Abstract: The invention is a ceramic membrane reactor for syngas production having a reaction chamber, an inlet in the reactor for natural gas intake, a plurality of oxygen permeating ceramic slabs inside the reaction chamber with each slab having a plurality of passages paralleling the gas flow for transporting air through the reaction chamber, a manifold affixed to one end of the reaction chamber for intake of air connected to the slabs, a second manifold affixed to the reactor for removing the oxygen depleted air, and an outlet in the reaction chamber for removing syngas.

Abstract: A highly adsorbent, temperature-resistant monolithic activated carbon article is obtained by forming an aqueous emulsion of a polymeric binder, combining the resulting aqueous emulsion with wet, activated carbon particles to produce a slip mixture, forming the obtained slip mixture into a shaped article, and thereafter curing the shaped article.

Abstract: A highly adsorbent, temperature-resistant monolithic activated carbon article is obtained by forming an aqueous emulsion of a polymeric binder, combining the resulting aqueous emulsion with wet, relatively high surface area (>2000 m.sup.2 /g) carbon particles to produce a slip mixture, forming the obtained slip mixture into a shaped structure, and thereafter curing the shaped structure.

Abstract: A highly adsorbent, temperature-resistant monolithic activated carbon article is obtained by forming an aqueous emulsion of a silsesquioxane binder, combining the resulting aqueous emulsion with wet or dry, relatively high surface area (>2000 m.sup.2 /g) carbon particles to produce a slip mixture, forming the obtained slip mixture into a shaped structure, and thereafter curing the shaped structure.

Abstract: An exhaust gas emissions control system lowers cold-start hydrocarbon emissions by using heat exchange structure to lower the temperature of exhaust gas prior to the exhaust gas passing through a hydrocarbon adsorbent and using the extracted heat to heat a catalytic converter to its light-off temperature. In some embodiments, multi-component hydrocarbon adsorbers effective under different operating conditions further reduce cold-start hydrocarbon emissions.

Abstract: An exhaust gas emissions control system lowers cold-start hydrocarbon emissions by using heat exchange structure to lower the temperature of exhaust gas prior to the exhaust gas passing through a hydrocarbon adsorbent and using the extracted heat to heat a catalytic converter to its light-off temperature. In some embodiments, multi-component hydrocarbon adsorbers effective under different operating conditions further reduce cold-start hydrocarbon emissions.

Abstract: An exhaust gas emissions control system lowers cold-start hydrocarbon emissions by using heat exchange structure to lower the temperature of exhaust gas prior to the exhaust gas passing through a hydrocarbon adsorbent and using the extracted heat to heat a catalytic converter to its light-off temperature. In some embodiments, multi-component hydrocarbon adsorbers effective under different operating conditions further reduce cold-start hydrocarbon emissions.

Abstract: A membrane of an oxidative conversion contact material of a mixed oxide of aluminum and at least one multivalent activator metal with the membrane permitting selective conveyance of a form of oxygen therethrough, as well as methods for the oxidative conversion of a gaseous hydrocarbon reactant using such membranes are provided.

Abstract: There is disclosed a catalyst for the reforming of hydrocarbon streams. This catalyst comprises iridium as a hydrogenation component on a support of zirconia and alumina. The support comprises zirconia in an amount of about 3 wt.% to about 15 wt.% zirconia or at least 60 wt.% zirconia. The iridium is present in an amount of about 0.05 wt.% to about 1.5 wt.%, calculated as the metal and based upon the total weight of the catalyst.Also disclosed is a reforming process, which process comprises contacting a hydrocarbon stream in a reaction zone under reforming conditions and in the presence of hydrogen with the above-described catalyst.

Abstract: There is disclosed a catalyst for the reforming of hydrocarbon streams. This catalyst comprises iridium as a hydrogenation component on a support of zirconia and alumina. The support comprises zirconia in an amount of about 3 wt. % to about 15 wt. % zirconia or at least 60 wt. % zirconia. The iridium is present in an amount of about 0.05 wt. % to about 1.5 wt. %, calculated as the metal and based upon the total weight of the catalyst.Also disclosed is a reforming process, which process comprises contacting a hydrocarbon stream in a reaction zone under reforming conditions and in the presence of hydrogen with the above-described catalyst.

Abstract: Catalyst composition comprising highly purified alumina containing essentially no silica with a surface area of at least 100 m.sup.2 /g and up to 5% rhodium and up to 10% zinc.

Abstract: There are disclosed a method for sulfiding a multi-metallic catalyst or a bi-metallic catalyst and a method for initiating the reforming of a petroleum hydrocarbon feedstock in a reforming reaction zone containing a multi-metallic catalyst or a bi-metallic catalyst.The method for sulfiding is employed when a hydrogen-rich gas containing light hydrocarbons is used in the sulfiding of the catalyst. The method comprises passing a stream of said gas over said catalyst at a temperature of about 350.degree. F. to about 470.degree. F., injecting a sulfur-containing compound into the stream of gas up-stream from said catalyst in order to provide a sulfur-carrying gas, and contacting said catalyst with said sulfur-carrying gas at said temperature for a time that is sufficient to provide a sulfur concentration on said catalyst of about 0.1 to about 2.5 moles of sulfur per mole of total active metal. A typical sulfur-containing compound is dimethyl sulfide.