WO2003029385A2 - Procede de transformation de dechets de petrole mixtes et installation pour sa mise en oeuvre - Google Patents

Procede de transformation de dechets de petrole mixtes et installation pour sa mise en oeuvre Download PDF

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Publication number
WO2003029385A2
WO2003029385A2 PCT/AZ2002/000001 AZ0200001W WO03029385A2 WO 2003029385 A2 WO2003029385 A2 WO 2003029385A2 AZ 0200001 W AZ0200001 W AZ 0200001W WO 03029385 A2 WO03029385 A2 WO 03029385A2
Authority
WO
WIPO (PCT)
Prior art keywords
fact
syρya
temperature
distillation
installation
Prior art date
Application number
PCT/AZ2002/000001
Other languages
English (en)
Russian (ru)
Other versions
WO2003029385A3 (fr
Inventor
Gamlet Alievich Mirzoev
Namik Niyaz Ogly Mamedov
Ali Girmaevich Asaev
Original Assignee
Gamlet Alievich Mirzoev
Namik Niyaz Ogly Mamedov
Ali Girmaevich Asaev
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
Priority claimed from EA200200475A external-priority patent/EA200200475A1/ru
Application filed by Gamlet Alievich Mirzoev, Namik Niyaz Ogly Mamedov, Ali Girmaevich Asaev filed Critical Gamlet Alievich Mirzoev
Priority to JP2003532609A priority Critical patent/JP2006510745A/ja
Priority to KR10-2004-7008750A priority patent/KR20040075870A/ko
Priority to AU2002325463A priority patent/AU2002325463A1/en
Priority to DE60232460T priority patent/DE60232460D1/de
Priority to EP02757985A priority patent/EP1452576B1/fr
Priority to AT02757985T priority patent/ATE432333T1/de
Publication of WO2003029385A2 publication Critical patent/WO2003029385A2/fr
Publication of WO2003029385A3 publication Critical patent/WO2003029385A3/fr

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
    • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M175/00—Working-up used lubricants to recover useful products ; Cleaning

Definitions

  • the objective of the present invention is to provide a means and equipment for the processing of inadequate waste of goods, which increase the profit of the carbohydrates. 4
  • a vacuum distillate is selected from the middle of the vacuum distillation cube column.
  • the obtained cubical method is the boiler fuel with a quick heating of 40560 UJ / kg;
  • ⁇ eshaemaya task us ⁇ an ⁇ v ⁇ e for ⁇ susches ⁇ vleniya s ⁇ s ⁇ ba ⁇ e ⁇ e ⁇ ab ⁇ i smeshanny ⁇ ne ⁇ yany ⁇ ⁇ d ⁇ v, v ⁇ lyuchayuschey node ⁇ bezv ⁇ zhivaniya is ⁇ dn ⁇ g ⁇ sy ⁇ ya Node dis ⁇ illyatsii, us ⁇ ys ⁇ v ⁇ for nag ⁇ eva sy ⁇ ya, ⁇ e ⁇ l ⁇ bmenni ⁇ , ⁇ ndensa ⁇ , se ⁇ a ⁇ a ⁇ y and ⁇ il ⁇ y, d ⁇ s ⁇ igae ⁇ sya ⁇ em, ch ⁇ ⁇ bezv ⁇ zhivaniya node s ⁇ vmescheniem ⁇ un ⁇ tsy ⁇ bess ⁇ livaniya and ⁇ chis ⁇ i is ⁇ dn ⁇ g ⁇ sy ⁇ ya vy ⁇ lnen in in the form
  • the distillation unit provides vacuum distillation.
  • Received on the installation of the target product in the form of a slurry is a bulk fuel and has a load of 40560 UJ / kg.
  • the resulting liver oil has an ignition temperature of 40 ° C, and a light hydrocarbon fraction has a temperature of ⁇ 180 ° C.
  • Two-stage preparation of raw materials, two-stage heating, circulation and recirculation of the heated mass of hydrocarbon have the advantage of reducing the consumption of heat. 7 niz ⁇ m ⁇ le ⁇ ulya ⁇ ny ⁇ ⁇ m ⁇ nen ⁇ v sy ⁇ ya, ch ⁇ in sv ⁇ yu ⁇ che ⁇ ed snizhae ⁇ ⁇ ud ⁇ em ⁇ s ⁇ and s ⁇ ve ⁇ s ⁇ venn ⁇ ene ⁇ g ⁇ za ⁇ a ⁇ y and ⁇ a ⁇ zhe znachi ⁇ eln ⁇ umenshae ⁇ ⁇ dy ⁇ e ⁇ e ⁇ ab ⁇ i and vyb ⁇ sy a ⁇ m ⁇ s ⁇ e ⁇ u in making this ⁇ e ⁇ n ⁇ l ⁇ giyu e ⁇ l ⁇ giches ⁇ i s ⁇ ve ⁇ shenn ⁇ bezv ⁇ edn ⁇ y.
  • FIG. 1 shows the general scheme of the installation for the processing of mixed non-food products; on ⁇ ig. 2 - vertical dental furnace in the case of; on ⁇ ig. 3 - town, view of the sky; on ⁇ ig. 4 - town, view ⁇ ⁇ - ⁇ .
  • Spaces 1 and 2 have spacious, rotating vibrating devices 15, which are stored in the upper part of the tanks.
  • the plant is connected in the general technological scheme with lines 16 - 32.
  • ⁇ ubcha ⁇ aya ⁇ ech ( ⁇ ig. 2) ⁇ as ⁇ l ⁇ zhennaya ve ⁇ i ⁇ aln ⁇ , s ⁇ de ⁇ zhi ⁇ zmeevi ⁇ i 33, 34, 35, and ⁇ b ⁇ azuyuschie ⁇ adian ⁇ nuyu ⁇ nventsi ⁇ nnuyu ⁇ ame ⁇ y and g ⁇ el ⁇ u 36 as ⁇ e ⁇ i ⁇ vann ⁇ y ⁇ las ⁇ iny ( ⁇ ig. 3) in ⁇ nus ⁇ b ⁇ aznymi ⁇ ve ⁇ s ⁇ iyami ⁇ e ⁇ echn ⁇ m section ( ⁇ ig. 4).
  • Heating in the furnace 4 carries out the supply of 36 hot agents to the city, for example, a mixture of air and natural gas. By doing this, the cooking of the city and the inconvenience of the process will speed up the achievement of the required mode of operation.
  • the raw material in the liquid is empty of line 22;
  • the distillate is removed from the middle of the column with a vacuum distillation pipe at a temperature of 180 ° C to 360 ° C and a constant pressure of 50 mm rt.
  • the physical and mechanical indicators of the cubic discharge are provided in the table.
  • the total vacuum in the system is created by known components, for example, by type ⁇ -12. With this, capacities 12, 13, 14 turn off the vacuum system for unloading the target products through line 28, 29, 30 to the receiver, and not to the receiver.
  • the mass of hydrocarbons is circulating throughout the system and through line 32 through tank 2 and line 20 under pressure, generated, for example, by the pump returning to the system.
  • the dispensing control for lines 27 and 32 is carried out by any known means, such as valves.
  • P ⁇ i is ⁇ lz ⁇ vanii iz ⁇ b ⁇ e ⁇ eniya d ⁇ s ⁇ igae ⁇ sya s ⁇ aschenie v ⁇ emeni ⁇ s ⁇ ya and demulsification siln ⁇ ⁇ bv ⁇ dnenny ⁇ smeshanny ⁇ ne ⁇ yany ⁇ ⁇ d ⁇ v, reduction ene ⁇ g ⁇ za ⁇ a ⁇ d ⁇ 1, 5 -.

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)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Processing Of Solid Wastes (AREA)
  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)

Abstract

Le procédé de transformation de déchets de pétrole mixtes et l'installation pour sa mise en oeuvre appartiennent aux procédés et dispositifs de transformation de matières premières pétrolières. L'invention permet d'augmenter sensiblement la production d'hydrocarbures commercialisables grâce à une préparation préalable efficace de la matière première et de réduire la consommation d'énergie et l'impact négatif sur l'environnement. Le procédé comprend les opérations suivantes, menées simultanément: déshydratation, dessalement des déchets pétroliers, purification de ceux-ci des impuretés mécaniques et du soufre par des oscillations vibratoires de cavitation, générées par un vibreur, réchauffement de la masse d'hydrocarbures, circulation de cette dernière et son recyclage. Pour mettre en oeuvre ce procédé, l'installation comprend des vibreurs (15) intégrés aux cuves de préparation de la matière première (1), (2), reliées au dispositif de réchauffement de la matière première qui se présente comme un four tubulaire vertical (4) muni de serpentins et d'un brûleur se présentant comme une plaque perforée avec des trous coniques. Le four (4) est relié à une unité de distillation qui se présente comme un bouilleur pour distillation sous vide (5), relié à la cuve (2). Cette invention peut s'utiliser dans la fabrication de combustibles pour fours, pour chaudières ou autres.
PCT/AZ2002/000001 2001-12-07 2002-08-26 Procede de transformation de dechets de petrole mixtes et installation pour sa mise en oeuvre WO2003029385A2 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP2003532609A JP2006510745A (ja) 2001-12-07 2002-08-26 混合石油残留物の再処理方法及びそれを実行するための装置
KR10-2004-7008750A KR20040075870A (ko) 2001-12-07 2002-08-26 혼합된 석유 폐기물을 처리하는 방법 및 장치
AU2002325463A AU2002325463A1 (en) 2001-12-07 2002-08-26 Method for recycling mixed oil waste and device for carrying out said method
DE60232460T DE60232460D1 (de) 2001-12-07 2002-08-26 Verfahren zum rezyklieren von mischölabfall und vorrichtung zur durchführung des verfahrens
EP02757985A EP1452576B1 (fr) 2001-12-07 2002-08-26 Procede de transformation de dechets de petrole mixtes et installation pour sa mise en oeuvre
AT02757985T ATE432333T1 (de) 2001-12-07 2002-08-26 Verfahren zum rezyklieren von mischölabfall und vorrichtung zur durchführung des verfahrens

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
AZA20010201 2001-12-07
AZA20010201 2001-12-07
EA200200475A EA200200475A1 (ru) 2001-12-07 2002-05-20 Способ переработки смешанных нефтяных отходов и установка для его осуществления
EA200200475 2002-05-20

Publications (2)

Publication Number Publication Date
WO2003029385A2 true WO2003029385A2 (fr) 2003-04-10
WO2003029385A3 WO2003029385A3 (fr) 2003-11-06

Family

ID=25646915

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AZ2002/000001 WO2003029385A2 (fr) 2001-12-07 2002-08-26 Procede de transformation de dechets de petrole mixtes et installation pour sa mise en oeuvre

Country Status (4)

Country Link
EP (1) EP1452576B1 (fr)
AT (1) ATE432333T1 (fr)
AU (1) AU2002325463A1 (fr)
WO (1) WO2003029385A2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2455341C1 (ru) * 2010-12-07 2012-07-10 Государственное образовательное учреждение высшего профессионального образования "Самарский государственный аэрокосмический университет имени академика С.П. Королева (национальный исследовательский университет)" (СГАУ) Способ кавитационной обработки жидких нефтепродуктов

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8197673B2 (en) 2008-11-19 2012-06-12 Saudi Arabian Oil Company Converting heavy sour crude oil/emulsion to lighter crude oil using cavitations and filtration based systems
RU2434050C1 (ru) 2010-12-06 2011-11-20 Общество С Ограниченной Ответственностью "Лаборатория Карбон" Способ переработки углеводородного сырья
CA2942744C (fr) 2014-05-01 2021-01-05 Exxonmobil Research And Engineering Company Systeme et procedes de deparaffinage de combustibles de distillat
US20150315491A1 (en) * 2014-05-01 2015-11-05 Exxonmobil Research And Engineering Company Methods and systems for improving performance of desalting units

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2134920A (en) * 1983-02-09 1984-08-22 Intevep Sa Upgrading heavy hydrocarbons employing a diluant
RU2079328C1 (ru) * 1993-02-15 1997-05-20 Товарищество с ограниченной ответственностью "ЭФАТ" Способ обработки нефти и устройство для его осуществления
RU2111061C1 (ru) * 1996-09-30 1998-05-20 Алексей Васильевич Иванайский Устройство для переработки нефтешламов
RU2124550C1 (ru) * 1998-05-19 1999-01-10 Общество с ограниченной ответственностью "КЭТЭ" Способ переработки тяжелого углеводородного сырья и устройство для его осуществления

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2100403C1 (ru) * 1996-05-12 1997-12-27 Валерий Георгиевич Леонтьевский Способ фракционирования нефти и установка для его осуществления
RU2161176C1 (ru) * 2000-06-28 2000-12-27 Закрытое акционерное общество "ПОМ-ТЭК" Способ переработки отработанных нефтепродуктов и установка для его осуществления

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2134920A (en) * 1983-02-09 1984-08-22 Intevep Sa Upgrading heavy hydrocarbons employing a diluant
RU2079328C1 (ru) * 1993-02-15 1997-05-20 Товарищество с ограниченной ответственностью "ЭФАТ" Способ обработки нефти и устройство для его осуществления
RU2111061C1 (ru) * 1996-09-30 1998-05-20 Алексей Васильевич Иванайский Устройство для переработки нефтешламов
RU2124550C1 (ru) * 1998-05-19 1999-01-10 Общество с ограниченной ответственностью "КЭТЭ" Способ переработки тяжелого углеводородного сырья и устройство для его осуществления

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP1452576A2 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2455341C1 (ru) * 2010-12-07 2012-07-10 Государственное образовательное учреждение высшего профессионального образования "Самарский государственный аэрокосмический университет имени академика С.П. Королева (национальный исследовательский университет)" (СГАУ) Способ кавитационной обработки жидких нефтепродуктов

Also Published As

Publication number Publication date
WO2003029385A3 (fr) 2003-11-06
EP1452576A2 (fr) 2004-09-01
AU2002325463A1 (en) 2003-04-14
EP1452576B1 (fr) 2009-05-27
EP1452576A4 (fr) 2007-03-07
ATE432333T1 (de) 2009-06-15

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