected such that the free inner cross section of the hollow fiber at the intersections is more than 98% of the inner cross section of the hollow fiber outside of the intersections.

### Claim 13 (depends on 9)

The hollow fiber fluid separation module as set forth in claim 9, wherein the outermost layer of the winding is enclosed by a shell that tightly surrounds the outermost layer and comprises access or exit means for circulation gas.

### Claim 14 (depends on 4)

The hollow fiber fluid separation module as set forth in claim 4, wherein the wind angle α ranges between about 20° and about 70°.

### Claim 15 (depends on 14)

The hollow fiber fluid separation module as set forth in claim 14, wherein the wind angle α is about 45°.

### Claim 16 (depends on 9)

The hollow fiber fluid separation module as set forth in claim 9, further comprising at least one of (i) at least one ring and (ii) at least one mechanical clamp, disposed over the windings along the coil to further stabilize the windings.