A method of treatment of plasma with a physiologically compatible spray dry stable acidic substance (SDSAS) prior to or contemporaneously with spray drying of the plasma that results in greater recovery and greater long-term stabilization of the dried plasma proteins as compared to spray dried plasma that has not be subject to the formulation method of the present invention, as well as compositions related to plasma dried by the methods of the present invention.

A method of treatment of plasma with a physiologically compatible spray dry stable acidic substance (SDSAS) prior to or contemporaneously with spray drying of the plasma that results in greater recovery and greater long-term stabilization of the dried plasma proteins as compared to spray dried plasma that has not be subject to the formulation method of the present invention, as well as compositions related to plasma dried by the methods of the present invention.

Systems and methods of recovering solid waste (solid waste brine) from produced water in an oil sands system for the production of oil and other hydrocarbons utilizing a fluidized bed spray granulator system to provide evaporative drying.

Systems and methods of recovering solid waste (solid waste brine) from produced water in an oil sands system for the production of oil and other hydrocarbons utilizing a fluidized bed spray granulator system to provide evaporative drying.

A reflective particulate material includes a particulate substrate having high total solar reflectance, bulk and apparent densities and toughness, and a low dust index. The reflective particulate can have a total solar reflectance of 80% to 87%, a toughness of 1% or fewer fines, an apparent density of 2.75 g/cm.sup.3 or greater, and a dust index of 1 or lower. A method of manufacturing the reflective particulate material includes preparing a slurry of the particulate substrate, spray drying the slurry to form a spray dried particulate, crushing the spray dried particulate to form a crushed particulate, and heating/calcining the crushed particulate. The heated, crushed particulate may further be coated to form a coated roofing granule.

An apparatus is described. The apparatus comprises a liquid dispenser comprising a liquid outlet, the liquid dispenser being configured to generate a droplet stream. The apparatus also comprises a first fluid flow device configured to generate a confinement fluid flow for confining a trajectory of the droplet stream therein, the first fluid flow device comprising an outlet arranged to allow the droplet stream to exit therefrom, wherein the fluid outlet is arranged within the confinement fluid flow device. Furthermore, the apparatus comprises a second fluid flow device configured to generate a reaction fluid flow for reacting with droplets in the droplet stream, wherein the outlet of the first fluid flow device is arranged within the second fluid flow device. A method is also described.

An apparatus is described. The apparatus comprises a liquid dispenser comprising a liquid outlet, the liquid dispenser being configured to generate a droplet stream. The apparatus also comprises a first fluid flow device configured to generate a confinement fluid flow for confining a trajectory of the droplet stream therein, the first fluid flow device comprising an outlet arranged to allow the droplet stream to exit therefrom, wherein the fluid outlet is arranged within the confinement fluid flow device. Furthermore, the apparatus comprises a second fluid flow device configured to generate a reaction fluid flow for reacting with droplets in the droplet stream, wherein the outlet of the first fluid flow device is arranged within the second fluid flow device. A method is also described.

A spray drying process and apparatus for drying a spray dryable liquid composition to a spray dried powder is described, in which the spray dryable liquid composition contains no carrier. The spray dryable liquid composition is processed at a solids concentration not exceeding 80% by weight, based on total weight of the spray dryable liquid composition, being atomized to generate an atomized spray of liquid particles of the spray dryable liquid composition into a spray drying chamber, in which the atomized spray is contacted with a stream of drying fluid flowed at temperature not exceeding 100 C. into the spray drying chamber, to form the spray dried powder.

Particulate compositions solid at 20 C. and comprising at least one copolymer based on at least the following comonomers a) to d) a) conjugated diene, b) ,-unsaturated nitrile, c) at least one polyfunctional radically polymerizable comonomer and d) at least one carboxyl-, hydroxyl-, epoxy- and/or amino-group-functional radically polymerizable comonomer,
which possess an average particle diameter of the primary particles of 5 to 500 nm, characterized in that these compositions possess a pourability to EN DIN 6186:1998 (funnel diameter 15 mm) of not more than 33 s.

Particulate compositions solid at 20 C. and comprising at least one copolymer based on at least the following comonomers a) to d) a) conjugated diene, b) ,-unsaturated nitrile, c) at least one polyfunctional radically polymerizable comonomer and d) at least one carboxyl-, hydroxyl-, epoxy- and/or amino-group-functional radically polymerizable comonomer,
which possess an average particle diameter of the primary particles of 5 to 500 nm, characterized in that these compositions possess a pourability to EN DIN 6186:1998 (funnel diameter 15 mm) of not more than 33 s.