| Class / Patent application number | Description | Number of patent applications / Date published |
|---|
| 422212000 | With means removing and recovering product from extended surface contact material | 6 |
| 20090252661 | Fuel reformer - A fuel reformer includes a reforming portion having a tubular catalytic converter that is composed of a substrate supporting the catalytic component, and is arranged to have a center axis extending along the supply direction of the fuel and oxidizer derived from a supply portion, and a communication passage arranged along an inner wall of the catalytic converter and communicating with the supply portion. The fuel and oxidizer supplied from the supply portion to the communication passage pass from the inner wall of the catalytic converter to an outer wall thereof by forced convection, thereby reforming the fuel. | 10-08-2009 |
| 20090269260 | METHOD AND APPARATUS FOR FINE SOLIDS RECYCLE - A fine solids recycle apparatus for a fluidized bed reactor comprises an eductor connected to a dipleg extending from a cyclone connected to the reactor, wherein the fine solids particles are removed from the dipleg, mixed with an eductor gas to form an eductor gas-fine solids particles mixture, which allows the return of the fine solids particles to the fluidized bed region, whereby the fine solids is further reacted in the fluidized region to improve reaction efficiency. | 10-29-2009 |
| 20090285731 | Conversion of nitrogen dioxide (NO2) to nitric oxide (NO) - Inhalation of low levels of nitric oxide can rapidly and safely decrease pulmonary hypertension in mammals. A nitric oxide delivery system that converts nitrogen dioxide to nitric oxide employs a surface-active material, such as silica gel, coated with an aqueous solution of antioxidant, such as ascorbic acid. | 11-19-2009 |
| 20100028224 | Oxygenate Conversion Reactor Catalyst Coolers - A process of converting oxygenates to light olefins is disclosed including an oxygenate feedstream with contacting catalyst inside a reactor and converting the oxygenate feedstream to said light olefins. The catalyst becomes spent as deposits from the reaction clog up pores on the catalyst surface. A portion of the spent catalyst is regenerated in a regenerator and a portion is circulated back to contact more of the oxygenate feedstream. A catalyst cooler attached to the reactor can cool the spent catalyst circulated through the cooler before the spent catalyst contacts more of the oxygenate feedstream. In an embodiment, all of the spent catalyst that enters the catalyst cooler is withdrawn from the bottom of the catalyst cooler. | 02-04-2010 |
| 20100290961 | Hydrogen transport membranes for dehydrogenation reactions - A method of converting C | 11-18-2010 |
| 20160151740 | ACIDIC-GAS SEPARATION MODULE | 06-02-2016 |
