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WO1996013562A1 - Procede de retraitement de produits petroliers liquides et dispositif de traitement de produits petroliers liquides - Google Patents

Procede de retraitement de produits petroliers liquides et dispositif de traitement de produits petroliers liquides Download PDF

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Publication number
WO1996013562A1
WO1996013562A1 PCT/RU1995/000218 RU9500218W WO9613562A1 WO 1996013562 A1 WO1996013562 A1 WO 1996013562A1 RU 9500218 W RU9500218 W RU 9500218W WO 9613562 A1 WO9613562 A1 WO 9613562A1
Authority
WO
WIPO (PCT)
Prior art keywords
liquid
channel
προ
petroleum products
гем
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.)
Ceased
Application number
PCT/RU1995/000218
Other languages
English (en)
Russian (ru)
Inventor
David Bentsionovich Bernshtein
Valery Rasimovich Minyazov
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of WO1996013562A1 publication Critical patent/WO1996013562A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
    • B05B1/26—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means with means for mechanically breaking-up or deflecting the jet after discharge, e.g. with fixed deflectors; Breaking-up the discharged liquid or other fluent material by impinging jets
    • B05B1/262—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means with means for mechanically breaking-up or deflecting the jet after discharge, e.g. with fixed deflectors; Breaking-up the discharged liquid or other fluent material by impinging jets with fixed deflectors
    • B05B1/267—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means with means for mechanically breaking-up or deflecting the jet after discharge, e.g. with fixed deflectors; Breaking-up the discharged liquid or other fluent material by impinging jets with fixed deflectors the liquid or other fluent material being deflected in determined directions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
    • B05B1/02—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops, or having an outlet of particular shape
    • B05B1/04—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops, or having an outlet of particular shape in flat form, e.g. fan-like, sheet-like
    • B05B1/042—Outlets having two planes of symmetry perpendicular to each other, one of them defining the plane of the jet
    • 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 deteriorating fluid is not susceptible to the conversion of carbohydrate oils, but is more likely to result in a loss of fluid.
  • This device provides intensive mechanical agitation of the RAW.
  • the main task of the invention is the creation of a medium
  • ve ⁇ have a slant in the place of its intersection with an axis of symmetry in the corner.
  • the channel 5 was located in the range of :: from 5 to 30 °, and the extension of the channel from the channel to the channel ⁇ .
  • the channel diameter was in the range from 0.7 to 3.5.
  • Fractions that ⁇ I ⁇ D ⁇ ⁇ . an increase in the output of light :: Fractions: enzine, kerosina and diesel fuel.
  • Fractions enzine, kerosina and diesel fuel.
  • ⁇ a ⁇ zhe restoreyS ⁇ s ⁇ s ⁇ e and us ⁇ ys ⁇ v ⁇ ⁇ zv ⁇ lya- yu ⁇ snizi ⁇ ene ⁇ g ⁇ za ⁇ a ⁇ y na me :: aniches ⁇ e dis ⁇ e ⁇ gi ⁇ vanie and ⁇ vysi ⁇ e ⁇ ⁇ ⁇ izv ⁇ di ⁇ eln ⁇ s ⁇ ⁇ tsessa ⁇ e ⁇ e ⁇ ae ⁇ i.
  • non-powered air conditioners impair the use of liquid non-active air conditioner in the event of pressure and are unavoidable;
  • Fig. 6 is depicted in the form
  • the flat-panel camera has a channel of 16 diameters. ⁇ with a good 17 in the upper part. Hemisphere 17 is dissected by an equidistant wedge, upper than 18 ⁇ (in FIG.
  • OPTIONS of the liquid not. ⁇ DU ⁇ G. 2 with a mass of 400 to 600 g with the use of :: One standard viscosity of 2.8 ° C and 20 ° C with optional
  • the maximum output is the total amount of light: The fractions are achieved with a size of droplet 11, not exceeding 0.30 mm. Increase in size droplet 11,: a sharp decrease in the degree of: anical dispersion of dispersion ⁇ and dispersal. ⁇ I ⁇ DI ⁇ ⁇ to reduce light output :: ⁇ réelle ⁇ elecommunication ⁇ .
  • a corner with an angle of inclination of 15 degrees is 1 / ⁇ from 0.7 to 6.
  • Table 3 presents data for the total :: Light output is connected to a power outlet. 15 Angelica 3
  • PRODUCT INCREASE OUTPUT LIGHT FACTORS
  • This invention can be used for homeopathy * - liquid products :: non-hazardous products ⁇ in order to increase its efficiency.

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)
  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

Le procédé proposé de retraitement de produits pétroliers liquides consiste à réduire lesdits produits en gouttelettes par atomisation hydraulique continue puis fractionnement thermique, la grosseur moyenne des gouttelettes (11) n'excédant pas 0,30 mm et l'intervalle entre l'atomisation et le fractionnement n'exédant pas 5 minutes. Le dispositif de retraitement de produits pétroliers liquides comprend les éléments suivants reliés par des tubes (7): une cuve (1) destinée aux produits pétroliers liquides initiaux (2); un collecteur (3) doté d'une unité de chauffage; une pompe (4) et une tête de pulvérisation (5) présentant une buse de pulvérisation plane ou à déflecteur. Pour atomiser les produits pétroliers (2) à l'aide d'efforts de cisaillement, on utilise une buse de pulvérisation plane présentant une voie cylindrique (16) dotée d'un profil hémisphérique (17) dans la partie supérieure de décharge, dans laquelle est découpé un profil de coin isocèle; le bord supérieur (18) du coin fait face au flux de produits pétroliers liquides (2) et forme un angle droit à son intersection avec l'axe (19) de la voie (16). Pour procéder à l'atomisation utilisant des contraintes de compression, on utilise une buse à déflecteur contenant une voie (12) ainsi qu'un bloc incliné (13); l'axe de symétrie (15) de la voie (12) et la perpendiculaire (14) à la surface du bloc (13) où cette dernière est en intersection avec l'axe (15) forment un angle aigu α.
PCT/RU1995/000218 1994-10-26 1995-10-03 Procede de retraitement de produits petroliers liquides et dispositif de traitement de produits petroliers liquides Ceased WO1996013562A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU94037438 1994-10-26
RU94037438A RU2057785C1 (ru) 1994-10-27 1994-10-27 Способ переработки жидких нефтяных продуктов и устройство для его осуществления (варианты)

Publications (1)

Publication Number Publication Date
WO1996013562A1 true WO1996013562A1 (fr) 1996-05-09

Family

ID=20161336

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/RU1995/000218 Ceased WO1996013562A1 (fr) 1994-10-26 1995-10-03 Procede de retraitement de produits petroliers liquides et dispositif de traitement de produits petroliers liquides

Country Status (2)

Country Link
RU (1) RU2057785C1 (fr)
WO (1) WO1996013562A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011006853A1 (fr) 2009-07-13 2011-01-20 Cambi As Dispositif de buse échangeable pour décompression de matériaux contenant des composés érosifs

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1505870A (en) * 1919-04-04 1924-08-19 Harry H Culmer Process of treating hydrocarbon oils
SU67610A1 (ru) * 1945-03-30 1945-11-30 П.Ф. Похил Способ крекировани нефт ного и подобного сырь
US3736248A (en) * 1972-05-25 1973-05-29 G Hussong Method for the manufacture of coke
SU923633A1 (ru) * 1980-04-18 1982-04-30 Dn Metall Inst Сопло для получения плоской струи i
SU1690852A1 (ru) * 1989-02-27 1991-11-15 Государственный Научно-Исследовательский И Проектный Институт Хлорной Промышленности С Опытным Заводом И Конструкторским Бюро Насадок дл создани вод ной завесы

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1505870A (en) * 1919-04-04 1924-08-19 Harry H Culmer Process of treating hydrocarbon oils
SU67610A1 (ru) * 1945-03-30 1945-11-30 П.Ф. Похил Способ крекировани нефт ного и подобного сырь
US3736248A (en) * 1972-05-25 1973-05-29 G Hussong Method for the manufacture of coke
SU923633A1 (ru) * 1980-04-18 1982-04-30 Dn Metall Inst Сопло для получения плоской струи i
SU1690852A1 (ru) * 1989-02-27 1991-11-15 Государственный Научно-Исследовательский И Проектный Институт Хлорной Промышленности С Опытным Заводом И Конструкторским Бюро Насадок дл создани вод ной завесы

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011006853A1 (fr) 2009-07-13 2011-01-20 Cambi As Dispositif de buse échangeable pour décompression de matériaux contenant des composés érosifs

Also Published As

Publication number Publication date
RU2057785C1 (ru) 1996-04-10

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