BRPI0416327A - method and installation for enriching a gas stream with one of the components thereof - Google Patents

method and installation for enriching a gas stream with one of the components thereof

Info

Publication number
BRPI0416327A
BRPI0416327A BRPI0416327-3A BRPI0416327A BRPI0416327A BR PI0416327 A BRPI0416327 A BR PI0416327A BR PI0416327 A BRPI0416327 A BR PI0416327A BR PI0416327 A BRPI0416327 A BR PI0416327A
Authority
BR
Brazil
Prior art keywords
fraction
enriching
components
installation
gas stream
Prior art date
Application number
BRPI0416327-3A
Other languages
Portuguese (pt)
Inventor
Patrick Le Bot
Xavier Pontone
Original Assignee
Air Liquide
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Air Liquide filed Critical Air Liquide
Publication of BRPI0416327A publication Critical patent/BRPI0416327A/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/0446Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the heat generated by mixing two different phases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04248Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
    • F25J3/04284Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
    • F25J3/0429Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams of feed air, e.g. used as waste or product air or expanded into an auxiliary column
    • F25J3/04303Lachmann expansion, i.e. expanded into oxygen producing or low pressure column
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/0446Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the heat generated by mixing two different phases
    • F25J3/04466Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the heat generated by mixing two different phases for producing oxygen as a mixing column overhead gas by mixing gaseous air feed and liquid oxygen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04551Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the metal production
    • F25J3/04557Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the metal production for pig iron or steel making, e.g. blast furnace, Corex
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04593The air gas consuming unit is also fed by an air stream
    • F25J3/046Completely integrated air feed compression, i.e. common MAC
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763Start-up or control of the process; Details of the apparatus used
    • F25J3/04769Operation, control and regulation of the process; Instrumentation within the process
    • F25J3/04812Different modes, i.e. "runs" of operation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/04Processes or apparatus using separation by rectification in a dual pressure main column system
    • F25J2200/06Processes or apparatus using separation by rectification in a dual pressure main column system in a classical double column flow-sheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2235/00Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
    • F25J2235/42Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being nitrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2235/00Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
    • F25J2235/50Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being oxygen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2240/00Processes or apparatus involving steps for expanding of process streams
    • F25J2240/40Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval
    • F25J2240/42Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval the fluid being air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2250/00Details related to the use of reboiler-condensers
    • F25J2250/30External or auxiliary boiler-condenser in general, e.g. without a specified fluid or one fluid is not a primary air component or an intermediate fluid
    • F25J2250/40One fluid being air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2250/00Details related to the use of reboiler-condensers
    • F25J2250/30External or auxiliary boiler-condenser in general, e.g. without a specified fluid or one fluid is not a primary air component or an intermediate fluid
    • F25J2250/42One fluid being nitrogen

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Blast Furnaces (AREA)
  • Sampling And Sample Adjustment (AREA)

Abstract

"MéTODO E INSTALAçãO PARA ENRIQUECIMENTO DE UMA CORRENTE DE GáS COM UM DOS COMPONENTES DO MESMO". A invenção se refere a um método de enriquecimento de uma corrente de gás pressurizado (1) com um dos componentes (A) da mesma. O método inventivo compreende as etapas a seguir: a corrente é separada em pelo menos uma primeira e uma segunda frações (2, 3) pelo menos uma parte da primeira fração (2) é enviada para uma unidade de separação (ASU); a unidade de separação supre pelo menos duas descargas, incluindo uma primeira descarga (10) que tem um teor de A maior do que aquele da fração (2) suprida para a unidade de separação; pelo menos uma parte da primeira descarga (10) é misturada com pelo menos uma parte da segunda fração (3), de modo a formar uma mistura de gás pressurizado (15); a segunda fração (3) é expandida e, subseqüentemente, pelo menos uma parte da primeira descarga (10) é misturada ali."METHOD AND INSTALLATION FOR ENRICHING A GAS CURRENT WITH ONE OF THE SAME COMPONENTS". The invention relates to a method of enriching a pressurized gas stream (1) with one of its components (A). The inventive method comprises the following steps: the stream is separated into at least a first and a second fraction (2, 3) at least a portion of the first fraction (2) is sent to a separation unit (ASU); the separation unit supplies at least two discharges, including a first discharge (10) having an A content greater than that of the fraction (2) supplied to the separation unit; at least a portion of the first discharge (10) is mixed with at least a portion of the second fraction (3) to form a pressurized gas mixture (15); the second fraction (3) is expanded and subsequently at least a portion of the first discharge (10) is mixed there.

BRPI0416327-3A 2003-11-10 2004-11-05 method and installation for enriching a gas stream with one of the components thereof BRPI0416327A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0350819A FR2862004B3 (en) 2003-11-10 2003-11-10 METHOD AND INSTALLATION FOR ENRICHING A GASEOUS FLOW IN ONE OF ITS CONSTITUENTS
PCT/FR2004/050570 WO2005047790A2 (en) 2003-11-10 2004-11-05 Method and installation for enriching a gas stream with one of the components thereof

Publications (1)

Publication Number Publication Date
BRPI0416327A true BRPI0416327A (en) 2007-01-09

Family

ID=34508749

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0416327-3A BRPI0416327A (en) 2003-11-10 2004-11-05 method and installation for enriching a gas stream with one of the components thereof

Country Status (7)

Country Link
US (2) US20080034790A1 (en)
EP (1) EP1697690A2 (en)
JP (1) JP2007512491A (en)
CN (1) CN100543388C (en)
BR (1) BRPI0416327A (en)
FR (1) FR2862004B3 (en)
WO (1) WO2005047790A2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2884305A1 (en) * 2005-04-08 2006-10-13 Air Liquide Carbon dioxide separating method for iron and steel industry, involves receiving flow enriched in carbon dioxide from absorption unit, sending it towards homogenization unit and subjecting carbon dioxide to intermediate compression stage
CZ302279B6 (en) * 2005-07-04 2011-01-26 Cervenka@Jan Balancing method of fluctuating concentration of component or components in flowing gas
FR2960555A1 (en) * 2010-05-31 2011-12-02 Air Liquide Integrated installation comprises an air separation apparatus, a blast furnace, a unit for preheating the air, an adiabatic air compressor, a first pipe to introduce the air towards the preheating unit, and a unit for heating water
US20130000352A1 (en) * 2011-06-30 2013-01-03 General Electric Company Air separation unit and systems incorporating the same
US9920987B2 (en) * 2015-05-08 2018-03-20 Air Products And Chemicals, Inc. Mixing column for single mixed refrigerant (SMR) process

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3126265A (en) * 1964-03-24 Process and apparatus for separating
US3731495A (en) * 1970-12-28 1973-05-08 Union Carbide Corp Process of and apparatus for air separation with nitrogen quenched power turbine
IT961138B (en) * 1971-02-01 1973-12-10 Air Liquide PLANT FOR COMPRESSING A FLUID BY EXPANSION OF ANOTHER FLUID
LU70847A1 (en) * 1973-09-25 1975-01-02
JPS61139609A (en) * 1984-12-13 1986-06-26 Kawasaki Steel Corp Oxygen enriching method of industrial furnace
FR2677667A1 (en) * 1991-06-12 1992-12-18 Grenier Maurice METHOD FOR SUPPLYING AN OXYGEN-ENRICHED AIR STOVE, AND CORRESPONDING IRON ORE REDUCTION INSTALLATION.
FR2680114B1 (en) * 1991-08-07 1994-08-05 Lair Liquide METHOD AND INSTALLATION FOR AIR DISTILLATION, AND APPLICATION TO THE GAS SUPPLY OF A STEEL.
FR2712383B1 (en) * 1993-11-12 1995-12-22 Air Liquide Combined installation of a metal production unit and an air separation unit.
US5454227A (en) * 1994-08-17 1995-10-03 The Boc Group, Inc. Air separation method and apparatus
FR2753638B1 (en) * 1996-09-25 1998-10-30 PROCESS FOR SUPPLYING A GAS CONSUMER UNIT
FR2758621B1 (en) * 1997-01-22 1999-02-12 Air Liquide METHOD AND INSTALLATION FOR SUPPLYING AN AIR GAS CONSUMER UNIT
FR2774158B1 (en) * 1998-01-23 2000-03-17 Air Liquide COMBINED INSTALLATION OF AN OVEN AND AN AIR DISTILLATION APPARATUS AND METHOD OF IMPLEMENTING IT
FR2774159B1 (en) * 1998-01-23 2000-03-17 Air Liquide COMBINED INSTALLATION OF AN OVEN AND AN AIR DISTILLATION APPARATUS AND METHOD OF IMPLEMENTING IT
US5979183A (en) * 1998-05-22 1999-11-09 Air Products And Chemicals, Inc. High availability gas turbine drive for an air separation unit
FR2814178B1 (en) * 2000-09-18 2002-10-18 Air Liquide SUPPLY OF OXYGEN-ENRICHED AIR TO A NON-FERROUS METAL PRODUCTION UNIT
US6568207B1 (en) * 2002-01-18 2003-05-27 L'air Liquide-Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Integrated process and installation for the separation of air fed by compressed air from several compressors
US20060266048A1 (en) * 2005-05-27 2006-11-30 Bell Leonard E Fluid catalytic cracking flue gas utility optimizing system and process

Also Published As

Publication number Publication date
EP1697690A2 (en) 2006-09-06
CN100543388C (en) 2009-09-23
US20110192193A1 (en) 2011-08-11
WO2005047790A2 (en) 2005-05-26
JP2007512491A (en) 2007-05-17
CN1878999A (en) 2006-12-13
US20080034790A1 (en) 2008-02-14
WO2005047790A3 (en) 2005-08-11
FR2862004B3 (en) 2005-12-23
WO2005047790A8 (en) 2006-06-01
FR2862004A1 (en) 2005-05-13

Similar Documents

Publication Publication Date Title
NO20060977L (en) Mitokinone derivatives used as mitochondrial mole-seeking antioxidants
BR9915687A (en) Composition comprising soy protein, dietary fibers and a phytoestrogen compound and its use in the prevention and / or treatment of cardiovascular diseases
BRPI0409068A (en) pharmaceutical compositions for hepatitis viral protease inhibitors c.
AR032932A1 (en) PROCEDURE TO PREPARE A LUBRICANT BASED OIL AND OIL GAS
MXPA05001061A (en) Aqueous 2,6-diisopropylphenol pharmaceutical compositions.
BR0306583A (en) Provision and synchronization of preferred travel list and travel indicator
AR032930A1 (en) PROCEDURE TO PREPARE AN OIL BASED OIL AND GAS OIL
BR0100017A (en) Pressure oscillation adsorption process (psa) for removing a preferred gas from a gas mixture
BRPI0512326A (en) compositions comprising amphotericin b, methods and systems
BRPI0404605A (en) aviation gasoline formulation
BRPI0416327A (en) method and installation for enriching a gas stream with one of the components thereof
GB2450666A (en) Method and apparatus for treating a hydrocarbon stream
ATE367810T1 (en) COMPOSITION FOR THE PREVENTION OF OSTEOPOROSIS CONSISTING OF A COMBINATION OF ISOFLAVONES AND POLYUNSATURATED FATTY ACIDS
NO20032441L (en) Combination of GABA agonists and sorbitol dehydrogenase inhibitors
BRPI0417672A (en) processes for producing storage stable virus compositions, virus and immunogenic compositions
BR0210113A (en) Stabilized dispersion of phytosterols in oil
WO2003009457A3 (en) Method and device for short-circuiting temporary power failures in a matrix converter
BR0306991A (en) Integrated process and installation for compressed air separation of multiple compressors
BR0318321A (en) emulsified composition and process for producing an emulsified composition
BR0309949A (en) Method and equipment for compressing a liquid-liquid extraction dispersion
MY112152A (en) Chromotographic simulated mobile bed separation process with dead volume correction using length reduction
BR0200713B1 (en) process and device for the decomposition of a gas mixture in a decomposition facility.
PE20001364A1 (en) USE OF INSAPPONABLE VEGETABLE OILS FOR THE PREPARATION OF A MEDICINAL PRODUCT THAT STIMULATES THE EXPRESSION OF TGF-ß OR THE EXPRESSION OF THE INHIBITOR PAI-1 OF THE PLASMINOGEN ACTIVATOR
BR0114772A (en) Process for selective hydrogenation of an olefin feed stream containing acetylenic and diolefin impurities
BRPI0700647A (en) olefin separation process

Legal Events

Date Code Title Description
B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE A 10A ANUIDADE.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 2278 DE 02/09/2014.