EP0489974B1 - Procédé pour diminuer la quantité de contaminants métalliques à partir d'huile hydrocarbonée - Google Patents
Procédé pour diminuer la quantité de contaminants métalliques à partir d'huile hydrocarbonée Download PDFInfo
- Publication number
- EP0489974B1 EP0489974B1 EP19900203247 EP90203247A EP0489974B1 EP 0489974 B1 EP0489974 B1 EP 0489974B1 EP 19900203247 EP19900203247 EP 19900203247 EP 90203247 A EP90203247 A EP 90203247A EP 0489974 B1 EP0489974 B1 EP 0489974B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- diameter
- hydrocarbon oil
- solid material
- pore volume
- process according
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
Classifications
-
- 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
- C10G25/00—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
- C10G25/003—Specific sorbent material, not covered by C10G25/02 or C10G25/03
-
- 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/16—Metal oxides
Definitions
- the present invention relates to a process for reducing the amount of metal(s)-containing solid contaminants present in a hydrocarbon oil containing such contaminants.
- hydrogen may be present, preferably together with a catalytically active metal.
- metal content of some other metals such as certain metals from Group 1a, 2a, 3a, 4a, 6b and/or 8 of the Periodic Table of the Elements such as given in the CRC Handbook of Chemistry and Physics, 63rd edition, e.g. sodium, calcium, iron and/or molybdenum, can be brought down to an acceptable level by removing solids containing such contaminating metals.
- Such process can be carried out without adding hydrogen to the process and at ambient temperature and atmospheric pressure. Solid contaminants having a relatively large diameter can be removed in a conventional desalting step.
- the present invention relates to a process for reducing the amount of metal(s)-containing solid contaminants present in a hydrocarbon oil containing such contaminants, which process comprises contacting the hydrocarbon oil with porous solid material having a pore volume of at least 0.05 ml/g in pores having a diameter of at least 15 microns, which process is carried out without adding hydrogen.
- the pore diameter in which a substantial amount of pore volume is preferred to be present depends on the diameter of the solid contaminants which are to be removed. Generally a pore volume of at least 0.05 ml/g in pores having a diameter of at least 15 microns is suitable. Preferably, a substantial pore volume, e.g. 0.03 ml/g, is present in pores having a diameter of at least 100 microns. Very suitable porous material to be used has a pore volume of at least 0.02 ml/g in pores having a diameter of at least 200 micons.
- the pore size distribution and pore volume of the material employed can be readily measured by the mercury intrusion method.
- the shape of the material is not critical and may take the form of spheres, hollow tubes, wheels, trilobes, quadrulobes, etc.
- the diameter of the porous solid material particles is between 0.50 and 60 mm, more preferably between 1 and 40 mm.
- the surface area of the porous solid material is not critical. However, due to the requirements on the pore diameter and pore volume, the porous material to be employed in the process according to the present invention will generally have a surface area of less than 2 m2/gram.
- Porous solid material to be used comprises e.g. silica, alumina and silica/alumina.
- Preferred materials comprise pumice stone and some commercially available catalyst carriers, e.g. as used in the preparation of ethylene oxyde catalysts. Suitable materials are mentioned in European patent specification 399.592, in which a hydrotreating process for the removal of suspended and dissolved (organo)metallic compounds has been described.
- the process can be carried out at ambient temperature and atmospheric pressure. If desired, the process can be carried out at a temperature up to 500 °C and a pressure up to 20,000 kPa (200 bar).
- the operating conditions which are preferred depend on the hydrocarbon oil which is subjected to the process. If for example a short residue, i.e. a residual hydrocarbon oil boiling above 520 °C, is to be subjected to the process of the present invention, the temperature and optionally pressure will be elevated due to the viscosity of such residue; suitable process conditions would comprise a temperature of between 200 and 350 °C and a pressure up to 8000 kPa (80 bar).
- a long residue, containing hydrocarbons boiling above 270 °C is preferably processed at a temperature of between 150 and 350 °C and a pressure up to 8000 kPa (80 bar).
- the amount of metal(s)-containing solid contaminants which is to be removed from the hydrocarbon oil by the present process can vary. Suitably, a substantial amount of the metal(s)-containing solid contaminants is removed.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Claims (7)
- Procédé pour réduire la quantité de contaminants solides contenant des métaux des groupes 1a, 2a, 3a, 4a, 6b et/ou 8 du Tableau Périodique des Eléments présente dans une huile d'hydrocarbures, lequel procédé comprend la mise en contact de l'huile d'hydrocarbures avec une matière solide poreuse ayant un volume de pores d'au moins 0,05 ml/g dans des pores ayant un diamètre de moins de 15 micromètres, ce procédé étant mis en oeuvre sans addition d'hydrogène.
- Procédé selon la revendication 1, dans lequel les contaminants solides comprennent du sodium, du calcium, du fer et/ou du molybdène.
- Procédé selon la revendication 1 ou 2, dans lequel la matière solide poreuse a un volume de pores d'au moins 0,03 ml/g dans des pores ayant un diamètre d'au moins 100 micromètres.
- Procédé selon l'une quelconque des revendications 1 à 3, dans lequel la matière solide poreuse a un volume de pores d'au moins 0,02 ml/g dans des pores ayant un diamètre d'au moins 200 micromètres.
- Procédé selon l'une quelconque des revendications 1-4, dans lequel la matière solide poreuse a un diamètre compris entre 0,5 et 60 mm.
- Procédé selon l'une quelconque des revendications 1-5, qui est mis en oeuvre à une température d'au maximum 500°C et une pression d'au maximum 200 bars.
- Procédé selon l'une quelconque des revendications 1-6, dans lequel on utilise une matière solide poreuse comprenant de la pierre ponce.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1990619527 DE69019527T2 (de) | 1990-12-10 | 1990-12-10 | Verfahren zur Verminderung des Gehaltes metallischer Verunreinigungen aus Kohlenwasserstofföl. |
EP19900203247 EP0489974B1 (fr) | 1990-12-10 | 1990-12-10 | Procédé pour diminuer la quantité de contaminants métalliques à partir d'huile hydrocarbonée |
CA 2056973 CA2056973A1 (fr) | 1990-12-10 | 1991-12-04 | Procede servant a reduire la quantite de contaminants metalliques dans l'huile minerale |
JP3349816A JP2997906B2 (ja) | 1990-12-10 | 1991-12-10 | 炭化水素油中の金属汚染物の量を低減する方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP19900203247 EP0489974B1 (fr) | 1990-12-10 | 1990-12-10 | Procédé pour diminuer la quantité de contaminants métalliques à partir d'huile hydrocarbonée |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0489974A1 EP0489974A1 (fr) | 1992-06-17 |
EP0489974B1 true EP0489974B1 (fr) | 1995-05-17 |
Family
ID=8205187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19900203247 Expired - Lifetime EP0489974B1 (fr) | 1990-12-10 | 1990-12-10 | Procédé pour diminuer la quantité de contaminants métalliques à partir d'huile hydrocarbonée |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0489974B1 (fr) |
JP (1) | JP2997906B2 (fr) |
CA (1) | CA2056973A1 (fr) |
DE (1) | DE69019527T2 (fr) |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE508479A (fr) * | ||||
EP0175799B1 (fr) * | 1983-06-20 | 1990-08-16 | Ashland Oil, Inc. | Immobilisation de vanadium déposé sur des adsorbants pendant la viscoréduction d'huiles contenant des métaux et des précurseurs de carbone |
US4414098A (en) * | 1981-07-30 | 1983-11-08 | Ashland Oil, Inc. | Upgrading carbo-metallic oils with used catalyst |
-
1990
- 1990-12-10 EP EP19900203247 patent/EP0489974B1/fr not_active Expired - Lifetime
- 1990-12-10 DE DE1990619527 patent/DE69019527T2/de not_active Expired - Fee Related
-
1991
- 1991-12-04 CA CA 2056973 patent/CA2056973A1/fr not_active Abandoned
- 1991-12-10 JP JP3349816A patent/JP2997906B2/ja not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH04339892A (ja) | 1992-11-26 |
DE69019527T2 (de) | 1995-11-09 |
EP0489974A1 (fr) | 1992-06-17 |
JP2997906B2 (ja) | 2000-01-11 |
CA2056973A1 (fr) | 1992-06-11 |
DE69019527D1 (de) | 1995-06-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3870623A (en) | Hydroconversion process of residuum oils | |
US3887455A (en) | Ebullating bed process for hydrotreatment of heavy crudes and residua | |
US4452911A (en) | Frangible catalyst pretreatment method for use in hydrocarbon hydrodemetallization process | |
US5925238A (en) | Catalytic multi-stage hydrodesulfurization of metals-containing petroleum residua with cascading of rejuvenated catalyst | |
RU2376059C2 (ru) | Способ и катализатор гидроконверсии тяжелого углеводородного исходного сырья | |
US4454240A (en) | Catalyst regeneration process including metal contaminants removal | |
US3964995A (en) | Hydrodesulfurization process | |
JPH10251666A (ja) | 金属で汚染された炭化水素系原料の水素処理方法 | |
CA2017181C (fr) | Procede d'hydrotraitement | |
JPH0753967A (ja) | 重質油の水素化処理方法 | |
JPH025797B2 (fr) | ||
US5124024A (en) | Method for extending hydroconversion catalyst life | |
US4595666A (en) | Catalyst rejuvenation process for removal of metal contaminants | |
CA1050915A (fr) | Demetallisation des matieres d'alimentation a forte teneur de metaux a l'aide de catalyseurs regeneres | |
US3932269A (en) | Hydrogenation of hydrocarbon residuum | |
CA2162017C (fr) | Catalyseur et methode d'hydrotraitement | |
EP1237651B1 (fr) | Catalyseur d'hydrogenation a base de nickel-fer-silice-alumine | |
JPS6322183B2 (fr) | ||
EP1010744A1 (fr) | Procede d'hydrotraitement pour des huiles residuelles | |
EP0489974B1 (fr) | Procédé pour diminuer la quantité de contaminants métalliques à partir d'huile hydrocarbonée | |
CA1275785C (fr) | Methode et dispositif d'extraction de particules solides d'une cuve sous haute pression | |
CA1122555A (fr) | Procede de deshydrosulfuration comprenant un recyclage des produits | |
JP3715893B2 (ja) | 水素化処理触媒の再生方法 | |
JP2000144151A (ja) | 水素化処理触媒の再生方法 | |
US3590007A (en) | Process for regeneration of spent hydroconversion catalyst |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): BE DE FR GB IT NL |
|
17P | Request for examination filed |
Effective date: 19921020 |
|
17Q | First examination report despatched |
Effective date: 19921218 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE DE FR GB IT NL |
|
REF | Corresponds to: |
Ref document number: 69019527 Country of ref document: DE Date of ref document: 19950622 |
|
ITF | It: translation for a ep patent filed |
Owner name: ING. C. GREGORJ S.P.A. |
|
ET | Fr: translation filed | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19981023 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19981126 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19981207 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19981218 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19981230 Year of fee payment: 9 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19991210 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19991231 |
|
BERE | Be: lapsed |
Owner name: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. Effective date: 19991231 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20000701 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19991210 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20000831 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 20000701 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20001003 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20051210 |