A packing member for use in a packed bed, preferably a support for use as a catalyst support in a packed bed reactor. The packing member includes ceramic material and has a geometric surface area per volume of ?0.7 cm.sup.2/cm.sup.3 and a side crush strength of ?250 kgf; or a geometric surface area per volume of ?1.5 cm.sup.2/cm.sup.3 and a side crush strength of ?150 kgf; or a geometric surface area per volume of ?3 cm.sup.2/cm.sup.3 and a side crush strength of ?60 kgf. The packing member optionally has a porosity of at least 6%, such as at least 15% or at least 20%.

A method for facilitating the distribution of the flow of one or more streams within a bed vessel is provided. Disposed within the bed vessel are internal materials and structures including multiple operating zones. One type of operating zone can be a processing zone composed of one or more beds of solid processing material. Another type of operating zone can be a treating zone. Treating zones can facilitate the distribution of the one or more streams fed to processing zones. The distribution can facilitate contact between the feed streams and the processing materials contained in the processing zones.

A method for facilitating the distribution of the flow of one or more streams within a bed vessel is provided. Disposed within the bed vessel are internal materials and structures including multiple operating zones. One type of operating zone can be a processing zone composed of one or more beds of solid processing material. Another type of operating zone can be a treating zone. Treating zones can facilitate the distribution of the one or more streams fed to processing zones. The distribution can facilitate contact between the feed streams and the processing materials contained in the processing zones.

In a fixed-bed flow reaction using a multitubular heat exchange type reactor, an object of the present invention is to provide a novel packing for a reaction tube, which can control the reaction ratio in the vicinity of the reaction tube inlet, reduce the load unevenly placed on the catalyst in the reaction region, and distribute the load on the entire catalyst layer, a heat exchange type reactor, and a reaction method using the reaction tube. The packing for a reaction tube of the present invention is characterized in that the volume is continuously or step-by-step decreased from one end part or midway toward the other end part.

A generally spherical high strength ceramic body for use in an ATR and/or SR unit covering a catalyst media bed. The ceramic body is a fully stabilized YSZ composite composition having at least about 13% yttria YSZ, and more typically from about 12% to about 20% yttria YSZ, with a porosity of less than 20 percent and a diameter of at least 25 mm and, more typically, selected from the group comprising 25 mm, 50 mm, 76 mm and 100 mm.

A corrosion resistant refractory ceramic hexagonal target tile body for use covering a catalyst, including a generally flat hexagonal portion and a plurality of generally right circular cylindrical aperture portions extending therethrough, wherein the hexagonal tile body has a thickness of about 89 mm and a width of about 42 cm and is 13 percent yttria fully stabilized YSZ. Each respective aperture has a diameter of about 19 mm.

Assemblies, apparatuses, systems, and method to extract or convey a material from a source of the material may include a vacuum generation and sound attenuation assembly to enhance conveyance the material from the source of the material. The vacuum generation and sound attenuation assembly may include a vacuum source including a plurality of vacuum generators. Each of the plurality of vacuum generators may be positioned to cause a vacuum flow between the source of the material and the vacuum generation and sound attenuation assembly. The vacuum generation and sound attenuation assembly may further include a sound attenuation chamber connected to the vacuum source. The sound attenuation chamber may include an attenuation housing at least partially defining a chamber interior volume being positioned to receive at least a portion of the vacuum flow from the vacuum source and attenuate sound generated by the vacuum source.

There is described a packing member for use in a packed bed, preferably a support for use as a catalyst support in a packed bed reactor. The packing member comprises ceramic material and has a geometric surface area per volume of ?0.7 cm.sup.2/cm.sup.3 and a side crush strength of ?250 kgf; or a geometric surface area per volume of ?1.5 cm.sup.2/cm.sup.3 and a side crush strength of ?150 kgf; or a geometric surface area per volume of ?3 cm.sup.2/cm.sup.3 and a side crush strength of ?60 kgf. The packing member optionally has a porosity of at least 6%, such as at least 15% or at least 20%.

In a method of manufacturing objects, extrudable ceramic forming material is extruded through multiple dies arrayed around an extrusion axis, the dies mounted to permit controlled movement of the dies during the course of extrusion to vary the position of several extrudate streams exiting the dies. Extruded objects are defined by spokes corresponding to the extrudate streams with the streams having a varying spacing from a central axis.

A method for facilitating the distribution of the flow of one or more streams within a bed vessel is provided. Disposed within the bed vessel are internal materials and structures including multiple operating zones. One type of operating zone can be a processing zone composed of one or more beds of solid processing material. Another type of operating zone can be a treating zone. Treating zones can facilitate the distribution of the one or more streams fed to processing zones. The distribution can facilitate contact between the feed streams and the processing materials contained in the processing zones.