Various examples of systems and methods for making microspheres, microparticles, and emulsions are provided. In one example, a system and method for forming microspheres comprises: pumping a dispersed phase liquid and a continuous phase liquid into a levitating magnetic impeller pump to subject the dispersed phase liquid and continuous phase liquid to a high shear environment within the impeller pump's pump chamber. In another example, a system and method for forming an emulsion comprises: pumping a dispersed phase liquid and an inner aqueous phase liquid into a levitating magnetic impeller pump to subject the dispersed phase and the inner aqueous phase to a high shear environment within the impeller pump's pump chamber.

A syringe assembly for a hydraulic fracturing system includes a syringe having a material chamber, a base fluid chamber, and a piston. The material chamber is configured to be fluidly connected to a fluid conduit. The piston retracts to draw material into the material chamber. The piston extends to push the material into the fluid conduit. The syringe assembly includes a diverter fluidly connected to the base fluid chamber and moveable between first and second positions. The first position of the diverter fluidly connects the base fluid chamber to a base fluid reservoir of the hydraulic fracturing system and fluidly disconnects the base fluid chamber from an outlet of a frac pump of the hydraulic fracturing system. The second position of the diverter fluidly connects the base fluid chamber to the outlet of the frac pump and fluidly disconnects the base fluid chamber from the base fluid reservoir.

Embodiments of the present application relate to compositions bupivacaine multivesicular liposomes (MVLs) prepared by a commercial manufacturing process with large particle diameter span.

A method for producing a resin particle dispersion includes using a resin particle dispersion production apparatus including: two or more resin particle dispersion production lines each including an emulsification tank in which a resin is subjected to phase inversion emulsification using two or more organic solvents and an aqueous medium to thereby obtain a phase-inverted emulsion, a distillation tank in which the organic solvents are removed from the phase-inverted emulsion by reduced pressure distillation to thereby obtain a resin particle dispersion, and plural distillate collection tanks that collect distillates formed during the reduced pressure distillation according to respective target distillate compositions; and a reusable distillate storage tank A that collects and stores a distillate collected in at least one distillate collection tank A among the distillates collected in the plural distillate collection tanks in each of the two or more resin particle dispersion production lines. The distillate collected in the reusable distillate storage tank A is delivered to the emulsification tank in at least one resin particle dispersion production line among the two or more resin particle dispersion production lines to reuse the distillate for production of a phase-inverted emulsion in the at least one resin particle dispersion production line.

A method for producing a single-phase phase-stable liquid is provided, in which, in an embodiment: in a first step, a lipophilic liquid is mixed with a hydrophilic liquid, so that a mixture of the liquids is obtained; in a second step, the static pressure of the mixture is brought below the vapor pressure of at least one of the liquids, so that cavitation bubbles occur, for example, as a result of what is known as hard cavitation; and in a third step, the cavitation bubbles are caused to implode, a single-phase phase-stable liquid being obtained.

Embodiments of the present application relate to commercial manufacturing processes for making bupivacaine multivesicular liposomes (MVLs) using independently operating dual tangential flow filtration modules.

The present application discloses powder and aqueous formulations. These include but are not limited to water dispersible cannabinoid formulations, especially those comprising cannabidiol (CBD), cannabigerol (CBG), and cannabinol (CBN) as well as other cannabinoids. Generally, these embodiments do not include major amounts of Tetrahydrocannabinol (THC), but certain embodiments are envisioned that do contain measurable concentrations of THC. Embodiments may include one or more emulsifiers selected from the group consisting of Tween (polysorbate) 20, Tween 60, Tween 80, Span 20, Span 60, Span 80, Poloxamer 188, Vit E-TPGS (TPGS), TPGS-1000, TPGS-750-M, Solutol HS 15, PEG-40 hydrogenated castor oil, PEG-35 Castor oil, PEG-8-glyceryl capylate/caprate, PEG-32-glyceryl laurate, PEG-32-glyceryl palmitostearate, Polysorbate 85, polyglyceryl-6-dioleate, sorbitan monooleate, Capmul MCM, Maisine 35-1, glyceryl monooleate, glyceryl monolinoleate, PEG-6-glyceryl oleate, PEG-6-glyceryl linoleate, oleic acid, linoleic acid, propylene glycol monocaprylate, propylene glycol monolaurate, polyglyceryl-3 dioleate, polyglyceryl-3 diisostearate and lecithin.

Systems, methods, and devices for forming an array of emulsions. An exemplary device comprises a frame and at least one or a plurality of separate microfluidic modules mounted to the frame and each configured to form an array of emulsions. In some embodiments, each module may be mounted by snap-fit attachment. The device also may include the same sealing member bonded to a top side of each module and hermetically sealing each of the modules. Another exemplary microfluidic device for forming an array of emulsions comprises a stack of layers bonded together. The stack may comprise a port layer forming a plurality of ports. Each port may have a top rim formed by a protrusion that encircles the central axis of the port. The rims may be coplanar with one another to facilitate bonding of a sealing member to each rim.

The present invention relates to a process of producing a nano-Tan IIA microemulsion system comprising the following steps: (i) preparing a dispersed phase by dissolving Tan IIA in ethanol solvent in a ratio of mass of Tan IIA:volume of ethanol solvent of 8:10; (ii) preparing a carrier by heating liquid PEG (polyethylene glycol) to 60-80° C.; (iii) adding the carrier to the dispersed phase in a mass ratio of 40:60 with further heating of the dispersed phase to 40-60° C.; (iv) elmusifying by heating until the temperature reaches 100° C., adding ACRYSOL K-140 to the mixture of the carrier and dispersed phase obtained in step (iii) in a mass ratio of 40:60 with further stirring at 500-700 rpm at about 100° C. under vacuum; and (v) filtering the product by injection through a nanofilter system before filling-packing.

A method for continuously processing at least two liquid feed streams is provided. A system for continuously processing at least two liquid feed streams is also provided.