Provided is an assembly including a vessel having first and second ends and an interior, an inlet diverter disposed in the interior at the first end, at least one flow baffle disposed in the interior and having a gas section including a plurality of gas openings extending through the baffle, a liquid section below the gas section including a plurality of liquid openings extending through the baffle, and a bottom surface spaced from a bottom interior surface of the vessel to define a fluid flow path between the bottom surface and the bottom interior surface, and at least one vane section disposed in the interior downstream of the at least one flow baffle, the at least one vane section having a bottom surface spaced from the bottom interior surface of the vessel to define a fluid flow path between the bottom surface and the bottom interior surface.

A grease trap for separating waste from wastewater includes a tank having an outer wall, bottom and open top. An inlet invert in the tank receives incoming wastewater, and an outlet invert removes water from the tank. The tank has a cover on the open top, and the cover has a hatch. A barrier spans a diameter of the open top below the cover and has an opening vertically below the hatch. A divider divides the tank into an upper chamber and a lower chamber and has a hole for allowing FOG into the upper chamber from the lower chamber, the hole being colinearly aligned with the hatch and the opening in the barrier.

The present invention discloses an oil-contained wastewater treatment apparatus applying the integrative physical methods. The wastewater treatment system of the invention may include a main tank, where the upper part is a rectangular body and the lower part is designed to a multi-bucket bottom structure. Two oil collection boxes are arranged to both outside ends of tank. A mud discharging outlet is attached to the bottom of the tank. Meanwhile, both of a water outlet and an electric polarizer are localized at the end face of the effluent on the tank. A power supply for the electro-adsorber is fixed to the inlet end on the top face of the tank. Divided by upper and lower deflectors, the inside of the tank is divided to three processing units, i.e., sludge-water separation unit, degradation-coalescence treatment unit, and sedimentation-electric polarization unit. Vortex centripetal gas flotation is applied to remove oil. Electro-adsorption induces the micelle clustering to achieve the decolorization. The electric polarization functions as anti-scaling, descaling, sterilization, and corrosion inhibition. Moreover, the referred physical treatment can be fulfilled in virtue of centrifugal force, buoyancy, gravity, adsorption force, coalescence force, inertia, shifting, and modification. Through the application of the system, the oil-contained wastewater can be treated environmentally friendly, safe and pollution-free. Besides the above advantages, high removal efficiency can make the apparatus and method a widely used approach on the oil-contained wastewater treatment.

A flotation apparatus for separating oil from a dispersion containing water as a continuous phase and oil as a dispersed phase. The apparatus comprises a vessel having one or more longitudinal cell sections in its longitudinal direction, at least one of the one or more longitudinal cell sections comprising: an underflow weir, an overflow weir displaced downstream from the underflow weir, a gas injection structure located below the underflow weir or in the channel formed between the underflow weir and the overflow weir, a removal structure for removing a fraction formed during the operation of the flotation apparatus on the liquid level from the liquid level, and a hydraulic structure for hydraulically pushing the fraction formed during the operation of the flotation apparatus on the liquid level into the removal structure using a liquid stream, a liquid/gas stream and/or a gas stream that is ejected by the hydraulic structure.

Formation fluid sampled from within a wellbore is separated into gas and liquid fractions while downhole and in a wellbore. A separator vessel is used to isolate the gas and liquid fractions from one another. Baffles are arranged in a staggered formation within the separator vessel and in the path of the flow of the sampled formation fluid. Contact with the baffles perturbs the flow of sampled formation fluid, which promotes escape of the gas fraction from the fluid. The gas fraction is ported from an upper end of the sample vessel to a sample bottle for analysis. The liquid fraction collects in a lower end of the sample vessel, and is discharged into the wellbore.

Methods of separating a multiphase mixture are provided. The multiphase flow can include petrochemicals. The multiphase flow is flowed through a vane assembly having a plurality of curved passages. The multiphase mixture is gradually decelerated such that it collides with surfaces of the vane assembly at relatively oblique angles and at lower relative speeds. Such a configuration can reduce droplet breakup which, in turn, can preserve larger droplet sizes that are more likely to settle to a liquid bed below the inlet diverter due to gravity.

An effluent processing apparatus comprises a housing having an inlet port and a chamber. A coalescing element is located in the chamber and arranged coaxially with the inlet port. The coalescing element has pleats in a predefined pattern of paths arranged to separate oil and water from an effluent mixture containing air, oil, and water. The effluent mixture flows into the inlet port along an axis of the coalescing element. The effluent mixture is deflected by a portion of the housing to flow perpendicular to the axis along major surfaces of the pleats to separate oil and water from the effluent mixture.

A scum removal system for use with a wastewater treatment clarification tank containing wastewater is provided and includes a debris intake conduit, a debris discharge conduit, and a pump article. The pump article is configured to be in flow communication with the debris intake conduit and the debris discharge conduit, wherein the pump article and debris intake conduit are configured to generate a suction within the debris intake conduit and wherein the debris intake conduit is configured to be located proximate the wastewater. Additionally, the debris intake conduit is sloped downwardly at a debris intake conduit angle β, and the second discharge conduit is sloped downwardly at a debris discharge conduit angle Ω

Provided is a gas supply system for supplying hydrogen to a vehicle, the vehicle including: a tank loaded with a hydrogen storage alloy, storing and releasing hydrogen; and a thermal medium distribution unit attached to the tank and configured such that a thermal medium for heating or cooling the hydrogen storage alloy is distributable from outside, includes: a reservoir reserving hydrogen at a pressure of 0.2 MPa or greater and less than 3.0 MPa; a hydrogen flow path connectable to the vehicle for supplying hydrogen from the reservoir to the tank; a cooling medium reservoir reserving the thermal medium for cooling; and a thermal medium flow path connectable to the vehicle for distributing the thermal medium to the thermal medium distribution unit in the vehicle, in which the hydrogen flow path and the thermal medium flow path are combined at least at an end portion connectable to the vehicle.

Flotation separation apparatus and methods are described herein, comprising a vessel having a plurality of flow guides oriented vertically in the vessel, a liquid inlet at a lower part of the vessel, a gas inlet at the lower part of the vessel, a first liquid outlet at an upper part of the vessel, a second liquid outlet at the lower part of the vessel, and a gas outlet at the upper part of the vessel.