B01D19/0036

Upgrading of heavy residues by distillation and supercritical water treatment

A method of upgrading an overflash stream from a vacuum distillation unit comprising the steps of separating the overflash stream from an atmospheric residue stream, the overflash stream comprises an overflash fraction having a T10% between 475 and 530° C. and a T90% between 600 and 700° C.; introducing the reactor feed to a supercritical reactor at a temperature between 380° C. and 500° C. and a pressure between 25 MPa and 30 MPa; maintaining upgrading reactions in the supercritical reactor to upgrade the overflash fraction such that a reactor effluent comprises upgraded hydrocarbons relative to the overflash fraction; reducing a temperature of a reactor effluent in a cooling device to produce a cooled stream; reducing a pressure of the cooled stream in a depressurizing device to produce a discharged stream; and separating the discharged stream in a gas-liquid separator to produce a liquid phase product.

SUBSEA FLUID PROCESSING SYSTEM

A subsea fluid processing system which receives a wellstream flow. The subsea fluid processing system includes a pressure control device which regulates a pressure of the wellstream flow, a gas-liquid separator unit which receives the wellstream flow downstream of the pressure control device and which provides a liquid stream and a gas stream, a first membrane separator which receives the gas stream and which provides a retentate stream and a permeate stream, a compressor which receives the permeate stream and which provides a compressed permeate stream, and a discharge cooler which receives the compressed permeate stream and which provides a cooled compressed permeate stream for injection into a subsurface reservoir. A density of the cooled compressed permeate stream is higher than a density of the compressed permeate stream.

HYDROCARBON PRODUCTION AND STORAGE FACILITY
20180010312 · 2018-01-11 · ·

A subsea fluids storage facility comprises a tank for holding and separating fluids which is equipped with ballast capacity and a separable base to be deployed upon the seabed in shallow or deep water, and the storage facility is connectable to a surface production facility, especially a buoy for processing fluids. In deep water the tank is held at a depth above the base for temperature controlled stabilization of produced oil in the tank.

GAS-LIQUID SEPARATOR

The present invention provides a gas-liquid separator with enhanced performance and easy operation, capable of performing gas-liquid separation such as advanced defoaming or degassing, and with a structure that facilitates easy CIP cleaning and disassembly cleaning, allowing it to meet sanitary specifications. In the gas-liquid separator for gas-liquid separation performed by centrifugal force of an impeller mounted on a shaft which rotates in a casing provided with a suction inlet, a discharge outlet and an exhaust outlet, a separation impeller part carrying out gas-liquid centrifugal separation is formed around the rotating peripheral area of the impeller, a discharge impeller part providing discharge force to the passing fluid is formed by expanding an outer diameter of a part of the separation impeller part, the discharge outlet of the casing is disposed in a position opposite the discharge impeller part, the opening of the exhaust outlet to the inside of the casing is disposed in a position near the center of rotation of the impeller, a vacuum device is connected to the exhaust outlet, and the opening of the suction inlet to the inside of the casing is disposed in a position inwardly apart from the inner peripheral wall of the casing by a predetermined distance.

UREA PRODUCTION WITH TRIPLE MP STREAMS
20230227402 · 2023-07-20 ·

The disclosure pertains to a urea production plant and process using a high-pressure CO.sub.2 stripper, downstream medium-pressure treatment unit and a medium-pressure dissociator receiving urea synthesis solution from the reactor, wherein gas from the treatment unit and dissociator are condensed in a first condenser and off-gas from the synthesis section is condensed separately in a second condenser. A revamping method is also described.

Systems and methods for the preparation of tablets of botanical extracts including tea
11700863 · 2023-07-18 ·

The present invention includes a method for creating a portable and quickly dissolving tea or other tea-like botanical tablet that can be used to prepare a flavorful, visually appealing, and clear cup of tea. The novel process may include the steps of: (1) extraction/infusion, (2) clarification, (3) concentrate preparation, (4) degassing the concentrate, and (5) chunkification. A spinning cone column may be used during the extraction/infusion step to preserve the aromatics and nutrients from the tea leaves, leading to better taste and improved retention of compounds thought to be beneficial to human health. A centrifuge may be used to remove suspended solids during the clarification step and a pressure chamber or sonication device may be used during the degassing step. Chunkification may involve the freezing of the concentrate followed by the removal of water from the concentrate to create a solid tablet of easily portable shape and size. The tea tablet quickly dissolves when added to hot or warm water, and it dissolves in cold water with some additional agitation.

METHOD FOR DEGASSING A FLUID
20230017163 · 2023-01-19 ·

The invention relates to a method for degassing a fluid comprising the following steps: supplying, at the inlet of a reactor comprising at least one microfluidic conduit, a fluid which can comprise at least one dissolved gas; then causing the fluid to flow through the reactor, the at least one conduit comprising a portion having a reduced hydraulic diameter, and the flow being set such that bubbles are generated by micro-cavitation, the fluid then comprising a liquid phase and a gas phase, then allowing the at least partial transfer of the at least one dissolved gas present in the fluid of the liquid phase to the gas phase; separating the liquid phase and the gas phase; and recovering the liquid phase to obtain the degassed fluid, the method not involving the application of ultrasound to the fluid between the step in which the fluid is supplied to the reactor and the step of separating the liquid phase and the gas phase.

POST-PRINT VACUUM DEGASSING
20230016091 · 2023-01-19 ·

A degassing chamber for degassing a material located on a workpiece, comprises a vacuum source and a vacuum reservoir in fluid communication with the vacuum source, a secondary chamber, a port valve which is movable between an open position to allow passage of a workpiece therethrough between the exterior of the degassing chamber and the secondary chamber and a closed position in which the port valve is fluidly sealed, and a reservoir valve which is movable between an open position to provide fluid communication between the secondary chamber and the vacuum reservoir and a closed position in which the reservoir valve is fluidly sealed. The degassing chamber may be provided subsequent to a printing machine in a production line, and has particular application for degassing silicone material when producing fuel cells.

VACUUM EJECTOR SYSTEMS
20220410039 · 2022-12-29 ·

A vacuum generation system includes a main ejector having a first fluid inlet and a second fluid inlet. The second fluid inlet is configured and adapted to pull dissolved gases out of fuel. The system includes a plurality of fluid sources configured and adapted to be variably supplied to the first fluid inlet of the main ejector. A method of modulating pressure in an ejector to generate a vacuum includes supplying a fluid to an ejector from at least one of a plurality of fluid sources, and generating a vacuum with the ejector for removing dissolved gasses out of fuel.

Techniques for checking state of analyzers

An automated method for detecting and/or monitoring a state of a degasser of an analyzer is provided, the degasser including a container configured to be evacuated. The method includes obtaining a time series of values indicative of pressures inside the container. The time series spans a period during which the container is evacuated or pressurized. The method further includes determining a liquid level state of the degasser which is determined by an amount of liquid present in the container based on the time series.