A system holds a roll of film that includes a core and film wound around the core. The system includes a rod having an outer diameter that is smaller than an inner diameter of the core, a proximal wing located on the rod and configured to rotate about the rod, and a distal wing located on the rod and configured to rotate about the rod. Each of the proximal and distal wings includes contact surfaces configured to contact diametrically-opposed locations on a side of an inner surface of the core and non-contact surfaces that span between the contact surfaces of the wing. The non-contact surfaces of the wings do not contact the core if the core has a cylindrical shape. The distal wing is capable of rotating around the rod independently of the proximal wing.

A system includes a dip tube, a feed line, and a check valve. The dip tube is inserted through an opening in a source of chemical precursor and into the chemical precursor in the source. A portion of the feed line is located in the dip tube. The feed line passes out of the dip tube. The chemical precursor is capable of flowing out of the source through the feed line in a downstream direction. The check valve is located in the portion of the feed line in the dip tube. The check valve permits the chemical precursor to pass substantially only in the downstream direction. The feed line is coupled to a transfer pump that draws the chemical precursor out of the source through the portion of the feed line in the dip tube.

An exhaust aftertreatment system for use with over-the-road vehicle is disclosed. The exhaust aftertreatment system includes a reducing agent mixer with a mixing can and a flash-boil doser configured to inject heated and pressurized reducing agent into the mixing can for distribution throughout exhaust gases passed through the mixing can.

The present invention relates to a process of producing a nano resveratrol microemulsion system includes: (i) preparing a dispersal phase by dissolving resveratrol in an ethanol solvent; (ii) preparing a carrier by heating a liquid PEG (polyethylene glycol) accounted from 40 to 60% by mass of the mixture of PEG and water to a temperature ranging from 60 to 80 C., then adding zeolite catalyst (0.1-0.4% by mass of mixture of PEG and water), stirring evenly; (iii) adding the carrier to the dispersal phase (in a ratio by mass of 40:60), continuing heating the said dispersal phase to 100 C., stirring at a speed of 400 to 800 rpm; (iv) elmusifying as follows: when the temperature arrives at 100 C., adding Tween to the mixture of the carrier and dispersal phase in step (iii) in a ratio by mass of 40:60, continuing to stir at a speed of 500 to 700 rpm, at a temperature of 100 C. to 130 C. perform emulsification at speed of 2500 to 3500 rpm, combining stirring at a speed of 400 and 600 rpm, in vacuum, the reaction temperature is maintained at 150 C. for 3 to 5 hours, the reation is quenched, the temperature is decreased slowly until it is in the range of 40 to 60 C.; (v) filtrating the product by injecting through nanofilter system before filling-packaging.

A longitudinal sealer includes a housing, an arm, and a heating element. The housing is configured to be installed in a foam-in-bag system. The arm is movably coupled to the housing. The heating element has a leading edge exposed through an exterior surface of the arm. A position of the arm with respect to the housing is controllable so that the arm is movable between a first location where the leading edge of the heating element is not in contact with a film in a film path of the foam-in-bag system and a second location where the leading edge of the heating element is in contact with the film in the film path of the foam-in-bag system.

An exhaust aftertreatment system for use with over-the-road vehicle is disclosed. The exhaust aftertreatment system includes a reducing agent mixer with a mixing can and a flash-boil doser configured to inject heated and pressurized reducing agent into the mixing can for distribution throughout exhaust gases passed through the mixing can.

Provided in one implementation is a method that includes introducing a volume of raw material into a chamber of a cavitation machine. The raw material can include a mixture comprising a powder and a solvent. The powder can have a first average particle size in the raw material. The method includes applying a hydrodynamic cavitation process to the raw material to produce a product material. The powder can have a second average particle size, smaller than the first average particle size, in the product material. The method includes causing the product material to exit the cavitation chamber and drying the product material to remove the solvent. Apparatus employed to apply the method are also provided.

An apparatus for producing a composition includes a holding device for holding first and second capsules including first and second deformable compartments, respectively, which contain a first formulation and a second formulation, respectively; a first compression element including a first compression surface designed to apply a pressure to the first deformable compartment of the first capsule; and a second compression element including a second compression surface designed to apply a pressure to the second deformable compartment of the second capsule. The first compression surface is designed to conduct and guide the contents of the first capsule to a first passage in the first capsule that can be fluidically connected to the first deformable compartment and the second compression surface is designed to conduct and guide the contents of the second capsule to a second passage in the second capsule that can be fluidically connected to the second deformable compartment.

A method for continuously producing a conversion product, in particular starch glue, fried starch, dissolved gelatin or protein glue, wherein a starch-containing and/or protein-containing, preferably powdery starting material, in particular flour, starch powder, cereal grains, coarse cereal meal, gelatin powder or gluten powder, is fed to a mixing chamber (2) and the starting material, preferably powder, descending in the mixing chamber (2) is subjected to a liquid heated to a processing temperature (T.sub.U) of at least 50 C. for converting the starting material into the conversion product, in particular to at least a gelatinization temperature of the starch-containing starting material, a protein-dissolving and/or denaturing temperature of the protein-containing starting material or a frying temperature, in the form of a pressure jet (7) and is thereby conveyed against a baffle (10) preferably formed by an inner wall of the mixing chamber or by an installation in the mixing chamber.

A method for producing a lignocellulose plastic composite material, in particular a simpler and more cost-effective option for producing lignocellulose plastic composite materials. Thermoplastic particles and a mixture of water and lignocellulose-containing particles are supplied to a refiner, and the lignocellulose-containing particles are reduced to fibers in the refiner. The thermoplastic particles are supplied to the refiner in a melted or fused state, or are melted or fused in the refiner, so that the melted or fused thermoplastic particles and the lignocellulose-containing particles that are reduced to fibers form material composite particles in the refiner.