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Patent

Separation of gas mixtures by partial condensation

TLDR
In this article, the authors present a process for the separation of a gas mixture at superatmospheric pressure by partial condensation at cryogenic temperatures, where the separated condensate and uncondensed vapor are passed back as returning streams in indirect countercurrent heat exchange relationship with the incoming feed mixture.
Abstract
In a process for the separation of a gas mixture at superatmospheric pressure by partial condensation at cryogenic temperatures and wherein the separated condensate and uncondensed vapor are passed back as returning streams in indirect countercurrent heat exchange relationship with the incoming feed mixture, the power required for providing the refrigeration and energy requirements for the separation are reduced by supplying said requirements by means of a heat pump alone or together with at least one separate refrigeration cycle and/or some Joule-Thomson expansion of the condensate, and in the heat pump a compressed multi-component gaseous medium is condensed by heat exchange with said returning streams over a first temperature range and then expanded by Joule-Thomson expansion, and the expanded condensate is evaporated by heat exchange with the feed gas mixture over a lower temperature range than said first temperature range, and recycled for recompression.

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Lng production using dual independent expander refrigeration cycles

TL;DR: In this paper, a process for producing a liquified natural gas stream that includes cooling at least a portion of a pressurized natural gas feed stream by heat exchange contact with first and second expanded refrigerants that are used in independent refrigeration cycles is described.
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Staged multicomponent refrigerant cycle for a process for recovery of C3+ hydrocarbons

TL;DR: In this article, a process for phase separating, dephlegmating and optionally distilling a feed gas stream to recover a light gas product and a heavy hydrocarbon product is presented.
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Monomer recovery in gas phase fluid bed olefin polymerization

TL;DR: In this paper, a gaseous stream was obtained by subjecting a portion of the effluent from the fluidized bed to a partial condensation, separating the liquid phase from the Gaseous phase obtained and employing the gas as the gas to purge unreacted monomer from the copolymer product.
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Process for recovery and purification of c3-c4+ hydrocarbons using segregated phase separation and dephlegmation

TL;DR: In this article, a low temperature phase separation, dephlegmation and distillation process is described for resolving a light hydrocarbon gas stream to recover and purify C3+ and/or C4+ hydrocarbons.
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Method For Cooling A Cryogenic Exchange Line

TL;DR: In this paper, the authors proposed a method for the cryogenic separation, the cooling or the liquefaction of a fluid using an exchange line, that comprises extracting from said exchange line at least one dual phase fluid (11), separating one vapour fraction (4) and one liquid fraction (5) in a phase separator (40), expanding at least 1 portion of the liquid fraction(5) using a first expansion means (60, 90), reinjecting, reheating and at least partially vaporising said expanded liquid fraction in the exchange line.
References
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Patent

Gas liquefaction by a fractionally condensed refrigerant

TL;DR: In this article, a gas stream is liquefied by indirect heat exchange with a multi-component refrigerant in a closed cooling cycle, and the refrigerant is fractionally condensed and the fractions are separately evaporated in the closed cycle to cool and liquefy the gas stream.
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Process for the liquefaction and subcooling of natural gas

TL;DR: In this article, a process for the liquefaction and subcooling of natural gas with a Claude closed refrigerating cycle is described, where the cycle medium is a mixture of nitrogen and methane.
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Rectification column with two component closed heat exchange cycle

TL;DR: In this paper, a rectification process for separating mixtures of individual components whose boiling temperatures or vapor pressure curves are far apart is described, where for the intensification of the rectification, the column adsorption layer is heated with circulating gas and the column head is cooled with a circulating gas; is characterized by having as the circulating gas a multicomponent mixture consisting of at least two individual components.
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Method and apparatus for recovering vapor

TL;DR: In this paper, a method and apparatus for recovering condensable vapor which is expelled from a container during filling by collecting and compressing the vapor after which the compressed vapor is cooled by cooling means.