Patent application number | Description | Published |
20080220205 | HONEYCOMB STRUCTURE AND HONEYCOMB CATALYST - A honeycomb structure | 09-11-2008 |
20080229931 | HONEYCOMB STRUCTURE BODY AND METHOD FOR PRODUCING THE SAME - There is provided a honeycomb structure capable of suitably be used for a filter for trapping particulate matter, such as a diesel particulate filter (DPF) and capable of detecting an accumulation amount of particulate matter easily with high accuracy when the honeycomb structure is used for a filter for trapping particulate matter. The honeycomb structure 1 has a plurality of cells functioning as gas passages and partitioned and formed by the porous partition walls and has two or more electrodes therein. | 09-25-2008 |
20080264010 | HONEYCOMB FILTER SYSTEM - A honeycomb filter system comprising a first honeycomb filter disposed upstream: first filter having partition wall matrix of a mean pore diameter of 25 μm or more and below 70 μm and a porosity of 40% or more and below 70%, and carrying an oxidation catalyst containing at least one material selected from the group consisting of platinum (Pt), palladium, ceria, and alumina in at least a part of inner surfaces of pores of the matrix; and a second honeycomb filter disposed downstream; having a surface layer of a peak pore diameter of 0.3 μm or more and below 20 μm which is equivalent to or smaller than that of its matrix, and a porosity of 60% or more and below 95% which is higher than that of the matrix; and having the other specified relations. | 10-30-2008 |
20080292513 | CATALYST CARRIER - Disclosed is a catalyst carrier which is used for carrying a catalyst thereon. The catalyst carrier is characterized in that the apparent specific heat measured at 800° C. is 1.8 times or more greater than that measured at room temperature, wherein the apparent specific heat means a charge heat amount required for substantially increasing the temperature of a unit mass (kg) by 1 K, inclusive of the influence of endotherm or exotherm caused by change in crystalline form, partial melting, coagulation, phase transformation, vitrification, amorphous-formation, crystallization and the like. | 11-27-2008 |
20080295469 | HONEYCOMB FILTER - A honeycomb filter | 12-04-2008 |
20090047188 | HONEYCOMB CATALYST STRUCTURE - There is provided a honeycomb catalyst body | 02-19-2009 |
20090176053 | HONEYCOMB STRUCTURE, HONEYCOMB CATALYTIC BODY AND MANUFACTURING METHOD OF THE SAME - There are disclosed a honeycomb structure capable of providing a honeycomb catalytic body which is excellent in purification efficiency with a small pressure loss and which can be mounted even in a limited space, a honeycomb catalytic body which is excellent in purification efficiency with a small pressure loss and which can be mounted even in a limited space, and a manufacturing method of the same. A honeycomb catalytic body | 07-09-2009 |
20090196800 | Plasma reaction vessel, and method of producing the same - In the plasma reaction vessel ( | 08-06-2009 |
20090282817 | PLASMA PROCESSING APPARATUS - A plasma processing apparatus includes a main body that has an inlet for a purification target gas and an outlet for a purified gas, an insulator honeycomb that includes a plurality of cells that are partitioned by a partition wall and serve as gas passages, a conductor honeycomb that is disposed to be able to transmit heat to the insulator honeycomb, a discharge electrode that is disposed opposite to the conductor honeycomb and forms a pair of electrodes with the conductor honeycomb, and a pulse power supply that applies a pulse voltage between the pair of electrodes, the insulator honeycomb, the conductor honeycomb, and the discharge electrode being disposed in an inner space of the main body. The plasma processing apparatus generates plasma by applying a pulse voltage to promote purification of the purification target gas in the insulator honeycomb by utilizing heat generated by plasma. | 11-19-2009 |
20090309571 | PARTICULATE MATTER SENSOR - A particulate matter sensor ( | 12-17-2009 |
20100135866 | HONEYCOMB FILTER - A honeycomb filter including partition walls having a porous partition wall base material and a surface layer provided on only inflow side or both inflow and outflow sides of the partition wall base material, and satisfying the following conditions capable of using as a DPF. The surface layer has a peak pore diameter of from 0.3 μm to 20 μm (exclusive) being equal to or smaller than the average pore diameter of the base material; the porosity of from 60% to 95% (exclusive) when measured by mercury porosimetry being larger than that of the base material; and the thickness L | 06-03-2010 |
20100184589 | HONEYCOMB CATALYTIC ARTICLE - There is provided a honeycomb structure where a catalyst is loaded on surfaces of inner pores of the surface layer and on a surface of the surface layer; a relation between a catalyst area proportion A of the catalyst to a gap area proportion B of a gap in a cross-section of the surface layer on the inlet side is 1% | 07-22-2010 |
20110201493 | HONEYCOMB CATALYST BODY - There is provided a honeycomb catalyst body including, a honeycomb substrate, plugging portions, and a three way catalyst. All the cells are open in the inflow side end face, the honeycomb substrate has two regions of an inflow side region and an outflow side region, the inflow side region of the honeycomb substrate is a region from the inflow side end face to a position of 10 to 90% of a length in an central axial direction of the honeycomb substrate from the inflow side end face, and 100 to 400 g/L of the three way catalyst is loaded on the partition walls in the inflow side region, no catalyst is loaded on the partition walls in the outflow side region, and a ratio of the length to a diameter of the inflow side end face of the honeycomb substrate is 1.1 to 2.0. | 08-18-2011 |
20110203242 | HONEYCOMB STRUCTURE - A honeycomb structure wherein the thickness of each partition wall is 50.8 μm inclusive to 161.5 μm exclusive, the cell density is 15.5 to 62.0 cells/cm | 08-25-2011 |
20110212831 | SUBSTRATE WITH SURFACE-COLLECTION-LAYER AND CATALYST-CARRYING SUBSTRATE WITH SURFACE-COLLECTION-LAYER - A substrate with a surface-collection-layer comprising a honeycomb substrate having a porous partition wall that defines and forms cells, and a plurality of plugging portions, a surface-collection-layer being formed on a surface of the partition wall that forms the remaining cells, the thickness of the surface-collection-layer on the outlet-side open end being larger than the thickness of the surface-collection-layer in a center area of the substrate, the partition wall having predetermined thickness, porosity and pore size, the surface-collection-layer having predetermined thickness, porosity, and average pore size, and the substrate having predetermined cell density. | 09-01-2011 |
20110224069 | HONEYCOMB CATALYST BODY - There is provided a honeycomb catalyst body comprising a honeycomb base body having porous partition walls forming a plurality of divided cells which extend from one end face of honeycomb base body to its other end face and which function as a fluid passage, and an outer wall present at the outermost peripheral portion of honeycomb base body, plugged portions provided so as to plug part of the plurality of divided cells, and a catalyst loaded on the partition walls of honeycomb base body. The plurality of divided cells include outermost peripheral cells formed by the partition walls and the outer wall, and of the outermost peripheral cells, those cells whose hydraulic diameter ratio to the hydraulic diameters of the cells other than the outermost peripheral cells is 5 to 75%, are through-cells having no plugged portion. | 09-15-2011 |
20120009092 | HONEYCOMB FILTER AND METHOD FOR PRODUCING HONEYCOMB FILTER - There is provided a honeycomb filter wherein particles having an average particle diameter smaller that of the particles constituting partition walls are deposited at least in open pores formed by the particles constituting the partition walls and/or gaps between the particles in a surface layer portion of the partition walls on the exhaust gas inflow side, thereby forming a composite region. The average pore diameter of the partition walls is 5 to 40 μm, and the porosity of the partition wall is 35 to 75%. The particles to be deposited have an average particle diameter of 1 to 15 μm, and the height of the composite region is not more than 80 μm in the direction from the outermost contour line of the partition walls to the surface of the partition walls. | 01-12-2012 |
20120009093 | HONEYCOMB FILTER AND METHOD FOR PRODUCING HONEYCOMB FILTER - There is provided a honeycomb filter wherein particles having an average particle diameter smaller than the average pore diameter of partition walls are deposited at least in open pores formed in the surface layer of the partition wall and in the pores of the partition wall in a surface layer portion of the partition walls on the exhaust gas inflow side, thereby forming a composite region. The average pore diameter of the partition walls is 5 to 40 μm, and the porosity of the partition wall is 35 to 75%. The particles to be deposited have an average particle diameter of 1 to 15 μm, and the height of the composite region is not more than 80 μm in the direction from the outermost contour line of the partition walls to the surface of the partition walls. | 01-12-2012 |
20120058019 | HONEYCOMB FILTER - A honeycomb filter includes a cell having one open end and another closed end that serves as a fluid flow path and a cell having one closed end and another open end, wherein the cells are alternately disposed. The honeycomb filter includes an undeposited region in an upstream region of a partition portion, which has no trapping layer and has a length of 5% or more and 30% or less of the length of the inlet cell. The upstream region of the partition portion includes an undeposited region having an area of 10% or more of that of the cell in a cross-section perpendicular to the exhaust gas flow direction. The undeposited region with no trapping layer in the upstream region decreases the permeation resistance of the partition portion in the upstream region and facilitates fluid passage through the partition portion in the upstream region. | 03-08-2012 |
20120064286 | HONEYCOMB STRUCTURAL BODY - A honeycomb structural body includes porous partition walls arranged to form a plurality of cells which become through channels of a fluid, porosities of the partition walls are from 45 to 70%, a pore diameter distribution of the partition walls is measured by mercury porosimetry, the pore diameter distribution indicates a bimodal distribution, in the bimodal distribution, a pore diameter at the maximum peak value of a small pore side distribution is from 1 to 10 μm, and a pore diameter at the maximum peak value of a large pore side distribution exceeds 10 μm, and a ratio between a pore volume of the small pores and a pore volume of the large pores is in a range of 1:7 to 1:1 in the honeycomb structural body. | 03-15-2012 |
20120070346 | HONEYCOMB FILTER - A honeycomb filter includes a partition portion having a thickness t | 03-22-2012 |
20120251398 | HONEYCOMB FILTER - A honeycomb filter | 10-04-2012 |
20120317945 | EXHAUST GAS PURIFICATION FILTER - An exhaust gas purification filter | 12-20-2012 |
20120317946 | EXHAUST GAS PURIFICATION FILTER - An exhaust gas purification filter | 12-20-2012 |
20130029088 | HONEYCOMB CATALYST CARRIER - There is provided a honeycomb catalyst carrier provided with porous partition walls containing cordierite or aluminum titanate as a main component and separating and forming a plurality of cells functioning as fluid passages. The partition walls have a porosity of 0.5% or more and 10% or less. The honeycomb catalyst carrier can be warmed up fast, and the temperature of the catalyst loaded on the honeycomb catalyst carrier can be raised faster. | 01-31-2013 |
20130058839 | WALL FLOW TYPE EXHAUST GAS PURIFICATION FILTER - There is provided a wall flow type exhaust gas purification filter is provided with a honeycomb structure having porous ceramic partition walls | 03-07-2013 |
20130059724 | HONEYCOMB STRUCTURE AND HONEYCOMB CATALYST BODY - Partition walls are provided with small pores and large pores, a porosity of the partition walls is from 50 to 70%, a porosity of the large pores of the partition walls is 30% or larger, a ratio of a total volume of the small pores to a total volume of the large pores is 20% or larger, and in a graph showing a pore diameter distribution of the partition walls, the pore diameter at a maximum peak value of the large pores is from 20 to 200 μm, and the pore diameter at a maximum peak value of the small pores is from 0.1 to 8 μm. Furthermore, a value obtained by dividing a porosity value (%) of the large pores by a thickness value (μm) of the partition walls is 0.2 or larger in a honeycomb structure. | 03-07-2013 |
20130236687 | HONEYCOMB STRUCTURE AND HONEYCOMB CATALYST - There is disclosed a honeycomb structure usable as a support of a honeycomb catalyst onto which a large amount of catalyst can be loaded and which has a good purification efficiency, and the honeycomb structure includes porous partition walls | 09-12-2013 |
20130243999 | HONEYCOMB STRUCTURE, HONEYCOMB CATALYST BODY USING THE SAME, AND MANUFACTURING METHOD OF HONEYCOMB STRUCTURE - A honeycomb structure including porous partition walls, a porosity of the partition walls is from 45 to 70%, and when pores having the maximum width in excess of 10 μm in a cross section of each of the partition walls are large pores and the partition wall is equally divided into three regions of a center region and surface layer regions present on both sides of the center region, a total area of cross sections of the large pores which appear in the surface layer regions is from 60 to 100% of a total area of cross sections of all the pores which appear in the surface layer regions, and a total area of cross sections of the large pores which appear in the center region is from 0 to 40% of the total area of cross sections of all the pores which appear in the center region. | 09-19-2013 |
20140093436 | HONEYCOMB FILTER - A honeycomb filter | 04-03-2014 |
20140116016 | HONEYCOMB FILTER - A honeycomb filter includes a honeycomb structure and plugged portions. Partition walls of the honeycomb structure are made of a partition wall material including a plurality of aggregates containing silicon carbide or silicon nitride as a main component, and a binding material at a content of 15 to 35 mass %. The binding material is made of a material in which mullite particles as reinforcing particles may be dispersed in cordierite. A thermal expansion coefficient of the partition walls at 40 to 800° C. is 4.2×10 | 05-01-2014 |
20140165519 | FINE PARTICLE COLLECTING FILTER - A fine particle collecting filter includes a honeycomb structure in which a plurality of honeycomb segments are integrally joined by a joining material, and has a constitution where an exhaust gas allowed to flow from an inlet end surface into cells passes partition walls, and then flows out from an outlet end surface to the outsides of the cells. The partition walls are made of a material containing SiC as a main component, at least one of an average open diameter of pores of an inlet side of the exhaust gas passing the partition wall and an average open diameter of the pores of an outlet side of the exhaust gas passing is from 0.1 to 5 μm, an average pore diameter of the whole partition wall is from 10 to 30 μm, and a thermal conductivity of the partition walls at room temperature is from 80 to 110 W/mK. | 06-19-2014 |
20140165520 | FINE PARTICLE COLLECTING FILTER - A fine particle collecting filter includes a honeycomb structure in which a plurality of honeycomb segments are integrally joined by a joining material, and has a constitution where an exhaust gas allowed to flow from an inlet end surface into cells passes partition walls, and then flows out from an outlet end surface to the outsides of the cells. In the partition walls, SiC which is an aggregate is bound by Si which is a binding agent, at least one of an average open diameter of the pores of an inlet side of the exhaust gas passing the partition wall and an average open diameter of the pores of an outlet side is from 0.1 to 5 μm, an average pore diameter of the whole partition wall is from 10 to 30 μm, and a thermal conductivity of the partition walls at room temperature is from 50 to 80 W/mK. | 06-19-2014 |
20140298779 | WALL FLOW TYPE EXHAUST GAS PURIFICATION FILTER - A wall flow type exhaust gas purification filter includes a honeycomb structure body and plugging portions. Four inlet opening cells having a substantially hexagonal shape in cross section surround one outlet opening cell having a substantially square shape in cross section, where one side of an inlet opening cell and one side of the outlet opening cell have a substantially same length and are substantially parallel and adjacent to each other. Distance a between the partition wall defining a first side of the outlet opening cell and the partition wall defining an opposed second side is in a range of exceeding 0.8 mm and less than 2.4 mm, and distance b between the partition wall defining a third side of the inlet opening cell and the partition wall defining an opposed fourth side has a ratio to the distance a in a range exceeding 0.4 and less than 1.1. | 10-09-2014 |