HIGH TEMPERATURE AND PRESSURE LIQUID DEGASSING SYSTEMS
20190054423 ยท 2019-02-21
Inventors
Cpc classification
F23K2900/05082
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
C10G31/00
CHEMISTRY; METALLURGY
B01D61/00
PERFORMING OPERATIONS; TRANSPORTING
B64D37/34
PERFORMING OPERATIONS; TRANSPORTING
C10L2290/548
CHEMISTRY; METALLURGY
B01D71/66
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01D63/04
PERFORMING OPERATIONS; TRANSPORTING
B64D37/34
PERFORMING OPERATIONS; TRANSPORTING
B01D71/66
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A hollow fiber cartridge for a hollow fiber membrane degassing system, comprising a tube bundle of selectively permeable membrane tubes having inner channels, the bundle including two ends, and a tube sheet at each end of the tube bundle binding the ends of tube bundle. The tube sheets are configured to mount the tube bundle within a housing of the degassing system. The tube sheets are comprised of one or more of at least one Fluorosilicone, at least one Fluorocarbon, or at least one Polysulfide.
Claims
1. A hollow fiber cartridge for a hollow fiber membrane degassing system, comprising: a tube bundle of selectively permeable membrane tubes having inner channels, the bundle including two ends; and a tube sheet at each end of the tube bundle binding the ends of tube bundle, wherein the tube sheets are configured to mount the tube bundle within a housing of the degassing system, wherein the tube sheets are comprised of one or more of at least one Fluoro silicone, at least one Fluorocarbon, or at least one Polysulfide.
2. The cartridge of claim 1, wherein the selectively permeable membrane tubes include at least one of Teflon amorphous fluoropolymer (Teflon AF) (tetrafluoroethylene containing 2,2-bistrifluoromethyl-4,5-difluoro-1,3-dioxole) or Hyflon AD (tetra-fluoroethylene (TFE)-2,2,4-trifluoro-5-tri-fluorometoxy-1,3-dioxole).
3. The cartridge of claim 1, wherein the at least one Polysulfide includes a poly-thio-ether.
4. The cartridge of claim 1, wherein the at least one Polysulfide includes low-density manganese dioxide-cured polysulfide.
5. The cartridge of claim 1, wherein the tube sheets are made entirely of the at least one Fluorosilicone.
6. The cartridge of claim 1, wherein the tube sheets are made entirely of the at least one Fluorocarbon.
7. The cartridge of claim 1, wherein the tube sheets are made entirely of the at least one Polysulfide.
8. A hydrocarbon fuel degassing device, comprising: a housing; and a a hollow fiber cartridge of claim 1 disposed within the housing and sealed to the housing at the tube sheets, wherein a first flow path is defined through the channels of the tubes and a second flow path is defined through the housing such that a fluid flowing in the housing traverses an outer surface of the tubes in the tube bundle and a gas permeates from the fluid through a wall of the tubes to enter the channel of the tubes and into the first flow path.
9. The device of claim 8, wherein the selectively permeable membrane tubes include at least one of Teflon amorphous fluoropolymer (Teflon AF) (tetrafluoroethylene containing 2,2-bistrifluoromethyl-4,5-difluoro-1,3-dioxole) or Hyflon AD (tetra-fluoroethylene (TFE)-2,2,4-trifluoro-5-tri-fluorometoxy-1,3-dioxole).
10. The device of claim 8, wherein the at least one Polysulfide includes a poly-thio-ether.
11. The device of claim 8, wherein the at least one Polysulfide includes low-density manganese dioxide-cured polysulfide.
12. The device of claim 8, wherein the tube sheets are made entirely of the at least one Fluorosilicone.
13. The device of claim 8, wherein the tube sheets are made entirely of the at least one Fluorocarbon.
14. The device of claim 8, wherein the tube sheets are made entirely of the at least one Polysulfide.
15. A method, comprising: binding an end of a tube bundle of selectively permeable membrane tubes with an elastomer comprising one or more of at least one Fluorosilicone, at least one Fluorocarbon, or at least one Polysulfide.
16. The method of claim 15, further comprising inserting the tube bundle with bound ends into a housing and sealing the bound ends to the housing to define two liquidly isolated flow paths.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0011] So that those skilled in the art to which the subject disclosure appertains will readily understand how to make and use the devices and methods of the subject disclosure without undue experimentation, embodiments thereof will be described in detail herein below with reference to certain figures, wherein:
[0012]
[0013]
[0014]
DETAILED DESCRIPTION
[0015] Reference will now be made to the drawings wherein like reference numerals identify similar structural features or aspects of the subject disclosure. For purposes of explanation and illustration, and not limitation, an illustrative view of an embodiment of a cartridge in accordance with the disclosure is shown in
[0016] Referring to
[0017] The tube sheets 105 can be made of any suitable material that is less rigid than epoxy and can be chemically unreactive with the degassed fluid and temperature capable. For example, the tube sheets 105 can be made of any suitable material that is more flexible than epoxy, solid within a range of expected fuel temperatures, solid in range of expected pressures, and unreactive chemically with hydrocarbon based fuels. A suitable material can also exhibit very low creep when challenged with the combination of fuel pressure and temperature and its coefficient of thermal expansion can be similar to that of the hollow fiber membrane tubes, for example. During the potting process a suitable material can be liquid and it can be selected to properly wet the surface (e.g., Teflon AF or other suitable material) of the hollow fiber membrane tubes; hence it should have relatively low viscosity when in its liquid state (uncured) and good adhesion to the Teflon AF surface.
[0018] The selectively permeable membrane tubes can include (e.g., as a surface layer) at least one of Teflon amorphous fluoropolymer (Teflon AF) (tetrafluoroethylene containing 2,2-bistrifluoromethyl-4,5-difluoro-1,3-dioxole) or Hyflon AD (tetra-fluoroethylene (TFE)-2,2,4-trifluoro-5-tri-fluorometoxy-1,3-dioxole), for example, or any other suitable material for allowing permeation of a desired gas through the walls of the tubes. In certain embodiments, the at least one Polysulfide can include a poly-thio-ether. In certain embodiments, the at least one Polysulfide can include low-density manganese dioxide-cured polysulfide.
[0019] In certain embodiments, the tube sheets 105 can be made entirely of the at least one Fluorosilicone. In certain embodiments, the tube sheets 105 can be made entirely of the at least one Fluorocarbon. In certain embodiments, the tube sheets 105 can be made entirely of the at least one Polysulfide.
[0020] In accordance with at least one aspect of this disclosure, referring to
[0021] This general concept of two flow paths can also be achieved by any other suitable module configurations, not shown in
[0022] In accordance with at least one aspect of this disclosure, a method can include binding an end 103a, 103b of a tube bundle 101 of selectively permeable membrane tubes with an elastomer comprising one or more of at least one Fluorosilicone, at least one Fluorocarbon, or at least one Polysulfide. The method can include inserting the tube bundle 101 with bound ends into a housing 107 and sealing the bound ends 103a, 103b to the housing 107 to define two liquidly isolated flow paths.
[0023] In embodiments, many fibers/tubes (e.g., thousands) form a tube bundle, which is potted at its two ends with an elastomer. Upon curing, the elastomer is cut at each end to expose the ends of the fibers, as shown in
[0024] As appreciated by those having ordinary skill in the art, existing hollow-fiber module tube sheet technology, which is derived from gas separation applications, is inadequate for properly sealing a jet fuel deoxygenator in the combination of fuel temperature and pressure. The interface between the fiber and the potting compound will be challenged directly under fuel pressure at elevated temperatures. Also, the tube bundles are traditionally made of a Teflon-like material (e.g., Teflon AF 1600) which is notoriously difficult to adhere to. Hence, embodiments utilize an elastomeric material rather than an inflexible epoxy because it affords much better durability under multiple temperature and pressure cycles, both in terms of stress dissipation as well as in terms of adhesion. The elastomeric materials can achieve the combination of properties desired for use in fuel degassing systems, e.g., temperature stability, adhesion to Teflon AF, compatibility with hot jet fuel, and form-in-place capability.
[0025] One concern in the potting process is the shrinking of the potting compound during the curing process. Certain embodiments utilize one or more Fluorosilicones and/or fluorocarbons. Certain embodiments utilize a polysulfide which can have working temperature of at least 250 F, for example. Embodiments can utilize a low-density manganese dioxide-cured polysulfide, which has low viscosity immediately after mixing and can cure at ambient temperature.
[0026] The methods and systems of the present disclosure, as described above and shown in the drawings, provide for degassing systems with superior properties. While the apparatus and methods of the subject disclosure have been shown and described with reference to embodiments, those skilled in the art will readily appreciate that changes and/or modifications may be made thereto without departing from the spirit and scope of the subject disclosure.