Provided herein is a gas mixer for the safe mixing of a hydrocarbon containing gas with a gaseous oxidant. The gas mixer and method for mixing described includes a closed mixing vessel where bubbles of gas injected at the bottom of the vessel are mixed during their rise to the top of the vessel, forming a homogeneous mixture that can safely be removed. This simple design and method allows for safe mixing of gases and is applicable to catalytic oxidative processes such as oxidative dehydrogenation of paraffins where there is a risk of thermal runaway of reactions.

A method of packaging a filter media that is pre-folded for insertion is a filter assembly is provided.

The present invention describes a packing with a three-dimensional structure which is particularly suited to creating homogenous and anisotropic mixing between the gas phase and a dispersed solid phase moving in counter-current flow. Application of this packing to the stripper of fluidized catalytic cracking units.

The present invention describes a packing with a three-dimensional structure which is particularly suited to creating homogenous and anisotropic mixing between a gas phase and a dispersed solid phase moving in counter-current flow. Application of this packing to the stripper of fluidized catalytic cracking units.

A catalytic reactor includes: a reaction-side flow channel in which a reaction fluid flows; a structured catalyst removably located in the reaction-side flow channel; and a protrusion formed in the structured catalyst or an inner surface of the reaction-side flow channel, having a height forming a clearance between the structured catalyst and the inner surface of the reaction-side flow channel.

The present invention describes a packing with a three-dimensional structure which is particularly suited to creating homogenous and anisotropic mixing between a gas phase and a dispersed solid phase moving in counter-current flow. Application of this packing to the stripper of fluidized catalytic cracking units.

The present invention describes a packing with a three-dimensional structure which is particularly suited to creating homogenous and anisotropic mixing between the gas phase and a dispersed solid phase moving in counter-current flow. Application of this packing to the stripper of fluidized catalytic cracking units.

A catalytic reactor includes: a reaction-side flow channel in which a reaction fluid flows; a structured catalyst removably located in the reaction-side flow channel; and a protrusion formed in the structured catalyst or an inner surface of the reaction-side flow channel, having a height forming a clearance between the structured catalyst and the inner surface of the reaction-side flow channel.

The inventive systems include solar receivers that are used to heat chemical reactors (110, 310). When solar radiation is plentiful. the systems utilize the solar radiation to heat chemical reactors (110, 310) and store excess heat from the solar radiation in a heat storage component (104, 702). When solar radiation is not plentiful. the systems heat the chemical reactors (110, 310) using heat stored in the heat storage component (104, 702). Also described are methods of using and methods of constructing such systems.

A spacer array including a plurality of spacers. Each spacer defines a longitudinal axis and includes a main body, a leading pin, and a trailing pin. The main body has a main body cross-sectional dimension. The leading pin extends from the main body and is upstream of the main body. The leading pin has a leading pin cross-sectional dimension. The trailing pin extends from the main body and is downstream of the main body. The trailing pin has a trailing pin cross-sectional dimension. The main body cross-sectional dimension is greater than the leading pin cross-sectional dimension and the trailing pin cross-sectional dimension.