A mechanical separator for separating a fluid sample into first and second phases within a collection container is disclosed. The mechanical separator may have a separator body having a through-hole defined therein, with the through-hole adapted for allowing fluid to pass therethrough. The separator body includes a float, having a first density, and a ballast, having a second density greater than the first density. A portion of the float is connected to a portion of the ballast. Optionally, the float may include a first extended tab adjacent a first opening of the through-hole and a second extended tab adjacent the second opening of the through-hole. In certain configurations, the separator body also includes an extended tab band disposed about an outer surface of the float. The separator body may also include an engagement band circumferentially disposed about at least a portion of the separator body.

A device for separating immiscible fluids of different densities from a liquid-containing emulsion, includes a longitudinal rotary drum having a longitudinal axis of rotation. The drum includes, longitudinally from upstream to downstream and between at least one upstream inlet and downstream outlets: a solid body rotation stage having an inlet and including at least one longitudinal inner partition for causing circumferential solid body rotation; a migration and coalescence stage including at least one longitudinal partition for causing circumferential solid body rotation, the partition delimiting at least one longitudinal channel communicating with the solid body rotation stage; and an extraction stage including at least one liquid outlet that has an overflow edge and extends along a longitudinal flow space communicating with the migration and coalescence stage via at least one longitudinal passage, and including a downstream liquid discharge space communicating with the outlet and connected to a downstream discharge port.

A method for protein isolation as a co-product of alcohol production is disclosed. The method includes receiving grain product at a holding receptacle, the grain product being at least one of whole stillage, dried distillers grain, and wet distillers grain. The method further includes directing the grain product from the holding receptacle over a plurality of screens, thereby allowing a fiber-containing portion to be collected on the screens and further allowing a protein-containing portion and an oil-containing portion to pass through the screens. The method further includes directing the protein-containing portion and the oil-containing portion optionally over a finishing screen, thereby allowing remaining fiber fractions to be collected on the finishing screen and further allowing the protein-containing and oil-containing portion to pass through the finishing screen. Further, the method includes centrifuging the protein-containing portion and the oil-containing portion for isolating a protein fraction and an oil, water, sugar and minerals fraction.

The present invention relates to a tubular oil separator providing separation of respective fluid components mixed in fluids from oil wells, wherein the tubular oil separator A is arranged to mitigate problems related to turbulence and possible non-Newtonian fluid behaviors of fluid components mixed in the fluids from the oil wells in the oil separator. The invention further relates to a method of operating a separator. Moreover the invention relates to a system of multiple separators. Inventive aspects of the separator comprises an elongated outer, closed tubular section and an elongated, inner tubular section, which is closed in one end and open in another end, —where the inner tubular section is arranged inside the outer tubular section, —and where oil well substances are introduced into the open end of the inner tubular section via a tube feed section passing through the outer tubular section and into the inner tubular section, —and where the inner tubular section comprises multiple, elongated and parallel slots arranged in a longitudinal direction of the inner tubular section in a circumferential manner, —where the inclination of the separator facilitates separation of the oil well substances into lower density substances and higher density substances, —where the lower density substances by buoyancy drift upward through the slots and exit via an upper outlet in the outer tubular section and higher density substances sink downward through the slots and by gravitation exit via a lower outlet in the outer tubular section.

A fluid treatment system, a fluid processing apparatus and a method of treating a mixture are provided in which a separator has two outlets for different components of mixed fluid. A conduit connecting one of the outlets of the separator to the inlet of the separator is provided to recycle fluid from an outlet of the separator back to the inlet and a pump at the inlet of the separator regulates the fluid flow through the separator at a constant rate. As a result, the flow rate through the separator is increased, which increases the separation efficiency of the separation system. The conduit also functions as a bypass line should the flow of fluid be obstructed through the separator. The conduit may preferably be operated in conjunction with an energy harvester.

Method for control of an inner tube of an inclined tubular separator, wherein the inner tube is provided with an outlet adapted the viscosity of oil introduced into the inner tube.

A centrifugal, liquid-liquid separator relies on a sweep flow in excess of the flow rate naturally occurring in the heavy constituent or species being separated out from a lighter species, in order to prevent access by the long-chain polymers of the lighter species to solids that may separate out and make a durable composition of polymers and particles that adheres and compacts against the shell wall of the centrifuge.

Sterilization of a liquid substance is performed by causing cavitation in the liquid substance by stirring the liquid substance with a rotary blade of a suction stirring pump and generating plasma with a plasma generation mechanism in air bubbles generated in the liquid substance by the cavitation.

A separation system including a control unit, a first pump connected to the control unit, and a first valve in fluid communication with the first pump and connected to the control unit. Also, a first density meter in fluid communication with the first valve and connected to the control unit. The system further includes a separator in fluid communication with the density meter and connected to the control unit and a tank in fluid communication with the separator. The system also includes a second pump in fluid communication with the tank and connected to the control unit, as well as a second density meter in fluid communication with the second pump and connected to the control unit and a second valve in fluid communication with the second density meter and connected to the control unit.

A method to remove oil from an oily water stream includes the step of pressure controlling a release of dissolved gases from the stream as the stream passes through two or more stages of gas flotation treatment. The operating pressure of the first stage of flotation treatment is purposefully reduced relative to that of an upstream unit so that a certain controlled percent volume of dissolved gases is released. The operating pressure of the second stage of flotation treatment is then purposefully reduced relative to that of the first stage so that another controlled percent volume of dissolved gases is released. Any subsequent flotation treatment stage is at a lower operating pressure than that of the previous stage so that the subsequent treatment stage releases a controlled percent volume of dissolved gases. By controlling the operating pressure in this way, overall separation performance is improved.