WO2024097047A1 - Enhanced tensile strength low wall drag ceramic precursor paste with polyethylene glycol - Google Patents
Enhanced tensile strength low wall drag ceramic precursor paste with polyethylene glycol Download PDFInfo
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- WO2024097047A1 WO2024097047A1 PCT/US2023/035752 US2023035752W WO2024097047A1 WO 2024097047 A1 WO2024097047 A1 WO 2024097047A1 US 2023035752 W US2023035752 W US 2023035752W WO 2024097047 A1 WO2024097047 A1 WO 2024097047A1
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- batch mixture
- peo
- methylcellulose
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- molecular weight
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- 239000012700 ceramic precursor Substances 0.000 title description 4
- 239000002202 Polyethylene glycol Substances 0.000 title description 3
- 229920001223 polyethylene glycol Polymers 0.000 title description 3
- 239000000203 mixture Substances 0.000 claims abstract description 105
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims abstract description 98
- 229920000609 methyl cellulose Polymers 0.000 claims abstract description 64
- 239000001923 methylcellulose Substances 0.000 claims abstract description 64
- 239000011230 binding agent Substances 0.000 claims abstract description 38
- 239000010954 inorganic particle Substances 0.000 claims abstract description 25
- 239000000314 lubricant Substances 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 235000014113 dietary fatty acids Nutrition 0.000 claims abstract description 10
- 239000000194 fatty acid Substances 0.000 claims abstract description 10
- 229930195729 fatty acid Natural products 0.000 claims abstract description 10
- 150000004665 fatty acids Chemical class 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 claims abstract description 7
- 239000000470 constituent Substances 0.000 claims description 60
- 238000000034 method Methods 0.000 claims description 23
- 238000001125 extrusion Methods 0.000 claims description 20
- 229920013639 polyalphaolefin Polymers 0.000 claims description 7
- 150000001875 compounds Chemical class 0.000 claims description 6
- LNAZSHAWQACDHT-XIYTZBAFSA-N (2r,3r,4s,5r,6s)-4,5-dimethoxy-2-(methoxymethyl)-3-[(2s,3r,4s,5r,6r)-3,4,5-trimethoxy-6-(methoxymethyl)oxan-2-yl]oxy-6-[(2r,3r,4s,5r,6r)-4,5,6-trimethoxy-2-(methoxymethyl)oxan-3-yl]oxyoxane Chemical compound CO[C@@H]1[C@@H](OC)[C@H](OC)[C@@H](COC)O[C@H]1O[C@H]1[C@H](OC)[C@@H](OC)[C@H](O[C@H]2[C@@H]([C@@H](OC)[C@H](OC)O[C@@H]2COC)OC)O[C@@H]1COC LNAZSHAWQACDHT-XIYTZBAFSA-N 0.000 claims description 5
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims description 5
- 229920000663 Hydroxyethyl cellulose Polymers 0.000 claims description 5
- 239000004354 Hydroxyethyl cellulose Substances 0.000 claims description 5
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 claims description 5
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 claims description 5
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 claims description 5
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 claims description 5
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 claims description 5
- 235000010981 methylcellulose Nutrition 0.000 claims description 5
- 239000000919 ceramic Substances 0.000 description 19
- 239000003921 oil Substances 0.000 description 13
- 229910052878 cordierite Inorganic materials 0.000 description 9
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 9
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 238000010304 firing Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 3
- 229910010271 silicon carbide Inorganic materials 0.000 description 3
- 229920003091 Methocel™ Polymers 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 238000009864 tensile test Methods 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229920003086 cellulose ether Polymers 0.000 description 1
- 229910002106 crystalline ceramic Inorganic materials 0.000 description 1
- 239000011222 crystalline ceramic Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910021485 fumed silica Inorganic materials 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- -1 synthetic oil Chemical class 0.000 description 1
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/16—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay
- C04B35/18—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay rich in aluminium oxide
- C04B35/195—Alkaline earth aluminosilicates, e.g. cordierite or anorthite
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/515—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
- C04B35/56—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides
- C04B35/565—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides based on silicon carbide
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/632—Organic additives
- C04B35/634—Polymers
- C04B35/63448—Polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C04B35/63488—Polyethers, e.g. alkylphenol polyglycolether, polyethylene glycol [PEG], polyethylene oxide [PEO]
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/632—Organic additives
- C04B35/636—Polysaccharides or derivatives thereof
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- C04B38/0006—Honeycomb structures
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- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
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- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/32—Metal oxides, mixed metal oxides, or oxide-forming salts thereof, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
- C04B2235/3217—Aluminum oxide or oxide forming salts thereof, e.g. bauxite, alpha-alumina
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- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/34—Non-metal oxides, non-metal mixed oxides, or salts thereof that form the non-metal oxides upon heating, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
- C04B2235/349—Clays, e.g. bentonites, smectites such as montmorillonite, vermiculites or kaolines, e.g. illite, talc or sepiolite
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- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/42—Non metallic elements added as constituents or additives, e.g. sulfur, phosphor, selenium or tellurium
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- C04B2235/42—Non metallic elements added as constituents or additives, e.g. sulfur, phosphor, selenium or tellurium
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- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/60—Aspects relating to the preparation, properties or mechanical treatment of green bodies or pre-forms
- C04B2235/602—Making the green bodies or pre-forms by moulding
- C04B2235/6021—Extrusion moulding
Definitions
- the present specification relates to ceramic pastes (ceramic and/or ceramicforming pastes), methods of making such pastes, and methods of making self-standing extruded articles by extruding such pastes.
- Ceramic products in a wide range of fields from refractory tubing to automotive and diesel exhaust filters and catalytic converter substrates can be manufactured by extrusion of pastes. The cost of such products can be driven by the rate of production of quality products.
- a ceramic-forming batch mixture comprising: an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, a liquid vehicle component comprised of water, and polyethylene oxide.
- a ratio of the amounts (in wt%) of the cellulosic binder component to the polyethylene oxide is between 0.5: 1 and 1.5: 1.
- the cellulosic binder component comprises a methylcellulose constituent comprised of one or more of methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethyl cellulose, and related cellulosic compounds.
- the cellulosic binder component consists of a methylcellulose constituent.
- the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1.
- the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
- the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
- the batch mixture is in a low wall drag state.
- the PEO has a molecular weight of 1 million or more.
- the PEO has a molecular weight of 1-2 million, such as 2 million or more, such as 5 million or more, such as 7 million or more.
- the PEO has a molecular weight of 5 million or less, such as 2 million or less, such as 1 million or less.
- a method of manufacturing a ceramic-forming batch mixture comprising: adjusting a composition of a starting low wall drag ceramic-forming batch mixture (“starting batch mixture”), the mixture comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, and a liquid vehicle component comprised of water, adding PEO to the low wall drag mixture on a weight % basis with respect to the inorganic particles, and reducing either the amount of the cellulosic binder component on a weight % basis with respect to the inorganic particles.
- starting batch mixture the mixture comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, and a liquid vehicle component comprised of water, adding PEO to the low wall drag mixture on a weight % basis with respect to the inorganic particles, and reducing either the amount of the cellulo
- extrudate of the resulting batch mixture extruded through an extrusion die under extrusion conditions has a higher tensile strength than extrudate of the starting batch mixture extruded through the same extrusion die under the same extrusion conditions.
- the resulting batch mixture has a higher strain at break than the starting batch mixture under the same test conditions.
- the resulting batch mixture is in a lower wall drag state than the starting low wall drag batch mixture.
- a ratio of the amounts (in wt%) of the cellulosic binder component to the polyethylene oxide is between 0.5: 1 and 1.5: 1.
- the cellulosic binder component comprises a methylcellulose constituent comprised of one or more of methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethyl cellulose, and related cellulosic compounds.
- the cellulosic binder component consists of a methylcellulose constituent.
- the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1.
- the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
- the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
- the batch mixture is in a low wall drag state.
- the PEO has a molecular weight of 1 million or more.
- the PEO has a molecular weight of 1-2 million, such as 2 million or more, such as 5 million or more, such as 7 million or more.
- the synthetic oil comprises a polyalphaolefin.
- the PEO has a molecular weight of 5 million or less, such as 2 million or less, such as 1 million or less.
- FIG. 1 shows a cordierite-forming batch mixture, composition Ex. A, which was adjusted such that in a modified/adjusted composition of cordierite-forming batch mixture Ex. B, a portion of the methylcellulose (Methocel) was replaced by polyethylene oxide (PEO), which also enabled a reduction in the amount of lubricant in a mixture.
- PEO polyethylene oxide
- FIG. 2 graphically illustrates capillary rheometer measurements (wall shear stress Tw plotted versus Rate of extrusion, for 3 separate paste temperature conditions: 20 °C, 30 °C, and 40 °C) of paste of the modified composition of FIG. 1 Ex. B having 1% PEO by weight of inorganics vs. the unmodified starting composition Ex. A having 0% PEO, including best fit curves for each.
- FIG. 3 graphically illustrates capillary rheometer die pressure Pdie plotted versus Penetrometer reading, for compositions Ex. A and Ex. B of FIGS. 1-2.
- FIG. 4 graphically illustrates capillary rheometer wall shear stress Ty plotted versus Strain at Break (SAB), for compositions Ex. A and Ex. B of FIGS. 1-3.
- FIG. 5 graphically illustrates extrusion pressure in a twin screw extruder for compositions Ex. A and Ex. B of FIGS. 1-4.
- ceramic batch mixture comprises a mixture which comprises, among other constituents, an inorganic component comprised of either ceramic constituents (e.g. cordierite or silicon carbide) or ceramic-forming precursor constituents (e.g. oxide constituents capable of being transformed into a ceramic material such as cordierite upon firing), or both.
- the inorganic particles can comprise single-constituent particulates such as cordierite or silicon carbide, or mixtures of oxides or other compounds that are convertible to crystalline ceramic materials upon firing, such as cordierite. Ceramic products may be manufactured by employing such batch mixtures.
- a method of manufacturing a ceramic body comprises mixing an inorganic (ceramic and/or ceramic-forming) powder component such as a cordierite and/or cordierite forming component, water as the liquid vehicle, a cellulose ether binder, and a lubricant component comprised of a fatty acid constituent and an oil constituent such as a synthetic oil constituent; the method can further comprise extruding the paste through an extrusion die, such as a honeycomb extrusion die, to produce a self-standing, or self-supporting, extrudate body.
- the extrudate body, or a portion thereof can be fired to sinter and/or reactively sinter the extruded composition into a ceramic composition.
- the mixture can be thoroughly blended to form a plasticized ceramic paste, and the method can further comprise pressing or extruding the ceramic paste through an extrusion die to form a self-standing body.
- the extrusion die is a honeycomb die and the extruded self-standing body is an unfired honeycomb body that retains its extruded shape despite the presence of retained water.
- ceramic paste comprises a paste which comprises, among other constituents, a liquid vehicle component such as water, and an inorganic component comprised of either ceramic constituents (e.g. cordierite or silicon carbide) or ceramic-forming precursor constituents (e.g. oxide constituents capable of being transformed into a ceramic material such as cordierite upon firing), or both.
- a liquid vehicle component such as water
- an inorganic component comprised of either ceramic constituents (e.g. cordierite or silicon carbide) or ceramic-forming precursor constituents (e.g. oxide constituents capable of being transformed into a ceramic material such as cordierite upon firing), or both.
- the “die life” or footage of batch through an extrusion die before recoating is needed can be a significant cost factor.
- the rate at which products can be extruded is dependent on die pressure which includes contributions of the “wall drag” induced by the batch being forced through an extrusion die. Reduction of wall drag helps to achieve both higher rates of extrusion and longer die life.
- Low Wall Drag (LWD) ceramic pastes may also comprise a lubricant package, such as a lubricant package of fatty acid and an oil, such as synthetic oil, such as polyalphaolefin.
- a lubricant package such as a lubricant package of fatty acid and an oil, such as synthetic oil, such as polyalphaolefin.
- the amounts, or ratio, of fatty acid and polyalphaolefin can vary, but while such lubricant package helps to achieve a LWD state for the paste, the lubricant package can also result in a reduced tensile characteristic of the paste.
- the reduced tensile behavior occurs because the water content in the paste may need to be reduced in order to maintain stiffness (i.e.
- lubricant addition may displace water), and for aqueous based pastes that comprise a cellulosic ether binder such as methylcellulose, the reduced water content or amount in the paste reduces the hydration of the methylcellulose binder responsible for achieving acceptable tensile properties.
- aqueous based pastes that comprise a cellulosic ether binder such as methylcellulose
- low wall drag ceramic precursor batch mixtures, or ceramic pastes can be imbued with enhanced tensile strength by substituting a portion of cellulosic binder with polyethylene glycol (PEO) while still maintaining a low wall drag state of the ceramic mixture or paste.
- the methylcellulose constituent can be comprised of one or more of: methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethylcellulose, and related cellulosic compounds.
- the ratio of the amounts (in wt% with respect to the inorganic component) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1.
- the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1.
- the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
- the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
- a measure of tensile strength is strain at break (“SAB” or “SAB%) as measured by capillary rheometer tensile test.
- ceramic precursor batch mixtures, or ceramic-forming pastes or ceramic pastes comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, a liquid vehicle component comprised of water, and polyethylene oxide.
- a ratio of the amounts (in wt% with respect to the inorganic component) of the cellulosic binder component to the polyethylene oxide is between 0.5: 1 and 1.5: 1.
- the cellulosic binder component comprises a methylcellulose constituent comprised of one or more of methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethyl cellulose, and related cellulosic compounds.
- the cellulosic binder component consists of a methylcellulose constituent.
- the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1.
- the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1.
- the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1.
- the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic component.
- the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic component.
- the cellulosic binder component consists of methylcellulose.
- the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is between 0.75: 1 and 1.25: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is between 0.80: 1 and 1.20: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is between 0.90: 1 and 1.10: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is between 0.95: 1 and 1.05: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is about 1 : 1. In embodiments, the resulting batch mixture is in a lower wall drag state than the starting low wall drag batch mixture.
- the PEO constituent has a molecular weight of 1 million or more. In embodiments, the PEO constituent has a molecular weight of 1-2 million. In embodiments, the PEO constituent has a molecular weight of 2 million or more. In embodiments, the PEO constituent has a molecular weight of 5 million or more. In embodiments, the PEO constituent has a molecular weight of 7 million or more.
- the PEO constituent has a molecular weight of 5 million or less. In embodiments, the PEO constituent has a molecular weight of 4 million or less. In embodiments, the PEO constituent has a molecular weight of 3 million or less. In embodiments, the PEO constituent has a molecular weight of 2 million or less. In embodiments, the PEO constituent has a molecular weight of 1-2 million. In embodiments, the PEO constituent has a molecular weight of 1-3 million. In embodiments, the PEO constituent has a molecular weight of 1-4 million.
- the oil constituent comprises a synthetic oil.
- the synthetic oil comprises a polyalphaolefin.
- the inorganic particles are comprised of cordierite precursors.
- the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
- methods disclosed herein comprise adjusting a paste composition of a starting low wall drag ceramic and/or ceramic-forming paste or batch mixture (“starting batch mixture”), the mixture comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, and a liquid vehicle component comprised of water, the method comprising adding PEO, or increasing the amount of PEO, to the low wall drag mixture on a weight % basis with respect to the inorganic particles, and reducing the amount of the cellulosic binder component on a weight % basis with respect to the inorganic particles, such that the resulting batch mixture is in a low wall drag state.
- starting batch mixture the mixture comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, and a liquid vehicle component comprised of water
- the method comprising adding PEO, or increasing
- FIG. 1 shows a batch mixture composition adjustment such that in a modified/adjusted composition, PEO replaced a portion of the methylcellulose (Methocel), which enable a reduction in the amount of lubricant in a cordierite-forming mixture.
- PEO methylcellulose
- FIG. 2 graphically illustrates capillary rheometer measurements (wall shear stress Tw plotted versus Rate of extrusion, for 3 separate paste temperature conditions: 20 °C, 30 °C, and 40 °C) of paste of the modified composition of FIG. 1 having 1% PEO by weight of inorganics vs. the unmodified starting composition having 0% PEO (and starting or standard lubricant package), including best fit curves for each.
- FIG. 2 shows similar wall drag vs velocity of the unmodified paste with standard lubricant versus the modified composition of FIG. 1 having 1% PEO.
- FIG. 3 graphically illustrates capillary rheometer measurements (die pressure Pdie plotted versus Penetrometer reading, for the modified composition of FIG. 1 having 1% PEO by weight of inorganics vs. the unmodified starting composition having 0% PEO (and starting or standard lubricant package), including best fit curves for each.
- the 1% PEO composition of FIG. 1 exhibits lower die pressure at stiffness compared to the 0% PEO composition.
- FIG. 4 graphically illustrates capillary rheometer measurements (wall shear stress Ty plotted versus Strain at Break (SAB) for the modified composition of FIG. 1 having 1% PEO by weight of inorganics vs. the unmodified starting composition having 0% PEO (and starting or standard lubricant package), that is FIG. 4 shows stiffness vs Strain at Break (SAB%) from tensile test, wherein the 1% PEO composition of FIG. 1 exhibits significant SAB improvement over the paste composition without PEO (0% PEO).
- SAB stiffness vs Strain at Break
- FIG. 5 graphically illustrates extrusion pressure in a twin screw extruder comparing the 0% PEO paste and the 1% PEO paste of FIG. 1, where both compositions exhibited similar pressure stability.
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Abstract
An enhanced tensile strength low wall drag ceramic-forming batch mixture of an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, a liquid vehicle component comprised of water, and polyethylene oxide. A method of manufacturing a ceramic-forming batch mixture wherein a composition of a starting low wall drag ceramic-forming batch mixture is adjusted by substituting a portion of its methylcellulose type binder with polyethylene oxide, and optionally reducing the amount of lubricant in the mixture while the resulting batch mixture is also in a low wall drag state, and has improved tensile property.
Description
ENHANCED TENSILE STRENGTH LOW WALL DRAG CERAMIC PRECURSOR PASTE WITH POLYETHYLENE GLYCOL
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application claims the benefit of priority under 35 U.S.C. §119 of U.S. Provisional Application Serial No. 63/420905 filed on October 31, 2022, the content of which is relied upon and incorporated herein by reference in its entirety.
BACKGROUND
Field
[0002] The present specification relates to ceramic pastes (ceramic and/or ceramicforming pastes), methods of making such pastes, and methods of making self-standing extruded articles by extruding such pastes.
Technical Background
[0003] Ceramic products in a wide range of fields from refractory tubing to automotive and diesel exhaust filters and catalytic converter substrates can be manufactured by extrusion of pastes. The cost of such products can be driven by the rate of production of quality products.
SUMMARY
[0004] Aspects of the disclosure pertain to porous filter bodies and methods for their manufacture and use.
[0005] In one aspect, a ceramic-forming batch mixture is disclosed herein comprising: an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, a liquid vehicle component comprised of water, and polyethylene oxide.
[0006] In embodiments, a ratio of the amounts (in wt%) of the cellulosic binder component to the polyethylene oxide is between 0.5: 1 and 1.5: 1.
[0007] In embodiments, the cellulosic binder component comprises a methylcellulose constituent comprised of one or more of methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethyl cellulose, and related cellulosic compounds.
[0008] In embodiments, the cellulosic binder component consists of a methylcellulose constituent.
[0009] In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1.
[0010] In embodiments, the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
[0011] In embodiments, the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
[0012] In embodiments, the batch mixture is in a low wall drag state.
[0013] In embodiments, the PEO has a molecular weight of 1 million or more.
[0014] In embodiments, the PEO has a molecular weight of 1-2 million, such as 2 million or more, such as 5 million or more, such as 7 million or more.
[0015] In embodiments, the synthetic oil comprises a polyalphaolefin.
[0016] In embodiments, the PEO has a molecular weight of 5 million or less, such as 2 million or less, such as 1 million or less.
[0017] In another aspect, a method of manufacturing a ceramic-forming batch mixture is disclosed herein, the method comprising: adjusting a composition of a starting low wall drag ceramic-forming batch mixture (“starting batch mixture”), the mixture comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, and a liquid vehicle component comprised of water, adding PEO to the low wall drag mixture on a weight % basis with respect to the inorganic particles, and reducing either the amount of the cellulosic binder component on a weight % basis with respect to the inorganic particles.
[0018] In embodiments, extrudate of the resulting batch mixture extruded through an extrusion die under extrusion conditions has a higher tensile strength than extrudate of the starting batch mixture extruded through the same extrusion die under the same extrusion conditions. In embodiments, the resulting batch mixture has a higher strain at break than the starting batch mixture under the same test conditions. In embodiments, the resulting batch mixture is in a lower wall drag state than the starting low wall drag batch mixture.
[0019] In embodiments, a ratio of the amounts (in wt%) of the cellulosic binder component to the polyethylene oxide is between 0.5: 1 and 1.5: 1.
[0020] In embodiments, the cellulosic binder component comprises a methylcellulose constituent comprised of one or more of methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethyl cellulose, and related cellulosic compounds.
[0021] In embodiments, the cellulosic binder component consists of a methylcellulose constituent.
[0022] In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1, or the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1.
[0023] In embodiments, the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
[0024] In embodiments, the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
[0025] In embodiments, the batch mixture is in a low wall drag state.
[0026] In embodiments, the PEO has a molecular weight of 1 million or more.
[0027] In embodiments, the PEO has a molecular weight of 1-2 million, such as 2 million or more, such as 5 million or more, such as 7 million or more.
[0028] In embodiments, the synthetic oil comprises a polyalphaolefin.
[0029] In embodiments, the PEO has a molecular weight of 5 million or less, such as 2 million or less, such as 1 million or less.
[0030] Additional features and advantages will be set forth in the detailed description, which follows, and in part will be readily apparent to those skilled in the art from that description or recognized by practicing the embodiments described herein, comprising the detailed description, which follows, the claims, as well as the appended drawings.
[0031] It is to be understood that both the foregoing general description and the following detailed description describe various embodiments and are intended to provide an overview or framework for understanding the nature and character of the claimed subject matter. The accompanying drawings are included to provide a further understanding of the various embodiments, and are incorporated into and constitute a part of this specification. The drawings illustrate the various embodiments described herein, and together with the description serve to explain the principles and operations of the claimed subject matter.
BRIEF DESCRIPTION OF THE DRAWINGS
[0032] FIG. 1 shows a cordierite-forming batch mixture, composition Ex. A, which was adjusted such that in a modified/adjusted composition of cordierite-forming batch mixture Ex. B, a portion of the methylcellulose (Methocel) was replaced by polyethylene oxide (PEO), which also enabled a reduction in the amount of lubricant in a mixture.
[0033] FIG. 2 graphically illustrates capillary rheometer measurements (wall shear stress Tw plotted versus Rate of extrusion, for 3 separate paste temperature conditions: 20 °C, 30 °C, and 40 °C) of paste of the modified composition of FIG. 1 Ex. B having 1% PEO by
weight of inorganics vs. the unmodified starting composition Ex. A having 0% PEO, including best fit curves for each.
[0034] FIG. 3 graphically illustrates capillary rheometer die pressure Pdie plotted versus Penetrometer reading, for compositions Ex. A and Ex. B of FIGS. 1-2.
[0035] FIG. 4 graphically illustrates capillary rheometer wall shear stress Ty plotted versus Strain at Break (SAB), for compositions Ex. A and Ex. B of FIGS. 1-3.
[0036] FIG. 5 graphically illustrates extrusion pressure in a twin screw extruder for compositions Ex. A and Ex. B of FIGS. 1-4.
DETAILED DESCRIPTION
[0037] Reference will now be made in detail to embodiments of articles for emissions treatment, for example, filtration articles, comprising a plugged honeycomb filter body comprising inorganic deposits disposed on walls defining inlet channels of the plugged honeycomb filter body, the inorganic deposits comprising fumed silica particles, embodiments of which are illustrated in the accompanying drawings. Whenever possible, the same reference numerals will be used throughout the drawings to refer to the same or like parts.
[0038] As used herein, “ceramic batch mixture” comprises a mixture which comprises, among other constituents, an inorganic component comprised of either ceramic constituents (e.g. cordierite or silicon carbide) or ceramic-forming precursor constituents (e.g. oxide constituents capable of being transformed into a ceramic material such as cordierite upon firing), or both. The inorganic particles can comprise single-constituent particulates such as cordierite or silicon carbide, or mixtures of oxides or other compounds that are convertible to crystalline ceramic materials upon firing, such as cordierite. Ceramic products may be manufactured by employing such batch mixtures. For example, a method of manufacturing a ceramic body comprises mixing an inorganic (ceramic and/or ceramic-forming) powder component such as a cordierite and/or cordierite forming component, water as the liquid vehicle, a cellulose ether binder, and a lubricant component comprised of a fatty acid constituent and an oil constituent such as a synthetic oil constituent; the method can further comprise extruding the paste through an extrusion die, such as a honeycomb extrusion die, to produce a self-standing, or self-supporting, extrudate body. The extrudate body, or a portion
thereof, can be fired to sinter and/or reactively sinter the extruded composition into a ceramic composition. In embodiments, the mixture can be thoroughly blended to form a plasticized ceramic paste, and the method can further comprise pressing or extruding the ceramic paste through an extrusion die to form a self-standing body. In embodiments, the extrusion die is a honeycomb die and the extruded self-standing body is an unfired honeycomb body that retains its extruded shape despite the presence of retained water.
[0039] As used herein, “ceramic paste” comprises a paste which comprises, among other constituents, a liquid vehicle component such as water, and an inorganic component comprised of either ceramic constituents (e.g. cordierite or silicon carbide) or ceramic-forming precursor constituents (e.g. oxide constituents capable of being transformed into a ceramic material such as cordierite upon firing), or both.
[0040] In addition to production rate of extruded ceramic products, the “die life” or footage of batch through an extrusion die before recoating is needed can be a significant cost factor. The rate at which products can be extruded is dependent on die pressure which includes contributions of the “wall drag” induced by the batch being forced through an extrusion die. Reduction of wall drag helps to achieve both higher rates of extrusion and longer die life.
[0041] Low Wall Drag (LWD) ceramic pastes may also comprise a lubricant package, such as a lubricant package of fatty acid and an oil, such as synthetic oil, such as polyalphaolefin. Depending on inorganic component and binder (such as cellulosic ether binder) amounts, the amounts, or ratio, of fatty acid and polyalphaolefin can vary, but while such lubricant package helps to achieve a LWD state for the paste, the lubricant package can also result in a reduced tensile characteristic of the paste. The reduced tensile behavior occurs because the water content in the paste may need to be reduced in order to maintain stiffness (i.e. lubricant addition may displace water), and for aqueous based pastes that comprise a cellulosic ether binder such as methylcellulose, the reduced water content or amount in the paste reduces the hydration of the methylcellulose binder responsible for achieving acceptable tensile properties.
[0042] We have found that low wall drag ceramic precursor batch mixtures, or ceramic pastes, can be imbued with enhanced tensile strength by substituting a portion of cellulosic binder with polyethylene glycol (PEO) while still maintaining a low wall drag state of the
ceramic mixture or paste. The methylcellulose constituent can be comprised of one or more of: methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethylcellulose, and related cellulosic compounds. Surprisingly we have found that the introduction of PEO brings a paste in an already low wall drag (LWD) state to even an even lower low wall drag state while increasing the tensile properties of the batch.
[0043] We have found that such substitution is particularly effective when the cellulosic binder comprises a methylcellulose constituent. In embodiments, the ratio of the amounts (in wt% with respect to the inorganic component) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1. In embodiments, the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles. In embodiments, the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
[0044] A measure of tensile strength is strain at break (“SAB” or “SAB%) as measured by capillary rheometer tensile test.
[0045] In one aspect, ceramic precursor batch mixtures, or ceramic-forming pastes or ceramic pastes, are disclosed herein, comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, a liquid vehicle component comprised of water, and polyethylene oxide. In embodiments, a ratio of the amounts (in wt% with respect to the inorganic component) of the cellulosic binder component to the polyethylene oxide is between 0.5: 1 and 1.5: 1. In embodiments, the cellulosic binder component comprises a methylcellulose constituent comprised of one or more of methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethyl cellulose, and related cellulosic compounds.
[0046] In embodiments, the cellulosic binder component consists of a methylcellulose constituent. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1. In embodiments, the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic component. In embodiments, the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic component.
[0047] In embodiments, the cellulosic binder component consists of methylcellulose. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is between 0.75: 1 and 1.25: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is between 0.80: 1 and 1.20: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is between 0.90: 1 and 1.10: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is between 0.95: 1 and 1.05: 1. In embodiments, the ratio of the amounts (in wt%) of the methylcellulose to the polyethylene oxide is about 1 : 1. In embodiments, the resulting batch mixture is in a lower wall drag state than the starting low wall drag batch mixture.
[0048] In embodiments, the PEO constituent has a molecular weight of 1 million or more. In embodiments, the PEO constituent has a molecular weight of 1-2 million. In embodiments, the PEO constituent has a molecular weight of 2 million or more. In embodiments, the PEO constituent has a molecular weight of 5 million or more. In embodiments, the PEO constituent has a molecular weight of 7 million or more.
[0049] In embodiments, the PEO constituent has a molecular weight of 5 million or less. In embodiments, the PEO constituent has a molecular weight of 4 million or less. In
embodiments, the PEO constituent has a molecular weight of 3 million or less. In embodiments, the PEO constituent has a molecular weight of 2 million or less. In embodiments, the PEO constituent has a molecular weight of 1-2 million. In embodiments, the PEO constituent has a molecular weight of 1-3 million. In embodiments, the PEO constituent has a molecular weight of 1-4 million.
[0050] In embodiments, the oil constituent comprises a synthetic oil. In embodiments, the synthetic oil comprises a polyalphaolefin.
[0051] In embodiments, the inorganic particles are comprised of cordierite precursors. [0052] In embodiments, the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
[0053] In another aspect, methods disclosed herein comprise adjusting a paste composition of a starting low wall drag ceramic and/or ceramic-forming paste or batch mixture (“starting batch mixture”), the mixture comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, and a liquid vehicle component comprised of water, the method comprising adding PEO, or increasing the amount of PEO, to the low wall drag mixture on a weight % basis with respect to the inorganic particles, and reducing the amount of the cellulosic binder component on a weight % basis with respect to the inorganic particles, such that the resulting batch mixture is in a low wall drag state.
EXAMPLES
[0054] Embodiments will be further understood by the following non-limiting examples.
[0055] FIG. 1 shows a batch mixture composition adjustment such that in a modified/adjusted composition, PEO replaced a portion of the methylcellulose (Methocel), which enable a reduction in the amount of lubricant in a cordierite-forming mixture.
[0056] FIG. 2 graphically illustrates capillary rheometer measurements (wall shear stress Tw plotted versus Rate of extrusion, for 3 separate paste temperature conditions: 20 °C, 30 °C, and 40 °C) of paste of the modified composition of FIG. 1 having 1% PEO by weight of inorganics vs. the unmodified starting composition having 0% PEO (and starting or standard
lubricant package), including best fit curves for each. FIG. 2 shows similar wall drag vs velocity of the unmodified paste with standard lubricant versus the modified composition of FIG. 1 having 1% PEO.
[0057] FIG. 3 graphically illustrates capillary rheometer measurements (die pressure Pdie plotted versus Penetrometer reading, for the modified composition of FIG. 1 having 1% PEO by weight of inorganics vs. the unmodified starting composition having 0% PEO (and starting or standard lubricant package), including best fit curves for each. The 1% PEO composition of FIG. 1 exhibits lower die pressure at stiffness compared to the 0% PEO composition.
[0058] FIG. 4 graphically illustrates capillary rheometer measurements (wall shear stress Ty plotted versus Strain at Break (SAB) for the modified composition of FIG. 1 having 1% PEO by weight of inorganics vs. the unmodified starting composition having 0% PEO (and starting or standard lubricant package), that is FIG. 4 shows stiffness vs Strain at Break (SAB%) from tensile test, wherein the 1% PEO composition of FIG. 1 exhibits significant SAB improvement over the paste composition without PEO (0% PEO).
[0059] FIG. 5 graphically illustrates extrusion pressure in a twin screw extruder comparing the 0% PEO paste and the 1% PEO paste of FIG. 1, where both compositions exhibited similar pressure stability.
[0060] It will be apparent to those skilled in the art that various modifications and variations can be made to the embodiments described herein without departing from the spirit and scope of the claimed subject matter. Thus, it is intended that the specification cover the modifications and variations of the various embodiments described herein provided such modification and variations come within the scope of the appended claims and their equivalents.
Claims
1. A ceramic-forming batch mixture comprising: an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, a liquid vehicle component comprised of water, and polyethylene oxide, wherein a ratio of the amounts (in wt%) of the cellulosic binder component to the polyethylene oxide is between 0.5: 1 and 1.5: 1.
2. The batch mixture of claim 1 wherein the cellulosic binder component comprises a methylcellulose constituent comprised of one or more of methylcellulose, hydroxypropyl methylcellulose, hydroxyethyl cellulose, carboxylmethyl cellulose, and related cellulosic compounds.
3. The batch mixture of claim 1 wherein the cellulosic binder component consists of a methylcellulose constituent.
4. The batch mixture of claim 3 wherein the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.75: 1 and 1.25: 1.
5. The batch mixture of claim 3 wherein the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.80: 1 and 1.20: 1.
6. The batch mixture of claim 3 wherein the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.90: 1 and 1.10: 1.
7. The batch mixture of claim 3 wherein the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is between 0.95: 1 and 1.05: 1.
8. The batch mixture of claim 3 wherein the ratio of the amounts (in wt%) of the methylcellulose constituent to the polyethylene oxide is about 1 : 1.
9. The batch mixture of claim 1 wherein the batch mixture comprises methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
10. The batch mixture of claim 1 wherein the cellulosic binder component is methylcellulose in an amount greater than 3.0 wt% and less than 5.40 wt% with respect to the inorganic particles.
11. The batch mixture of claim 1 wherein the batch mixture is in a low wall drag state.
12. The batch mixture of claims 1-11 wherein the PEO has a molecular weight of 1 million or more.
13. The batch mixture of claims 1-11 wherein the PEO has a molecular weight of 1-2 million.
14. The batch mixture of claims 1-11 wherein the PEO has a molecular weight of 2 million or more.
15. The batch mixture of claims 1-11 wherein the PEO has a molecular weight of 5 million or more.
16. The batch mixture of claims 1-11 wherein the PEO has a molecular weight of 7 million or more.
17. The batch mixture of claims 1-11 wherein the synthetic oil comprises a polyalphaolefin.
18. The batch mixture of claims 1-11 wherein the PEO has a molecular weight of 5 million or less.
19. The batch mixture of claims 1-11 wherein the PEO has a molecular weight of 2 million or less.
20. The batch mixture of claims 1-11 wherein the PEO has a molecular weight of 1 million or less.
21. A method of manufacturing a ceramic-forming batch mixture, the method comprising: adjusting a composition of a starting low wall drag ceramic-forming batch mixture (“starting batch mixture”), the mixture comprising an inorganic component comprised of inorganic particles, a cellulosic binder component, a lubricant component comprised of fatty acid and/or synthetic oil, and a liquid vehicle component comprised of water, adding PEO to the low wall drag mixture on a weight % basis with respect to the inorganic particles, and reducing either the amount of the cellulosic binder component on a weight % basis with respect to the inorganic particles, or the amount of the lubricant component on a weight % basis with respect to the inorganic particles, or both, such that the resulting batch mixture is in a low wall drag state.
22. The method of claim 21 wherein extrudate of the resulting batch mixture extruded through an extrusion die under extrusion conditions has a higher tensile strength than extrudate of the starting batch mixture extruded through the same extrusion die under the same extrusion conditions.
23. The method of claim 21 wherein the resulting batch mixture has a higher strain at break than the starting batch mixture under the same test conditions.
24. The method of claim 21 wherein the resulting batch mixture is in a lower wall drag state than the starting low wall drag batch mixture.
25. The method of claim 21 wherein the cellulosic binder component comprises methylcellulose.
26. The method of claim 21 wherein the cellulosic binder component consists of methylcellulose.
27. The method of claims 22-26 wherein the PEO has a molecular weight of 1 million or more.
28. The method of claims 22-26 wherein the PEO has a molecular weight of 1-2 million.
29. The method of claims 22-26 wherein the PEO has a molecular weight of 2 million or more.
30. The method of claims 22-26 wherein the PEO has a molecular weight of 5 million or more.
31. The method of claims 22-26 wherein the PEO has a molecular weight of 7 million or more.
32. The method of claims 22-26 wherein the synthetic oil comprises a polyalphaolefin.
33. The method of claims 22-26 wherein the PEO has a molecular weight of 5 million or less.
34. The method of claims 22-26 wherein the PEO has a molecular weight of 2 million or less.
35. The method of claims 22-26 wherein the PEO has a molecular weight of 1 million or less.
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US20190169072A1 (en) * | 2015-03-30 | 2019-06-06 | Corning Incorporated | Ceramic batch mixtures having decreased wall drag |
US20200361825A1 (en) * | 2017-08-11 | 2020-11-19 | Corning Incorporated | Green ceramic batch mixtures comprising an inverse emulsion and methods for forming a ceramic body |
CN112206766A (en) * | 2020-10-23 | 2021-01-12 | 湖北群有长物环保科技有限公司 | Honeycomb SCR denitration catalyst with high temperature of 550 ℃ and preparation method thereof |
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