DK2855638T3 - Fremgangsmåde til modernisering af et raffinaderi til konventionelle mineralolier til et bioraffinaderi - Google Patents

Fremgangsmåde til modernisering af et raffinaderi til konventionelle mineralolier til et bioraffinaderi Download PDF

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DK2855638T3
DK2855638T3 DK12773399.6T DK12773399T DK2855638T3 DK 2855638 T3 DK2855638 T3 DK 2855638T3 DK 12773399 T DK12773399 T DK 12773399T DK 2855638 T3 DK2855638 T3 DK 2855638T3
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unit
reactor
hydrodesulfurization
line
units
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DK12773399.6T
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Giacomo Fernando Rispoli
Claudia Prati
Andrea Amoroso
Paolo Pollesel
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Eni Spa
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/42—Catalytic treatment
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/50—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids in the presence of hydrogen, hydrogen donors or hydrogen generating compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/50—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids in the presence of hydrogen, hydrogen donors or hydrogen generating compounds
    • C10G3/52—Hydrogen in a special composition or from a special source
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/043—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a change in the structural skeleton
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4056—Retrofitting operations
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/10—Recycling of a stream within the process or apparatus to reuse elsewhere therein
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/49346—Rocket or jet device making

Claims (12)

1. Fremgangsmåde til modernisering af et raffinaderi, omfattende et system indeholdende to hydrodesulfuriseringssenheder, U1 og U2, i et bioraffinaderi, omfattende en produktionsenhed af carbonhydridfraktioner fra blandinger af biologisk oprindelse, indeholdende fedtsyreestere ved hjælp af deres hydro-deoxygenering og isomerisering, hvor enhver af hydrodesulfuriseringssenhederne U1 og U2 omfatter: - en hydrodesulfuriseringsreaktor (A1) til enheden U1 og (A2) til enheden U2, hvor reaktoren indeholder en hydrodesulfuriseringskatalysator; - en eller flere varmevekslere mellem råmaterialet og udledningen fra reaktoren; - et varmesystem til råmaterialet opstrøms for reaktoren; - en syregasbehandlingsenhed nedstrøms for reaktoren, indeholdende et absorberende middel (B) til H2S, T1 i enheden U1 og T2 i enheden U2, og hvor fremgangsmåden omfatter: - installere en ledning L mellem enhederne U1 og U2, som forbinder dem i serier; - installere en genanvendelsesledning af produktet til enheden U1 og muligvis til enheden U2, - erstatte hydrodesulfuriseringskatalysatoren i reaktoren A1 med en hydro-deoxygeneringskatalysator; - erstatte hydrodesulfuriseringskatalysatoren i reaktoren A2 med en isome-ringskatalysator; - installere en omløbsledning X af syregasbehandlingsenheden T2 af enheden U2; - erstatte det absorberende middel (B) i syregasbehandlingsenheden T1 med et specifikt absorberende middel til C02 og H2S.
2. Fremgangsmåde ifølge krav 1 til modernisering af et raffinaderi, omfattende et system indeholdende to hydrodesulfuriseringsenheder, U1 og U2, til et bioraffinaderi, omfattende en HDO/ISO-enhed, hvor enhver af hydrodesulfu-riseringsenhederne U1 og U2 omfatter: - en hydrodesulfuriseringsreaktor (A1) til enheden U1 og (A2) til enheden U2, hvor reaktoren indeholder en hydrodesulfuriseringskatalysator; - en eller flere varmevekslere mellem råmaterialet og udledningen fra reaktoren; - et varmesystem til råmaterialet opstrøms for reaktoren; - en syregasbehandlingsenhed nedstrøms for reaktoren, indeholdende et absorberende middel (B) til H2S, enheden kaldet T1 i enheden U1 og T2 i enheden U2, og hvor fremgangsmåden omfatter: - installere en ledning L mellem enhederne U1 og U2, som forbinder dem i serier; - installere en genanvendelsesledning af produktet til enheden U1 og muligvis til enheden U2, - erstatte hydrodesulfuriseringskatalysatoren i reaktoren A1 med en hydro-deoxygeneringskatalysator; - erstatte hydrodesulfuriseringskatalysatoren i reaktoren A2 med en isome-ringskatalysator; - installere en omløbsledning X af syregasbehandlingsenheden T2 af enheden U2, - erstatte det absorberende middel (B) i syregasbehandlingsenheden T1 med et specifikt absorberende middel til C02 og H2S; - installere en syregasbehandlingsenhed T3 nedstrøms for syregasbehandlingsenheden T1 for at adskille H2S; - genanvende H2S til reaktoren A1.
3. Fremgangsmåde ifølge krav 1 eller 2, hvor enhederne U1 og U2 anvendes, indeholdende hydrogengenanvendelsesledninger, som forbinder syre-gasbehandlingsenhederne T1 og T2 med reaktorerne A1 og A2.
4. Fremgangsmåde ifølge krav 1,2, eller 3, til modernisering af et raffinaderi, omfattende et system indeholdende to hydrodesulfuriseringssenheder, U1 og U2, i et bioraffinaderi, omfattende en produktionsenhed af carbonhydridfrak-tioner fra blandinger af biologisk oprindelse, indeholdende fedtsyreestere ved hjælp af deres hydrodeoxygenering og isomerisering, hvor enhver af hydro-desulfuriseringssenhederne U1 og U2 omfatter: - en hydrodesulfuriseringsreaktor (A1) til enheden U1 og (A2) til enheden U2, hvor reaktoren indeholder en hydrodesulfuriseringskatalysator; - en eller flere varmevekslere mellem råmaterialet og udledningen fra reaktoren; - et varmesystem til råmaterialet opstrøms for reaktoren; - en syregasbehandlingsenhed nedstrøms for reaktoren, indeholdende et absorberende middel (B) til H2S, T1 i enheden U1 og T2 i enheden U2, - en hydrogengenanvendelsesledning og en kompressor på ledningen, K1 til enheden U1 og K2 til enheden U2, og hvor fremgangsmåden omfatter: - installere en ledning L mellem enhederne U1 og U2, som forbinder dem i serier; - installere en genanvendelsesledning af produktet til enheden U1 og muligvis til enheden U2, - erstatte hydrodesulfuriseringskatalysatoren i reaktoren A1 med en hydro-deoxygeneringskatalysator; - erstatte hydrodesulfuriseringskatalysatoren i reaktoren A2 med en isome-ringskatalysator; - installere en omløbsledning X af syregasbehandlingsenheden T2 af enheden U2; - erstatte det absorberende middel (B) i syregasbehandlingsenheden T1 med et specifikt absorberende middel til C02 og H2S; - installere en syregasbehandlingsenhed T3 nedstrøms for syregasbehandlingsenheden T1; - installere en genanvendelsesledning R3 af H2S fra enheden T3 til kompressoren K1 af hydrogengenanvendelsesledningen af enhed U1.
5. Fremgangsmåde ifølge krav 4, hvor syregasbehandlingsenheden T3 indeholder to absorberende områder, som hver indeholder et specifikt absorberende middel til C02.
6. Fremgangsmåde ifølge krav 1, omfattende: - forbinde enheden U1 til en svovlgenvindingsenhed, indeholdende et ther-malområde og et katalytisk område gennem installationen, fra enhedenTI af U1, af en omløbsledning af det thermale område af svovlgenvindingsenheden; - erstatte katalysatoren af den første reaktor af det katalytiske område af svovlgenvindingsenheden med en kold selektiv redoxkatalysator.
7. Fremgangsmåde ifølge krav 1, hvor en væskeudskiller (S) installeres opstrøms for enhver af reaktorerne A1 og A2.
8. Fremgangsmåde ifølge krav 1, hvor enhederne U1 og U2, som indeholder højtryksseparatorer, lavtryksseparatorer, adskillelsessøjler og eventuelt tørringsindretninger, anvendes.
9. Fremgangsmåde ifølge krav 1, hvor enhederne U1 og U2 anvendes, indeholdende ledninger til forsyning af suppleringshydrogen, eventuelt efter blanding med genanvendt hydrogen, til enhver af reaktorerne (A1) og (A2) og/eller indeholdende gasadskillelse/vask nedstrøms for enhver af reaktorerne (A1) and (A2).
10. Fremgangsmåde ifølge krav 9, hvor hydrogenforsyningsledningerne kommer fra reformeringsenheder.
11. Fremgangsmåde ifølge et eller flere af de foregående krav, hvor carbon-hydridfraktionerne, som kan opnås fra bioraffinaderiet, er brændstoffer eller brændstofkomponenter.
12. Fremgangsmåde ifølge krav 11, hvor de brændstoffer eller brændstofkomponenter, som kan opnås fra bioraffinaderiet, er LPG, kerosin, diesel, naphta.
DK12773399.6T 2012-09-03 2012-09-04 Fremgangsmåde til modernisering af et raffinaderi til konventionelle mineralolier til et bioraffinaderi DK2855638T3 (da)

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IT001465A ITMI20121465A1 (it) 2012-09-03 2012-09-03 Metodo per convertire una raffineria convenzionale di oli minerali in una bioraffineria
PCT/IT2012/000268 WO2014033762A1 (en) 2012-09-03 2012-09-04 Method for revamping a conventional mineral oils refinery to a biorefinery

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US (2) US9845432B2 (da)
EP (2) EP2855638B1 (da)
CN (1) CN104704086B (da)
DK (1) DK2855638T3 (da)
ES (1) ES2550358T3 (da)
IT (1) ITMI20121465A1 (da)
MY (1) MY185369A (da)
PL (1) PL2855638T3 (da)
PT (1) PT2855638E (da)
RS (1) RS54242B1 (da)
RU (1) RU2607771C2 (da)
SG (1) SG11201501584TA (da)
WO (1) WO2014033762A1 (da)

Families Citing this family (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015181279A1 (en) * 2014-05-29 2015-12-03 Eni S.P.A. Biorefinery and method for revamping a conventional refinery of mineral oils into said biorefinery
EP3095839A1 (en) 2015-05-20 2016-11-23 Total Marketing Services Biodegradable hydrocarbon fluids by hydrogenation
EP3095838A1 (en) 2015-05-20 2016-11-23 Total Marketing Services Process for the production of biodegradable hydrocarbon fluids
CN105939288A (zh) * 2015-07-31 2016-09-14 杭州迪普科技有限公司 会话控制方法及装置
EP3331969B1 (en) * 2015-08-06 2020-06-17 Uop Llc Process for reconfiguring existing treating units in a refinery
EP3143981A1 (fr) 2015-09-16 2017-03-22 Total Marketing Services Composition émolliente biosourcée
IT201600075881A1 (it) * 2016-07-20 2018-01-20 Mph S R L Semplificata Metodo di conversione di raffinerie di petrolio convenzionali, di stabilimenti petrolchimici o chimici e di depositi di stoccaggio petroliferi in bioraffinerie di seconda e terza generazione integrate e multiprodotto.
EP3315590A1 (en) 2016-10-27 2018-05-02 Total Marketing Services Use of hydrocarbon fluids in electric vehicles
EP3315586A1 (en) 2016-10-27 2018-05-02 Total Marketing Services Use of biodegradable hydrocarbon fluids as heat-transfer media
EP3315592A1 (en) 2016-10-27 2018-05-02 Total Marketing Services Use of biodegradable hydrocarbon fluids as drilling fluids
EP3315587A1 (en) 2016-10-27 2018-05-02 Total Marketing Services Use of biodegradable hydrocarbon fluids for aluminium cold-rolling
EP3378463A1 (fr) 2017-03-20 2018-09-26 Total Marketing Services Utilisation non-therapeutique d'une huile hydrocarbonee biodegradable
EP3378464A1 (fr) 2017-03-20 2018-09-26 Total Marketing Services Composition gelifiee biosourcée
EP3378467A1 (fr) 2017-03-20 2018-09-26 Total Marketing Services Huile hydrocarbonee pour une utilisation therapeutique
FR3065961B1 (fr) 2017-05-02 2020-01-10 Total Marketing Services Fluxant biosource pour composition bitumineuse
US20180370871A1 (en) * 2017-06-22 2018-12-27 Uop Llc Process and apparatus for hydroisomerizing a hydroprocessed liquid stream
IT201700098243A1 (it) * 2017-09-01 2019-03-01 Water & Soil Remediation S R L Metodo per la conversione di un impianto petrolifero, petrolchimico o chimico convenzionale in una bioraffineria.
IT201700122279A1 (it) * 2017-10-27 2019-04-27 Water & Soil Remediation S R L Metodo per il recupero di una raffineria di petrolio dismessa.
FR3073228B1 (fr) 2017-11-09 2020-10-23 Total Marketing Services Composition lubrifiante pour engrenage
EP3483278B1 (en) * 2017-11-14 2020-06-17 Water & Soil Remediation S.r.l. Method for reusing components of disused oil facilities for biogas production
IT201800000312A1 (it) * 2018-01-03 2019-07-03 Water & Soil Remediation S R L Procedimento per ottenere bioraffinerie integrate di biomasse lignocellulosiche tramite ri-uso di unita' produttive di ex-raffinerie di petrolio.
SG10201803633UA (en) * 2018-04-30 2019-11-28 Green Technology Research Co Ltd Process using bio-based material and the products thereof
ES2927544T3 (es) 2018-05-30 2022-11-08 Totalenergies Onetech Belgium Producción de combustible diésel renovable en refinería de petróleo fósil adaptada para producir biocombustible y materia prima procedente de biomasa para unidades de craqueo con vapor de agua
CA3044153C (en) 2018-07-04 2020-09-15 Eavor Technologies Inc. Method for forming high efficiency geothermal wellbores
FR3083800B1 (fr) 2018-07-13 2020-12-25 Total Marketing Services Composition refroidissante et ignifugeante pour systeme de propulsion d'un vehicule electrique ou hybride
FR3083802B1 (fr) 2018-07-13 2021-02-12 Total Marketing Services Composition refroidissante et ignifugeante pour systeme de propulsion d'un vehicule electrique ou hybride
FR3083803B1 (fr) 2018-07-13 2020-07-31 Total Marketing Services Composition de refroidissement et ignifugeante pour systeme de propulsion d'un vehicule electrique ou hybride
FR3083801B1 (fr) 2018-07-13 2021-02-12 Total Marketing Services Composition de refroidissement et ignifugeante pour systeme de propulsion d'un vehicule electrique ou hybride
FR3091653B1 (fr) 2019-01-10 2023-01-13 Total Marketing Services Composition epaississante biosourcee
FR3092754B1 (fr) 2019-02-18 2022-06-03 Total Marketing Services Composition adjuvante pour vaccin
US10876050B2 (en) 2019-03-01 2020-12-29 Uop Llc Process for producing diesel fuel from a biorenewable feed
US11136514B2 (en) 2019-06-07 2021-10-05 Uop Llc Process and apparatus for recycling hydrogen to hydroprocess biorenewable feed
KR20220030946A (ko) * 2019-07-05 2022-03-11 할도르 토프쉐 에이/에스 저압 분리기로부터의 액체 재순환이 있는 옥시게네이트 공급원료의 수소화처리
US11549061B2 (en) * 2020-07-08 2023-01-10 Axens Process for hydroprocessing of biological feedstocks
WO2022013117A1 (en) 2020-07-15 2022-01-20 Totalenergies Marketing Services Lubricant composition for water-based compositions
KR20230051485A (ko) 2020-08-07 2023-04-18 토탈에너지스 원테크 유체의 제조를 위한 방법
US11248182B1 (en) * 2020-08-31 2022-02-15 Janus Technology Solutions, LLC Reduction of SOx and NOx emissions from renewable diesel plants
FR3124188A1 (fr) 2021-06-17 2022-12-23 Total Marketing Services Fluides hydrocarbones biosources
FR3134810A1 (fr) 2022-04-25 2023-10-27 Totalenergies Onetech Fluide de refroidissement biodegradable par immersion directe
FR3135462A1 (fr) 2022-05-13 2023-11-17 Totalenergies Onetech Fluides de barrage hydrocarbones biosources
FR3139346A1 (fr) 2022-09-07 2024-03-08 Totalenergies Onetech Diluant biosource pour extraction liquide-liquide de metaux pour le recyclage de batteries

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4992605A (en) 1988-02-16 1991-02-12 Craig Wayne K Production of hydrocarbons with a relatively high cetane rating
FR2783818B1 (fr) 1998-09-24 2000-11-10 Elf Exploration Prod Procede pour oxyder directement en soufre, par voie catalytique et en phase vapeur, l'h2s contenu a faible teneur dans un gaz
US6337059B1 (en) 1999-05-03 2002-01-08 Union Carbide Chemicals & Plastics Technology Corporation Absorbent compositions for the removal of acid gases from gas streams
KR100571731B1 (ko) * 2000-11-11 2006-04-17 할도르 토프쉐 에이/에스 개선된 수소화공정 방법 및 기존의 수소화공정 반응기를개장하는 방법
ATE356858T1 (de) 2002-09-06 2007-04-15 Neste Oil Oyj Vefahren zur herstellung einer kohlenwasserstoffkomponente biologischer herkunft
US20060264684A1 (en) 2005-05-19 2006-11-23 Petri John A Production of diesel fuel from biorenewable feedstocks
AU2006264899B2 (en) * 2005-07-04 2011-03-31 Neste Oil Oyj Process for the manufacture of diesel range hydrocarbons
US8278492B2 (en) 2005-07-05 2012-10-02 Neste Oil Oyj Process for the manufacture of diesel range hydrocarbons
ITMI20062193A1 (it) 2006-11-15 2008-05-16 Eni Spa Processo per produrre frazioni idrocarburiche da miscele di origine biologica
ITMI20070522A1 (it) 2007-03-16 2008-09-17 Eni Spa Composizione idrocarburica utile come carburante e combustibile contenente una componente petrolifera e una componente di origine biologica
JP4784569B2 (ja) 2007-07-13 2011-10-05 トヨタ自動車株式会社 分析装置用のガス導入装置のモニター装置
US20090077864A1 (en) 2007-09-20 2009-03-26 Marker Terry L Integrated Process of Algae Cultivation and Production of Diesel Fuel from Biorenewable Feedstocks
US7999143B2 (en) 2007-09-20 2011-08-16 Uop Llc Production of diesel fuel from renewable feedstocks with reduced hydrogen consumption
US7982075B2 (en) 2007-09-20 2011-07-19 Uop Llc Production of diesel fuel from biorenewable feedstocks with lower hydrogen consumption
US20090321311A1 (en) 2008-06-27 2009-12-31 Uop Llc Production of diesel fuel from renewable feedstocks containing phosphorus
US8283506B2 (en) * 2008-12-17 2012-10-09 Uop Llc Production of fuel from renewable feedstocks using a finishing reactor
US8686204B2 (en) * 2010-11-08 2014-04-01 Uop Llc Methods for co-processing biorenewable feedstock and petroleum distillate feedstock
BR112013014687B1 (pt) * 2010-12-16 2019-02-05 Energia Technologies, Inc. método de desoxigenação de hidrocarbonetos oxigenados

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