EP0892030A2 - Installation pour la séparation destillative d'huile brute - Google Patents

Installation pour la séparation destillative d'huile brute Download PDF

Info

Publication number
EP0892030A2
EP0892030A2 EP98890204A EP98890204A EP0892030A2 EP 0892030 A2 EP0892030 A2 EP 0892030A2 EP 98890204 A EP98890204 A EP 98890204A EP 98890204 A EP98890204 A EP 98890204A EP 0892030 A2 EP0892030 A2 EP 0892030A2
Authority
EP
European Patent Office
Prior art keywords
crude oil
heat exchanger
furnace
exhaust gas
gas heat
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.)
Granted
Application number
EP98890204A
Other languages
German (de)
English (en)
Other versions
EP0892030B1 (fr
EP0892030A3 (fr
Inventor
Georg Dipl.-Ing. Dr. Sipos
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.)
OMV Downstream GmbH
Original Assignee
OMV AG
OEMV AG
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 OMV AG, OEMV AG filed Critical OMV AG
Priority to SI9830296T priority Critical patent/SI0892030T1/xx
Publication of EP0892030A2 publication Critical patent/EP0892030A2/fr
Publication of EP0892030A3 publication Critical patent/EP0892030A3/fr
Application granted granted Critical
Publication of EP0892030B1 publication Critical patent/EP0892030B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C10G7/00—Distillation of hydrocarbon oils

Definitions

  • the invention has a device for continuous distillation Separation of crude oil with a distillation tower for Object.
  • standing cylinder furnaces which provided a vertical cylindrical combustion chamber is surrounded by standing tubes arranged in a circle is. At the bottom of the cylinder furnace are the burning nozzles for one Gas heating arranged, whereas in the upper area Radiation cone is provided for an even heat transfer care of the gases on the tube bundle.
  • waste heat is particularly important dedicated. This is how the waste heat from individual fractions becomes used to preheat air, for example for the Incinerators or preheating other fractions too to reach.
  • the waste heat is also used for steam generation own needs in the refinery as well as district heating.
  • the aim of the present invention is a device for the continuous distillative processing of crude oil create, in which the crude oil particularly gently continuously and even up to even with different heat requirements can be heated to temperatures between 350 ° C and 400 ° C, whereby at the same time electrical energic is gained and the waste heat can be used for high quality.
  • the device according to the invention for continuous distillation Separation of crude oil, at least through a pipeline a, in particular gas-heated, furnace can be fed, which via a pipeline directly or indirectly with the evaporation zone a distillation tower with shelves, especially bell bottoms, is connected with strippers, which with at least two different shelves and with a steam generator and / or superheater are connected and a head cooler, is essentially that in addition a gas turbine connected to a power generator is provided with an exhaust gas heat exchanger for the crude oil, through which the crude oil can be heated directly and / or indirectly.
  • a furnace is provided in addition to the gas turbine, can do the distillative separation during maintenance work on the gas turbine of the crude oil continue to be carried out by Control of the heating power of the furnace of different heat requirements covered and thus a uniform performance of the gas turbine can be ensured.
  • the gas turbine GT shown in FIG. 1 with a speed of 3,000 or 3,600 rpm is mechanically coupled to the power generator G.
  • the gas turbine has a consumption of 7,500 m 3 / h natural gas. It is an aeroderiative turbine, e.g. B. LM 2500+ General Electric or DLE 2.500+ General Electric with lower nitrogen oxide emissions.
  • the generator delivers 30,000 kW.
  • the gases emerging from the gas turbine with a temperature of 510 ° C. enter an additional firing NB, in which the remaining oxygen content is burned with additionally introduced natural gas (arrow a).
  • the gases emerging from the additional firing have a temperature of 700 ° C.
  • the exhaust gases give their heat to a heat transfer fluid, u.
  • the heat transfer fluid in line w connects the exhaust gas heat exchanger W 1 to a further heat exchanger W 2 .
  • crude oil at 140 ° C. is introduced via line L 1 and passes through line L 2 at 250 ° C. into gas furnace 1, 2, in which it is additionally heated to 370 ° C.
  • the further heat exchanger W 2 and the furnace 1, 2 are connected in series.
  • the line w can also lead to a steam generator D, in which steam is generated for the stripping process.
  • the exhaust gases are passed from the heat exchanger W 1 into a heat exchanger W 3 , in which water is heated for district heating.
  • the exhaust gases from the gas furnace 1, 2 are cooled via a heat exchanger W 4 and the heat is used for process steam within the refinery.
  • the temperature of the exhaust gases is kept above 100 ° C so that no condensation occurs in the chimney.
  • the crude oil heated to 370 ° C. is fed to the distillation tower via line L 3 .
  • a temperature sensor T 1 is arranged, which controls the flow of a valve V 1 for the gas of the furnace 1, 2 but also the fuel supply, arrow a, regulates additional firing NB.
  • a further temperature sensor T 2 is arranged, which in turn takes care of regulating and controlling the flow rate of the valve V 2 , which also allows the amount of gas supplied to the furnace but also the fuel supply for the additional firing and thus the heating power to be regulated and controlled .
  • the crude oil arrives from furnaces 1 and 2 in line L 3 into stripping column 3, into which steam is introduced according to arrow X 1 .
  • a part of the bottom product also enters the stripper column 3 (arrow L) from the bottom of the distillation tower 4.
  • the crude oil, which is introduced via line L 3 was heated to 370 ° C. by means of the waste heat from the gas turbine and the furnaces 1, 2.
  • the stripping column 3 the crude oil is expanded from 5 bar to 3 bar and is then passed along the line X 2 into the evaporation zone of the distillation tower 4. A further relaxation to 1.5 bar occurs in this. 45 bubble trays are arranged in the distillation tower 4. In the strippers 5.
  • the products withdrawn from the distillation tower are introduced, steam is applied to them via lines D 1 , D 2 , D 3 and the more volatile constituents are thus expelled.
  • the material to be recovered is drawn off in the bottom of the strippers, whereas the top product is fed back to the column.
  • the steam which is used in the strippers was obtained with the exhaust gas heat from the gas turbine in the steam generator D (FIG. 1).
  • the end product drawn off from the strippers is cooled by heat exchangers W 5 , W 6 , W 7 and the heat thus obtained is recovered.
  • the distillation tower 4 also has a head cooler 8.

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)
EP98890204A 1997-07-18 1998-07-14 Installation pour la séparation destillative d'huile brute Expired - Lifetime EP0892030B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SI9830296T SI0892030T1 (en) 1997-07-18 1998-07-14 Apparatus for the distillative separation of crude oil

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
AT122997 1997-07-18
AT0122997A AT406165B (de) 1997-07-18 1997-07-18 Vorrichtung zur kontinuierlichen destillativen auftrennung von rohöl
AT1229/97 1997-07-18

Publications (3)

Publication Number Publication Date
EP0892030A2 true EP0892030A2 (fr) 1999-01-20
EP0892030A3 EP0892030A3 (fr) 1999-07-28
EP0892030B1 EP0892030B1 (fr) 2002-09-11

Family

ID=3509403

Family Applications (1)

Application Number Title Priority Date Filing Date
EP98890204A Expired - Lifetime EP0892030B1 (fr) 1997-07-18 1998-07-14 Installation pour la séparation destillative d'huile brute

Country Status (9)

Country Link
EP (1) EP0892030B1 (fr)
AT (1) AT406165B (fr)
BG (1) BG63400B1 (fr)
DE (1) DE59805483D1 (fr)
ES (1) ES2181156T3 (fr)
HR (1) HRP980400B1 (fr)
PT (1) PT892030E (fr)
SI (1) SI0892030T1 (fr)
SK (1) SK283465B6 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2417984A (en) * 2004-09-09 2006-03-15 M W Kellogg Ltd Integrated process plant

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3567628A (en) * 1968-10-25 1971-03-02 Phillips Petroleum Co Production of high flash point topped crude and high flash point asphalt
EP0569796A2 (fr) * 1992-05-05 1993-11-18 The M. W. Kellogg Company Four de traitement ayant une conduite de fumée divisée dans la zone de convection des fumées
JPH06207530A (ja) * 1992-10-26 1994-07-26 Mitsubishi Heavy Ind Ltd コンバインド・サイクル発電方法

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2258443B1 (fr) * 1974-01-17 1976-11-26 Spie Batignolles

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3567628A (en) * 1968-10-25 1971-03-02 Phillips Petroleum Co Production of high flash point topped crude and high flash point asphalt
EP0569796A2 (fr) * 1992-05-05 1993-11-18 The M. W. Kellogg Company Four de traitement ayant une conduite de fumée divisée dans la zone de convection des fumées
JPH06207530A (ja) * 1992-10-26 1994-07-26 Mitsubishi Heavy Ind Ltd コンバインド・サイクル発電方法

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
"APPLICATION OF GAS TURBINE EXHAUST HEAT RECOVERY TO AN EXISTING CRUDE PREHEAT TRAIN" RESEARCH DISCLOSURE, Nr. 320, 1. Dezember 1990, Seite 960 XP000163354 *
BAJEK ET AL: "How boiling point monitors can increase profits" HYDROCARBON PROCESSING, Bd. 63, Nr. 3, - M{rz 1999 Seiten 77-81, XP002104267 Houston *
KIRK-OTHMER: "Encyclopedia of Chemical Technology Bd. 20, S. 23-24", 1996, JOHN WILEY & SONS, NEW YORK *
PATENT ABSTRACTS OF JAPAN vol. 018, no. 569 (M-1695), 31. Oktober 1994 & JP 06 207530 A (MITSUBISHI HEAVY IND LTD), 26. Juli 1994 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2417984A (en) * 2004-09-09 2006-03-15 M W Kellogg Ltd Integrated process plant
GB2417984B (en) * 2004-09-09 2009-11-04 M W Kellogg Ltd Integrated process plant utilising a fractionating auxilliary treatment system

Also Published As

Publication number Publication date
SI0892030T1 (en) 2003-04-30
PT892030E (pt) 2003-01-31
DE59805483D1 (de) 2002-10-17
BG63400B1 (bg) 2001-12-29
EP0892030B1 (fr) 2002-09-11
ES2181156T3 (es) 2003-02-16
EP0892030A3 (fr) 1999-07-28
BG102642A (en) 1999-02-26
HRP980400B1 (en) 2001-08-31
HRP980400A2 (en) 1999-10-31
SK97398A3 (en) 1999-02-11
ATA122997A (de) 1999-07-15
SK283465B6 (sk) 2003-08-05
AT406165B (de) 2000-03-27

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