A method for regulating the humidity in a gas. In the first step, the humidity in a gas entering a bubbler at a flow rate is regulated between 200 NL/h and 2,000 NL/h. The gas entering the bubbler through the inlet of the bubbler tank passes throughout the first porous matrix. The humidified gas comes out through the outlet of the bubbler tank and circulates towards a compressor. In the second step, the gas derived from the first step is dried. The gas coming out of the compressor passes through a T-shaped tube including one inlet and two outlets. One of the outlets is arranged vertically and lets the liquid phase of the gas flow by gravity effect, thereby creating a condensate. The other outlet is connected at the bottom of a desiccant reservoir.

The invention relates to an emulsification device for continuously producing emulsions, nano-emulsions, and/or dispersions having a liquid crystalline structure, comprising a) at least one mixing system, b) at least one drive for the stirring element, and c) at least one delivery unit for each component or each component mixture.

Embodiments of the present disclosure include suspensions for use in enhanced oil recovery, and methods of using the suspensions for recovering oil. Suspensions of the present disclosure include a nonionic surfactant that can dissolve in supercritical carbon dioxide, and a metal salt having a concentration of 200 to 1 parts-per-million.

The invention relates to a method and a device for anaerobic digestion from an organic liquid sludge (21), comprising, in a known manner, a step of hydrolysis/acidogenesis of the sludge in a digester (47, 100), a step of acetogenesis for producing acetate from the hydrolysed sludge and a step of methanogenesis from the acetates for producing methane. The method comprises an initial step of creating a hydrolysed sludge emulsion (23) obtained by means of the impact of the sludge with gas (27) injected into the sludge, then continuously supplying the hydrolysed sludge to a reactor (25, 101) pressurised in line relative to the digester, before discharging said sludge from the reactor via a member (29) generating a pressure drop in the hydrolysed sludge, the initial stage being repeated at least once before supplying the, and/or via the, digester.

A mixing spool is utilized to mix a liquid coagulant into water flowing through a large conduit. The mixing spool is inserted as a segment into the conduit. The mixing spool utilizes a pair of opposite facing nozzles which extend through a wall of the spool into the interior of the spool. The nozzles receive a pressurized liquid flow through a manifold. A chemical injection quill has an open end positioned between the opposite facing nozzles, wherein the chemical injection quill is configured to deliver the liquid coagulant into the water flowing through the conduit.

The invention relates to an emulsification device for continuously producing emulsions, nano-emulsions, and/or dispersions having a liquid crystalline structure, comprising a) at least one mixing system, b) at least one drive for the stirring element, and c) at least one delivery unit for each component or each component mixture.

Apparatus and method for mixing a tank containing a fluid with a gas, wherein the gas is fired with a periodic intensity and duration through the employment of a gas container containing an inverted siphon, with one end contained in the container and the other end extending into a fluid.

The present invention is related to an installation and to a method for recirculating and mixing a fluid which is preferably a shear-thinning fluid. The installation comprises a tank, a pump, a piping assembly connected to the pump and comprising an injection piping for injecting said fluid into the tank and a return piping coupled to the injection piping for pumping the said fluid from the tank to the injection piping, wherein the piping assembly and the tank form a flow recirculation path in which fluid is homogenized by recirculation of the fluid upon action of the said pump, the injection piping being designed such as to reinject the fluid in at least two peripheral bottom locations with an horizontal and/or inclined orientation such as to create a swirl movement in the tank and to reinject simultaneously said fluid upwardly through a central location in a zone comprised between the central axis of the tank and the half radius of the tank such as to create a jet of fluid having a main vertical component.

A compact and transportable equipment adapted to be used for hydraulic fracturing operations on gas or oil fields includes a means for unloading powder polymer, a means for supplying a polymer powder to a silo, and a silo for storing polymer in powder form, the silo having inside a vertical screw located in a vertical pipe, the lower end of the shaft of the vertical screw extending outside of the silo. The equipment has a feed hopper of a polymer metering device, a device for metering out the powder polymer, at least one tank for hydrating and dissolving the dispersed polymer originating from the dispersing and grinding device, and at least one volumetric pump enabling injection and metering of the polymer solution. The lower end of the shaft of the vertical screw has a rotating ring, the rotating ring being perpendicularly fixed on the shaft and being equipped with at least three straight paddles, positioned perpendicularly to the horizontal plan of the ring.

Gas-liquid injection apparatus, having a body, a liquid passage, a bypass passage, a gas inlet, a gas-liquid mixing cavity and a gas-liquid mixing passage, wherein the body includes an inlet end face and an outlet end face, and the liquid passage includes a liquid inlet that opens onto the inlet end face and a passage outlet that is arranged on the outlet end face, and includes a converging section and a throat section that are arranged in sequence downstream of the liquid inlet; one end of the bypass passage opens to the converging section, and the other end is connected to the gas-liquid mixing cavity, and the bypass passage allows liquid flowing in the liquid passage to bypass to the gas-liquid mixing cavity; the gas-liquid mixing cavity is located at the periphery of the liquid passage; the gas inlet opens onto the inlet end face.