Honeycomb filter and method of making it

• US 4,417,908 A
• Filed: 02/22/1982
• Issued: 11/29/1983
• Est. Priority Date: 02/22/1982
• Status: Expired due to Term

• Current Assignee: Corning Glass Works Inc. (Corning Incorporated)
• Original Assignee: Corning Glass Works Inc. (Corning Incorporated)
• Inventors: Pitcher, Wayne H. Jr.
• Primary Examiner(s): LACEY, DAVID LYNN
• Application Number:
  US06/350,995
• Time in Patent Office: 645 Days
• Field of Search: 55/484, 55/502, 55/523, 55/DIG. 5, 55/DIG. 30, 210/510, 422/171, 422/180, 252/477 R, 428/116-118, 501/112, 501/119, 501/80, 60/295, 60/299, 60/311, 29/163.5 F, 165/8
• US Class Current: 55/523
• CPC Class Codes: B01D 46/0001 Making filtering elements
• CPC Class Codes: B01D 46/0039 with flow guiding by feed or discharge devices
• CPC Class Codes: B01D 46/2429 of the honeycomb walls or cells
• CPC Class Codes: B01D 46/24491 Porosity
• CPC Class Codes: B01D 46/24492 Pore diameter
• CPC Class Codes: B01D 46/247 of the cells
• CPC Class Codes: B01D 46/2484 Cell density, area or aspect ratio
• CPC Class Codes: B01D 46/2488 Triangular
• CPC Class Codes: B01D 46/249 Quadrangular e.g. square or diamond
• CPC Class Codes: B01D 46/2498 The honeycomb filter being defined by mathematical relationships
• CPC Class Codes: F01N 2330/06 Ceramic, e.g. monoliths
• CPC Class Codes: F01N 2350/02 Fitting ceramic monoliths in a metallic housing
• CPC Class Codes: F01N 3/0222 the structure being monolithic, e.g. honeycombs
• CPC Class Codes: Y02T 10/12 Improving ICE efficiencies
• CPC Class Codes: Y10S 55/05 Methods of making filter
• CPC Class Codes: Y10S 55/30 Exhaust treatment
• CPC Class Codes: Y10T 29/49604 Filter
• CPC Class Codes: Y10T 428/24149 Honeycomb-like

Abstract

The filter of honeycomb construction has a matrix of thin, interconnected walls which define a multiplicity of cells and which have interconnected open porosity of a volume and size sufficient to enable the fluid to flow completely across the thin walls in their narrow dimensions between adjoining cells and through the thin walls in their longer dimensions between adjoining or neighboring cells and to restrict the particulates in the fluid from flowing either completely across or through any of the thin walls, and has the cells divided into an inlet group and an outlet group and providing the inlet group of cells with substantially greater desirably about 25% or more greater, collective thin wall surface area than is provided to the outlet group of cells. Portions of the inlet group cells adjoin one another and share in common the same thin wall. Method of fabricating the filter comprises providing the matrix, and closing oen end of each of the inlet and outlet group cells, the closed ends of the inlet group cells being at an end face of the matrix opposite to the other end face thereof at which occur the closed ends of the outlet group cells, to provide the inlet group of cells with the aforesaid substantially greater collective thin wall surface area.

Claims

1. A filter for removing all or substantially all of the solid particulates in fluids passed through the filter comprising:

a multiplicity of interconnected thin porous walls defining inlet end faces and outlet end faces of the filter and a multiplicity of cells, each cell extending through the filter from at least one of the inlet and outlet end faces and having a surface area defined by surfaces of the thin walls exposed within the cell,

the thin walls containing interconnected open porosity of a volume and size sufficient to enable the fluid to flow across the narrow dimension of the thin walls between adjoining cells and through the longer dimensions of the thin walls between adjoining or neighboring cells and to restrain at least a significant portion of the solid particulates from passing either across or through any of the thin walls,

an outlet group of cells, each cell of the outlet group being open at a said outlet face and closed where adjoining any said inlet end face,

an inlet group of cells, each cell of the inlet group being open at a said inlet end face and closed where adjoining any said outlet end face, and

the collective thin wall surface area of the inlet group of cells being significantly greater than the collective thin wall surface area of the outlet group of cells.

2. The filter of claim 1 having a single inlet end face and a single outlet end face on opposing sides of the filter and said plurality of cells extends longitudinally through the filter between the inlet and outlet end faces.

3. The filter of claim 1 wherein said collective thin wall surface area of the inlet group of cells is at least about 25% greater than said collective thin wall surface area of the outlet group of cells.

4. The filter of claim 3 wherein said collective thin wall surface area of the inlet group of cells is between about 2 and 4 times greater than said collective thin wall surface area of the outlet group of cells.

5. The filter of claim 1 wherein each of substantially all cells of the inlet group shares two or more of its defining thin walls in common with other adjoining cells of the inlet group.

6. The filter of claim 5 wherein each of substantially all cells of the inlet group shares at least 75% of its defining thin walls in common with other adjoining cells of the inlet group.

7. The filter of claim 1 or 5 wherein substantially all of said plurality of cells have substantially square, transverse cross-sectional geometries.

8. The filter of claim 1 wherein the number of inlet cells is also substantially greater than the number of outlet cells.

9. The filter of claim 1 wherein the number of cells in the inlet group and the outlet group are substantially equal and the average individual, transverse cross-sectional areas of the inlet cells is greater than the average individual, transverse cross-sectional areas of the outlet cells.

10. The filter of claim 1 wherein the open porosity of the thin walls is at least about 25% or more by volume.

11. The filter of claim 10 wherein said open porosity is formed by pores having mean diameters of about 1 micron or more.

12. The filter of claim 11 wherein the open porosity of the thin walls is at least about 35% or more by volume.

13. The filter of claim 12 wherein the open porosity of the thin walls is also less than about 70% by volume.

14. In a diesel engine exhaust conduit, including the filter of claim 13 positioned in said conduit so as to remove carbonaceous solid particulate from diesel engine exhaust gas and wherein said pores have mean diameters of between about 10 and 50 microns.

15. The filter of claim 1 wherein said thin walls are formed from a ceramic-based material.

19. The filter of claim 1 wherein each of substantially all cells of the inlet group shares at least 33% of its defining thin walls in common with other adjoining cells of the inlet group.

16. In the method of fabricating a filter for removing solid particulates from fluid streams comprising the steps of providing a honeycomb structure formed from a matrix of thin, intersecting porous walls which define a pair of open end faces and a multiplicity of hollow cells extending in a substantially mutually parallel fashion, closing a first group of cells near their end portions at one end face and the remaining cells near their end portion at the remaining end face, the interconnected open porosity of the thin walls being of volume and size sufficient to enable fluid flowing into the first group of cells to flow completely across the narrow dimensions of the thin walls into adjoining cells of the second group and through the thin walls in their longer dimension to adjoining or neighboring cells of the second group and preventing at least a significant portion of the solid particulates from passing completely across or through the walls in any of their dimensions, the improvement comprising the step of:

further closing said cells to provide substantially greater collective thin wall surface area to the inlet group of cells than the collective thin wall surface area provided by the outlet group of cells.

17. A compact through flow exhaust particulate filter element for diesel engines, said element comprising a ceramic monolith having a plurality of interlaced, thin gas filtering porous internal walls defining a plurality of parallel passages extending to opposite ends of the element, said passages including a first group comprising inlet passages open at one end of the element and closed at the other end and a second group comprising outlet passages closed to said one end of the element and open at the other end, the plurality of interlaced thin porous internal walls having internal interconnected open porosity of a volume and size sufficient to enable the fluid to flow across said walls in their narrow dimensions and through said walls in their longer dimensions and to restrain at least a significant portion of the particulates from passing either completely across or through any of the walls in any of their dimensions, and the improvement comprising:

the inlet passages having collective surface areas substantially greater than the respective collective surface areas of the outlet passages, and

portions of said inlet passages adjoining one another and sharing in common said interlaced, porous internal walls.

18. The filter element of claim 17 wherein the individual cross-sectional areas of the inlet passages are substantially greater than the respective individual cross-sectional areas of the outlet passages.