Abstract: A method is provided for producing vacuum in a vacuum oil-stock distillation column and includes pumping a gas-vapor medium out of a column by an ejector into a condenser; feeding a gas mixture and a high-pressure gas into a second gas-gas ejector from which the vapor-gas mixture is fed into a second condenser. A condensate is directed from the condensers into a separator in which the condensate is separated into a water-containing condensate and a hydrocarbon-containing condensate. The hydrocarbon-containing condensate is removed while the water-containing condensate is fed into a steam generator in which heat is supplied to the water-containing condensate from a hot distillate removed from the vacuum column and steam is produced from the water-containing condensate, the steam is fed as a high-pressure gas into the gas-gas ejectors. A plant for carrying out the method is also provided.

Abstract: The invention relates to the oil processing industry and can be used for producing vacuum in a vacuum petroleum distillation column. The inventive method involves pumping out a vapor-gas medium from the column by of a gas-gas ejector in such a way that a vapor-gas mixture is formed at the entry thereof and supplying said mixture to a condenser for producing a gas mixture and a vapor phase condensate. The gas mixture is supplied from the condenser to a liquid-gas jet apparatus and the condensate is delivered to an additional separator. A hydrocarbon-containing condensate is removed from the additional separator for the intended use thereof and a water-containing condensate is fed to a steam generator for producing steam by supplying heat of a hot distillate evacuated from the vacuum column. The thus obtained steam is used in the gas-gas ejector as a high-pressure gas.

Abstract: A method is provided for producing vacuum in a vacuum oil-stock distillation column and includes pumping a gas-vapor medium out of a column by an ejector into a condenser; feeding a gas mixture and a high-pressure gas into a second gas-gas ejector from which the vapour-gas mixture is fed into a second condenser. A condensate is directed from the condensers into a separator in which the condensate is separated into a water-containing condensate and a hydrocarbon-containing condensate. The hydrocarbon-containing condensate is removed while the water-containing condensate is fed into a steam generator in which heat is supplied to the water-containing condensate from a hot distillate removed from the vacuum column and steam is produced from the water-containing condensate, the steam is fed as a high-pressure gas into the gas-gas ejectors. A plant for carrying out the method is also provided.

Abstract: A method for cleaning hydrocarbons from a gas-vapor medium ejected to the atmosphere, formed while storing oil or gasoline or filling a container therewith is provided. The medium is pumped out and compressed in a gas-liquid jet apparatus due to energy of oil or gasoline supplied by a pump. The formed mixture is separated in a separator, where a pressure of 0.7 to 2.5 MPa is maintained, and gas from the separator is compressed in a jet apparatus by oil or gasoline supplied by a pump. The gas medium cleaned from the hydrocarbons is outputted and the saturated absorbent is directed to a desorber where a pressure is generated to be lower than the pressure in the separator. The liquid medium is removed from the separators and to a container or to a storage tank from which oil or gasoline is simultaneously supplied to pump inlets or to the separators.

Abstract: The invention relates to the oil processing industry and can be used for producing vacuum in a vacuum petroleum distillation column. The inventive method involves pumping out a vapour-gas medium from the column by means of a gas-gas ejector in such a way that a vapour-gas mixture is formed at the entry thereof and supplying said mixture to a condenser for producing a gas mixture and a vapour phase condensate. The gas mixture is supplied from the condenser to a liquid-gas jet apparatus and the condensate is delivered to an additional separator. A hydrocarbon-containing condensate is removed from the additional separator for the intended use thereof and a water-containing condensate is fed to a steam generator for producing steam by supplying heat of a hot distillate evacuated from the vacuum column. The thus obtained steam is used in the gas-gas ejector as a high-pressure gas.

Abstract: A method for cleaning hydrocarbons from a gas-vapor medium ejected to the atmosphere, formed while storing oil or gasoline or filling a container therewith is provided. The medium is pumped out and compressed in a gas-liquid jet apparatus due to energy of oil or gasoline supplied by a pump. The formed mixture is separated in a separator, where a pressure of 0.7 to 2.5 MPa is maintained, and gas from the separator is compressed in a jet apparatus by oil or gasoline supplied by a pump. The gas medium cleaned from the hydrocarbons is outputted and the saturated absorbent is directed to a desorber where a pressure is generated to be lower than the pressure in the separator. The liquid medium is removed from the separators and to a container or to a storage tank from which oil or gasoline is simultaneously supplied to pump inlets or to the separators.

Abstract: The invention relates to the field of petrochemistry, in particular to a method of compressing a gaseous hydrocarbon-containing medium, for example, different hydrocarbon gases including flares produced in the oil refining and petrochemical industries. A distillate of a rectifying column of an atmosphere-vacuum oil refining unit is fed as the fresh liquid working medium into a circulation loop of a liquid hydrocarbon-containing medium, which contains a liquid-gas jet device, a separator and a pump. The liquid hydrocarbon-containing medium is removed from the circulation loop to a cracking and rectifying unit in which the liquid hydrocarbon-containing medium is subjected to cracking with subsequent rectification in the rectifying column of that unit.

Abstract: The invention relates to the field of petrochemistry, in particular to a method of compressing a gaseous hydrocarbon-containing medium, for example, different hydrocarbon gases including flares produced in the oil refining and petrochemical industries. A distillate of a rectifying column of an atmosphere-vacuum oil refining unit is fed as the fresh liquid working medium into a circulation loop of a liquid hydrocarbon-containing medium, which contains a liquid-gas jet device, a separator and a pump. The liquid hydrocarbon-containing medium is removed from the circulation loop to a cracking and rectifying unit in which the liquid hydrocarbon-containing medium is subjected to cracking with subsequent rectification in the rectifying column of that unit.

Abstract: The invention relates to the field of petrochemistry, in particular to a method of compressing a gaseous hydrocarbon-containing medium, for example, different hydrocarbon gases including flares produced in the oil refining and petrochemical industries. A distillate of a rectifying column of an atmosphere-vacuum oil refining unit is fed as the fresh liquid working medium into a circulation loop of a liquid hydrocarbon-containing medium, which contains a liquid-gas jet device, a separator and a pump. The liquid hydrocarbon-containing medium is removed from the circulation loop to a cracking and rectifying unit in which the liquid hydrocarbon-containing medium is subjected to cracking with subsequent rectification in the rectifying column of that unit.

Abstract: The invention relates to the field of petrochemistry, in particular to a method of compressing a gaseous hydrocarbon-containing medium, for example, different hydrocarbon gases including flares produced in the oil refining and petrochemical industries. A distillate of a rectifying column of an atmosphere-vacuum oil refining unit is fed as the fresh liquid working medium into a circulation loop of a liquid hydrocarbon-containing medium, which contains a liquid-gas jet device, a separator and a pump. The liquid hydrocarbon-containing medium is removed from the circulation loop to a cracking and rectifying unit in which the liquid hydrocarbon-containing medium is subjected to cracking with subsequent rectification in the rectifying column of that unit.

Abstract: A vacuum-creating apparatus of the unit is provided with a pump and a separator, wherein the pump is connected at its inlet to the separator, a jet device is made as a liquid-gas device and is connected at its outlet, by means of a pressure main, to the separator and at its liquid input to an output of the pump, wherein the longitudinal axis of the jet device is positioned vertically, the permissible deviation from the vertical axis being .+-.15.degree., an outlet cross section of a liquid supply nozzle of the jet device is positioned at a height of from 5 m to 35 m above an inlet to the separator and an outlet section of the pressure main is positioned below the level of the liquid in the separator to form a hydraulic seal.

Abstract: A method for vacuum distillation includes separation of a liquid product delivered to a reservoir under vacuum into a vapour-gaseous phase and at least one liquid fraction, withdrawal of the vapour-gaseous phase from the reservoir using a vacuum-creating device, and subsequent separation of the vapour-gaseous phase into gas and a liquid phase by condensing performed directly in the vacumm-creating device. A portion of the liquid phase is used as a fluid working medium in the vacuum-creating device.An equipment for vacuum distillation includes a reservoir under vacuum conditions equipped with mains and a vacuum-creating device, which has an ejector, a separator and a pump, interconnected by mains.