ES2154929T3 - Procedimiento de purificacion de naftaleno por hidrotratamiento selectivo seguido de una separacion. - Google Patents

Procedimiento de purificacion de naftaleno por hidrotratamiento selectivo seguido de una separacion.

Info

Publication number
ES2154929T3
ES2154929T3 ES98400046T ES98400046T ES2154929T3 ES 2154929 T3 ES2154929 T3 ES 2154929T3 ES 98400046 T ES98400046 T ES 98400046T ES 98400046 T ES98400046 T ES 98400046T ES 2154929 T3 ES2154929 T3 ES 2154929T3
Authority
ES
Spain
Prior art keywords
procedure
naftalene
naftalen
selective
separation
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
Application number
ES98400046T
Other languages
English (en)
Inventor
Samuel Mignard
Guenael Drouglazet
Slavik Kasztelan
Jean Cosyns
Michel Bloch
Rene Genin
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BEFS PROKEM
IFP Energies Nouvelles IFPEN
Original Assignee
BEFS PROKEM
IFP Energies Nouvelles IFPEN
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 BEFS PROKEM, IFP Energies Nouvelles IFPEN filed Critical BEFS PROKEM
Application granted granted Critical
Publication of ES2154929T3 publication Critical patent/ES2154929T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/14—Purification; Separation; Use of additives by crystallisation; Purification or separation of the crystals
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/005—Processes comprising at least two steps in series
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
    • C07C7/163—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/24—Chromium, molybdenum or tungsten
    • C07C2523/28—Molybdenum
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/24—Chromium, molybdenum or tungsten
    • C07C2523/30—Tungsten
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74—Iron group metals
    • C07C2523/75—Cobalt
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74—Iron group metals
    • C07C2523/755—Nickel
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
    • C07C2523/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/85—Chromium, molybdenum or tungsten
    • C07C2523/88—Molybdenum
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
    • C07C2523/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/85—Chromium, molybdenum or tungsten
    • C07C2523/888—Tungsten

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

LA INVENCION SE REFIERE A UN PROCEDIMIENTO DE PURIFICACION DE NAFTALENO. DICHO PROCEDIMIENTO COMPRENDE UN HIDROTRATAMIENTO SELECTIVO CORRESPONDIENTE A UNA HIDRODESULFURACION Y/O HIDRODESNITROGENACION Y/O HIDRODESHIDROXILACION Y/O HIDROGENACION DE LAS OLEFINAS LIMITANDO LA HIDROGENACION DEL NAFTALENO. EL CATALIZADOR EMPLEADO COMPRENDE UNA MATRIZ , AL MENOS UN METAL DEL GRUPO VIII, AL MENOS UN METAL DEL GRUPO VI Y, EVENTUALMENTE, FOSFORO. PRESENTA UNA SUPERFICIE ESPECIFICA DE MAS DE 220 M SUP,2 /G, UN VOLUMEN POROSO DE 0,35 - 0,7 ML/G Y UN DIAMETRO MEDIO DE POROS DE MAS DE 10 NM. EL PROCEDIMIENTO TIENE LUGAR A 150 - 325 C, BAJO 0,1 - 0,9 MPA, CON UNA VVH DE 0,05 - 10H SUP,1 , UNA RELACION H 2 /NAFTALENO DE 0,1 - 1,3 MOL/MOL. EL EFLUENTE DESPOJADO DE H 2 /S, DE NH 3 Y DE AGUA, SE SOMETE A UN PROCEDIMIENTO DE SEPARACION DEL NAFTALENO POR DESTILACION O, PREFERENTEMENTE, POR CRISTALIZACION. ASIMISMO, UN RECICLAJE DE LA TETRALINA SEPARADA HACIA EL HIDROTRATAMIENTO, PERMITE AUMENTAR NOTABLEMENTE ELRENDIMIENTO EN NAFTALENO. EN ESTE CASO, LA RELACION PONDERAL TETRALINA/NAFTALENO A LA ENTRADA DEL REACTOR ESTA COMPRENDIDA ENTRE 0,005 Y 0,08.
ES98400046T 1997-01-20 1998-01-13 Procedimiento de purificacion de naftaleno por hidrotratamiento selectivo seguido de una separacion. Expired - Lifetime ES2154929T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR9700618A FR2758555B1 (fr) 1997-01-20 1997-01-20 Procede de purification de naphtalene par hydrotraitement selectif suivi d'une separation

Publications (1)

Publication Number Publication Date
ES2154929T3 true ES2154929T3 (es) 2001-04-16

Family

ID=9502842

Family Applications (1)

Application Number Title Priority Date Filing Date
ES98400046T Expired - Lifetime ES2154929T3 (es) 1997-01-20 1998-01-13 Procedimiento de purificacion de naftaleno por hidrotratamiento selectivo seguido de una separacion.

Country Status (7)

Country Link
US (1) US6217750B1 (es)
EP (1) EP0854126B1 (es)
JP (1) JP4304353B2 (es)
CN (1) CN1158232C (es)
DE (1) DE69800340T2 (es)
ES (1) ES2154929T3 (es)
FR (1) FR2758555B1 (es)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6664433B1 (en) 1999-04-28 2003-12-16 Nippon Steel Chemical Co., Ltd. Process for the purification of aromatic hydrocarbons and process for the preparation of high-purity aromatic hydrocarbons
KR100754744B1 (ko) * 2006-05-01 2007-09-03 주식회사 효성 2,6-디메틸나프탈렌의 분리 및 정제방법
CN101311150B (zh) * 2007-05-25 2012-05-30 宝山钢铁股份有限公司 一种高纯萘的生产工艺
CN106699708B (zh) * 2015-11-12 2020-06-09 中国石油化工股份有限公司 一种生产苯酐的方法
CN106699500B (zh) * 2015-11-12 2020-03-17 中国石油化工股份有限公司 一种苯酐原料的生产方法
CN108409522B (zh) * 2018-03-12 2021-10-29 江苏华达化工集团有限公司 一种重苯萘生产精萘方法
CN110256187B (zh) * 2018-03-12 2021-11-02 中国科学院宁波材料技术与工程研究所 一种精萘的生产方法
CN110256191B (zh) * 2018-03-12 2021-11-02 中国科学院宁波材料技术与工程研究所 一种工业萘生产的精萘方法
CN110252325B (zh) * 2018-03-12 2022-01-28 中国科学院宁波材料技术与工程研究所 工业萘选择性加氢催化剂及其制备方法

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2981773A (en) * 1954-03-01 1961-04-25 Phillips Petroleum Co Separation by crystallization
US3277199A (en) * 1962-01-22 1966-10-04 Union Oil Co Selective hydrofining
US3394074A (en) * 1967-04-03 1968-07-23 Exxon Research Engineering Co Single reactor hydrocracking process with mixed nonnoble metal catalyst for full boiling raw feed
US3531398A (en) * 1968-05-03 1970-09-29 Exxon Research Engineering Co Hydrodesulfurization of heavy petroleum distillates
US4267033A (en) * 1979-10-22 1981-05-12 Mobil Oil Corporation Upgrading of aromatic liquids
US4469590A (en) * 1983-06-17 1984-09-04 Exxon Research And Engineering Co. Process for the hydrogenation of aromatic hydrocarbons
US4600703A (en) * 1983-12-19 1986-07-15 Intevep, S.A. Catalyst for the hydrocracking of heavy vacuum gas oils, method of preparation of catalyst and process for use thereof in the mild hydrocracking of heavy vacuum gas oils
JPH0585960A (ja) * 1991-09-27 1993-04-06 Osaka Gas Co Ltd 精製ナフタリンの製造方法

Also Published As

Publication number Publication date
JP4304353B2 (ja) 2009-07-29
CN1192430A (zh) 1998-09-09
DE69800340D1 (de) 2000-11-16
EP0854126B1 (fr) 2000-10-11
CN1158232C (zh) 2004-07-21
US6217750B1 (en) 2001-04-17
FR2758555B1 (fr) 1999-02-19
DE69800340T2 (de) 2001-02-15
JPH10204005A (ja) 1998-08-04
EP0854126A1 (fr) 1998-07-22
FR2758555A1 (fr) 1998-07-24

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