PROCESS FOR DETERMINING THE INCOMPATIBILITY OF CRUDES MIXTURES CONTAINING ASPHALTENE

The present invention refers to a process based on density measurement of crudes mixtures of heavy and light crudes at constant temperature and pressure, using the vibrating tube densimeter technique in order to determine the incompatibility in the crudes mixture containing asphaltenes; wherein the...

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Hauptverfasser: Marco Antonio AQUINO OLIVOS, Juan Carlos CEDILLO RAMÍREZ, Blanca Estela GARCÍA FLORES, Verónica RAMOS CORZO, Adriana De Jesús AGUIRRE GUTIÉRREZ, José Luis MENDOZA DE LA CRUZ, Jacinto ÁGUILA HERNÁNDEZ
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creator Marco Antonio AQUINO OLIVOS
Juan Carlos CEDILLO RAMÍREZ
Blanca Estela GARCÍA FLORES
Verónica RAMOS CORZO
Adriana De Jesús AGUIRRE GUTIÉRREZ
José Luis MENDOZA DE LA CRUZ
Jacinto ÁGUILA HERNÁNDEZ
description The present invention refers to a process based on density measurement of crudes mixtures of heavy and light crudes at constant temperature and pressure, using the vibrating tube densimeter technique in order to determine the incompatibility in the crudes mixture containing asphaltenes; wherein the crudes mixture is preferably carried out at 10 to 22.3 DEG API and light crude of DEG API > 31.1, at a temperature of 293 to 423 K and pressure of 0.1 to 68.9 MPa. The crudes mixing process includes the procedure for determining the incipient point of asphaltenes incompatibility threshold in crudes mixture. The present invention uses a sample volume of 25 mL to measure the crudes mixture density and provides quick and reliable results with an uncertainty in the density measurement of 1 kg/m3. La presente invención se refiere a un proceso basado en la medición de la densidad de mezclas de crudos pesados con crudos ligeros a temperatura y presión constantes, usando la técnica de densimetría de tubo vibrante, para determinar la incompatibilidad en el mezclado de crudos que contienen asfaltenos; donde el mezclado de crudos preferentemente se realiza con crudo pesado de 10 a 22.3°API y crudo ligero de °API>31.1, a temperatura de 293 a 423 K y presión de 0.1 a 68.9 MPa. El proceso de mezclado de crudos incluye el procedimiento para determinar el punto incipiente del umbral de incompatibilidad de asfaltenos en la mezcla de crudos. La presente invención utiliza un volumen de muestra de 25 mL para medir la densidad de la mezcla de crudos y proporciona resultados rápidos y confiables, con una incertidumbre en la medición de la densidad de 1 kg/m3.
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The crudes mixing process includes the procedure for determining the incipient point of asphaltenes incompatibility threshold in crudes mixture. The present invention uses a sample volume of 25 mL to measure the crudes mixture density and provides quick and reliable results with an uncertainty in the density measurement of 1 kg/m3. La presente invención se refiere a un proceso basado en la medición de la densidad de mezclas de crudos pesados con crudos ligeros a temperatura y presión constantes, usando la técnica de densimetría de tubo vibrante, para determinar la incompatibilidad en el mezclado de crudos que contienen asfaltenos; donde el mezclado de crudos preferentemente se realiza con crudo pesado de 10 a 22.3°API y crudo ligero de °API&gt;31.1, a temperatura de 293 a 423 K y presión de 0.1 a 68.9 MPa. El proceso de mezclado de crudos incluye el procedimiento para determinar el punto incipiente del umbral de incompatibilidad de asfaltenos en la mezcla de crudos. 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The crudes mixing process includes the procedure for determining the incipient point of asphaltenes incompatibility threshold in crudes mixture. The present invention uses a sample volume of 25 mL to measure the crudes mixture density and provides quick and reliable results with an uncertainty in the density measurement of 1 kg/m3. La presente invención se refiere a un proceso basado en la medición de la densidad de mezclas de crudos pesados con crudos ligeros a temperatura y presión constantes, usando la técnica de densimetría de tubo vibrante, para determinar la incompatibilidad en el mezclado de crudos que contienen asfaltenos; donde el mezclado de crudos preferentemente se realiza con crudo pesado de 10 a 22.3°API y crudo ligero de °API&gt;31.1, a temperatura de 293 a 423 K y presión de 0.1 a 68.9 MPa. El proceso de mezclado de crudos incluye el procedimiento para determinar el punto incipiente del umbral de incompatibilidad de asfaltenos en la mezcla de crudos. La presente invención utiliza un volumen de muestra de 25 mL para medir la densidad de la mezcla de crudos y proporciona resultados rápidos y confiables, con una incertidumbre en la medición de la densidad de 1 kg/m3.</description><subject>ADHESIVES</subject><subject>CHEMISTRY</subject><subject>CRACKING HYDROCARBON OILS</subject><subject>DYES</subject><subject>FUELS</subject><subject>INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIRCHEMICAL OR PHYSICAL PROPERTIES</subject><subject>LUBRICANTS</subject><subject>MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FORELSEWHERE</subject><subject>MEASURING</subject><subject>METALLURGY</subject><subject>MINERAL WAXES</subject><subject>MISCELLANEOUS APPLICATIONS OF MATERIALS</subject><subject>MISCELLANEOUS COMPOSITIONS</subject><subject>NATURAL RESINS</subject><subject>PAINTS</subject><subject>PEAT</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PHYSICS</subject><subject>POLISHES</subject><subject>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</subject><subject>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</subject><subject>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</subject><subject>REFORMING OF NAPHTHA</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><subject>TESTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2018</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZAgJCPJ3dg0OVnDzD1JwcQ1xDfL19PP0c1cI8XBV8PRz9vcNcAzxdPL08QyJVPB3U3AOCnVxDVbw9YwICQ0CMpz9_UIcITocgwM8HH1CXP1ceRhY0xJzilN5oTQ3g5yba4izh25qQX58anFBYnJqXmpJvG-EsZmhoaWlkzFBBQBUuy-S</recordid><startdate>20181120</startdate><enddate>20181120</enddate><creator>Marco Antonio AQUINO OLIVOS</creator><creator>Juan Carlos CEDILLO RAMÍREZ</creator><creator>Blanca Estela GARCÍA FLORES</creator><creator>Verónica RAMOS CORZO</creator><creator>Adriana De Jesús AGUIRRE GUTIÉRREZ</creator><creator>José Luis MENDOZA DE LA CRUZ</creator><creator>Jacinto ÁGUILA HERNÁNDEZ</creator><scope>EVB</scope></search><sort><creationdate>20181120</creationdate><title>PROCESS FOR DETERMINING THE INCOMPATIBILITY OF CRUDES MIXTURES CONTAINING ASPHALTENE</title><author>Marco Antonio AQUINO OLIVOS ; Juan Carlos CEDILLO RAMÍREZ ; Blanca Estela GARCÍA FLORES ; Verónica RAMOS CORZO ; Adriana De Jesús AGUIRRE GUTIÉRREZ ; José Luis MENDOZA DE LA CRUZ ; Jacinto ÁGUILA HERNÁNDEZ</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_MX361199B3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; spa</language><creationdate>2018</creationdate><topic>ADHESIVES</topic><topic>CHEMISTRY</topic><topic>CRACKING HYDROCARBON OILS</topic><topic>DYES</topic><topic>FUELS</topic><topic>INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIRCHEMICAL OR PHYSICAL PROPERTIES</topic><topic>LUBRICANTS</topic><topic>MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FORELSEWHERE</topic><topic>MEASURING</topic><topic>METALLURGY</topic><topic>MINERAL WAXES</topic><topic>MISCELLANEOUS APPLICATIONS OF MATERIALS</topic><topic>MISCELLANEOUS COMPOSITIONS</topic><topic>NATURAL RESINS</topic><topic>PAINTS</topic><topic>PEAT</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PHYSICS</topic><topic>POLISHES</topic><topic>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</topic><topic>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</topic><topic>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</topic><topic>REFORMING OF NAPHTHA</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><topic>TESTING</topic><toplevel>online_resources</toplevel><creatorcontrib>Marco Antonio AQUINO OLIVOS</creatorcontrib><creatorcontrib>Juan Carlos CEDILLO RAMÍREZ</creatorcontrib><creatorcontrib>Blanca Estela GARCÍA FLORES</creatorcontrib><creatorcontrib>Verónica RAMOS CORZO</creatorcontrib><creatorcontrib>Adriana De Jesús AGUIRRE GUTIÉRREZ</creatorcontrib><creatorcontrib>José Luis MENDOZA DE LA CRUZ</creatorcontrib><creatorcontrib>Jacinto ÁGUILA HERNÁNDEZ</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>Marco Antonio AQUINO OLIVOS</au><au>Juan Carlos CEDILLO RAMÍREZ</au><au>Blanca Estela GARCÍA FLORES</au><au>Verónica RAMOS CORZO</au><au>Adriana De Jesús AGUIRRE GUTIÉRREZ</au><au>José Luis MENDOZA DE LA CRUZ</au><au>Jacinto ÁGUILA HERNÁNDEZ</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PROCESS FOR DETERMINING THE INCOMPATIBILITY OF CRUDES MIXTURES CONTAINING ASPHALTENE</title><date>2018-11-20</date><risdate>2018</risdate><abstract>The present invention refers to a process based on density measurement of crudes mixtures of heavy and light crudes at constant temperature and pressure, using the vibrating tube densimeter technique in order to determine the incompatibility in the crudes mixture containing asphaltenes; wherein the crudes mixture is preferably carried out at 10 to 22.3 DEG API and light crude of DEG API &gt; 31.1, at a temperature of 293 to 423 K and pressure of 0.1 to 68.9 MPa. The crudes mixing process includes the procedure for determining the incipient point of asphaltenes incompatibility threshold in crudes mixture. The present invention uses a sample volume of 25 mL to measure the crudes mixture density and provides quick and reliable results with an uncertainty in the density measurement of 1 kg/m3. La presente invención se refiere a un proceso basado en la medición de la densidad de mezclas de crudos pesados con crudos ligeros a temperatura y presión constantes, usando la técnica de densimetría de tubo vibrante, para determinar la incompatibilidad en el mezclado de crudos que contienen asfaltenos; donde el mezclado de crudos preferentemente se realiza con crudo pesado de 10 a 22.3°API y crudo ligero de °API&gt;31.1, a temperatura de 293 a 423 K y presión de 0.1 a 68.9 MPa. El proceso de mezclado de crudos incluye el procedimiento para determinar el punto incipiente del umbral de incompatibilidad de asfaltenos en la mezcla de crudos. La presente invención utiliza un volumen de muestra de 25 mL para medir la densidad de la mezcla de crudos y proporciona resultados rápidos y confiables, con una incertidumbre en la medición de la densidad de 1 kg/m3.</abstract><oa>free_for_read</oa></addata></record>
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language eng ; spa
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subjects ADHESIVES
CHEMISTRY
CRACKING HYDROCARBON OILS
DYES
FUELS
INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIRCHEMICAL OR PHYSICAL PROPERTIES
LUBRICANTS
MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FORELSEWHERE
MEASURING
METALLURGY
MINERAL WAXES
MISCELLANEOUS APPLICATIONS OF MATERIALS
MISCELLANEOUS COMPOSITIONS
NATURAL RESINS
PAINTS
PEAT
PETROLEUM, GAS OR COKE INDUSTRIES
PHYSICS
POLISHES
PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION
RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES
REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS
REFORMING OF NAPHTHA
TECHNICAL GASES CONTAINING CARBON MONOXIDE
TESTING
title PROCESS FOR DETERMINING THE INCOMPATIBILITY OF CRUDES MIXTURES CONTAINING ASPHALTENE
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-18T18%3A40%3A05IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-epo_EVB&rft_val_fmt=info:ofi/fmt:kev:mtx:patent&rft.genre=patent&rft.au=Marco%20Antonio%20AQUINO%20OLIVOS&rft.date=2018-11-20&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EMX361199B%3C/epo_EVB%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true