WO2009108356A1 - Method for sealing cells in extruded monoliths and devices resulting - Google Patents
Method for sealing cells in extruded monoliths and devices resulting Download PDFInfo
- Publication number
- WO2009108356A1 WO2009108356A1 PCT/US2009/001266 US2009001266W WO2009108356A1 WO 2009108356 A1 WO2009108356 A1 WO 2009108356A1 US 2009001266 W US2009001266 W US 2009001266W WO 2009108356 A1 WO2009108356 A1 WO 2009108356A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- monolith
- plug
- cells
- cell
- mask
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B38/00—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
- C04B38/0006—Honeycomb structures
- C04B38/0012—Honeycomb structures characterised by the material used for sealing or plugging (some of) the channels of the honeycombs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2418—Honeycomb filters
- B01D46/2451—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
- B01D46/2459—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure of the plugs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0001—Making filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2418—Honeycomb filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2418—Honeycomb filters
- B01D46/2451—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
- B01D46/2476—Monolithic structures
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/248—Reactors comprising multiple separated flow channels
- B01J19/2485—Monolithic reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28B—SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28B11/00—Apparatus or processes for treating or working the shaped or preshaped articles
- B28B11/003—Apparatus or processes for treating or working the shaped or preshaped articles the shaping of preshaped articles, e.g. by bending
- B28B11/006—Making hollow articles or partly closed articles
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/009—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone characterised by the material treated
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/45—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
- C04B41/50—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials
- C04B41/5022—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials with vitreous materials
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/80—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone of only ceramics
- C04B41/81—Coating or impregnation
- C04B41/85—Coating or impregnation with inorganic materials
- C04B41/86—Glazes; Cold glazes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00034—Physico-chemical characteristics of the mixtures
- C04B2111/00068—Mortar or concrete mixtures with an unusual water/cement ratio
Definitions
- a method for sealing selected cells in an extruded monolith at an end face of the monolith includes providing an extruded monolith having a plurality of cells extending along a common direction and one or more end faces at which one or more of the cells are open, the open cells including some to be sealed and some to remain open.
- the method also includes filling the open end of at least one of the cells to be sealed with a plug comprising a glass frit, such that an exterior portion the plug extends beyond the end of the cell, and such that the exterior portion of the plug also extends beyond the width of the cell, then heating the extruded monolith together with the plug sufficiently to cause the glass frit to consolidate and flow sufficiently to seal the respective cell.
- Figure 1 is a perspective view of an extruded monolith 20 having a path 30 formed therein in part by plugs or continuous plugging material 40 at one or more end faces 70 thereof.
- Figure 2 is a cross section of a portion of a monolith 20 like that of Figure 1 , showing an arrangement of plugs or plug material 40.
- Figure 3 is a cross section of a portion of a monolith 20 like that of Figure 1, showing another arrangement of plugs or plug material 40.
- Figures 4A-4D are plan views of an extruded monolith 20 having a path formed therein in part by plugs or continuous plugging material 40 at one or more end faces 70 thereof, with varying arrangements of plugging material 40.
- Figure 5 is perspective view of an extruded monOlith 20 showing side access to the path 30 corresponding to Figure 4B.
- Figure 6A and 6B show a cross section of an individual plug 40 or row of plug material 40 being formed according to the methods of the present invention.
- Figures 7A-7C are cross sections like those of Figures 6A-6B illustrating plug formation as presently understood according to the methods of the present invention.
- Figures 8A-8B are cross sections like those of figures 6A-6B showing a plug 40 being formed according to another embodiment of the methods of the present invention.
- Figures 9A-9D are cross sections like those of figures 6A-6B showing a plug 40 being formed according to yet another embodiment of the methods of the present invention.
- Figure 10 is a digital photograph of a cross section of a plug 40 formed according to the methods of the present invention.
- reactant fluids flow in a path 30 comprised millimeter-scale channels formed along the cells of and extruded monolith 20, as shown generally in Figure 1.
- the path is desirably formed by shortening selected walls at the face 70 of the extruded monolith 20, selectively plugging with individual or essentially continuous plug material 40 to form a typically serpentine path 30.
- FIGS 2 and 3 Examples of two plugging schemes in a plane along the path 30 are shown in Figures 2 and 3.
- a generally serpentine 30 may be formed, lying in a direction mainly along the lengths of the cells of the monolith 20, with lateral connections between cells only near the end faces of the monolith.
- the path 30 may follow more than one cell at a time in parallel, as shown in Figure 3.
- the path 30, generally following the pattern of the plugs or continuous plugging material 40 in the plan views of Figures 4A-4D is desirably doubly serpentine, as in Figure 4B.
- the path may be parallel with internal manifolding, as in Figure 4C, or parallel with external manifolding, if any, as in Figure 4D.
- internal manifolding as in Figure 4C
- external manifolding if any, as in Figure 4D.
- width of the path in the plane perpendicular to the direction of the cells is generally only one cell wide, as in each of Figures 4A-4D.
- the path shown in Figure 4B allows long fluid channels to be formed, useful for reactants requiring significant dwell time, while heat exchange fluids flow parallel to the extrusion direction through many millimeter-scale heat exchange channels adjacent to the reactant fluid channels.
- side access can be provided the path or paths 30 through one or more holes 50 formed in a side, preferably a flat side or flattened side face 60 of the extruded monolith 20.
- the side is flat, or flattened by removing the outer walls down to a flat wall formerly within the extruded monolith, a wider variety of fluid porting options may be available, including, for example the use of O-rings against the flat 60.
- Various processes and compositions may be used for forming the plugs 40 or continuous plug material 40 to plug the cells of the monoliths 20. What is desirable is a robust and simple process to provide plugs that are leak-free at pressures up to 55 bar or even higher, and are chemically resistant to a wide range of acids, bases and solvents. The present invention provides such a process, an embodiment of which may be described with reference to Figure 6.
- the method further includes filling the open end of one or more of the cells to be sealed with a plug 40 comprising a glass frit, typically with an organic binder, such that an exterior portion 42 of the plug extends beyond the end of the cell, and such that the exterior portion 42 of the plug also extends beyond the width W of the cell, as shown in Figure 6A for one cell of a monolith 20.
- the monolith and the plug are then heated together sufficiently to cause the glass frit to consolidate and flow sufficiently to seal the respective cell, as shown in Figure 6B, which shows a representative plug profile after heating.
- a plug 40 comprising a glass frit
- an exterior portion 42 of the plug extends beyond the end of the cell
- the exterior portion 42 of the plug also extends beyond the outward surface of the walls of the cell, as shown in Figure 8A for one cell of a monolith 20, where the position of the outward surface of the walls of the cell is shown by the dotted lines extending upward therefrom.
- the depth of the unheated plug may also be adjusted as desired, with deeper plugs, such as the one in Figure 8, typically providing a more robust seal, at the expense of somewhat reduced internal volume.
- FIG. 9A shows a cross-section view of a monolith 20 at an end face thereof where all cells but the one in the middle are covered by a thick mask 80, such as a tape mask.
- the thick mask 80 may be 1-2 mm thick, and may be formed by one or two layers of a thick pressure sensitive tape material or a flexible molded mask material such as silicone, for example.
- the edges of the mask 80 are positioned so that they do not completely cover the tops of monolith walls on either side of the end channel to be plugged.
- the plug material is then applied to the monolith end face so that it flows between the two parts of the mask 80 and into the ends of the cells of monolith 20, as shown in Figure 9B.
- the plug material can be a paste at room temperature that is spread over the mask with a spatula so that excess plug material is removed.
- the plug material can be suspended in a wax binder, and a layer of plug material may be spread over a hot plate so that it forms a uniform thin layer (1-2 mm thick), and then the monolith end face with the thick mask 80 may be is pushed into the thin layer of melted plug material.
- the hot plate may then be cooled or allowed to cool, so that the plug material solidifies and adheres to the monolith and mask.
- the thick mask 80 is then removed from the monolith end face, leaving the glass-based plug material with an exterior portion 42 of the plug 40 extending beyond the end of the cell, that is, beyond the monolith end face, as shown in Figure 9C.
- the exterior portion 42 of the plug 40 extends beyond the width W of the cell to be plugged so that it contacts at least a portion of the tops of the monolith walls that are adjacent to the cell.
- the monolith is heated to bond the glass-based plug material to the monolith and form a leak-free seal as represented by the plug of Figure 9D.
- the plug material polymer binder is burned off, as described above with respect to Figure 7. This results in a partial shrinkage of the plug material. It is important that the plug material remains in contact or close proximity to the monolith walls during this and any subsequent plug shrinkage as the sintering cycle continues. This contact or proximity is required so that when the plug material is heated to an elevated temperature so that it flows, it is close enough to wet all four adjacent monolith walls, or at least all of the adjacent walls that remain after any previous machining or other process to selectively remove walls.
- This wall wetting prevents the formation of gaps and provides a robust seal.
- Surface tension effects can also work to coax plug materials into closer contact with the monolith walls. For example, the initially square corners on the plug material are rounded during sintering, resulting in limited transport of plug material downward to locations near the plug-wall interface.
- Alumina extruded monoliths were selected for study because of their strength, inertness, and reasonably good thermal conductivity.
- a glass composition was developed and selected for use because of its excellent CTE match to alumina and its very good chemical resistance. The glass composition is given in Table 1 below: Table 1
- the glass composition was joined with a wax-based binder (MX4462) (17% by weight), by to form the final plug composition.
- a mask was applied to the end face of an alumina monolith with machined end walls.
- the tape mask was positioned so that two long channel regions were not masked by the tape.
- the plug material was heated on a hot plate at 125 0 C so that it melted and spread into a thin layer 1-2 mm thick.
- the alumina monolith end face was then applied onto the molten plug material so that the plug material flowed through the gaps in the mask and into the ends of the cells of the monolith. After the plug material and the alumina monolith cooled, the mask was removed.
- FIG. 10 is a cross-sectional view of a sintered plug 40 showing a good bond with the cell sidewalls of an alumina monolith 20.
- the process described herein and the resulting selectively plugged extruded monolith structures may form a fluid processing device or a portion of such a device potentially useful for a wide range of fluid processes and chemical reactions, such as any process that involves mixing, separation, extraction, crystallization, precipitation, or otherwise processing fluids or mixtures of fluids, including multiphase mixtures of fluids — and including fluids or mixtures of fluids including multiphase mixtures of fluids that also contain solids.
- the processing may include a physical process, a chemical reaction defined as a process that results in the interconversion of organic, inorganic, or both organic and inorganic species, a biochemical process, or any other form of processing.
- reactions may be performed with the disclosed methods and/or devices: oxidation; reduction; substitution; elimination; addition; ligand exchange; metal exchange; and ion exchange. More specifically, reactions of any of the following non-limiting list may be performed with the disclosed methods and/or devices: polymerisation; alkylation; dealkylation; nitration; peroxidation; sulfoxidation; epoxidation; ammoxidation; hydrogenation; dehydrogenation; organometallic reactions; precious metal chemistry/ homogeneous catalyst reactions; carbonylation; thiocarbonylation; alkoxylation; halogenation; dehydrohalogenation; dehalogenation; hydroformylation; carboxylation; decarboxylation; amination; arylation; peptide coupling; aldol condensation; cyclocondensation; dehydrocyclization; esterification; amidation; heterocyclic synthesis; dehydration; alcoholysis; hydrolysis; ammonolysis; etherification; enzy
- the rounded upper surfaces of the plugs formed by the disclosed process are particularly pressure resistant to pressure on the rounded side.
- high fluid pressure may be applied at an end face of a selectively plugged monolith plugged as disclosed herein, allowing for high flow into the channels unplugged at that face.
- the thickness of the mask 80 or by other suitable means the portion of an unsintered plug extending beyond the monolith end face may be adjusted to optimize the after-sintering profile of the rounded upper surface for maximum pressure resistance.
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2010548735A JP2011514856A (en) | 2008-02-29 | 2009-02-27 | Method and apparatus for sealing cells in an extruded monolith |
EP09715836A EP2262749A1 (en) | 2008-02-29 | 2009-02-27 | Method for sealing cells in extruded monoliths and devices resulting |
CN200980112471.9A CN102036935B (en) | 2008-02-29 | 2009-02-27 | Method for sealing cells in extruded monoliths and devices resulting |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US6775208P | 2008-02-29 | 2008-02-29 | |
US61/067,752 | 2008-02-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2009108356A1 true WO2009108356A1 (en) | 2009-09-03 |
Family
ID=40636924
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2009/001266 WO2009108356A1 (en) | 2008-02-29 | 2009-02-27 | Method for sealing cells in extruded monoliths and devices resulting |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP2262749A1 (en) |
JP (1) | JP2011514856A (en) |
KR (1) | KR20100129309A (en) |
CN (1) | CN102036935B (en) |
TW (1) | TW200948748A (en) |
WO (1) | WO2009108356A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010099449A2 (en) | 2009-02-28 | 2010-09-02 | Corning Incorporated | Honeycomb body reactor optimized channel sizing |
CN102917783A (en) * | 2010-05-31 | 2013-02-06 | 康宁股份有限公司 | Honeycomb body reactor interface anchoring |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015157730A (en) * | 2014-02-24 | 2015-09-03 | 日本碍子株式会社 | honeycomb structure |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060272306A1 (en) * | 2005-06-01 | 2006-12-07 | Kirk Brian S | Ceramic wall flow filter manufacture |
WO2008121390A1 (en) * | 2007-03-31 | 2008-10-09 | Corning Incorporated | Extruded body devices and methods for fluid processing |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4411856A (en) * | 1981-07-15 | 1983-10-25 | Corning Glass Works | Method and apparatus for high speed manifolding of honeycomb structures |
US6673300B2 (en) * | 2002-02-28 | 2004-01-06 | Corning Incorporated | Method for plugging selected cells in a honeycomb |
JP4927405B2 (en) * | 2005-03-23 | 2012-05-09 | 日本碍子株式会社 | Method for manufacturing plugged honeycomb structure |
-
2009
- 2009-02-27 JP JP2010548735A patent/JP2011514856A/en not_active Withdrawn
- 2009-02-27 TW TW098106605A patent/TW200948748A/en unknown
- 2009-02-27 KR KR1020107021634A patent/KR20100129309A/en not_active Application Discontinuation
- 2009-02-27 EP EP09715836A patent/EP2262749A1/en not_active Withdrawn
- 2009-02-27 WO PCT/US2009/001266 patent/WO2009108356A1/en active Application Filing
- 2009-02-27 CN CN200980112471.9A patent/CN102036935B/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060272306A1 (en) * | 2005-06-01 | 2006-12-07 | Kirk Brian S | Ceramic wall flow filter manufacture |
WO2008121390A1 (en) * | 2007-03-31 | 2008-10-09 | Corning Incorporated | Extruded body devices and methods for fluid processing |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010099449A2 (en) | 2009-02-28 | 2010-09-02 | Corning Incorporated | Honeycomb body reactor optimized channel sizing |
CN102917783A (en) * | 2010-05-31 | 2013-02-06 | 康宁股份有限公司 | Honeycomb body reactor interface anchoring |
Also Published As
Publication number | Publication date |
---|---|
KR20100129309A (en) | 2010-12-08 |
CN102036935A (en) | 2011-04-27 |
EP2262749A1 (en) | 2010-12-22 |
CN102036935B (en) | 2013-07-31 |
TW200948748A (en) | 2009-12-01 |
JP2011514856A (en) | 2011-05-12 |
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