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| United States Patent Application |
20030192820
|
| Kind Code
|
A1
|
|
Cho, Kwantai
;   et al.
|
October 16, 2003
|
Hollow fiber membrane contactor
Abstract
The present invention is directed to a contactor for degassing a liquid.
The contactor includes a perforated core and a microporous membrane
fabric wrapped around the core. The fabric includes a polymethyl pentene
hollow fiber as a weft fiber and a warp yarn. A tube sheet secures the
ends of the wound fiber and a shell encases the tube sheet and fabric.
The shell has at least one opening to permit fluid flow through the shell
and an end cap. In a further embodiment the invention is directed to a
contactor for degassing a liquid wherein the contactor is adapted to
withstand pressures greater than 0.4 MPa and temperatures greater than
50.degree. C.
| Inventors: |
Cho, Kwantai; (Charlotte, NC)
; Delozier, Clifton J.; (Fort Mill, SC)
; Holstein, Linus I.; (Pineville, NC)
; Pittman, R. Allen; (Charlotte, NC)
; Runkle, Charles J.; (Charlotte, NC)
; Sengupta, Amitava; (Charlotte, NC)
|
| Correspondence Address:
|
ROBERT H. HAMMER III, P.C.
3121 SPRINGBANK LANE
SUITE I
CHARLOTTE
NC
28226
US
|
| Serial No.:
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424327 |
| Series Code:
|
10
|
| Filed:
|
April 28, 2003 |
| Current U.S. Class: |
210/321.83; 210/321.74; 210/498 |
| Class at Publication: |
210/321.83; 210/321.74; 210/498 |
| International Class: |
B01D 063/00 |
Claims
That which is claimed:
1. A contactor for degassing a liquid comprising: a perforated core; a
pre-shrunk microporous membrane fabric wrapped around said core, said
fabric comprising a polymethyl pentene hollow fiber weft and a polyolefin
warp yarn wherein the weft count is between 50 and 70 fibers per inch,
the warp count is between 3 and 12 yarns per inch, and the warp yarn is
finer than an 80 denier 40 filament yarn; a tube sheet securing the ends
of said fiber; a shell encasing said tube sheet and fabric; at least one
opening in said shell to permit fluid flow through said shell; and an end
cap affixed to the shell.
2. A contactor according to claim 1 wherein said polyolefin yarn is a 40
denier/20 filament polypropylene yarn.
3. A contactor according to claim 1 wherein said fabric is pre-shrunk by
heating said fabric to a temperature between about 55.degree. C. and
about 65.degree. C. for about 2 to 8 hours.
4. A contactor according to claim 1 wherein said polymethyl pentene hollow
fiber is a skinned fiber.
5. A contactor according to claim 1 wherein said weft fiber count is
between 60 and 65 fibers per inch.
6. A contactor according to claim 1 wherein the aspect ratio of said
fabric is between 0.10 to 6.0 inches.sup.-1.
7. A contactor according to claim 1 wherein a liquid passes through the
shell side of the contactor.
8. A contactor according to claim 1 wherein said polymethyl pentene hollow
fiber fabric equates to an active membrane area greater than 0.05
m.sup.2.
9. A contactor according to claim 1 wherein the packing fraction of the
wound fabric is between about 35% and 45%.
10. A contactor according to claim 1 wherein the said warp fiber count is
between 6 and 7 fibers per inch.
11. A contactor for degassing a liquid: wherein said contactor is adapted
to withstand pressures greater than 0.4 MPa and temperatures greater than
50.degree. C. and further comprises; a shell; a pre-shrunk microporous
membrane fabric comprising a polymethyl pentene hollow fiber weft and a
warp yarn wherein said weft count is between 50 and 70 fibers per inch
and said warp count is between 3 and 12 yarns per inch; and at least one
opening in said shell to permit the fluid flow through said shell.
12. A contactor according to claim 11 wherein said warp yarn is a
polyolefin yarn finer than an 80 denier 40 filament yarn.
13. A contactor according to claim 12 wherein said polyolefin yarn is a 40
denier/20 filament polypropylene yarn.
14. A contactor according to claim 11 wherein said polymethyl pentene
hollow fiber is a skinned fiber.
15. A contactor according to claim 11 wherein said fabric has a weft fiber
count of between 60 and 65 fibers per inch.
16. A contactor according to claim 11 wherein the aspect ratio of said
fabric is between 0.10 to 6.0 inches.sup.-1.
17. A contactor according to claim 11 wherein a liquid passes through the
shell side of the contactor.
18. A contactor according to claim 11 wherein said polymethyl pentene
hollow fiber fabric equates to an active membrane area greater than 0.05
m.sup.2.
19. A contactor according to claim 11 wherein packing fraction of the
wound fabric is between about 35% and 45%.
20. A contactor according to claim 11 wherein said warp yarn count is
between 6 and 7 yarns per inch.
Description
CROSS REFERENCE TO RELATED APPLICATION
[0001] This application is a continuation application from co-pending U.S.
patent application Ser. No. 09/886,653 filed Jun. 21, 2001.
FIELD OF THE INVENTION
[0002] This invention is directed to a hollow fiber membrane contactor.
BACKGROUND OF THE INVENTION
[0003] Hollow fiber membrane contactors are known. For example, see U.S.
Pat. Nos. 3,288,877; 3,755,034; 4,220,535; 4,664,681; 4,940,617;
5,186,832; 5,264,171; 5,284,584; and 5,449,457, each is incorporated
herein by reference. In general, such contactors utilize a thin walled
membrane to separate, via diffusion, gaseous, solid or liquid components
from a solution or colloidal mixture. Hollow fiber membrane diffusion
contactors are commercially available under the name of LIQUI-CEL.RTM.
from Celgard, Inc. of Charlotte, N.C. and under the name of SEPAREL.RTM.
from Dianippon Ink and Chemicals of Tokyo, Japan (DIC). Such contactors
have numerous uses, one being the degassing of fluids.
[0004] The SEPAREL.RTM. contactor comprises a shell surrounding a hollow
fiber fabric that is wound around a perforated core. The SEPAREL.RTM.
contactor uses a fabric made of polymethyl pentene (PMP) hollow fibers
and polyester yarn. Hollow fibers made from PMP exhibits unique diffusion
properties. See Japanese Kokai 2-102714 (published Apr. 16, 1990).
Additionally, the SEPAREL.RTM. contactor operating parameters are limited
to a maximum temperature of 50.degree. C. and a maximum feed water
pressure of 0.4 Mpa. See, Hollow Fiber Membrane Degassing
Module--SEPAREL.RTM., www.dic.co.jp.
[0005] Commercial PMP fabrics used in the manufacture of contactors
utilize the PMP hollow fibers as the fill or weft and polyester yarns as
the warp yarn. This fabric has a tendency to break if the fabric is wound
under tension. One possible explanation for this weakness is the use of
polyester warp yarn in the production of the fabric. Polyester is a
relatively stiff material that does not bend and flex well. When a PMP
fabric is wound around a mandrel the warp yarns absorb most of the
applied load, thus fabrics using polyester warp yarns break and tear.
Fabrics similar to those described in Japanese Kokai 2-102714 have been
shown to break at essentially zero tension during winding. Some degree of
winding tension is desirable to create a well-formed fiber bundle that
fits properly within a contactor shell.
[0006] Another possible explanation for the tearing exhibited by such PMP
fabrics is a failure to utilize properly spaced or sized warp yarn. For
example, fabrics similar to those described in Japanese Kokai 2-102714
(which tear during winding) exhibit a maximum warp yarn count of
approximately 5 lines (yarns) per inch. See JP 2-102714, Embodiment 3.
[0007] U.S. Pat. No. 4,911,846 discloses an artificial lung made with a
hollow fiber cord fabric. Note, U.S. Pat. No. 4,911,846, FIGS. 11 and 12.
The cord fabric comprises polyolefin hollow fibers (including PMP hollow
fibers), as weft fibers and warp fibers (including polyesters,
polyamides, polyimides, polyacrylonitriles, polypropylenes, polyarylates,
polyvinyl alcohols, etc.). The warp yarns are preferably multifilament
yarns of polyesters or polyamides having a yarn fineness of 10 to 150
deniers, more preferably 25 to 75 deniers. See U.S. Pat. No. 4,911,846
col. 6, lines 3-14. No information is provided regarding the spacing of
the warp yarn or the makeup of non-polyester, non-polyamide warp yarns.
[0008] Accordingly, a need exists for an improved contactor preferably
employing a fabric that is not susceptible to breakage and operable at
higher temperatures and pressures than known PMP hollow fiber contactors.
SUMMARY OF THE INVENTION
[0009] The present invention is directed to a contactor for degassing a
liquid comprising a perforated core and a microporous membrane fabric
wrapped around the core. The fabric comprises a polymethyl pentene hollow
fiber, as a weft fiber, and a polyolefin warp yarn. In preferred
embodiments the fabric has a weft fiber count between 50 and 70 fibers
per inch and a warp yarn count between 3 and 12 yarns per inch. A tube
sheet secures the ends of the wound fabric and a shell encases the tube
sheet and wound fabric. The shell has at least one opening to permit
liquid flow through the shell and an end cap.
[0010] In a further embodiment, the invention is directed to a contactor
for degassing a liquid wherein the contactor is adapted to withstand
pressures greater than 0.4 MPa and temperatures greater than 50.degree.
C. The contactor according to this embodiment further comprises a shell
and a microporous membrane fabric comprising a polymethyl pentene hollow
fiber, as a weft fiber, and a warp yarn with fiber and yarn counts
similar to those mentioned above. The fabric is preferably wrapped around
a perforated core and situated inside the shell. The shell has at least
one opening to permit the liquid flow through the shell.
DESCRIPTION OF THE DRAWINGS
[0011] For the purpose of illustrating the invention, there is shown in
the drawings a form which is presently preferred; it being understood,
however, that this invention is not limited to the precise arrangements
and instrumentalities shown.
[0012] FIG. 1 is a schematic illustration of a hollow fiber membrane
contactor.
[0013] FIG. 2 is an illustration of the fabric according to the invention.
[0014] FIG. 3 is a schematic illustration of a second embodiment of the
membrane contactor.
[0015] FIG. 4 is a schematic illustration of a third embodiment of the
membrane contactor.
DETAILED DESCRIPTION OF THE INVENTION
[0016] Referring to the drawings wherein like numerals indicate like
elements, there is shown in FIG. 1 an embodiment of a hollow fiber
membrane contactor 10 according to the invention. The contactor 10
includes a core tube 12. The core tube 12 has a plurality of perforations
14. Hollow fibers 16 surround the core tube 12. A shell 13 surrounds the
fibers and the core tube 12. Tube sheets 26 secure the lateral ends of
fibers 16 to tube 12. The lateral ends of shell 13 are closed with end
caps 15.
[0017] Referring to FIG. 1, a liquid 18 preferably enters the contactor 10
via a liquid inlet 20 of the core tube 12. The liquid 18 travels through
the inlet 20 of the core tube 12 and exits the core tube 12 via
perforations 14 when a block 22 diverts the liquid. The liquid 18 then
travels over the exterior surfaces of the hollow fibers 16. The liquid 18
re-enters the core tube 12 via perforations 14 on the other side of the
block 22 and exits the core tube 12 via a liquid outlet 24. The hollow
fibers 16 surround the core tube 12 and are maintained generally parallel
to core tube's 12 axis via tube sheets 26. The hollow fibers 16 extend
through the tube sheet 26 and are in communication with headspaces 28 on
either end of contactor 10, so that a vacuum 30 drawn at ports 32 and 34
is in communication with the lumen side of hollow fibers 16 via
headspaces 28. Port 34, for example, may also be used to introduce a
sweep gas, which facilitates entrained gas removal.
[0018] The membrane contactor 10 is preferably an external flow, hollow
fiber membrane module. The membrane contactor 10 has a lumen side and a
shell side. The lumen side, also known as the internal side, is defined,
in large part, by the lumen of the hollow fiber. The shell side, also
known as the external side, is defined, in part, by the external surface
of the hollow fiber. The liquid travels through the shell (or external)
side, while the vacuum (or vacuum and sweep gas) is applied to the lumen
(or internal) side. Thereby, entrained gases from the liquid pass, via
diffusion, from the shell side through the membrane to the lumen side.
[0019] Preferably, the hollow fibers 16 are semi-permeable, gas selective,
heterogeneous, integrally asymmetric, and liquid impermeable membranes.
The membrane is, preferably, a single layer membrane (e.g., not a
composite or multi-layered membrane) and is made from a homopolymer of
PMP. The membrane is, preferably, a skinned membrane and the skin is on
the shell side. The membrane has a permeability of less than 100 Barrers
(10.sup.-8 standard cm.sup.3.cm/sec.cm.sup.2.cm(Hg)). For example, see
U.S. Pat. No. 4,664,681, incorporated herein by reference. The total
membrane in the contactor preferably has an active surface area greater
than 0.05 m.sup.2 and most preferably between 0.1 m.sup.2 to 350 m.sup.2.
[0020] Referring now to FIG. 2, the hollow fibers 16 are preferably made
into a fabric 36 having a fill or weft yarn 38 and a warp yarn 40.
Preferably the fabric is a weft insertion knitted fabric where the warp
yarn is the knitting yarn. The weft yarn 38 is the hollow fiber 16. The
fabric 36 preferably has a weft fiber count between 50 and 70 fibers per
inch and most preferably between 60 and 65 fibers per inch.
[0021] The warp yarn 40 should be flexible, yet strong, and inert to the
liquid flowing through the contactor. The warp yarns 40 are preferably
multifilament polyolefin yarns. Most preferably the yarns are selected
from the group consisting of polypropylene and polyethylene. Those
skilled in the art recognize that the term filament is sometimes used
synonymously with cut filament which is also called staple fiber.
Accordingly, as used herein the term yarn should be interpreted to
include yarns made from filament and staple fiber. Preferably, the yarn
possesses a fineness sufficient to resist tearing but not too large as to
cause noticeable gaps between fabric layers. Preferably the warp yarn
should be between 80 denier/40 filament (i.e., a 80/40 yarn) and 20
denier/10 filament (a 20/10 yarn), most preferably around 40 denier/20
filament (a 40/20 yarn). Optionally, the warp yarn may include a surface
finish, e.g. a silicon oil surface finish.
[0022] The count of the warp yarn is also an important factor in the
design of the fabric. Too few warp yarns and the fabric will be
susceptible to tearing. Too many will diminish the efficiency of the
contactor by blocking surface area of the hollow fibers. In preferred
embodiments the warp yarn count is between about 3 and 12 yarns per inch
of fabric; most preferably around 6 to 7 yarns per inch.
[0023] When wound, the fabric 36 and the core tube 12 form a hollow
membrane unit 42. Unit 42 is preferably cylindrical. In use, it is
expected that the unit 42 will have a diameter ranging between about 2
in. and 16 in. and a length ranging between about 8 in. and 72 in. Larger
sizes are possible. The aspect ratio of the unit 42 is defined as
L/D.sup.2 where L is the nominal length of the unit and D is the nominal
diameter of the unit. Preferably, the aspect ratio will range between 0.1
to 6.0 in..sup.-1.
[0024] Furthermore, the fabric 36 is preferably wound under tension to
create a unit 42 having a packing fraction of between about 35% to 45%.
Packing fraction (PF) is defined as the number of fibers (n) multiplied
by the cross-sectional area of each fiber (A.sub.f) divided by the
cross-sectional area of the fiber bundle (A.sub.b) where the
cross-sectional area of the fiber bundle excludes the area occupied by
the core tube 12. Stated symbolically, 1 PF = n * A f A b
[0025] Additionally, PMP hollow fibers have a natural tendency to shrink
which increases with temperature. Accordingly, in preferred embodiments
of the invention, the PMP fabric 36 is preshrunk prior to winding. A
preferred method of preshrinking and stabilizing the fabric is to heat
the fabric to about 15.degree. C. above the expected operating
temperature for approximately 2 to 8 hours, preferably 4 hours. Heating
the fabric between about 55.degree. C. and about 65.degree. C. for about
2 to 8 hours, preferably 4 hours, should provide adequate fiber
stabilization for most anticipated applications. Preshrinking the fabric
and winding the fabric under tension aids in achieving a well-formed
bundle that contributes to the higher operating parameters (e.g.,
temperature and pressure) achieved by the invention.
[0026] Hollow fiber membrane units 42 formed according to the invention
may be combined with other structural elements to create a contactor.
Such structural elements are well known in the art and generally consist
of an outer shell with at least one opening in the shell to permit fluid
flow through the shell. Commonly assigned U.S. patent application Ser.
No. 09/816,730, filed Mar. 22, 2001, incorporated herein by reference,
discloses several possible structures for contactors, all of which are
applicable to the present invention.
[0027] Referring to FIG. 3, contactor 10' is the same as shown in FIG. 2
but for a flow diverting baffle 50 located within the shell side, and
port 34 has been moved. The baffle 50 is added to promote distribution of
liquid over all exterior surfaces of the hollow fibers 16. Port 34 is
moved to illustrate the non-criticality of port location.
[0028] Referring to FIG. 4, contactor 10" differs from contactors 10 and
10' by moving liquid outlet 24 from the terminal end of core tube 12 to
the contactor shell, as illustrated. Vacuum 30 is in communication with
headspace 28 which, in turn, is in communication with the lumens of
hollow fibers 16. The second headspace illustrated in the previous
embodiments has been eliminated. Liquid 18 enters the liquid inlet 20 of
the core tube 12. Liquid 18 exits the tube 12 via perforations 14,
travels over the exterior surfaces of the hollow fibers 16, and exits the
shell side via an outlet 24. The outlet designated 24 may be placed at
other locations on the exterior of the contactor so that it maintains
communication with the shell side.
[0029] The contactor according to the invention may be formed using any of
the methods known by those skilled in the art. One such method is set
forth in commonly assigned U.S. patent application Ser. No. 09/851,242,
filed May 8, 2001.
[0030] The present invention may be embodied in other specific forms
without departing from the spirit or essential attributes thereof, and,
accordingly, reference should be made to the appended claims, rather than
to the foregoing specification, as indicating the scope of the invention.
* * * * *