JP2007502353A5 - - Google Patents

Download PDF

Info

Publication number
JP2007502353A5
JP2007502353A5 JP2006529763A JP2006529763A JP2007502353A5 JP 2007502353 A5 JP2007502353 A5 JP 2007502353A5 JP 2006529763 A JP2006529763 A JP 2006529763A JP 2006529763 A JP2006529763 A JP 2006529763A JP 2007502353 A5 JP2007502353 A5 JP 2007502353A5
Authority
JP
Japan
Prior art keywords
ppm
present
catalyst composition
amount
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.)
Pending
Application number
JP2006529763A
Other languages
Japanese (ja)
Other versions
JP2007502353A (en
Filing date
Publication date
Application filed filed Critical
Priority claimed from PCT/EP2004/004943 external-priority patent/WO2004101713A1/en
Publication of JP2007502353A publication Critical patent/JP2007502353A/en
Publication of JP2007502353A5 publication Critical patent/JP2007502353A5/ja
Pending legal-status Critical Current

Links

Claims (7)

ヒ素および１以上の他の金属化合物を炭化水素供給原料から除く方法において、少なくとも２０ｐｐｂのヒ素および少なくとも０．３ｐｐｍの他の金属化合物を含有する炭化水素供給原料が水素の存在下に、担体上にモリブデン化合物およびニッケル化合物を含む触媒組成物であって、該モリブデン化合物が三酸化物として計算されて８〜１８重量％の量で存在し、かつ該ニッケル化合物が酸化物として計算されて８〜２０重量％の量で存在し、かつ該触媒組成物が少なくとも２００ｍ２／ｇの表面積を持つ触媒組成物と接触させられる方法。 In a method of removing arsenic and one or more other metal compounds from a hydrocarbon feed, a hydrocarbon feed containing at least 20 ppb arsenic and at least 0.3 ppm of other metal compounds is present on the support in the presence of hydrogen. A catalyst composition comprising a molybdenum compound and a nickel compound, wherein the molybdenum compound is present in an amount of 8 to 18% by weight calculated as a trioxide, and the nickel compound is calculated as an oxide from 8 to 20 A process wherein the catalyst composition is present in an amount by weight and is contacted with a catalyst composition having a surface area of at least 200 m 2 / g. モリブデン化合物が三酸化物として計算されて１０〜１５重量％の量で存在し、かつニッケル化合物が酸化物として計算されて８〜１５重量％の量で存在する、請求項１記載の方法。 The process according to claim 1, wherein the molybdenum compound is present in an amount of 10-15% by weight calculated as trioxide and the nickel compound is present in an amount of 8-15% by weight calculated as oxide. 触媒組成物が９〜１５ｎｍのＭＰＤを持つ、請求項１〜２のいずれか１項記載の方法。 The catalyst composition has a MPD of 9 ~15nm, any one method according to claim 1-2. 他の金属化合物の１つがケイ素である、請求項１〜３のいずれか１項記載の方法。 4. A method according to any one of claims 1 to 3, wherein one of the other metal compounds is silicon. 供給原料が、少なくとも２０ｐｐｂ（１０億当りの重量部）のヒ素、好ましくは０．０２〜２ｐｐｍのヒ素含有量、約０〜１２０℃、好ましくは約３０〜９０℃の初留点および約１５０〜２５０℃、好ましくは約１６０〜２２０℃の蒸留終点を持つナフサタイプの供給原料である、請求項１〜４のいずれか１項記載の方法。 The feedstock has an arsenic content of at least 20 ppb (parts per billion), preferably 0.02 to 2 ppm, an initial boiling point of about 0 to 120 ° C., preferably about 30 to 90 ° C. and about 150 to A process according to any one of the preceding claims, which is a naphtha type feedstock with a distillation end point of 250 ° C, preferably about 160-220 ° C. ナフサタイプの供給原料が、少なくとも０．５ｐｐｍ、特に１ｐｐｍ〜１００ｐｐｍのケイ素含有量を持つ、請求項５記載の方法。 Process according to claim 5, wherein the naphtha type feedstock has a silicon content of at least 0.5 ppm, in particular 1 ppm to 100 ppm. １０〜２００バール、好ましくは３０〜１５０バールの水素分圧で、２００〜４８０℃、好ましくは３００〜４１５℃の温度で、２００〜２０００Ｎｌ（リットル）／ｌ（リットル）、好ましくは５００〜１０００Ｎｌ／ｌの水素と供給原料との比で、および０．１〜１０時−１、好ましくは０．５〜３時−１のＬＨＳＶで実施される、請求項１〜６のいずれか１項記載の方法。 At a hydrogen partial pressure of 10 to 200 bar, preferably 30 to 150 bar and at a temperature of 200 to 480 ° C., preferably 300 to 415 ° C., 200 to 2000 Nl (liter) / l (liter), preferably 500 to 1000 Nl / 7. The process according to claim 1, carried out at a ratio of 1 hydrogen to the feedstock and at a LHSV of 0.1 to 10 h −1 , preferably 0.5 to 3 h −1 . Method.
JP2006529763A 2003-05-16 2004-05-06 Method and catalyst for removing arsenic and one or more other metal compounds from a hydrocarbon feed Pending JP2007502353A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US47086403P 2003-05-16 2003-05-16
EP03076720 2003-06-03
PCT/EP2004/004943 WO2004101713A1 (en) 2003-05-16 2004-05-06 Process and catalyst for removing arsenic and one or more other metal compounds from a hydrocarbon feedstock

Publications (2)

Publication Number Publication Date
JP2007502353A JP2007502353A (en) 2007-02-08
JP2007502353A5 true JP2007502353A5 (en) 2007-06-21

Family

ID=34923946

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006529763A Pending JP2007502353A (en) 2003-05-16 2004-05-06 Method and catalyst for removing arsenic and one or more other metal compounds from a hydrocarbon feed

Country Status (5)

Country Link
US (1) US20070080099A1 (en)
EP (1) EP1627027A1 (en)
JP (1) JP2007502353A (en)
CA (1) CA2525635A1 (en)
RU (1) RU2005139395A (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8734740B1 (en) 2013-03-15 2014-05-27 Clariant Corporation Process and composition for removal of arsenic and other contaminants from synthetic gas
FR3103822B1 (en) 2019-12-02 2022-07-01 Ifp Energies Now METHOD FOR TREATMENT OF PYROLYSIS OILS FROM PLASTICS WITH A VIEW TO RECYCLING THEM IN A STEAM CRACKING UNIT
FR3107530B1 (en) 2020-02-21 2022-02-11 Ifp Energies Now OPTIMIZED PROCESS FOR THE TREATMENT OF PLASTICS PYROLYSIS OILS WITH A VIEW TO THEIR RECOVERY
FR3113061B1 (en) 2020-07-30 2023-04-21 Ifp Energies Now METHOD FOR TREATMENT OF PLASTICS PYROLYSIS OILS INCLUDING ONE-STEP HYDROCRACKING
FR3113060B1 (en) 2020-07-30 2023-04-28 Ifp Energies Now PROCESS FOR TREATMENT OF PLASTICS PYROLYSIS OILS INCLUDING TWO-STAGE HYDROCRACKING
FR3114598B1 (en) 2020-09-25 2023-09-29 Ifp Energies Now METHOD FOR TREATMENT OF PLASTIC PYROLYSIS OILS AND/OR RECOVERED SOLID FUELS LOADED WITH IMPURITIES
FR3118629B1 (en) 2021-01-04 2023-12-15 Ifp Energies Now METHOD FOR PROCESSING PLASTICS PYROLYSIS OILS INCLUDING A HYDROGENATION STEP
FR3122663B1 (en) 2021-05-07 2024-04-26 Ifp Energies Now INTEGRATED PROCESS FOR TREATMENT OF PLASTICS PYROLYSIS OILS AND/OR RECOVERED SOLID FUELS LOADED WITH IMPURITIES
FR3122662B1 (en) 2021-05-07 2024-04-26 Ifp Energies Now METHOD FOR SIMULTANEOUS TREATMENT OF PLASTICS PYROLYSIS OILS AND A FEED FROM RENEWABLE SOURCES
CN113231067B (en) * 2021-05-28 2023-08-22 中国海洋石油集团有限公司 Dearsenifying agent for light distillate oil hydrogenation and preparation method and application thereof
FR3128225A1 (en) 2021-10-19 2023-04-21 IFP Energies Nouvelles METHOD FOR TREATMENT OF PYROLYSIS OILS FROM PLASTICS AND/OR SOLID RECOVERY FUELS LOADED WITH IMPURITIES
FR3129945A1 (en) 2021-12-03 2023-06-09 IFP Energies Nouvelles PROCESS FOR TREATMENT OF PYROLYSIS OILS FROM PLASTICS INCLUDING A HYDROGENATION STEP AND A HOT SEPARATION
FR3135090A1 (en) 2022-04-29 2023-11-03 IFP Energies Nouvelles METHOD FOR PROCESSING PLASTICS PYROLYSIS OIL INCLUDING AN H2S RECYCLING STEP
FR3144155A1 (en) 2022-12-21 2024-06-28 IFP Energies Nouvelles METHOD FOR TREATMENT OF PYROLYSIS OILS OF PLASTICS AND/OR TIRES INCLUDING THE ELIMINATION OF HALIDES PRIOR TO A HYDROTREATMENT STEP
FR3144153A1 (en) 2022-12-21 2024-06-28 IFP Energies Nouvelles METHOD FOR TREATING PLASTICS AND/OR TIRES PYROLYSIS OILS INCLUDING THE ELIMINATION OF HALIDES BY WASHING BEFORE A HYDROTREATMENT STEP

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5183561A (en) * 1990-01-25 1993-02-02 Mobil Oil Corp. Demetallation of hydrocarbon feedstocks with a synthetic mesoporous crystalline material

Similar Documents

Publication Publication Date Title
JP2007502353A5 (en)
TWI301127B (en) Catalyst for selective front-end hydrogenation of acetylene and its manufacture process and uses
JP5231991B2 (en) A selective hydrogenation process of acetylene to ethylene.
JP6636162B2 (en) Palladium-based hydrogenation catalyst, method for producing the same, and use thereof
JP5639595B2 (en) Catalytic cracking of hydrocarbon streams to maximize light olefins
McEwan et al. A review of the use of gold catalysts in selective hydrogenation reactions
JP4808212B2 (en) Method for producing low sulfur diesel fuel
US5601701A (en) Process for the elimination of mercury from hydrocarbons by passage over a presulphurated catalyst
KR870011227A (en) Hydrocarbon Conversion Processes and Catalysts
CA2560339A1 (en) Solid acid catalyst and method of using same
MX2008001232A (en) A selective hydrogenation catalyst and methods of making and using same.
JP2009515029A5 (en)
CA2627337A1 (en) Hydrocracking catalyst containing beta and y zeolites, and process for its use to produce naphtha
US20110308999A1 (en) Method for selective hydrogenation of phenylacetylene in the presence of styrene
JP5706335B2 (en) Selective catalytic hydrogenation of alkynes to the corresponding alkenes
CN101623633A (en) Catalyst for preparing olefin by dehydrogenating low-carbon alkane, and preparation method and application thereof
WO2008153759A3 (en) Catalyst for conversion of hydrocarbons, process of making and process of using thereof-bimetallic deposition
MY146921A (en) Hydrogenation process using catalyst comprising ordered intermetallic compound
WO2004028688A1 (en) Hydrocracking catalyst and process for production of liquid hydrocarbons
IN2012DN00751A (en)
RU2005139395A (en) METHOD AND CATALYST FOR REMOVING ARSENE AND COMPOUNDS OF ONE OR MORE OTHER METALS FROM ORIGINAL HYDROCARBON RAW MATERIAL
CN108147938B (en) Method for selectively hydrogenating acetylene to ethylene
JPS62123137A (en) Manufacture of 2-methyl-2-butene from c5 olefin fraction containing 2-methyl-1-butene and at least one n-pentene
RU2008129875A (en) METHOD FOR INTERACTION OF AROMATIC HYDROCARBON IN THE PRESENCE OF HYDROGEN
US11247898B2 (en) Catalyst carrier for bi-reforming processes