Institut Francais Du Pe'trole

Ifp Energies Nouvelles

Institute Francais Du Petrole

Eni S.p.a.

Compagnie Francaise Des Petroles

Agip Petroli S.p.a.

Cogebio

Alexandre Rojey

Jean-charles Viltard

Joseph Larue

Jean-claude Collin

Joseph Y Larue

Etienne Lebas

Ari Minkkinen

Alain Grehier

Jean-Claude P Collin

Georges Cohen

Isabelle Prevost

Claude Ramet

Michel Thomas

Nicole Doerler

Eric Lenglet

Jacques Cheron

Reynald Bonneau

Thierry Palermo

Christophe Lermite

Jean-Pierre Durand

Fabrice Lecomte

Fabrice Giroudiere

Jean Falcimaigne

Stephane Bertholin

B&eacute;atrice Fischer

Pierre Capron

Anne-Sophie Delion

Francois Benoist

Jean-Charles Viltard

Henri Paradowski

Andre Sugier

Andre Deschamps

Annick Pucci

Pierre Boucot

Renaud Cadours

Yves Charron

Choua Cohen

Eric Lemaire

Maurice Cessou

Lionel Asselineau

Jacques Denis

Jerome Weill

Pierre-Louis Carrette

Nicolas Boudet

Regis Bonifay

Emmanuel Behar

Sophie Jullian

Pierre-Yves Martin

Gérard Martin

Béatrice Fischer

Eric Robert

Paul Bourgmayer

Stéphane Bertholin

Bernard Juguin, Deceased

Alain Prinzhofer

Jean-Paul Cariou

Beatrice Fischer

Jean Claude Collin

Jean-Claude Collin

Alain Barreau

Claude J Moreau

G&eacute;rard Renard

Fabrice Giroudière

A system for energy storage, in particular for mechanical energy, including a system for quasi-isothermal compression of a gas via a hydraulic fluid. The mechanical energy stored is then released by quasi-isothermal expansion of the gas. The system is also configured to store electrical energy, in particular from intermittent sources such as photovoltaic or wind energy. The storage of excess electrical energy can also be considered for use during consumption peaks.

Method and apparatus for storing mechanical energy by quasi-isothermal expansion and compression of a gas

Process for producing liquid hydrocarbons from a heavy feedstock such as biomass, carbon, lignite, or heavy petroleum residue comprising: A partial oxidation b) of the heavy feedstock, producing a synthesis gas SG1, with an H2/CO ratio&#x3c;1; A steam reforming c) of a light feedstock that comprises hydrocarbons having at most 4 carbon atoms, for the production of a synthesis gas SG2 with an H2/CO ratio&#x3e;3; A Fischer-Tropsch conversion into liquid hydrocarbons of a synthesis gas SG, mixture of at least a portion of SG1 and at least a portion of SG2, in proportions such that SG has an H2/CO ratio of between 1.2 and 2.5. The light feedstock comprises hydrocarbons having less than 10 carbon atoms C1-C10 are obtained from a pretreatment of the heavy feedstock and/or are produced in the Fischer-Tropsch stage and/or during a downstream hydrocracking stage.

Method of producing synthetic gas with partial oxidation and steam reforming

A method of deacidizing a gaseous effluent comprising acid compounds where the gaseous effluent is contacted in Cwith an adsorbent solution so as to obtain a gaseous effluent depleted in acid compounds and an absorbent solution laden with acid compounds, the absorbent solution being selected for its property of forming two separable phases when it has absorbed an amount of acid compounds and when it is heated. The absorbent solution laden with acid compounds is then heated in Eand Eso as to separate two fractions: a first absorbent solution fraction depleted in acid compounds and a second absorbent solution fraction enriched in acid compounds. These two fractions are then separated in BS. The second fraction is regenerated in Cso as to release part of the acid compounds, and the first absorbent solution fraction and the regenerated absorbent solution are recycled as absorbent solution.

Method of deacidizing a gas by means of an absorbent solution with fractionated regeneration through heating

A process for refining or pre-refining a crude oil P is described in which P is fractionated into several fractions, wherein partial oxidation of an asphaltenic residue R1 derived from P is carried out to produce a synthesis gas SG1 with an H/CO ratio of less than 1, steam cracking is carried out of an external light hydrocarbon fraction to produce a synthesis gas SG2 with a H/CO ratio of more than 3; SG1 and SG2 are mixed to produce a synthesis gas SG with a H/CO ratio in the range 1.2 to 2.5, and SG is converted by Fischer-Tropsch synthesis, then the waxes produced are converted into middle distillates. Preferably, a vacuum distillate VGO and/or a deasphalted oil DAO derived from P are hydrocracked mixed with the waxes. The invention also pertains to a facility for carrying out the process.

Process and facility for treatment of crude oil with asphaltenic residue conversion

The invention concerns a process for producing synthesis gas, SG, from hydrocarbons and/or recycled compounds. In the process: a stream comprising a first feed Fsupplemented with steam undergoes steam reforming in a multi-tube reactor-exchanger R having a shell and reaction tubes containing a steam reforming catalyst within the shell; the reaction tubes are heated by convection by circulating in the shell, in overall counter-current mode, a heating fluid HF external to the tubes, which fluid comprises a first combustion gas stream of a second feed F, then fluid HF is mixed, in 1 to 4 complementary combustion zones internal to the shell, with a third feed Fand a gas comprising oxygen, to increase the temperature of the HF, and then the mixture obtained circulates in R to heat the reaction tubes in a complementary manner; and SG is produced from the steam reforming effluent from Fand optionally part or all of the HF.

Process for producing synthesis gas by steam reforming in a reactor-exchanger

Process for the production of liquid hydrocarbons from a feedstock that comprises at least one elementary feedstock from the group of biomass, coal, lignite, petroleum residues, methane, and natural gas, comprising: at least one stage a) for gasification of the feedstock by partial oxidation and/or steam reforming to produce a synthesis gas SG; a stage b) for separating CO2 from SG and a portion of the effluent of the subsequent stage c); the mixing of a portion of the CO2 that is separated with a gas of an H2/CO ratio of more than 3; a stage c) for partial conversion with hydrogen, thermal or thermocatalytic, of the CO2 that is present in said first mixture according to the reaction: CO2+H2&#x2192;CO+H2O in a specific reaction zone that is separated from said gasification zone or zones; a stage d) for Fisher-Tropsch synthesis on a synthesis gas that comprises at least a portion of SG and at least a portion of the CO that is produced by the conversion of CO2 into hydrogen.

Process for the production of synthesis gas with conversion of CO2 into hydrogen

A cogeneration method and device by turbine, particularly by gas turbine, uses a compression section, at least one expansion section, and a combustion chamber. A combustion agent including oxygen is compressed in the compression section; in the combustion chamber, one combustion step is carried out under pressure with a mixture of combustion agent compressed with a fuel; at least some of the hot gases obtained by pressurized combustion are used to effect an exchange with an external facility; and at least one postcombustion step is carried out of a mixture of hot gases coming from combustion with a fuel, prior to the exchange, and at least one other postcombustion step of a mixture of hot gases, coming from the exchange, with a fuel, in order to obtain hot gases that are sent to the expansion section.

Cogeneration method and device using a gas turbine comprising a post-combustion chamber

For producing synthesis gas, SG, from a hydrocarbon feed and optionally from recycled compounds, F, a first feed Fsupplemented with steam undergoes steam reforming in a multi-tube reactor-exchanger R comprising a plurality of reaction tubes () containing a steam reforming catalyst and a shell containing said tubes, to produce a first synthesis gas SG; reaction tubes () are heated principally by convection by circulating a fluid HF in the shell external to said tubes, in which HF is a staged partial oxidation stream with oxygen of a second feed Fat a pressure in the range 0.5 to 12 MPa, to produce a second synthesis gas SG; and the synthesis gas SG is produced by mixing SGand SG

Process for producing synthesis gas by steam reforming and partial oxidation

A method for quantitative monitoring of a gas injected into a reservoir and likely to react chemically with the injection medium includes injecting into a reservoir a mixture of the potentially reactive gas to be quantified with a low proportion of a tracer gas whose chemical inertness is total, and in determining the variation with time of the initial proportion of reactive gas that may have disappeared through conversion, by measuring the concentration variation of the tracer gas in the mixture. The tracer gas is preferably selected from the rare gas family and from isotopes thereof, unlikely to be contaminated by contact of the mixture with the injection medium, and which have physical properties such as solubility in water or diffusion coefficients as close as possible to the gas injected. The method is applicable to monitoring of the evolution and conversion of a reactive gas such as carbon dioxide or methane, injected into an underground reservoir for example.

Method for quantitative monitoring of a gas injected in a reservoir in particular in a natural environment

The natural gas is deacidized by contacting in zonewith a solvent containing amine in aqueous solution. The gas is then dehydrated by contacting in zonewith a solvent very rich in amine. After the contacting operations, the solvent containing HS. and water is expanded in drum, then regenerated in column. Part of the regenerated solvent is sent to zone. Another part of the regenerated solvent is vacuum distilled in columnso as to produce an amine-rich solvent that is sent to zone

Natural gas deacidizing and dehydration method

The natural gas flowing in through lineis cooled, then expanded in turbine T. The liquid at the bottom of drum Dis the liquefied natural gas. The gas at the top of drum Dis compressed by compressor K, then fed into the treating plant using a Fischer-Tropsch process to convert the natural gas to natural gas liquid.

Natural gas liquefaction and conversion method

The natural gas is successively contacted in column CA with a relatively methanol-rich solvent flowing in through linethen with a relatively poor solvent flowing in through lineThe acid gas-containing solvent recovered through lineat the bottom of column CA is expanded through valves Vand Vto release acid gases through lineA fraction of the expanded solvent is distilled in column CR. The regenerated solvent obtained at the bottom of column CR is sent to the top of column CA through lineA second fraction of the expanded solvent is mixed with a solvent drawn off from column CR at an intermediate point between the bottom and the top of this column. This mixture of solvents is sent through lineinto column CA.

Natural gas deacidizing method

The invention relates to a method for decreasing the level of carbon dioxide present in the fumes discharged by a power generator burning a mixture of a combustive agent and of a fuel containing hydrocarbons, wherein a gaseous mixture comprising at least part of said combustive agent and at least part of said fumes is compressed, all or part of the carbon dioxide present in the compressed gaseous mixture is eliminated by absorption, a fuel is mixed with the gaseous mixture, the resulting mixture of fuel and gaseous mixture is burnt and the fumes from the combustion process are expanded. The invention also relates to a power generator for implementing said method.

Power generator with low CO2 emissions and associated method

The invention relates to a process for converting a synthesis gas into liquid hydrocarbons used in at least two reactors that are arranged in series and that contain a catalytic suspension of at least one solid catalyst in suspension in a liquid phase, in which said reactors are essentially perfectly mixed, the last reactor is at least in part fed by at least a portion of at least one of the gaseous fractions that are collected at the outlet of at least one of the other reactors, at least one reactor is fed by a flow of catalytic suspension that is obtained directly from another reactor, and at least one flow of catalytic suspension that is obtained from a reactor is at least in part separated so as to obtain a liquid product that is essentially free of catalyst and a catalytic suspension that is high in catalyst, which is recycled.

Process for converting synthesis gas in reactors that are arranged in series

Installation for the production of synthesis gas from a hydrocarbon feedstock comprising at least one reactor for steam reforming, at least one reactor for converting COthat is equipped with at least one feed means by the effluent that is obtained from the steam reforming and at least one other feed means by a gas comprising carbon dioxide, characterized in that at least one reactor for steam reforming or for converting COis heated by a hot gas.

Installation and process for the production of synthesis gas comprising a reactor for steam reforming and a reactor for converting CO2 heated by a hot gas

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Rueil Malmaison, France

Alexandre Rojey