EP0176886B1 - Katalytisches Reformieren von Benzinen - Google Patents

Katalytisches Reformieren von Benzinen Download PDF

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Publication number
EP0176886B1
EP0176886B1 EP85111915A EP85111915A EP0176886B1 EP 0176886 B1 EP0176886 B1 EP 0176886B1 EP 85111915 A EP85111915 A EP 85111915A EP 85111915 A EP85111915 A EP 85111915A EP 0176886 B1 EP0176886 B1 EP 0176886B1
Authority
EP
European Patent Office
Prior art keywords
coal
reformer
petrol
derived
oil
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
Application number
EP85111915A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0176886A1 (de
Inventor
Alfons Dr. Jankowski
Albert Fehrer
Werner Dr. Döhler
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.)
Veba Oel Technologie und Automatisierung GmbH
Original Assignee
Veba Oel Technologie und Automatisierung GmbH
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 Veba Oel Technologie und Automatisierung GmbH filed Critical Veba Oel Technologie und Automatisierung GmbH
Publication of EP0176886A1 publication Critical patent/EP0176886A1/de
Application granted granted Critical
Publication of EP0176886B1 publication Critical patent/EP0176886B1/de
Expired legal-status Critical Current

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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
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming

Definitions

  • the invention relates to the catalytic reforming under elevated pressure and temperature of gasoline of the type specified in the preamble of claim 1.
  • Catalytic reforming is one of the most important processes for the production of gasoline fuels, which, in terms of their knock resistance, have to meet the increasing requirements in the increasingly powerful internal combustion engines.
  • the octane number for n-heptane is 0, that of iso-octane 100.
  • Octane numbers of more than 100 are achieved by adding lead tetraethyl to iso-octane.
  • noble metal catalysts such as platinum, possibly along with other metals such as rhenium, on high-purity alumina (Al 2 O 3 ) are used as supports.
  • the temperatures used are approximately 480-550 ° C. and the pressures approximately 8-30 bar, a high hydrogen partial pressure counteracting the inactivation of the catalyst by coke formation on the catalyst support. Lower pressures favor higher yields of reformate.
  • Typical conditions when operating a reformer are given, for example, in Hydrocarbon Processing, Sept. 1980, p. 162.
  • the adequate activity of the catalyst is maintained by suitable processes for regenerating the catalyst, for example by burning off the carbon on the catalyst in so-called swing reactors, but also by continuously discharging part of the catalyst from the fluidized catalyst bed maintained in the reformer.
  • the net hydrogen production that occurs in the reforming is an important source for covering the hydrogen demand existing in a refinery for various refining processes and other conversion processes.
  • the mixtures of carbon-based reformer feed product with reformer feed specification and mineral oil-derived reformer feed product are preferably used in a weight ratio of 20 to 80 to 40 to 60.
  • a typical petroleum-derived gasoline as a reformer feed consists for example of 44% by weight of paraffins, 41% by weight of monocycloparaffins, 2% by weight of dicycloparaffins and 13% of aromatics.
  • the carbon-based light oils or petrol from the liquefied hydrogenation of a gas flame coal of the Ruhr area according to the specified process of hydrogenation in the sump and gas phase, added as a reformer feed product, differ from the mineral oil-derived reformer feed products mainly by a lower content of paraffins and a higher content of monocycloparaffins.
  • ground coal In a sump phase hydrogenation at elevated pressure and temperature, ground coal, if appropriate with the addition of catalytically active substances, is mixed with a mashing oil mixed with gaseous hydrogen, the residue is discharged from the effluent from the sump phase hydrogenation, the residue-free volatile products are cooled, optionally separated from a fraction serving as mashing oil, subjected to gas phase hydrogenation on a Ni / Mo or Co / Mo catalyst applied to a support material made of A1 2 0 3 or A1 2 0 3 -Si0 2 and a refined carbon-derived naphtha or gasoline fraction won that as such or after
  • the catalyst service lives which are characterized by a predetermined activity of the platinum catalyst applied, for example, to a support material made of Al 2 O 3 , are also favorably influenced.
  • FIGS. 1 and 2 of the drawing in which the motor octane number (MOZ) and the research octane number (RON) are plotted on the ordinate and the C 5+ yield in% by weight are plotted on the abscissa
  • the improvements in C 5+ yield and octane number achieved for different mixtures of reformer feed products can be read off immediately.
  • the three curves in FIG. 1, seen from bottom to top, correspond to a commonly used petroleum-derived petrol (as a comparative example) and a mixture of a mixture of such petrol and a coal-based reformer feed in a weight ratio of 80:20 or in a weight ratio of 60:40 Reformer feed product.

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)
EP85111915A 1984-09-22 1985-09-20 Katalytisches Reformieren von Benzinen Expired EP0176886B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3434919 1984-09-22
DE3434919 1984-09-22

Publications (2)

Publication Number Publication Date
EP0176886A1 EP0176886A1 (de) 1986-04-09
EP0176886B1 true EP0176886B1 (de) 1988-03-30

Family

ID=6246142

Family Applications (1)

Application Number Title Priority Date Filing Date
EP85111915A Expired EP0176886B1 (de) 1984-09-22 1985-09-20 Katalytisches Reformieren von Benzinen

Country Status (11)

Country Link
US (1) US4629550A (enrdf_load_stackoverflow)
EP (1) EP0176886B1 (enrdf_load_stackoverflow)
JP (1) JPS6187791A (enrdf_load_stackoverflow)
AU (1) AU576460B2 (enrdf_load_stackoverflow)
BR (1) BR8504620A (enrdf_load_stackoverflow)
CA (1) CA1253106A (enrdf_load_stackoverflow)
DD (1) DD238392A5 (enrdf_load_stackoverflow)
DE (1) DE3562018D1 (enrdf_load_stackoverflow)
PL (1) PL145228B1 (enrdf_load_stackoverflow)
SU (1) SU1433418A3 (enrdf_load_stackoverflow)
ZA (1) ZA857254B (enrdf_load_stackoverflow)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4894153A (en) * 1988-11-28 1990-01-16 Shirdavant Hossain A Magnetic attachment for a filter
DE69709465T2 (de) * 1996-02-14 2002-07-11 Toyota Jidosha K.K., Toyota Verfahren und Vorrichtung zur Brennstoffversorgung einer Brennkraftmaschine
US6213104B1 (en) 1996-02-14 2001-04-10 Toyota Jidosha Kabushiki Kaisha Method and a device for supplying fuel to an internal combustion engine
US8679371B2 (en) 2007-04-11 2014-03-25 Sabic Innovative Plastics Ip B.V. Electrically conducting polymeric compositions, methods of manufacture thereof and articles comprising the same
US8999249B2 (en) * 2012-12-28 2015-04-07 Uop Llc Methods and apparatuses for reforming of hydrocarbons including recovery of products
CN118002300B (zh) * 2024-04-08 2024-06-18 山西潞安环保能源开发股份有限公司 一种末煤加工处理用选煤装置

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3533938A (en) * 1967-09-06 1970-10-13 Ashland Oil Inc Jet fuel from blended conversion products
DD113767A5 (enrdf_load_stackoverflow) * 1974-08-05 1975-06-20
CA1094004A (en) * 1977-11-18 1981-01-20 Her Majesty In Right Of Canada As Represented By The Minister Of Energy, Mines And Resources Canada Process for catalytically hydrocracking a heavy hydrocarbon oil
US4292167A (en) * 1979-06-28 1981-09-29 Mobil Oil Corporation Noble metal reforming of naphtha
US4377464A (en) * 1981-09-03 1983-03-22 The Pittsburg & Midway Coal Mining Co. Coal liquefaction process

Also Published As

Publication number Publication date
SU1433418A3 (ru) 1988-10-23
JPS6187791A (ja) 1986-05-06
US4629550A (en) 1986-12-16
JPH0572953B2 (enrdf_load_stackoverflow) 1993-10-13
CA1253106A (en) 1989-04-25
BR8504620A (pt) 1986-07-15
DE3562018D1 (en) 1988-05-05
EP0176886A1 (de) 1986-04-09
ZA857254B (en) 1986-05-28
PL145228B1 (en) 1988-08-31
DD238392A5 (de) 1986-08-20
AU576460B2 (en) 1988-08-25
AU4769185A (en) 1986-03-27
PL255462A1 (en) 1986-08-12

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