CA1095207A - Selective plugging of broken fibers in tubesheet- hollow fiber assemblies - Google Patents
Selective plugging of broken fibers in tubesheet- hollow fiber assembliesInfo
- Publication number
- CA1095207A CA1095207A CA310,108A CA310108A CA1095207A CA 1095207 A CA1095207 A CA 1095207A CA 310108 A CA310108 A CA 310108A CA 1095207 A CA1095207 A CA 1095207A
- Authority
- CA
- Canada
- Prior art keywords
- tubesheet
- sealant
- fibers
- fiber
- lengths
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 155
- 239000012510 hollow fiber Substances 0.000 title claims abstract description 25
- 230000000712 assembly Effects 0.000 title abstract description 14
- 238000000429 assembly Methods 0.000 title abstract description 14
- 239000000565 sealant Substances 0.000 claims abstract description 66
- 238000000034 method Methods 0.000 claims abstract description 45
- 230000006835 compression Effects 0.000 claims abstract description 5
- 238000007906 compression Methods 0.000 claims abstract description 5
- 230000002950 deficient Effects 0.000 claims description 17
- 239000011521 glass Substances 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- 239000003792 electrolyte Substances 0.000 claims description 6
- 239000000919 ceramic Substances 0.000 claims description 5
- 239000002657 fibrous material Substances 0.000 claims description 5
- 239000000725 suspension Substances 0.000 claims description 4
- 238000011065 in-situ storage Methods 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 2
- 239000004615 ingredient Substances 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 10
- 239000012530 fluid Substances 0.000 abstract description 4
- 239000003513 alkali Substances 0.000 abstract description 3
- 229910052717 sulfur Inorganic materials 0.000 abstract description 3
- 239000011593 sulfur Substances 0.000 abstract description 3
- 239000000463 material Substances 0.000 description 12
- 238000004382 potting Methods 0.000 description 11
- 150000001875 compounds Chemical class 0.000 description 10
- 239000011888 foil Substances 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 238000007789 sealing Methods 0.000 description 8
- 238000005245 sintering Methods 0.000 description 6
- 229910052783 alkali metal Inorganic materials 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000009740 moulding (composite fabrication) Methods 0.000 description 5
- 239000002002 slurry Substances 0.000 description 5
- 150000001340 alkali metals Chemical class 0.000 description 4
- 238000000280 densification Methods 0.000 description 4
- 238000000227 grinding Methods 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910000679 solder Inorganic materials 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 239000004020 conductor Substances 0.000 description 3
- 210000005239 tubule Anatomy 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- -1 alkali-metal cation Chemical class 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical compound CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000012260 resinous material Substances 0.000 description 2
- 239000012812 sealant material Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 102100035683 Axin-2 Human genes 0.000 description 1
- 101700047552 Axin-2 Proteins 0.000 description 1
- 229920001410 Microfiber Polymers 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 229910019884 NaxSy Inorganic materials 0.000 description 1
- 206010037660 Pyrexia Diseases 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000005385 borate glass Substances 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052681 coesite Inorganic materials 0.000 description 1
- 231100001010 corrosive Toxicity 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- JRBPAEWTRLWTQC-UHFFFAOYSA-N dodecylamine Chemical compound CCCCCCCCCCCCN JRBPAEWTRLWTQC-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010891 electric arc Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 235000015110 jellies Nutrition 0.000 description 1
- 239000008274 jelly Substances 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 239000003658 microfiber Substances 0.000 description 1
- 239000006060 molten glass Substances 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000005077 polysulfide Substances 0.000 description 1
- 150000008117 polysulfides Polymers 0.000 description 1
- 230000036647 reaction Effects 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000375 suspending agent Substances 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
- BSVBQGMMJUBVOD-UHFFFAOYSA-N trisodium borate Chemical compound [Na+].[Na+].[Na+].[O-]B([O-])[O-] BSVBQGMMJUBVOD-UHFFFAOYSA-N 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000003039 volatile agent Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/10—Testing of membranes or membrane apparatus; Detecting or repairing leaks
- B01D65/106—Repairing membrane apparatus or modules
- B01D65/108—Repairing membranes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/36—Accumulators not provided for in groups H01M10/05-H01M10/34
- H01M10/39—Accumulators not provided for in groups H01M10/05-H01M10/34 working at high temperature
- H01M10/3909—Sodium-sulfur cells
- H01M10/3918—Sodium-sulfur cells characterised by the electrolyte
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Secondary Cells (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Glass Compositions (AREA)
- Cell Separators (AREA)
Abstract
Abstract of the Disclosure There is disclosed a method of selectively plugging broken fibers included in a bundle of hollow fibers having open ends protruding from a tubesheet and closed ends distal from the tubesheet. The protruding open ends are immersed in a curable, fluid sealant and capillary attraction is utilized to draw the sealant into the broken fibers. The resistance to compression of the gases in the unbroken fibers is such that the sealant does not move into the latter fibers so far that they will not be open after the protruding ends are removed. The imbibed sealant is cured in place and the protruding fiber ends are cut off flush with the final surface of the tubesheet. This method is of particular value in preparing tubesheet-fiber assemblies for use in high temperature alkali metal-sulfur battery cells, wherein the hollow fibers function as an electrolyte-separator.
Description
;2~7 A variety of permeab~ility separatory devices in which the membrane takes the form of a large number of fine h' hollow fibers is known. In another type of application, ` hollow fibers~composed of~ma~terials capable of transporting 5;~ ~alkali metal~¢ations~and résIs~ànt~to~the-mQlten~metal, and to molten~alkali~metal polysul~ide~s,~have found use as~electrolyte-separators in~h~lgh~tampierature alkali metal-sulfur battery`cells~(see~U~.~S.~P~ 3,476~,~6~Q2; 3,765,944 and 3,791,868~, for example). ~
10~ ~ Common to both permeability~separatory devices and battery ~ells of the ~oregoin~ types ~is the use of at least one "tabesheet" or relatively~thin~wall~member which s~se~lingly~engaged ~w~ith~ iber exteriors and funstions to~separate"~diff~rént~ ~ lés-~of~ fluid`in~contact with the 15~ in~terior and~ex~erlor;~surfajc~es~of the fibers ~and to fix 2' ;the~positLon of the f~ibers with~in the;device or cell).
Hollow i~ers, i.e.~, thin-walled, hairlike tubules, a~re~relatively~fragile, parti¢ularly when composed of j~ matèrials, such~;~as glasses Qr~cerami~S~ whic~ are suit-2Q ~able~ or use~ln~hLgh temperature batteri~es~ Consequently, it is quite di~ficult to avoid breaking at least several fibers when fabricating t~besheet-fiber assemblies. Even though only a few~fibers out of a million may be broken, '~
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the resulting assembly will generally be useless for its intended purpose. This is particularly so in applications such as blood dialysis or high temperature batteries.
Several methods are known for salvaging tubesheet-hollow fiber assemblies made from resinous materials, butsuch methods are either inoperable or impractical when the assembly is composed of materials suitable for use in batteries operating at temperatures of 300C or more and containing molten alkali metals and corresponding poly-sulfides (or hali~es).
Exemplary of known salvage methods are thosedisclosed in U.S.P. 3,4~9,062 and 3~968,192.
The '062 patent discloses (at columns 23 and 24) a method of repairing leaks in a fluid separation apparatus ` 15 comprising a plurality of open-ended, generally parallel hollow fibers, potted at each end in "wall members" or tubesheets; and a tubular casing sealed to the peripheral surfaces of the tubesheets. Openings in the outer surface of a given tubesheet which connect to a leak through the tubesheet itself or to a leaking fiber are closed by form-ing a pool of a curable resinous liquid on the tubesheet surface, drawing enough of it into the leak-connected opening to close off the leak or leaking fiber, removing the excess liquid and solidifying the remainder in place.
(If the leak is in a fiber, the terminous of the fiber lumen in each of the two tubesheets must be so closed.) In this method, flow of the resinous li~uid into fibers which are not leaking is prevented by maintaining the li~uid under a pressure which is greater than that 3Q exterior to the ~ibers but less than the pressure applied to the fiber lumens at their uncovered ends.
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The '192 patent discloses an alternate method of salvaging leaky tubesheet-hollow fiber assemblies of the above-described type. The fiber and tubesheet materials are either thermoplastic or are heat-degradeable, and the leak-connected openings are first located and then closed by localized, temporary application of heat and mechanical pressure to the materials in their immediate vicinity.
Neither of the foregoing methods is applicable to tubesheet-fiber assemblies which must function in cor-rosive, high temperature environments. In order to effectivelyplug any broken fibers in such ~ssemblies, the plugging ~ material, or "sealant", must meet ~everal requirements i~ which cannot be met by resinous materials. That is, the sealant not only must be fluid enough to be forced into lS the broken fibers under practicable operating conditions but also must be convertible, in situ and at temperatures below the distortion temperatures of the assembly materials, to a rigid, non-porous solid which is bonded to the fiber walls, has a coefficient of expansion which adequately matches that of the fiber material and which will endure in the environment and at the temperatures it is exposed to during operation of the deviceO
Also, the technique used to prevent sealing off of good fibers in the process of the l062 patent cannot be used with fibers having closed ends. Al~hough entry of the sealant into good fibers will be resisted by compression of the air in those fibers, enough sealant can still enter to effectively plug them.
The present invention, broadly, is a method of fielectively plugging broken or imperfect fibers which, to~ether with unbroken fibers, constitute a bundle of hollow fibers potted in a tubesheet body, the majority of said fibers being unbroken, i.e., having closed ends distal from the tubesheet and open ends adjacent to and pro-truding from the tubesheet. The protruding open ends of 18,458F
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all fibers are immersed to an appropriate depth, in a liquid sealant, such that the sealant will be drawn by capillary attraction into the broken or imperfect fibers at least to a point beyond the nearest tubesheet surface.
The gas pressure in the closed fiber ends is such that the sealant will not be drawn into the good fibers so far that they too will remain plugged after the open fiber ends have been cut of flush with the final tubesheet surface (which may be the original face or a new face established by grinding off part of the tubesheet).
More precisely, the invention may be defined as the method of treatin~ a tubesheet/hollow fiber assembly to ensure that any defective fibers included therein will ~:
be selectively plugged, said method comprising : 15 A. providing as said assembly one which comprises a bundle of hollow fiber lengths passing through and engaged with a rigid wall member or tubesheet having first and second generally parallel faces, all of said lengths having open ends protruding from said first face and --at least a majority of said lengths having closed-ended portions extending from said second face, B. immersing said open fiber ends in a pool of a liquid sealant to a depth such that the distance between said first face and the sur-face of said pool external to the fiber ends is d, the force of capillary attraction between the walls of said fibers and said sealant being such that said sealant is drawn into said defective fibers for a distance greater than d, thereby filling them to a level beyond said face, 18,458F
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iO952~7 the resistance to compression of the gases within the closed end length being such that said capillary attraction does not suffice to draw the sealant into said closed ended lengths beyond a point substantially below said level, ~ C. remo~ing the unimbibed sealant from contact with :~ said protruding fiber end~, the imbibed sealant being so composed as to be cov~rtible, in-situ and at a temperature below the distortion temperature of said lengths, to plugs of a solid, non-porou~ material sealingly bonded to the fiher walls and having a coefficient of expansion suhstantially matching that of the : fiber mate~ial, .
` 15 D. converting the imbibed sealant to said plugs and E. severing the protruding fiber ends from said ~:
`~ tubesheet, with the result that the defective fibers in the treated assembly are plugged and the good fibers are not plugged.
Of particular value is the embodiment of the inven-tion, as above defined, wherein said closed ended lengths are adapted to function ~;: as the electrolyte/separator in a high tempera-ture battery cell, said sealant i~ a suspension, in an inert, volatilizable liquid, of glass or ceramic particles which have a maximum diameter of ~- about 1~3 or less of the inner diameter of said fiber lengths and will fuse together 3~ to form said plugs when heated to a temperature Tl, which is less than the distortion tempera-~ ture of said lengths, and 18,458F
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: . . . . .
. ,. :, . . .~ . ~, -````` ~0952~7 said assembly is heated to Tl, thereby devola- ;
tilizing said suspension in said defective fibers and converting said particleg therein to said plugs.
In a preferred mode of practising the invention, as above defined, a sealant is employed which exerts a vapor pressure o at least 12 mm of Hg at about 20C, thereby ensuring that the total gas pressure in the fibers will suffice to effectively reduce the distance the seal-ant will be drawn by capillary attraction into the good, i.e., closed ended, fibers. The extent, if anyr to which the tube~heet must be ground to ensure that the unbroken fiber~ will not be pluyged is accordingly reduced.
Certain of the terms used in the foregoing sum-mary require definition and, accordingly~ are defined as follows:
;~ The term "defectivel' fibers is intended to refer -to fiber lengths, the open ends o which ~protruding from the outer tubesheet ace) communicate with openings in the same lengths on the opposite side of the tubesheet, i.e., ~ -to fibers which are broken off or have incomplete walls or end closures.
The term "rigid" is intended to apply not only to fully cured or densified, non-porous tubesheets but also to green or partly cursd (or sintered) tube~heet s~ructures which may be porous and not fully densified but are ~elf-supporting and retain their shape under the con-ditions of fabrication employed.
The terms "closed ended portions" and "closed ended lengths" are intended to apply not only to unlooped fibers having only one open end but also to fiber loops having two open ends, both of which protrude from the outer tubesheet face.
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Og52Q 7 The term "severing" includes removal of the protruding "open" fiber ends and/or the portions of said ends initially within the tubesheet but immediately adjacent to said first face, by grinding.
The phrase "substantially below said level" refers to a distance such that the portion of the tubesheet imme-diately adjacent the face can be removed ~as by grinding), to reopen the clo~ed ended lengths, without effectively unplugging the defective lengths or rendering the remaining tubesheet structure too thin to serve its intended purpose.
The meaning of the term "substantially matching"
is made evident by the subsequent discussion herein of how the difference in coefficients of expansion (for the sealant and fiber materials) which can be tolerated depends on the flexibilities of those m~terials and on the tempera-ture at which the treated assembly is designed to operate.
Methods of constructing hollow fiber permeability separatory devices are now well known. Closed-end, unlooped fibers are generally not employed in such devices, since such purposes as may be so served can more efficiently be served by using fiber loops, i.e., fibers bent in an elongated U-shape and having both ends terminating at and opening upon the same surface of a given tubesheet. How-ever, if it is elected to use unlooped fibers having one end closed, no fabrication techniques or apparatus arrange-ments not alreadly familiar to those skilled in the art are required.
~o date, fiber loops have not been propos~d to ~e used in high temperature batteries. However, hollow fibers suitable for such use are not so stiff that they 18,458F
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cannot be bent in a radius of the dimensions appropriate to present cell designs~ The use of unlooped, closed-end, hollow fibers is presently preferred but is not considered essential to the fabrication o~ volume-efficient, high temperature battery cells in which the fibers will function as the electrolyte separator.
For an exemplary description of a method of assembling hollow fiber battery cells, reference may be had to the aforementioned U.S.P 3,7gl,868 and U.S.P.
3,917,490 (Example 4; column 9).
A typical, high temperature battery cell to which the present invention relates is an alkali-metal/sulfur cell in which the electrolyte takes the form of a large number of closely spaced, alkali-metal cation conductive, unlooped hairlike glass or ceramic tubules. A generally cylindrical cup or container for the catholyte (NaxSy, for example) and an inverted, generally cylindrical cup for the anolyte (Na, for example) are abutted against and joined in sealing arrangement to the peripheral portion of an intervening, horizontal, impervious, electrically non-conducting tubesheet/separator disc. The tubules or hollo~ fiber lengths have their lower ends closed and their upper ends open and pass through the tubesheet in sealing engagement therewith. The open ends of the fibers ~5 communicate with the molten alkali metal in the anolyte reservoir above the tubesheet and the portions of the fibers dependent from the tubesheet are immersed in the under lying molten catholyte. Wraps o a perforated, carbon--coated aluminum foil are interleaved between the (generally concentric) fiber rows and serve to collect and convey the cathode current to (or from) an external, electrical cathode connection. An anodic electrode is immersed in the molten metal, which also functions as a current 18,458F
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' Q9S20~7 g_ collector, and extends through the anolyte container, in sealing engagement with the same, to provide an external electrical anode connection.
Tubesheet-fiber assemblies of the type employed in the above-described cell can be made as follows. A
plurality of the hollow electrolyte ~ibers are closely ;~
spaced upon an elongated generally rectangular sheet o electrically and thermally conductive material, such as a foil. The sheet has ~lrst and second elongated edges.
The fibers are positioned generally parallel to one another and transversely to the elongated axis of the sheet. In positioning the fibers, the open ended portions are allowed to extend to a uniform degree beyond the first elongated edge of the sheet thereby to provide a margin. The opposite or closed ends of the fibers may be allowed to uniformly approach the second elongated edge of the sheet with the sheet extending beyond the closed ends of the fibers to form a skirt A very small amount of a readily decomposed or catholyte-compatible adhesive may be used 2Q to maintain the fibers in their respective places after they have been positioned.
Once the fibers are positioned, the fibers, foil and skirt can be rolled up. While this i9 being done, a band of a potting compound (of a solid or paste-like con-sistenay) is applied to the fibers between the open end ~- thereof and the first elongated edge of the sheet, i.e., the potting compound is applied along the open-ended portions of the fibers forming the margin, just ahead of the nip of the forming roll. (When the completed assembly is to 8a be processed by the method of the present invention, to ensure that any defective fibers are plugged, the width of the band of potting compound preferably i5 less than the width of the margin. That is, care is taken to be sure 18,458F
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that the unpotted terminal portions of the open fiber ends will protrude from the tubesheet, once it is formed by rolling up the assembly.) A strip of the same conductive material which is equal to or greater in thickness than a fiber diameter is positioned adjacent to the second elo~gated edge of the sheet to function as a conductive spacing tape having about the same width as the skirt.
The sheet, fibers, spacing tape and potting material are then rolled up, preferably about a mandrel or core. The core may be electrically conductive, in whiah case a lower protruding and thereof can serve as a cathode terminal; or, it may be non-conductin~. It can be left in the inal "jelly roll" or removed.
As the roll is wound up, the band of potting compound forms a continuous layer adjacent to the open ends of the fibers. The continuity of the layer of potting compound is ensured by applying the band in a thickness corresponding to the thickness of the spacer tape. The final step in forming the potting compound into a fluid-impermeable tubesheet in sealing engagement with all the fibers is to cause a change to occur within the potting compound to produce a uni-bodied structure. This can be accomplished, or example, by chemically and/or thermally "curing" the compound. As it is generally desirable to encase the sheet-fiber assembly in one or moxe container or reservoir members which are in sealing engagement with the tubesheet, it may be desirable to postpone final setting of the potting material until the container members have been contacted with it. If the materials forming the container members and potting com-pound have been properly selected, the potting compound will form a sealing engagement with the container members during the ~etting process. Optionally, an adhesive can be used to bind the container members to the tubesheet after it has been formed.
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At some stage of as~embly while the bottom of the rolled-up assembly is still accessible, one or more weld beads are formed thereon by using successive sheet and spacer-tape edge portions together with a helium-5 -shielded electric arc.
Although other asembly methods are considered feasible, they are not considered very practical. However, the practice of the invention is not limited to tubesheet--~iber assemblies made by any particular method. Also, it ~ill be recogni~ed that the presence of an electrically conductive material, such a~ a foil, between the rows of fibers in the assemhly, is not essential to the practice of the present invention. Other means of spacing the fiber rows from each other in the assem~ly will be apparent to those skilled in the art. Similarlyr other electrically conductive means~ such as micro-fibers of graphite mixed with the catholyte, may be introduced between the elec-trolyte fibers after the tubesheet-fiber assembly is formed.
In another option, an uncoated, porous sheet (gauze or perforated foil) formed from a conductive, non-corroding metal, such as molybdenum, for example, may be employed as the cathodic current collector.
~- Once the tube~heet has been "cured", at least to such an extent that it becomes "rigid", the tubesheet--fiber assembly can be treated by the method of the invention to remedy leak~ or to ensure the absence of same. If the assembly does not include foil wraps and/or a protruding mandrel end, extreme care must be taken in handling it to ensure that no unplugged fibers are broken after the plug-ging operation. This can be done by touching only thetubesheet edge during such manipulations as are necessary before the dependent portion of the fiber bundle is em-placed in and protected by the catholyte reservoir.
18,458F
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, ~ ~095~
-12~
However, the probability of damage is minimized and handling facilitated if the assembly does include the foil wraps, particularly when the assembly was formed about a mandrel which protrudes from the lower end of the assembly.
Accordingly, assemblie~ of the latter type are highly preferred for the practice of the invention in preparing high temperature battery cells.
It should be noted that fibers of the types known to be suitable for use in high temperature battery cells are generally delekeriously effected by moisture and should be kept in low humidity environments. Such cells should be fabricated in "glove boxes" or "dry room~".
The coefficients of expansion of the sealant and fiber materials should substantially match. The extent of mismatch between the coefficient~ of expansion of the cured sealant (plug) and the fiber materials which can be tolerated in a given assembly depends on the flexi-bilities of the different materials and on the absolute difference (~t, C) between the temperature at which the pluys are formed and the temperature furthest removed therefrom which the cell is likely to attain thereafter.
To avoid imposition of high thermal stresses, the difference between the coefficients of expansion ~x) should be such that the product ~x-~T~E is not greater than 3 kilograms per square millimeter, where E is the Youngs modulus of elastici~y (kg/mm2) for whichever material the sealant or the fibers has the lowest modulus.
For tubesheet/fiber assemblies to be used in 3Q high temperature batteries as describPd earlier herein, the maximum value of QT will usually be the difference between ordinary ambient temperatures (say 25C) and the 18,458F
_ ., .. . . ..
;
-` `` 1~9~;207 temperature (say about 400C) at which the sealant first becomes solid after being sintered.
At thig ~T (~375), assuming a modulus of 7000 kg/mm2 for the sealant, the value of ~x must be less than 1.143 x 10 6 units/C if ~x-~T-E is not to exceed 3 kg/mm2.
The general leak-plugging procedure is carried out as follows, at some point in the overall cell fab-rication sequence a~ter rigidification of the tubesheet and before removing the fiber ends protruding from it.
The assembly is positioned with respeat to a æuitably confined pool of the li~uid sealant composition, preferably by inverting the assembly and dipping the open fiber ends in the pool, in such manner that the protruding fiber ends extend, for at least part of their lengths, into the seal-ant. The distance (d) between the surface of the tube-sheet and the sealant pool should be short enough so that the capillary attraction between the sealant composition ~: and the fi~er walls will draw the sealant into the defective Cbroken or imperfect) fiber lengths to a level at least ~: 2Q beyond the face of the tubesheet nearest to the sealant pool.
That is, d must be less than h centimeters, the capillary rise, as defined by the relationship h a 4~cosQ/Dpg wherein ~ is the surface tension of the sealant (in dynes/cm), ~ is the liquid-solid wetting angle (in degrees), is the inner diameter of the fiber ~in cm), p is the fluid density of the sealant (in grams/cc) and g is the gravitational constant ~980 cm/sec ).
18,458~
: ~,c' .. ....
109~:aO7 It is apparent that h, the rise of the sealant in defective fibers of a given diameter can be increased by using a sealant composition which has a higher sur-face tension and/or a lower density. Or conversely, h may be made smaller by composing the sealant to have a lower surface tension and/or higher density. In any case, d must be small enough and h large enough to ensure that plugs will be present in the portions of the de~ective fiber lengths remaining in the assembly after the treat-ment of the present invention is finished, regardless ofwhether or not that treatment includes grinaing the tube-sheet . `, In order to ensure that the sealant will notrise too far in the closed-ended fiber lengths, the resis-tance to compression o the gases within those lengthsmust have a certain minimum value. This value can readily be calculated by those skilled in the art. For example, for fibers having an inner diameter of 50 microns, such calculations show that the total gas pressure in the closed ended lengths, expressed in millimeters of mercury should exceed 0.6y. Since most organic liquids have surface tensions between 20 and 30 dynes per centimeter, sealants comprising such solvents will usually have vapor pressures of from 12 to 18 mm Hg at ordinary ambient tem~eratures.
tToluene~ for example, has a vapor pressure of 20 mm Hg at 18C.) Thus, the total gas pressure in closed ended fibers immersed in such solvents will generally be at least 12 mm Hg.
The open fiber ends are allowed to remain in 3a the pool until the sealant has been drawn far enough into any defective fibers so that they will remain plugged 18,458F
. ~ . `
.
~.O~;Z07 after the protrudi~g open ends are severed. The assembly is then removed from contact with the sealant pool and the excess sealant adhering to the exterior surfaces of the fiber ends (and any which may adhere to the tubesheet) is washed off, as with some of the liquid medium employed in the sealant composition. The i~bibed sealant i8 solidified to non-porous, solid plugs, as by removing any volatiles and "curing" or "~etting" the non-volatile aonstituents thereof. The latter operation may be carried out by such means as sintering or by inducing chemical linking reac-tions (as by use of catalysts, simple heating or electro-magnetic irradiation).
The protruding fiber ends may be severed before the imbibed sealant is solidified but ordinarily it is preferable to effect plug formation first, for reasons which will be apparent.
The tubesheet may initially be thick enough so that the face from which the open fiber ends protrude can be ground down, to give the finished tubesheet a smooth working surface. In this event, it is not necessary to keep the sealant from moving into the closed ended fibers as far as the latter ace~ It is only necessary to keep it from advancing so far that the tubesheet whill have to be ground excessively to reopen the good fibers. (In any case, the use of the sealant in the good fibers can be controlled by manipulating the vapor pressure of the seal-ant, as discussed above.) 18,458F
-, :
,.".
In a preferred mode of operation the plugs in the defective fiber lengths are composed of the same re-lative amounts of the same ingredients as the tubesheet itself, thus assuring an even match in expansion coeffi-S cients and permitting plug formation and final tubesheet"curing" (densification) to be carried out in a single operation, such as sintering. In this mode, the sealant aonveniently (and preferably) is a solution ~or slurry) of the tubesheet material (or particles thereof) in a readily volatilized, or controllably reactive, and other-wise suitable liquid medium.
Any undissolved particles present in the sealant composikion should have maximum diameters which are 1/3 or less of the inner diameters of the fiber portions to be plugged. Otherwise, bridging of the particles may occur, thus preventing the sealant fLom flowing far enough into the defective fibers. Preferably, the particle diameter is not greater than 1/5 the fiber diameter.
In a typical application of the present method to high temperature batteries, tubesheet glass fines having maximum diameters of 10 microns or less will be ound suit-able for plugging defective fibers having an inner diameter withln the range of from 30 to 80 microns.
Although not indispensable, volatilizeable or nondetrimental suspending agents preferably are included in sealants comprising glass or ceramic particles. For example, aliphatic primary amines of from 12 to 42 carbons 18,458F
" ."
, , , , . ' - , ~.:
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llD~S2~7 have been ound particularly suitable for this purpose in preparing slurries (in aromatic solvents) of finely ground sodium borate glasses.
Tho method of the invention is most conveniently carried out in ordinary environments but may be practiced under such conditions as are feasible to establish and maintain in dry boxes ("glove boxes"), dry rooms and the like.
Practice o the invention with tubesheet/hollow fiber assemblies suitable for use in high temperature hatteries i~ illu6trated by ~but not limited to) the fol-lowing procedure.
Hollow glass fibers having an inner diameter of about 50 microns and an outer diameter of about 70 microns are prepared from a molten glass having the com-position Na2O-2B2O3 0.16NaCl 0.2 SiO2.
Fragments of a solder glass (94% B2O3, 6% Na2O) are converted to a fine powder (particle size less than 10 microns) by grinding them in the manner disclosed in U.S. Patent 3,917,490. An extrudable tubesheet composition is made hy mixing 2 parts by weight of the fines and 2 parts of -250 mesh (U.S. Std) spheres of the sam~ solder glass with about 0.4 parts of cumene.
A hollow fiber and tubesheet assembly adapted for use in a high temperature battery is assembled, essen-tially in the manner described earlier herein, from lengths of the preceding fibers, open at one end and closed at the other. The assembly includes a carbon-coated, per-forated aluminum foil strip, a spacer skirt of the same foil and a central mandrel taluminum rod). The tubesheet 18,458F
.,, . ,. . . ,i ,; .~ .: , ,. :. ;: , --is formed by extruding the proceding composition on theopen-ended portions of the fibers extending beyond the foil edge, as the assembly is rolled up, and heating the resulting disc or wall member with an infrared lamp until S (several hours) it is dry (essentially cumene-ree) and self-supporting (rigidified). The open ends o~ the fiber lengths protrude about 1 cm from the outer tupper? face of the tubesheet and the closed ends extend about 10 cm from the inner (lower) face.
A sealant slurry is prepaxed by mixing the pre-ceding solder glass powder with a 5 wt. % solution of dodecyl amine in toluene, in a ratio of 0.5 cc of the solution per gram of fines~
~he as~embly is inverted and the protruding open - 15 fiber ends immersed in the slurry of a depth of about 0.5 cm (d = 1.0-0.5 = 0.5 cm) for about 2 minutes. It is then lifted out of contact with the sealant slurry and washed by dipping the protruding fiber ends in toluene.
Heat is then applied to the assembly, with an 2Q infrared lamp, until the rate of toluene vaporization from the assembly is negligible. (This usually requires from 1 to several hours.) Next the non-volatile residium of the sealant (in the "open" fibers ends) and the tubesheet are rendered non-porous and bonded to the fibers by staged heating of the assembly. The assembly is first heated in vacuo to a temperature of up to about 385C and maintained at ~hat temperature until essentially no further densification occurs~ It is then heated to about 405, under N2 at 18,458F
'. . ' . . - -.:"`. ,. ;: ~. ~
.
10~5Z0!7 1 atmosphere of pressure for about 1.5 hour. (The distortion temperature of the fibers is about 440C).
Finally, the protruding fiber ends are cut off flush with the tubesheet face. The face may be ground smooth but this in not necessary to ensure that the un-broken fibers are unplugged in this case. That i9 ~ the sealant has risen in the defective fiber length~ about
10~ ~ Common to both permeability~separatory devices and battery ~ells of the ~oregoin~ types ~is the use of at least one "tabesheet" or relatively~thin~wall~member which s~se~lingly~engaged ~w~ith~ iber exteriors and funstions to~separate"~diff~rént~ ~ lés-~of~ fluid`in~contact with the 15~ in~terior and~ex~erlor;~surfajc~es~of the fibers ~and to fix 2' ;the~positLon of the f~ibers with~in the;device or cell).
Hollow i~ers, i.e.~, thin-walled, hairlike tubules, a~re~relatively~fragile, parti¢ularly when composed of j~ matèrials, such~;~as glasses Qr~cerami~S~ whic~ are suit-2Q ~able~ or use~ln~hLgh temperature batteri~es~ Consequently, it is quite di~ficult to avoid breaking at least several fibers when fabricating t~besheet-fiber assemblies. Even though only a few~fibers out of a million may be broken, '~
~; 18,458F
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the resulting assembly will generally be useless for its intended purpose. This is particularly so in applications such as blood dialysis or high temperature batteries.
Several methods are known for salvaging tubesheet-hollow fiber assemblies made from resinous materials, butsuch methods are either inoperable or impractical when the assembly is composed of materials suitable for use in batteries operating at temperatures of 300C or more and containing molten alkali metals and corresponding poly-sulfides (or hali~es).
Exemplary of known salvage methods are thosedisclosed in U.S.P. 3,4~9,062 and 3~968,192.
The '062 patent discloses (at columns 23 and 24) a method of repairing leaks in a fluid separation apparatus ` 15 comprising a plurality of open-ended, generally parallel hollow fibers, potted at each end in "wall members" or tubesheets; and a tubular casing sealed to the peripheral surfaces of the tubesheets. Openings in the outer surface of a given tubesheet which connect to a leak through the tubesheet itself or to a leaking fiber are closed by form-ing a pool of a curable resinous liquid on the tubesheet surface, drawing enough of it into the leak-connected opening to close off the leak or leaking fiber, removing the excess liquid and solidifying the remainder in place.
(If the leak is in a fiber, the terminous of the fiber lumen in each of the two tubesheets must be so closed.) In this method, flow of the resinous li~uid into fibers which are not leaking is prevented by maintaining the li~uid under a pressure which is greater than that 3Q exterior to the ~ibers but less than the pressure applied to the fiber lumens at their uncovered ends.
18,458F
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The '192 patent discloses an alternate method of salvaging leaky tubesheet-hollow fiber assemblies of the above-described type. The fiber and tubesheet materials are either thermoplastic or are heat-degradeable, and the leak-connected openings are first located and then closed by localized, temporary application of heat and mechanical pressure to the materials in their immediate vicinity.
Neither of the foregoing methods is applicable to tubesheet-fiber assemblies which must function in cor-rosive, high temperature environments. In order to effectivelyplug any broken fibers in such ~ssemblies, the plugging ~ material, or "sealant", must meet ~everal requirements i~ which cannot be met by resinous materials. That is, the sealant not only must be fluid enough to be forced into lS the broken fibers under practicable operating conditions but also must be convertible, in situ and at temperatures below the distortion temperatures of the assembly materials, to a rigid, non-porous solid which is bonded to the fiber walls, has a coefficient of expansion which adequately matches that of the fiber material and which will endure in the environment and at the temperatures it is exposed to during operation of the deviceO
Also, the technique used to prevent sealing off of good fibers in the process of the l062 patent cannot be used with fibers having closed ends. Al~hough entry of the sealant into good fibers will be resisted by compression of the air in those fibers, enough sealant can still enter to effectively plug them.
The present invention, broadly, is a method of fielectively plugging broken or imperfect fibers which, to~ether with unbroken fibers, constitute a bundle of hollow fibers potted in a tubesheet body, the majority of said fibers being unbroken, i.e., having closed ends distal from the tubesheet and open ends adjacent to and pro-truding from the tubesheet. The protruding open ends of 18,458F
.
all fibers are immersed to an appropriate depth, in a liquid sealant, such that the sealant will be drawn by capillary attraction into the broken or imperfect fibers at least to a point beyond the nearest tubesheet surface.
The gas pressure in the closed fiber ends is such that the sealant will not be drawn into the good fibers so far that they too will remain plugged after the open fiber ends have been cut of flush with the final tubesheet surface (which may be the original face or a new face established by grinding off part of the tubesheet).
More precisely, the invention may be defined as the method of treatin~ a tubesheet/hollow fiber assembly to ensure that any defective fibers included therein will ~:
be selectively plugged, said method comprising : 15 A. providing as said assembly one which comprises a bundle of hollow fiber lengths passing through and engaged with a rigid wall member or tubesheet having first and second generally parallel faces, all of said lengths having open ends protruding from said first face and --at least a majority of said lengths having closed-ended portions extending from said second face, B. immersing said open fiber ends in a pool of a liquid sealant to a depth such that the distance between said first face and the sur-face of said pool external to the fiber ends is d, the force of capillary attraction between the walls of said fibers and said sealant being such that said sealant is drawn into said defective fibers for a distance greater than d, thereby filling them to a level beyond said face, 18,458F
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'. . ''. r ' ~ ' :
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iO952~7 the resistance to compression of the gases within the closed end length being such that said capillary attraction does not suffice to draw the sealant into said closed ended lengths beyond a point substantially below said level, ~ C. remo~ing the unimbibed sealant from contact with :~ said protruding fiber end~, the imbibed sealant being so composed as to be cov~rtible, in-situ and at a temperature below the distortion temperature of said lengths, to plugs of a solid, non-porou~ material sealingly bonded to the fiher walls and having a coefficient of expansion suhstantially matching that of the : fiber mate~ial, .
` 15 D. converting the imbibed sealant to said plugs and E. severing the protruding fiber ends from said ~:
`~ tubesheet, with the result that the defective fibers in the treated assembly are plugged and the good fibers are not plugged.
Of particular value is the embodiment of the inven-tion, as above defined, wherein said closed ended lengths are adapted to function ~;: as the electrolyte/separator in a high tempera-ture battery cell, said sealant i~ a suspension, in an inert, volatilizable liquid, of glass or ceramic particles which have a maximum diameter of ~- about 1~3 or less of the inner diameter of said fiber lengths and will fuse together 3~ to form said plugs when heated to a temperature Tl, which is less than the distortion tempera-~ ture of said lengths, and 18,458F
. "
: . . . . .
. ,. :, . . .~ . ~, -````` ~0952~7 said assembly is heated to Tl, thereby devola- ;
tilizing said suspension in said defective fibers and converting said particleg therein to said plugs.
In a preferred mode of practising the invention, as above defined, a sealant is employed which exerts a vapor pressure o at least 12 mm of Hg at about 20C, thereby ensuring that the total gas pressure in the fibers will suffice to effectively reduce the distance the seal-ant will be drawn by capillary attraction into the good, i.e., closed ended, fibers. The extent, if anyr to which the tube~heet must be ground to ensure that the unbroken fiber~ will not be pluyged is accordingly reduced.
Certain of the terms used in the foregoing sum-mary require definition and, accordingly~ are defined as follows:
;~ The term "defectivel' fibers is intended to refer -to fiber lengths, the open ends o which ~protruding from the outer tubesheet ace) communicate with openings in the same lengths on the opposite side of the tubesheet, i.e., ~ -to fibers which are broken off or have incomplete walls or end closures.
The term "rigid" is intended to apply not only to fully cured or densified, non-porous tubesheets but also to green or partly cursd (or sintered) tube~heet s~ructures which may be porous and not fully densified but are ~elf-supporting and retain their shape under the con-ditions of fabrication employed.
The terms "closed ended portions" and "closed ended lengths" are intended to apply not only to unlooped fibers having only one open end but also to fiber loops having two open ends, both of which protrude from the outer tubesheet face.
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Og52Q 7 The term "severing" includes removal of the protruding "open" fiber ends and/or the portions of said ends initially within the tubesheet but immediately adjacent to said first face, by grinding.
The phrase "substantially below said level" refers to a distance such that the portion of the tubesheet imme-diately adjacent the face can be removed ~as by grinding), to reopen the clo~ed ended lengths, without effectively unplugging the defective lengths or rendering the remaining tubesheet structure too thin to serve its intended purpose.
The meaning of the term "substantially matching"
is made evident by the subsequent discussion herein of how the difference in coefficients of expansion (for the sealant and fiber materials) which can be tolerated depends on the flexibilities of those m~terials and on the tempera-ture at which the treated assembly is designed to operate.
Methods of constructing hollow fiber permeability separatory devices are now well known. Closed-end, unlooped fibers are generally not employed in such devices, since such purposes as may be so served can more efficiently be served by using fiber loops, i.e., fibers bent in an elongated U-shape and having both ends terminating at and opening upon the same surface of a given tubesheet. How-ever, if it is elected to use unlooped fibers having one end closed, no fabrication techniques or apparatus arrange-ments not alreadly familiar to those skilled in the art are required.
~o date, fiber loops have not been propos~d to ~e used in high temperature batteries. However, hollow fibers suitable for such use are not so stiff that they 18,458F
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. .
-.
, -' ' . -- : : ~ ~
: - :
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cannot be bent in a radius of the dimensions appropriate to present cell designs~ The use of unlooped, closed-end, hollow fibers is presently preferred but is not considered essential to the fabrication o~ volume-efficient, high temperature battery cells in which the fibers will function as the electrolyte separator.
For an exemplary description of a method of assembling hollow fiber battery cells, reference may be had to the aforementioned U.S.P 3,7gl,868 and U.S.P.
3,917,490 (Example 4; column 9).
A typical, high temperature battery cell to which the present invention relates is an alkali-metal/sulfur cell in which the electrolyte takes the form of a large number of closely spaced, alkali-metal cation conductive, unlooped hairlike glass or ceramic tubules. A generally cylindrical cup or container for the catholyte (NaxSy, for example) and an inverted, generally cylindrical cup for the anolyte (Na, for example) are abutted against and joined in sealing arrangement to the peripheral portion of an intervening, horizontal, impervious, electrically non-conducting tubesheet/separator disc. The tubules or hollo~ fiber lengths have their lower ends closed and their upper ends open and pass through the tubesheet in sealing engagement therewith. The open ends of the fibers ~5 communicate with the molten alkali metal in the anolyte reservoir above the tubesheet and the portions of the fibers dependent from the tubesheet are immersed in the under lying molten catholyte. Wraps o a perforated, carbon--coated aluminum foil are interleaved between the (generally concentric) fiber rows and serve to collect and convey the cathode current to (or from) an external, electrical cathode connection. An anodic electrode is immersed in the molten metal, which also functions as a current 18,458F
....
..;.
'. '-, .,, ' ~.
' Q9S20~7 g_ collector, and extends through the anolyte container, in sealing engagement with the same, to provide an external electrical anode connection.
Tubesheet-fiber assemblies of the type employed in the above-described cell can be made as follows. A
plurality of the hollow electrolyte ~ibers are closely ;~
spaced upon an elongated generally rectangular sheet o electrically and thermally conductive material, such as a foil. The sheet has ~lrst and second elongated edges.
The fibers are positioned generally parallel to one another and transversely to the elongated axis of the sheet. In positioning the fibers, the open ended portions are allowed to extend to a uniform degree beyond the first elongated edge of the sheet thereby to provide a margin. The opposite or closed ends of the fibers may be allowed to uniformly approach the second elongated edge of the sheet with the sheet extending beyond the closed ends of the fibers to form a skirt A very small amount of a readily decomposed or catholyte-compatible adhesive may be used 2Q to maintain the fibers in their respective places after they have been positioned.
Once the fibers are positioned, the fibers, foil and skirt can be rolled up. While this i9 being done, a band of a potting compound (of a solid or paste-like con-sistenay) is applied to the fibers between the open end ~- thereof and the first elongated edge of the sheet, i.e., the potting compound is applied along the open-ended portions of the fibers forming the margin, just ahead of the nip of the forming roll. (When the completed assembly is to 8a be processed by the method of the present invention, to ensure that any defective fibers are plugged, the width of the band of potting compound preferably i5 less than the width of the margin. That is, care is taken to be sure 18,458F
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.
.. .: ;- -: ~ . . -- ' ~09S2~7~
that the unpotted terminal portions of the open fiber ends will protrude from the tubesheet, once it is formed by rolling up the assembly.) A strip of the same conductive material which is equal to or greater in thickness than a fiber diameter is positioned adjacent to the second elo~gated edge of the sheet to function as a conductive spacing tape having about the same width as the skirt.
The sheet, fibers, spacing tape and potting material are then rolled up, preferably about a mandrel or core. The core may be electrically conductive, in whiah case a lower protruding and thereof can serve as a cathode terminal; or, it may be non-conductin~. It can be left in the inal "jelly roll" or removed.
As the roll is wound up, the band of potting compound forms a continuous layer adjacent to the open ends of the fibers. The continuity of the layer of potting compound is ensured by applying the band in a thickness corresponding to the thickness of the spacer tape. The final step in forming the potting compound into a fluid-impermeable tubesheet in sealing engagement with all the fibers is to cause a change to occur within the potting compound to produce a uni-bodied structure. This can be accomplished, or example, by chemically and/or thermally "curing" the compound. As it is generally desirable to encase the sheet-fiber assembly in one or moxe container or reservoir members which are in sealing engagement with the tubesheet, it may be desirable to postpone final setting of the potting material until the container members have been contacted with it. If the materials forming the container members and potting com-pound have been properly selected, the potting compound will form a sealing engagement with the container members during the ~etting process. Optionally, an adhesive can be used to bind the container members to the tubesheet after it has been formed.
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At some stage of as~embly while the bottom of the rolled-up assembly is still accessible, one or more weld beads are formed thereon by using successive sheet and spacer-tape edge portions together with a helium-5 -shielded electric arc.
Although other asembly methods are considered feasible, they are not considered very practical. However, the practice of the invention is not limited to tubesheet--~iber assemblies made by any particular method. Also, it ~ill be recogni~ed that the presence of an electrically conductive material, such a~ a foil, between the rows of fibers in the assemhly, is not essential to the practice of the present invention. Other means of spacing the fiber rows from each other in the assem~ly will be apparent to those skilled in the art. Similarlyr other electrically conductive means~ such as micro-fibers of graphite mixed with the catholyte, may be introduced between the elec-trolyte fibers after the tubesheet-fiber assembly is formed.
In another option, an uncoated, porous sheet (gauze or perforated foil) formed from a conductive, non-corroding metal, such as molybdenum, for example, may be employed as the cathodic current collector.
~- Once the tube~heet has been "cured", at least to such an extent that it becomes "rigid", the tubesheet--fiber assembly can be treated by the method of the invention to remedy leak~ or to ensure the absence of same. If the assembly does not include foil wraps and/or a protruding mandrel end, extreme care must be taken in handling it to ensure that no unplugged fibers are broken after the plug-ging operation. This can be done by touching only thetubesheet edge during such manipulations as are necessary before the dependent portion of the fiber bundle is em-placed in and protected by the catholyte reservoir.
18,458F
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-12~
However, the probability of damage is minimized and handling facilitated if the assembly does include the foil wraps, particularly when the assembly was formed about a mandrel which protrudes from the lower end of the assembly.
Accordingly, assemblie~ of the latter type are highly preferred for the practice of the invention in preparing high temperature battery cells.
It should be noted that fibers of the types known to be suitable for use in high temperature battery cells are generally delekeriously effected by moisture and should be kept in low humidity environments. Such cells should be fabricated in "glove boxes" or "dry room~".
The coefficients of expansion of the sealant and fiber materials should substantially match. The extent of mismatch between the coefficient~ of expansion of the cured sealant (plug) and the fiber materials which can be tolerated in a given assembly depends on the flexi-bilities of the different materials and on the absolute difference (~t, C) between the temperature at which the pluys are formed and the temperature furthest removed therefrom which the cell is likely to attain thereafter.
To avoid imposition of high thermal stresses, the difference between the coefficients of expansion ~x) should be such that the product ~x-~T~E is not greater than 3 kilograms per square millimeter, where E is the Youngs modulus of elastici~y (kg/mm2) for whichever material the sealant or the fibers has the lowest modulus.
For tubesheet/fiber assemblies to be used in 3Q high temperature batteries as describPd earlier herein, the maximum value of QT will usually be the difference between ordinary ambient temperatures (say 25C) and the 18,458F
_ ., .. . . ..
;
-` `` 1~9~;207 temperature (say about 400C) at which the sealant first becomes solid after being sintered.
At thig ~T (~375), assuming a modulus of 7000 kg/mm2 for the sealant, the value of ~x must be less than 1.143 x 10 6 units/C if ~x-~T-E is not to exceed 3 kg/mm2.
The general leak-plugging procedure is carried out as follows, at some point in the overall cell fab-rication sequence a~ter rigidification of the tubesheet and before removing the fiber ends protruding from it.
The assembly is positioned with respeat to a æuitably confined pool of the li~uid sealant composition, preferably by inverting the assembly and dipping the open fiber ends in the pool, in such manner that the protruding fiber ends extend, for at least part of their lengths, into the seal-ant. The distance (d) between the surface of the tube-sheet and the sealant pool should be short enough so that the capillary attraction between the sealant composition ~: and the fi~er walls will draw the sealant into the defective Cbroken or imperfect) fiber lengths to a level at least ~: 2Q beyond the face of the tubesheet nearest to the sealant pool.
That is, d must be less than h centimeters, the capillary rise, as defined by the relationship h a 4~cosQ/Dpg wherein ~ is the surface tension of the sealant (in dynes/cm), ~ is the liquid-solid wetting angle (in degrees), is the inner diameter of the fiber ~in cm), p is the fluid density of the sealant (in grams/cc) and g is the gravitational constant ~980 cm/sec ).
18,458~
: ~,c' .. ....
109~:aO7 It is apparent that h, the rise of the sealant in defective fibers of a given diameter can be increased by using a sealant composition which has a higher sur-face tension and/or a lower density. Or conversely, h may be made smaller by composing the sealant to have a lower surface tension and/or higher density. In any case, d must be small enough and h large enough to ensure that plugs will be present in the portions of the de~ective fiber lengths remaining in the assembly after the treat-ment of the present invention is finished, regardless ofwhether or not that treatment includes grinaing the tube-sheet . `, In order to ensure that the sealant will notrise too far in the closed-ended fiber lengths, the resis-tance to compression o the gases within those lengthsmust have a certain minimum value. This value can readily be calculated by those skilled in the art. For example, for fibers having an inner diameter of 50 microns, such calculations show that the total gas pressure in the closed ended lengths, expressed in millimeters of mercury should exceed 0.6y. Since most organic liquids have surface tensions between 20 and 30 dynes per centimeter, sealants comprising such solvents will usually have vapor pressures of from 12 to 18 mm Hg at ordinary ambient tem~eratures.
tToluene~ for example, has a vapor pressure of 20 mm Hg at 18C.) Thus, the total gas pressure in closed ended fibers immersed in such solvents will generally be at least 12 mm Hg.
The open fiber ends are allowed to remain in 3a the pool until the sealant has been drawn far enough into any defective fibers so that they will remain plugged 18,458F
. ~ . `
.
~.O~;Z07 after the protrudi~g open ends are severed. The assembly is then removed from contact with the sealant pool and the excess sealant adhering to the exterior surfaces of the fiber ends (and any which may adhere to the tubesheet) is washed off, as with some of the liquid medium employed in the sealant composition. The i~bibed sealant i8 solidified to non-porous, solid plugs, as by removing any volatiles and "curing" or "~etting" the non-volatile aonstituents thereof. The latter operation may be carried out by such means as sintering or by inducing chemical linking reac-tions (as by use of catalysts, simple heating or electro-magnetic irradiation).
The protruding fiber ends may be severed before the imbibed sealant is solidified but ordinarily it is preferable to effect plug formation first, for reasons which will be apparent.
The tubesheet may initially be thick enough so that the face from which the open fiber ends protrude can be ground down, to give the finished tubesheet a smooth working surface. In this event, it is not necessary to keep the sealant from moving into the closed ended fibers as far as the latter ace~ It is only necessary to keep it from advancing so far that the tubesheet whill have to be ground excessively to reopen the good fibers. (In any case, the use of the sealant in the good fibers can be controlled by manipulating the vapor pressure of the seal-ant, as discussed above.) 18,458F
-, :
,.".
In a preferred mode of operation the plugs in the defective fiber lengths are composed of the same re-lative amounts of the same ingredients as the tubesheet itself, thus assuring an even match in expansion coeffi-S cients and permitting plug formation and final tubesheet"curing" (densification) to be carried out in a single operation, such as sintering. In this mode, the sealant aonveniently (and preferably) is a solution ~or slurry) of the tubesheet material (or particles thereof) in a readily volatilized, or controllably reactive, and other-wise suitable liquid medium.
Any undissolved particles present in the sealant composikion should have maximum diameters which are 1/3 or less of the inner diameters of the fiber portions to be plugged. Otherwise, bridging of the particles may occur, thus preventing the sealant fLom flowing far enough into the defective fibers. Preferably, the particle diameter is not greater than 1/5 the fiber diameter.
In a typical application of the present method to high temperature batteries, tubesheet glass fines having maximum diameters of 10 microns or less will be ound suit-able for plugging defective fibers having an inner diameter withln the range of from 30 to 80 microns.
Although not indispensable, volatilizeable or nondetrimental suspending agents preferably are included in sealants comprising glass or ceramic particles. For example, aliphatic primary amines of from 12 to 42 carbons 18,458F
" ."
, , , , . ' - , ~.:
, .
..
llD~S2~7 have been ound particularly suitable for this purpose in preparing slurries (in aromatic solvents) of finely ground sodium borate glasses.
Tho method of the invention is most conveniently carried out in ordinary environments but may be practiced under such conditions as are feasible to establish and maintain in dry boxes ("glove boxes"), dry rooms and the like.
Practice o the invention with tubesheet/hollow fiber assemblies suitable for use in high temperature hatteries i~ illu6trated by ~but not limited to) the fol-lowing procedure.
Hollow glass fibers having an inner diameter of about 50 microns and an outer diameter of about 70 microns are prepared from a molten glass having the com-position Na2O-2B2O3 0.16NaCl 0.2 SiO2.
Fragments of a solder glass (94% B2O3, 6% Na2O) are converted to a fine powder (particle size less than 10 microns) by grinding them in the manner disclosed in U.S. Patent 3,917,490. An extrudable tubesheet composition is made hy mixing 2 parts by weight of the fines and 2 parts of -250 mesh (U.S. Std) spheres of the sam~ solder glass with about 0.4 parts of cumene.
A hollow fiber and tubesheet assembly adapted for use in a high temperature battery is assembled, essen-tially in the manner described earlier herein, from lengths of the preceding fibers, open at one end and closed at the other. The assembly includes a carbon-coated, per-forated aluminum foil strip, a spacer skirt of the same foil and a central mandrel taluminum rod). The tubesheet 18,458F
.,, . ,. . . ,i ,; .~ .: , ,. :. ;: , --is formed by extruding the proceding composition on theopen-ended portions of the fibers extending beyond the foil edge, as the assembly is rolled up, and heating the resulting disc or wall member with an infrared lamp until S (several hours) it is dry (essentially cumene-ree) and self-supporting (rigidified). The open ends o~ the fiber lengths protrude about 1 cm from the outer tupper? face of the tubesheet and the closed ends extend about 10 cm from the inner (lower) face.
A sealant slurry is prepaxed by mixing the pre-ceding solder glass powder with a 5 wt. % solution of dodecyl amine in toluene, in a ratio of 0.5 cc of the solution per gram of fines~
~he as~embly is inverted and the protruding open - 15 fiber ends immersed in the slurry of a depth of about 0.5 cm (d = 1.0-0.5 = 0.5 cm) for about 2 minutes. It is then lifted out of contact with the sealant slurry and washed by dipping the protruding fiber ends in toluene.
Heat is then applied to the assembly, with an 2Q infrared lamp, until the rate of toluene vaporization from the assembly is negligible. (This usually requires from 1 to several hours.) Next the non-volatile residium of the sealant (in the "open" fibers ends) and the tubesheet are rendered non-porous and bonded to the fibers by staged heating of the assembly. The assembly is first heated in vacuo to a temperature of up to about 385C and maintained at ~hat temperature until essentially no further densification occurs~ It is then heated to about 405, under N2 at 18,458F
'. . ' . . - -.:"`. ,. ;: ~. ~
.
10~5Z0!7 1 atmosphere of pressure for about 1.5 hour. (The distortion temperature of the fibers is about 440C).
Finally, the protruding fiber ends are cut off flush with the tubesheet face. The face may be ground smooth but this in not necessary to ensure that the un-broken fibers are unplugged in this case. That i9 ~ the sealant has risen in the defective fiber length~ about
2 cm, but has risen less than a millimeter in the closed ended length~.
lQ Optionally, the protruding densification can be carried only far enough (~y using a lower temperature and/or reduaing the residence time) so that the bond between the fibers and the solder glass will not be dis-turbed by removing the fiber ends. The fiber ends can then be removed and the final sintering carried out with the tubesheet periphery in contact with the anode and cathode cups, so that a unitary cell (sans anolyte and catholyte) is formed.
The sintering operation optionally may be car-ried out in a single heating stage (if the fiber ends arenot removed until ater sintering is complete).
EXAMPLE
The foregoing procedure (including two-stage sintering) was employed to prepare an assembly comprising a bundle of about a thousand fiber lengths, of which at least twelve had had their closed ends deliberately broken off. An o~herwise essentially identical assembly, known to contain only a few broken fibers, was pxepared without being treated according to the present in~ention. Both assem~lies were incorporated in identical cells (sans anolyte and catholyte) and tested for leaks by means of 18,458F
.
- . . , .:
. .
, 9S2~7 a leak rate detector having two glass chambers, an inlet chamber and a test chamb~r, each of about 5.0 ml volume.
The chambers are connected to each other by means of a bubbler tube immersed about 2 mm in kerosene and by a pressure equali~ing stopcock which bypasses the bubbler.
With the bypass stopcock open, the assembly to be tested is connected to the test chamber and both chambers and the test assembly are pressured to 5 pounds per square inch with nitrogen gas. The gas supply is then shut off and the bypass stopcock closed. Leaks from the asse~bly being tested lower the pressure in the test chamber and gas flows through the bubbler from the inlet chamber to maintain a balance. The gas flow rate between chambers, which is equal to the leak rate of the test assembly, is determined by counting the bubbles per unit of time.
The untreated assembly leaked at a rate of about ~`~ 0.1 cc (at standard conditions) of nitrogen per second, whereas the treated assembly exhibited a rate of less than 0.001 cc of N2 per second (due to imperfect densification of the tu~esheet itself; less than the leak rate calculable for one broken fiber).
From the foregoing detailed description, it will be understood that the present invention provides a sealant which meets the requirements for high temperature battery cells and also provides a method of sealing broken (or leaking) fibers in a tubesheet hollow fiber assemblies ~; comprising a plurality of unbroken fibers having closed ends distal from the tubesheet and open ends protruding from and adjacent to the tubesheet.
18,458F
~, ., -: . , . -., , . -, " ~ ";'~ " ' ",;- ,:
~' ;, : . "
: - .. , j '' ~, ~Lo~
The method can b~ applied to tubesheet-hollow fiber assemblies which, except for including broken or leaking fibers, is otherwise suitable to be processed for use as an electrolyte-separator in a high temperature battery.
The method may be employed to remedy leaks in tubesheet-hollow fiber a~semblies in which the hollow fibers and tubesheet are composed of glasses or ceramics.
The method salvages tubesheet-hollow fiber assemblies which include a sufficient number of broken or leaking fibers to be inoperable for their intended purpose.
The salvage method utilizes, to advantage, those portions of the open ends of the fibers protruding from the tubesheet at an intermediate stage in what is regarded as the most practical method of fabricating tubesheet -hollow fiber assemb]ies for use as electroltye-separators in high temperature batteries.
The present invention is also effective to close any cracks in the tubesheet itself (or along the area of contact between the tubesheet and one or more fiber walls) which extend clear through the tubesheet from one face to the other.
It should also be noted that the method of the invention is not limited in application to tubesheet/fiber assemblies in which the fibers are yenerally parallel to each other and generally perpendicular to the tubesheet faces.
18, 458F
- ' : ' ~ ' ,
lQ Optionally, the protruding densification can be carried only far enough (~y using a lower temperature and/or reduaing the residence time) so that the bond between the fibers and the solder glass will not be dis-turbed by removing the fiber ends. The fiber ends can then be removed and the final sintering carried out with the tubesheet periphery in contact with the anode and cathode cups, so that a unitary cell (sans anolyte and catholyte) is formed.
The sintering operation optionally may be car-ried out in a single heating stage (if the fiber ends arenot removed until ater sintering is complete).
EXAMPLE
The foregoing procedure (including two-stage sintering) was employed to prepare an assembly comprising a bundle of about a thousand fiber lengths, of which at least twelve had had their closed ends deliberately broken off. An o~herwise essentially identical assembly, known to contain only a few broken fibers, was pxepared without being treated according to the present in~ention. Both assem~lies were incorporated in identical cells (sans anolyte and catholyte) and tested for leaks by means of 18,458F
.
- . . , .:
. .
, 9S2~7 a leak rate detector having two glass chambers, an inlet chamber and a test chamb~r, each of about 5.0 ml volume.
The chambers are connected to each other by means of a bubbler tube immersed about 2 mm in kerosene and by a pressure equali~ing stopcock which bypasses the bubbler.
With the bypass stopcock open, the assembly to be tested is connected to the test chamber and both chambers and the test assembly are pressured to 5 pounds per square inch with nitrogen gas. The gas supply is then shut off and the bypass stopcock closed. Leaks from the asse~bly being tested lower the pressure in the test chamber and gas flows through the bubbler from the inlet chamber to maintain a balance. The gas flow rate between chambers, which is equal to the leak rate of the test assembly, is determined by counting the bubbles per unit of time.
The untreated assembly leaked at a rate of about ~`~ 0.1 cc (at standard conditions) of nitrogen per second, whereas the treated assembly exhibited a rate of less than 0.001 cc of N2 per second (due to imperfect densification of the tu~esheet itself; less than the leak rate calculable for one broken fiber).
From the foregoing detailed description, it will be understood that the present invention provides a sealant which meets the requirements for high temperature battery cells and also provides a method of sealing broken (or leaking) fibers in a tubesheet hollow fiber assemblies ~; comprising a plurality of unbroken fibers having closed ends distal from the tubesheet and open ends protruding from and adjacent to the tubesheet.
18,458F
~, ., -: . , . -., , . -, " ~ ";'~ " ' ",;- ,:
~' ;, : . "
: - .. , j '' ~, ~Lo~
The method can b~ applied to tubesheet-hollow fiber assemblies which, except for including broken or leaking fibers, is otherwise suitable to be processed for use as an electrolyte-separator in a high temperature battery.
The method may be employed to remedy leaks in tubesheet-hollow fiber a~semblies in which the hollow fibers and tubesheet are composed of glasses or ceramics.
The method salvages tubesheet-hollow fiber assemblies which include a sufficient number of broken or leaking fibers to be inoperable for their intended purpose.
The salvage method utilizes, to advantage, those portions of the open ends of the fibers protruding from the tubesheet at an intermediate stage in what is regarded as the most practical method of fabricating tubesheet -hollow fiber assemb]ies for use as electroltye-separators in high temperature batteries.
The present invention is also effective to close any cracks in the tubesheet itself (or along the area of contact between the tubesheet and one or more fiber walls) which extend clear through the tubesheet from one face to the other.
It should also be noted that the method of the invention is not limited in application to tubesheet/fiber assemblies in which the fibers are yenerally parallel to each other and generally perpendicular to the tubesheet faces.
18, 458F
- ' : ' ~ ' ,
Claims (11)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. The method of treating a tubesheet/hollow fiber assembly to ensure that any defective fibers included therein will be selectively plugged, said method comprising A. providing as said assembly one which comprises a bundle of hollow fiber lengths passing through and engaged with a rigid wall member or tubesheet having first and second generally parallel faces, all of said lengths having open ends pro-truding from said first face and at least a majority of said lengths having closed--ended portions extending from said second face, B. immersing said open fiber ends in a pool of a liquid sealant to a depth such that the distance between said first face and the surface of said pool external to the fiber ends is d, the force of capillary attraction between the walls of said fibers and said sealant being such that said sealant is drawn into said defective fibers for a distance greater than d, thereby filling them to a level beyond said face, the resistance to compression of the vapors within the closed ended lengths being such that said capillary attraction does not suffice to draw the sealant into said closed ended lengths beyond a point substantially below said level, C. removing the unimbibed sealant from contact with said protruding fiber ends, the imbibed sealant being so composed as to be convertible, in-situ and at a temperature below the distortion temperature of said lengths, to plugs of a solid, non-porous material sealingly bonded to the fiber walls and having a coefficient of expansion sub-stantially matching that of the fiber material D. converting the imbibed sealant to said plugs and E. severing the protruding fiber ends from said tubesheet, with the result that the defective fibers in the treated assembly are plugged and the good fibers are not plugged.
2. The method of Claim 1 wherein:
said closed ended lengths are adapted to function as the electrolyte/separator in a high temperature battery cell, said sealant is a suspension, in an inert, volatiliz-able liquid, of glass or ceramic particles which have a maximum diameter of about 1/3 or less of the inner diameter of said fiber lengths and will fuse together to form said plugs when heated to a temperature T1, which is less than the distortion temperature of said lengths, and said assembly is heated to T1, thereby devolatilizing said suspension in said defective fibers and converting said particles therein to said plugs.
18,458F
said closed ended lengths are adapted to function as the electrolyte/separator in a high temperature battery cell, said sealant is a suspension, in an inert, volatiliz-able liquid, of glass or ceramic particles which have a maximum diameter of about 1/3 or less of the inner diameter of said fiber lengths and will fuse together to form said plugs when heated to a temperature T1, which is less than the distortion temperature of said lengths, and said assembly is heated to T1, thereby devolatilizing said suspension in said defective fibers and converting said particles therein to said plugs.
18,458F
3. The method of Claim 2 wherein said tubesheet is initially porous but is rendered non-porous by said heating of said assembly to temperature T1.
4. The method of Claim 2 wherein said tubesheet is initially porous, remains porous after being heated to T1 and is rendered non-porous by further heating said assembly to a temperature T2 which is greater than T1 but is also less than said distortion temperature.
5. The method of Claim 3 wherein said tubesheet and said particles are composed of the same relative amounts of the the same ingredients.
6. The method of Claim 1 wherein said sealant exerts a vapor pressure of at least 12 mm Hg at a tempera-ture of about 20°C.
7. The method of Claim 2 wherein said fiber lengths have an inner diameter within the range of from about 30 to about 80 microns and said particles have maximum diameters of about 10 microns or less.
8. The method of Claim 2 wherein said assembly additionally comprises a perforated metallic sheet dis-posed therein as a plurality of generally concentric layers spiralled about the central axis of said bundle and separated by intervening, generally concentric layers of said closed ended fiber portions.
9. The method of Claim 8 wherein said tubesheet has essentially the same composition as said particles, is initially porous and is rendered non-porous by said heating to temperature T1.
10. The method of Claim 1 wherein the imbibed sealant is converted to said plugs before the protruding ends are severed.
11. The method of Claim 1 wherein said closed ended lengths are unlooped.
18,458F
18,458F
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US835,567 | 1977-09-22 | ||
| US05/835,567 US4170695A (en) | 1977-09-22 | 1977-09-22 | Selective plugging of broken fibers in tubesheet-hollow fiber assemblies |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1095207A true CA1095207A (en) | 1981-02-10 |
Family
ID=25269846
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA310,108A Expired CA1095207A (en) | 1977-09-22 | 1978-08-25 | Selective plugging of broken fibers in tubesheet- hollow fiber assemblies |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US4170695A (en) |
| JP (1) | JPS5461082A (en) |
| CA (1) | CA1095207A (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4226921A (en) * | 1979-07-16 | 1980-10-07 | The Dow Chemical Company | Selective plugging of broken fibers in tubesheet-hollow fiber assemblies |
| US4248648A (en) * | 1979-07-18 | 1981-02-03 | Baxter Travenol Laboratories, Inc. | Method of repairing leaks in a hollow capillary fiber diffusion device |
| US4505995A (en) * | 1981-10-19 | 1985-03-19 | The Dow Chemical Company | Plugging micro-leaks in multi-component, ceramic tubesheets with material leached therefrom |
| US5192478A (en) * | 1984-10-22 | 1993-03-09 | The Dow Chemical Company | Method of forming tubesheet for hollow fibers |
| JPS6437430A (en) * | 1987-07-24 | 1989-02-08 | Ppg Industries Inc | Hollow glass fiber |
| US5221388A (en) * | 1991-11-07 | 1993-06-22 | Hoechst Celanese Corp. | Selective sealing of defective gas separation hollow fibers |
| US5246589A (en) * | 1991-12-17 | 1993-09-21 | Wellman, Inc. | Repaired filtration elements for polymer manufacture |
| US5217659A (en) * | 1991-12-17 | 1993-06-08 | Wellman, Inc. | Repair of filtration elements for polymer manufacture |
| IL105875A (en) * | 1993-06-01 | 1998-04-05 | Aga Ab | Selective clogging of failed fibers |
| WO2014050702A1 (en) * | 2012-09-28 | 2014-04-03 | 日本碍子株式会社 | Defect detection method for monolithic separation membrane structures, repair method, and monolithic separation membrane structures |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3499062A (en) * | 1965-12-22 | 1970-03-03 | Du Pont | Method of repairing leaks in fluid separation apparatus |
| US3679480A (en) * | 1969-05-08 | 1972-07-25 | Dow Chemical Co | Electrical cell assembly |
| US3968192A (en) * | 1974-04-19 | 1976-07-06 | The Dow Chemical Company | Method of repairing leaky hollow fiber permeability separatory devices |
-
1977
- 1977-09-22 US US05/835,567 patent/US4170695A/en not_active Expired - Lifetime
-
1978
- 1978-08-25 CA CA310,108A patent/CA1095207A/en not_active Expired
- 1978-09-22 JP JP11739578A patent/JPS5461082A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5461082A (en) | 1979-05-17 |
| JPS6327962B2 (en) | 1988-06-06 |
| US4170695A (en) | 1979-10-09 |
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