A pharmaceutical composition is provided comprising a highly soluble arsenic carbonate and/or bicarbonate compound and which is useful in the treatment of a variety of cancers, including acute promyelocytic leukaemia. The arsenic carbonate and/or bicarbonate salt acts as a solid, and so orally deliverable, improved bioequivalent delivery form of arsenic trioxide IV solutions.

A fluid processing apparatus includes: a casing having a fluid inlet pipe and a fluid outlet pipe; multiple rectifying plates with holes in parallel with each other provided within the casing on a side of the fluid inlet pipe, the rectifying plates being perpendicular to a longitudinal axis of the casing; and a light source for irradiating fluid passing from the fluid inlet pipe through the casing to the fluid outlet pipe with ultraviolet rays.

A fluid processing apparatus includes: a casing having a fluid inlet pipe and a fluid outlet pipe; multiple rectifying plates with holes in parallel with each other provided within the casing on a side of the fluid inlet pipe, the rectifying plates being perpendicular to a longitudinal axis of the casing; and a light source for irradiating fluid passing from the fluid inlet pipe through the casing to the fluid outlet pipe with ultraviolet rays.

A wastewater plant and method for treatment of wastewater sludge or other wastewater fluids are described. The wastewater plant utilizes an electrical discharge system configured for receiving a wastewater fluid, and generating a transient voltage and arcing electric current pulse through the received wastewater fluid to create an electro-hydraulic shock wave within the wastewater fluid accompanied by a high electric field, intensive heat and light radiation.

Some embodiments of the present invention provide components for a serpentine fluid reactor which is optimized for one or more objective functions of interest such as pressure drop, erosion rate, fouling, coke deposition and operating costs. The components are designed by computer modeling the components individually and collectively in which the cross section of flow path is substantially circular under industrial conditions to validate the model design and its operation. Then iteratively the component designs are deformed and the operation of the deformed part(s) is modeled and compared to values obtained with other deformed models until the value of the objective function is optimized (e.g. at an extreme) or the change in the objective function is approaching zero.

A mixing device for a fuel reformer for mixing at least two fluids is provided. The mixing device includes at least a first plurality of holes which is arranged along a first row, and a second plurality of holes which is arranged along a second row. The mixing device can be used in a fuel reformer for converting hydrocarbon fuel into hydrogen rich gas by auto-thermal reaction process having a, preferably cylindrically shaped and double walled, housing with two side walls forming a reaction chamber of the fuel reformer, wherein hydrocarbon fuel and an oxidizing agent are mixed by the mixing device.

There is provided a thermal reactor (100) comprising: a vessel (101), said vessel comprising: a gas inlet (102), an outlet (103), a gas permeable cage (104) arranged in the vessel (101), and in fluid connection to the gas inlet (102), wherein the vessel (101) and the cage (104) are provided with a mutual gas outlet (103), and temperature generating means (105:105) arranged to create a thermal reaction zone (106) within the cage (104), wherein the cage (104) is provided with holes (107), and wherein a first subset of the holes (107) is arranged along at least a portion of a first circumferential surface (110) of the cage (104) and a second subset of the holes (107) is arranged along at least a portion of a second circumferential surface (111) of the cage (104), wherein the first (110) and second (111) circumferential surfaces are offset and non-parallel, and the first subset of holes (107) and the second subset of holes (107) are mutually distinct.

The present disclosure provides a method for reducing the aldehyde content in an amine catalyst by treating the amine catalyst with an organic acid. The organic acid-treated amine catalyst may then be used in the production of polyurethane materials which exhibit reduced aldehyde emissions.

The present disclosure relates to reactor components and their use, e.g., in regenerative reactors. A process and apparatus for utilizing different wetted areas along the flow path of a fluid in a pyrolysis reactor, e.g., a thermally regenerating reactor, such as a regenerative, reverse-flow reactor, is described.

In an embodiment, a method of producing a carbonate comprises reacting carbon monoxide and chlorine in a phosgene reactor in the presence of a catalyst to produce a first product comprising phosgene; wherein carbon tetrachloride is present in the first product in an amount of 0 to 10 ppm by volume based on the total volume of phosgene; and reacting a monohydroxy compound with the phosgene to produce the carbonate; wherein the phosgene reactor comprises a tube, a shell, and a space located between the tube and the shell; wherein the tube comprises one or more of a mini-tube section and a second tube section; a first concentric tube concentrically located in the shell; a twisted tube; an internal scaffold; and an external scaffold.