Abstract: According to embodiments, a batch mixture includes inorganic components, a non-polar carbon chain lubricant, and an organic surfactant having a polar head. The non-polar carbon chain lubricant and the organic surfactant are present in concentrations satisfying the relationship: B(C1(d+d0)+C2(f+f0))=SC, where: d0+d is an amount of non-polar carbon chain lubricant in percent by weight of the inorganic components, by super addition; f0+f is an amount of organic surfactant in percent by weight of the inorganic components, by super addition; B is a scaling factor; C1 is a scaling factor of the concentration of the non-polar carbon chain lubricant; and C2 is a scaling factor of the concentration of the organic surfactant. Embodiments provide that 3.6?SC?14.

Abstract: According to embodiments, a batch mixture includes inorganic components, a non-polar carbon chain lubricant, and an organic surfactant having a polar head. The non-polar carbon chain lubricant and the organic surfactant are present in concentrations satisfying the relationship: B(C1(d+d0)+C2(f+f0))=SC, where: d0+d is an amount of non-polar carbon chain lubricant in percent by weight of the inorganic components, by super addition; f0+f is an amount of organic surfactant in percent by weight of the inorganic components, by super addition; B is a scaling factor; C1 is a scaling factor of the concentration of the non-polar carbon chain lubricant; and C2 is a scaling factor of the concentration of the organic surfactant. Embodiments provide that 3.6?SC?14.

Abstract: According to embodiments, a batch mixture includes inorganic components, a non-polar carbon chain lubricant, and an organic surfactant having a polar head. The non-polar carbon chain lubricant and the organic surfactant are present in concentrations satisfying the relationship: B(C1(d+d0)+C2(f+f0))=SC, where: d0+d is an amount of non-polar carbon chain lubricant in percent by weight of the inorganic components, by super addition; f0+f is an amount of organic surfactant in percent by weight of the inorganic components, by super addition; B is a scaling factor; C1 is a scaling factor of the concentration of the non-polar carbon chain lubricant; and C2 is a scaling factor of the concentration of the organic surfactant. Embodiments provide that 3.6?SC?14.

Abstract: A ceramic particulate filter having a porous catalytic material deposited on walls within the filter. Particulate matter is trapped in the walls of the filter and the catalytic material removes gases, such as nitrogen oxides (NOx), from gases passing through the filter. The filter, in one embodiment, is adaptable for use with internal combustion (gas and diesel) engines. A method of making the filter is also described.

Abstract: This disclosure is directed to porous ceramic processing; and in particular to a method using selected pore forming materials to avoid high exotherms during the ceramic firing process, and the green bodies formed using the selected pore forming materials. The selected pore forming materials are homogeneous wax/non-ionic surfactant particles formed by a prilling process in which the wax is melted and the non-ionic surfactant is mixed into the wax prior to prilling. The disclosure is useful in the manufacture porous ceramic honeycomb bodies including ceramic honeycomb filter traps.

Abstract: A microreaction device or system (4) includes at least one thermal control fluidic passage (C,E) and a principal working fluidic passage (A) with average cross-sectional area in the range of 0.25 to 100 mm2, and having a primary entrance (92) and multiple secondary entrances (94) with the spacing between secondary entrances (94) having a length along the passage (A) of at least two times the root of the average cross-sectional area of the passage (A). The device or system (4) also includes at least one secondary working fluidic passage (B) having an entrance (102) and multiple exits (106) including a final exit (106), each exit (106) being in fluid communication with a corresponding one of the multiple secondary entrances (94) of the principal fluidic passage (A).

Abstract: A wall-flow honeycomb filter comprising a ceramic monolith having a plurality of porous walls formed therein. The plurality of porous walls define a plurality of inlet cells and a plurality of outlet cells extending between an inlet end face and an outlet end face of the monolith. The inlet cells are open at the inlet end face and plugged at or near the outlet end face. The outlet cells are open at the outlet end face and plugged at or near the inlet end face. The monolith has a ratio of a combined cross-sectional area of the inlet cells to a combined cross-sectional area of the outlet cells greater than 1. The monolith has at least one inlet cell cluster which contains an N×M group of inlet cells, N and M being integers greater than 1, each inlet cell cluster consisting of a plurality of inlet cells separated by inlet cluster walls.

Abstract: This disclosure is directed to porous ceramic processing; and in particular to a method using selected pore forming materials to avoid high exotherms during the ceramic firing process, and the green bodies formed using the selected pore forming materials. The selected pore forming materials are homogeneous wax/non-ionic surfactant particles formed by a prilling process in which the wax is melted and the non-ionic surfactant is mixed into the wax prior to prilling. The disclosure is useful in the manufacture porous ceramic honeycomb bodies including ceramic honeycomb filter traps.

Abstract: A ceramic particulate filter having a porous catalytic material deposited on walls within the filter. Particulate matter is trapped in the walls of the filter and the catalytic material removes gases, such as nitrogen oxides (NOx), from gases passing through the filter. The filter, in one embodiment, is adaptable for use with internal combustion (gas and diesel) engines. A method of making the filter is also described.

Abstract: Disclosed are washcoated ceramic honeycomb filters. The ceramic filters exhibit a relatively high level of washcoat loading while exhibiting minimized levels of backpressure. Also disclosed are methods for manufacturing the washcoated ceramic honeycomb filters. The method comprises providing an cell geometry derived from a predetermined level of washcoat loading to be applied to the ceramic honeycomb article.

Abstract: Methods of contacting two or more immiscible liquids comprising providing a unitary thermally-tempered microstructured fluidic device [10] comprising a reactant passage [26] therein with characteristic cross-sectional diameter [11] in the 0.2 to 15 millimeter range, having, in order along a length thereof, two or more inlets [A, B or A, B1] for entry of reactants, an initial mixer passage portion [38] characterized by having a form or structure that induces a degree of mixing in fluids passing therethrough, an initial dwell time passage portion [40] characterized by having a volume of at least 0.

Abstract: A wall-flow honeycomb filter comprising a ceramic monolith having a plurality of porous walls formed therein. The plurality of porous walls define a plurality of inlet cells and a plurality of outlet cells extending between an inlet end face and an outlet end face of the monolith. The inlet cells are open at the inlet end face and plugged at or near the outlet end face. The outlet cells are open at the outlet end face and plugged at or near the inlet end face. The monolith has a ratio of a combined cross-sectional area of the inlet cells to a combined cross-sectional area of the outlet cells greater than 1. The monolith has at least one inlet cell cluster which contains an N×M group of inlet cells, N and M being integers greater than 1, each inlet cell cluster consisting of a plurality of inlet cells separated by inlet cluster walls.

Abstract: Disclosed are washcoated ceramic honeycomb filters. The ceramic filters exhibit a relatively high level of washcoat loading while exhibiting minimized levels of backpressure. Also disclosed are methods for manufacturing the washcoated ceramic honeycomb filters. The method comprises providing an cell geometry derived from a predetermined level of washcoat loading to be applied to the ceramic honeycomb article.

Abstract: A microreaction device or system (4) includes at least one thermal control fluidic passage (C,E) and a principal working fluidic passage (A) with average cross-sectional area in the range of 0.25 to 100 mm2, and having a primary entrance (92) and multiple secondary entrances (94) with the spacing between secondary entrances (94) having a length along the passage (A) of at least two times the root of the average cross-sectional area of the passage (A). The device or system (4) also includes at least one secondary working fluidic passage (B) having an entrance (102) and multiple exits (106) including a final exit (106), each exit (106) being in fluid communication with a corresponding one of the multiple secondary entrances (94) of the principal fluidic passage (A).

Abstract: Methods and apparatus for treating a gas-liquid feed stream with structured monolithic catalysts of honeycomb configuration wherein the catalysts are configured as a stack of honeycomb sections with offset channels, the resulting channel dislocations between adjacent contacting honeycombs in the stack introducing controlled, limited turbulence and mixing of feed stream portions traversing the channels to significantly increase the catalytic efficiency of the reactor.

Abstract: A chemical processing apparatus is disclosed. The apparatus includes a pressure vessel and a microreactor disposed within the pressure vessel. The pressure vessel is constructed and arranged to maintain the pressure vessel and the microreactor at elevated pressure when a chemical operation is performed within the apparatus. A method of operating a microreactor at high pressure is also disclosed.

Abstract: Methods and apparatus for treating a gas-liquid feed stream with structured monolithic catalysts of honeycomb configuration wherein the catalysts are configured as a stack of honeycomb sections with offset channels, the resulting channel dislocations between adjacent contacting honeycombs in the stack introducing controlled, limited turbulence and mixing of feed stream portions traversing the channels to significantly increase the catalytic efficiency of the reactor.