Other

Kraftwerk Union Aktiengesellschaft

Siemens Aktiengesellschaft

Gerd Brunner

Siegfried Peter

Konrad Kunstle

Rainer Hoffmann

Konrad K/u/ Nstle

Jurgen Hoffmann

Rolf Riha

Dieter Stutzer

Till Dehrmann

Peter Siegfried

A process for the extraction of oils from oil-containing solid vegetable material by means of compressed gases, wherein said vegetable material is extracted with a mixture consisting of a supercritical gas and a subcritical entraining agent selected from the group consisting of propane, butane, pentane, ethanol, ethyl acetate, formaldehydedimethylacetal, CHF.sub.2 Cl and mixtures thereof, wherein the conditions of pressure, temperature and composition are selected so as to form a single fluid phase in said mixture of oil, supercritical gas and subcritical entraining agent, said extraction resulting in a loaded extractant which is separated from the extracted material in a separator and converted into an oil-rich liquid phase and a gaseous oil-exhausted phase in a regenerator by temperature increase and/or pressure decrease and said oil-rich phase and said oil-exhausted phase are separated and the oil-rich phase is pressure relieved, whereupon, if desired, the entraining agent remaining in the obtained oil is recovered.

Process for the extraction of oil containing vegetable materials

A process and system for low-temperature carbonization of oil shale, oil sands and similar oil-bearing solids includes low-temperature carbonization of oil-bearing solids in a high-pressure fluidized bed reactor in the presence of a substance selected from the group consisting of hydrogen and steam at temperatures substantially between 400.degree.and 600.degree. C. for producing low-temperature carbonization gas. The low-temperature carbonization gas is condensed in at least two stages for producing relatively higher boiling and relatively lower boiling oil fractions. The oil-bearing solids are peripherally mashed with the higher boiling oil fraction of the low-temperature carbonization gas, before introducing the oil-bearing solids into the high-pressure fluidized bed reactor. The oil-bearing solids mashed with the higher boiling oil fraction are returned to the high-pressure fluidized bed reactor.

Process and system for low-temperature carbonization of oil shale, oil

A process is disclosed of separating fine solids from oil in which the solids are dispersed which comprising contacting said oil with a combination of a compressed above-critical gas and an entraining agent at such temperature and such pressure that the system consisting of the oil, entraining agent and above-critical gas constitutes a single phase, withdrawing and separating the so-withdrawn phase into a liquid phase rich in oil and a gas phase lean in oil, the single-phase mixture of oil, entraining agent and above-critical gas from the solids.

Process for separating liquids from fine grained solids

Method of extracting liquid hydrocarbons from oil-containing stone or sand, wherein the oil-containing stone or the oil-containing sand undergoes hydrogenating, low temperature carbonization in a reactor at temperatures of 450.degree. to 520.degree. C. and a pressure of approximately 50 bar through the action of carbon monoxide, hydrogen and steam, and wherein the hydrocarbons are separated from the resulting gaseous, low temperature carbonization mixture. The low temperature carbonization mixture from the reactor is cooled in a first separation stage to a temperature of approximately 350.degree. C. to condense the less volatile hydrocarbons. The separated, liquid phase is fed to a solids separator and placed in contact with a circulating gas of carbon dioxide and a C.sub.6 /C.sub.7 hydrocarbon fraction. The low temperature carbonization mixture containing uncondensed gases and more volatile hydrocarbons are washed in a second separation stage with water and cooled to approximately 250.degree. C. Gas containing hydrogen separated from the volatile hydrocarbons is fed at least partly to the reactor again. Carbon monoxide is obtained from the solids through the action of carbon dioxide, contained in hot, combustion gases. This carbon monoxide together with carbon dioxide of the combustion gases is fed to the reactor.

Method of extracting hydrocarbons from oil-containing rock or sand

A process for extracting hydrocarbons from oil shale comprising the steps of subjecting oil shale under superatmospheric pressure in the presence of hydrogen and steam, to low temperature hydrogenating distillation; separating the resulting fluid distillation mixture into liquid and gaseous products; and returning water and hydrogen separated from the fluid distillation mixture to the low temperature distillation; in which:

Process and apparatus for extracting hydrocarbons from oil shale

An arrangement for extracting crude oil from oil shale comprising: a low temperature carbonization reactor; a processing means for feeding a slurry of oil shale, solvent and hydrogen into the low temperature carbonization reactor; a separating means for separating the resulting gaseous low temperature carbonization mixture from the used oil shale and for separating the low temperature carbonization mixture into gaseous and liquid low temperature carbonization products; a gas turbine the exhaust gas outlet of which is connected to two heat exchangers, one of which heat exchangers is disposed in a circulation system for a scavenging gas, which circulation system includes a separating reactor (which forms part of said separating means) in which in use the scavenging gas flows upwardly in counterflow to the oil shale for separation of the fluid low temperature carbonization mixture from the used oil shale, and the other of which heat exchangers is disposed between the low temperature carbonization reactor and said separating reactor; the low temperature carbonization reactor including a fluidizing cooler with a fluidized bed means for feeding used oil shale from the separating reactor to the fluidized bed and means for feeding turbine exhaust gas from either or both of said two heat exchangers to the fluidized bed for fluidizing the bed.

Plant for extracting crude oil from oil shale

The invention involves a process for substantially separating the components of mixtures of substances at least one of which is of low volatility while the other is of low or no volatility, the process using a compressed gas under supercritical conditions and an entrainer which increases the concentration of said mixture in the gaseous phase as well as the separation factor between the components to be separated. The process operates in two distillation zones the first of which substantially separates the components of low volatility in a process similar to a rectification process while the second distillation zone separates the top product of the first distillation zone from the gas with the aid of the entrainer which is condensed partially and in this state is passed in countercurrent to the gas carrying the separated component of low volatility.

Process for separating mixtures of substances of low volatility

The invention involves a process for the decaffeination of coffee, wherein--usually moistened--coffee is exposed to a circulating medium essentially composed of a compressed gas and an entrainer; this medium is subjected to partial condensation of the caffeine containing entrainer, in the absence of decompression; the caffeine is recovered from the condensate by evaporation of the entrainer portion thereof, and the medium is recycled to the coffee for continued extraction of caffeine therefrom.

Growing community of inventors

Roth, Germany

Gerd Brunner