Individual biological cells can be selected in a micro-fluidic device and moved into isolation pens in the device. The cells can then be lysed in the pens, releasing nucleic acid material, which can be captured by one or more capture objects in the pens. The capture objects with the captured nucleic acid material can then be removed from the pens. The capture objects can include unique identifiers, allowing each capture object to be correlated to the individual cell from which the nucleic acid material captured by the object originated.

A refrigerant regenerating apparatus is disclosed. A refrigerant regenerating apparatus of the present disclosure includes: a regenerator into which a refrigerant flows and from which the refrigerant is discharged, the regenerator configured to separate and discharge oil contained in a refrigerant flowing in the regenerator; and a recoverer into which the refrigerant discharged from the regenerator flows, the recoverer including a compressor configured to compress a refrigerant flowing in the recoverer and a heat exchanger configured to condense a refrigerant discharged from the compressor, in which the regenerator includes: a charger configured to charge oil contained in the refrigerant flowing in the regenerator with positive ions or negative ions using corona discharge; and a collector configured to electrically collect the oil charged through the charger.

The present invention relates to a method for the break-up of at least one emulsion and separation of the light and heavy phase with at least an de-emulsification rate of more than 95% in only one apparatus (module) within less than 5 min by applying at least one time dependent or temporal changeable electrical field wherein the at least one electrical field is a high frequency (HF) singular alternating current (AC) field with an electrical field strength between 2,000 and 100,000 V/m and a frequency (HF) between 12,000 Hz and 200,000 Hz. The present invention relates furthermore to a method for the treatment of at least one emulsion by applying at least one direct current (DC) field and at least one high frequency alternating current—HF/AC field wherein the at least one DC field, in particular a pulsed DC-field, and the at least one HF/AC field are applied in series to the emulsion to be treated. The present invention refers further to a device for conducting said methods.

The present invention relates to a method for the break-up of at least one emulsion and separation of the light and heavy phase with at least an de-emulsification rate of more than 95% in only one apparatus (module) within less than 5 min by applying at least one time dependent or temporal changeable electrical field wherein the at least one electrical field is a high frequency (HF) singular alternating current (AC) field with an electrical field strength between 2,000 and 100,000 V/m and a frequency (HF) between 12,000 Hz and 200,000 Hz. The present invention relates furthermore to a method for the treatment of at least one emulsion by applying at least one direct current (DC) field and at least one high frequency alternating current—HF/AC field wherein the at least one DC field, in particular a pulsed DC-field, and the at least one HF/AC field are applied in series to the emulsion to be treated. The present invention refers further to a device for conducting said methods.

The invention relates to devices for purifying hydraulic and dielectric fluids (oils and fuels) of mechanical impurities and dissolved and dispersed water. It could be used in any fields where clean and contaminated fluids are used. The apparatus for reclaiming hydraulic and dielectric fluids comprises a vacuum tank with an atomizer, a vacuum pump, a dielectric fluid feed pump and dielectric fluid removal pump, all of said pumps being connected to the tank by pipes, and an electric filter, wherein the atomizer is disposed in the lower part of the vacuum tank, is arranged vertically with a spray member oriented upward and consists of a T fitting with a lower inlet for fluid and with a lateral inlet for air, a mixing chamber disposed above the T fitting, and a spray member with a nozzle, said spray member being disposed above the mixing chamber, and the electric filter comprises a housing with an inlet pipe and outlet pipe, a high-voltage power supply, a composite unit disposed inside the housing and consisting of current-carrying plates and dielectric spacers with apertures for current-carrying and heavy-duty fastening elements, a front plug and rear plug, and is current-carrying and heavy-duty fastening elements, wherein the surface of the current-carrying plates is provided with a porous ceramic dielectric coating. The technical result is increasing the efficiency of purifying and reclaiming dielectric fluids; increasing the useful volume of the vacuum tank without increasing the dimensions thereof; reducing the dispersivity of the fluid sprayed from the atomizer; simplifying the design; stabilizing the electromagnetic field of the electric filter; increasing the surface area of the electric filter by creating a developed surface of current-carrying filter elements without changing filter size and mass; improving reliability and ease of use; and reducing materials consumption.

There is disclosed an ion diffuser for generating ions, the ion diffuser comprising a cavity arranged to receive a substance; and a power source arranged to provide a current to the substance to cause the emission of ions from the substance.

There is disclosed an ion diffuser for generating ions, the ion diffuser comprising a cavity arranged to receive a substance; and a power source arranged to provide a current to the substance to cause the emission of ions from the substance.

Provided are systems and methods involving a plasma electro-coalescence reactor. The reactor includes a set of ports configured to receive an emulsified mixture into the reactor, receive a non-oxidative gas into the reactor, expel oil from the reactor, and expel water from the reactor. The reactor includes a set of electrodes including a first electrode in a headspace of the reactor, and a second electrode, the set of electrodes configured to receive a voltage at or in excess of a breakdown voltage of the non-oxidative gas.

An electrostatic coalescer apparatus for separating water from a crude oil emulsion comprises a vessel housing having a cavity, an inlet for receiving a crude oil emulsion and outlets for water and purified crude oil. First and second pairs of electrodes are positioned in the vessel cavity. A first Scott-T transformer circuit is coupled to the first pair of electrodes and a second Scott-T transformer circuit is coupled to the second pair of electrodes. The first and second Scott-T transformer circuit receive as an input a 3-phase power supply and output a 2-phase high voltage signal pairs of electrodes. The 2-phase voltage generated between the first pair of electrodes is of the same amplitude and phase as the voltage generated between the second pair of electrodes via the respective Scott-T transformer circuits. A method comprises steps performed during operation of the apparatus.

An electrostatic coalescer apparatus for separating water from a crude oil emulsion comprises a vessel housing having a cavity, an inlet for receiving a crude oil emulsion and outlets for water and purified crude oil. First and second pairs of electrodes are positioned in the vessel cavity. A first Scott-T transformer circuit is coupled to the first pair of electrodes and a second Scott-T transformer circuit is coupled to the second pair of electrodes. The first and second Scott-T transformer circuit receive as an input a 3-phase power supply and output a 2-phase high voltage signal pairs of electrodes. The 2-phase voltage generated between the first pair of electrodes is of the same amplitude and phase as the voltage generated between the second pair of electrodes via the respective Scott-T transformer circuits. A method comprises steps performed during operation of the apparatus.