A packing element for use in a heat exchange or mass transfer tower includes a barrel and a plurality of fins spaced around a circumference of the barrel, each fin having a height approximately equal to a height of the barrel and a length extending radially from the barrel, a proximate end of each fin attached perpendicularly to the barrel. A protrusion extends outward from the distal end or each fin along its height. A method for mass transfer includes passing fluids through a vessel packed with randomly arranged packing elements.

The present invention relates to a catalyst bed comprising silver catalyst bodies and a reactor comprising such a catalyst bed. Further, the invention relates to the use of the catalyst bed and the reactor for gas phase reactions, in particular for the oxidative dehydrogenation of organic compounds under exothermic conditions. In a preferred embodiment, the present invention relates to the preparation of olefinically unsaturated carbonyl compounds from olefinically unsaturated alcohols by oxidative dehydrogenation utilizing a catalyst bed comprising metallic silver catalyst bodies.

A gas-solid contacting system (100) with structured packing (108) is disclosed. The structured packing (108) comprises a gas header (102) with an inlet to receive a gas. A plurality of vertically aligned tubes (104) is fluidically connected to the gas header (102), wherein each vertically aligned tube (104) comprises openings (180)to distribute the gas at different heights in a radial direction. A structured packing element (106) is arranged on each vertically aligned tube (104), wherein the structured packing element (106) comprises one or more plates attached to the vertically aligned tube (104) to create a convoluted 3-dimensional flow path for smooth flow and radial distribution of a solid particulate stream.

A system for controlling hydrogen production from water-reactive aluminum includes a regulator. For example, the regulator may include a plurality of discrete objects and a retainer. Each one of the discrete objects includes aluminum in an activated form reactable with water to produce hydrogen. The retainer may encase the plurality of discrete objects collectively in an elongate shape having an axial dimension greater than a radial dimension. Within the elongate shape, the plurality of discrete objects may define voids therebetween. The retainer may be permeable across its thickness such that water may enter the retainer to react with the activated form of aluminum of the discrete objects in a local concentration that promotes heat generation for rapid reaction while water about the retainer may globally cool the material in the retainer, with the combination promoting rapid and efficient reaction of aluminum to produce hydrogen.

A filter element (1) comprising a central tubular body/core (2) and a plurality of radially outwardly directed fins (3) forming the main structure of the element, the radially outwardly directed fins (3) projecting outwardly from said central tubular body/core (2) and whose radial length increases stepwise from each end of the central body or core to a maximum length located centrally of the length of the body or core (2), thereby effectively providing a generally double back-to-back conical appearance, a stiffening ring (8) arranged to encircle with a gap therebetween the body/core (2) at a mid-region thereof and whose plane is perpendicular to the axis of the body or core (2), the central tubular body/core (2) including one or more radially inwardly directed ribs (12).

A reformer suitable for micro-scale design has horizontal catalyst tube(s) passing through a baffled radiant section for convective and radiant heat transfer to the tube(s). To reduce the footprint and/or to facilitate field assembly a combustion chamber and convection section can be oriented transversely with respect to the radiant section; the tube(s) can be horizontal and/or include structured catalyst; and/or the combustion chamber provides flameless combustion or produces a flame without impinging on the tubes. Also, a skid frame-mountable version of the reformer; and a process for transporting, assembling, and/or operating the steam methane reformer.

A reformer suitable for micro-scale design has horizontal catalyst tube(s) passing through a baffled radiant section for convective and radiant heat transfer to the tube(s). To reduce the footprint and/or to facilitate field assembly a combustion chamber and convection section can be oriented transversely with respect to the radiant section; the tube(s) can be horizontal and/or include structured catalyst; and/or the combustion chamber provides flameless combustion or produces a flame without impinging on the tubes. Also, a skid frame-mountable version of the reformer; and a process for transporting, assembling, and/or operating the steam methane reformer.

Disclosed herein are apparatus and methods for producing emulsions, and, in particular, for maintaining laminar flow during production of emulsions containing microsuspensions.

Disclosed herein are apparatus and methods for producing emulsions, and, in particular, for maintaining laminar flow during production of emulsions containing microsuspensions. Disclosed herein are columns for receiving a packing material that permits fluid flow through the column. The columns have a periphery that defines an interior cavity in fluid communication with inlets and outlets of the column. Disclosed herein is a method of preparing an emulsion that includes (1) forming a first phase typically containing an organic solvent, a polymer, and one or more biologically active agents and/or chemicals; (2) forming a second phase typically containing water as the second solvent, an emulsion stabilizer and optionally a solvent; and (3) passing the first and the second phases through the column to form a water in oil type emulsion.

A catalyst for catalytic reactors of which the outer shape is a helix with n blades, where n is greater than or equal to 1, wherein the stack void fraction percentage is between 75% and 85% and the surface area/volume ratio is greater than 1000 square meters/square meters.