WO1997023262A1 - Installation pour la distillation de produits liquides - Google Patents
Installation pour la distillation de produits liquides Download PDFInfo
- Publication number
- WO1997023262A1 WO1997023262A1 PCT/RU1996/000303 RU9600303W WO9723262A1 WO 1997023262 A1 WO1997023262 A1 WO 1997023262A1 RU 9600303 W RU9600303 W RU 9600303W WO 9723262 A1 WO9723262 A1 WO 9723262A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- vχοdοm
- liquid
- magisτρali
- οτvοda
- installation
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/10—Vacuum distillation
- B01D3/101—Recirculation of the fluid used as fluid working medium in a vacuum creating device
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/10—Vacuum distillation
-
- 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
- C10G7/06—Vacuum distillation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S203/00—Distillation: processes, separatory
- Y10S203/16—Combination
Definitions
- the inventive product is not available for the installation of processed liquids or consumable products.
- the required vacuum depth in the above-mentioned installation is achieved by the e-waste pump, in the case of e-waste (active) operation.
- the task posed is solved by the fact that in the installation of a liquid product that is a part of a vacuum of a product of a product v ⁇ lyuchayuschee s ⁇ uyny a ⁇ a ⁇ a ⁇ , ⁇ d ⁇ lyuchenny gaz ⁇ vym v ⁇ d ⁇ m ⁇ magis ⁇ ali ⁇ v ⁇ da ⁇ a ⁇ gaz ⁇ v ⁇ y ⁇ azy va ⁇ uumn ⁇ y ⁇ l ⁇ nny, va ⁇ uums ⁇ zdayuschee us ⁇ ys ⁇ v ⁇ d ⁇ lni ⁇ eln ⁇ snabzhen ⁇ nas ⁇ s ⁇ m and se ⁇ a ⁇ a ⁇ m, ⁇ ichem nas ⁇ s v ⁇ d ⁇ m ⁇ d ⁇ lyuchen ⁇ se ⁇ a ⁇ a ⁇ u, s ⁇ uyny a ⁇ a ⁇ a ⁇ vy ⁇ lnen zhid ⁇ s ⁇ n ⁇ -gaz ⁇ vym and ⁇ d ⁇ lyuchen vy ⁇
- An articulated apparatus may have been carried out by a large number of transducers with a high discharge cross-section of the mainspring for the transfer of oil to the mains oil.
- P ⁇ edlagae maya us ⁇ an ⁇ v ⁇ a ⁇ zv ⁇ lyae ⁇ ⁇ dde ⁇ zhiva ⁇ ⁇ ebuemy ⁇ ⁇ e ⁇ n ⁇ l ⁇ gii u ⁇ ven ⁇ az ⁇ ezheniya in va ⁇ uumn ⁇ y ⁇ l ⁇ nne ⁇ u ⁇ em ⁇ ach ⁇ i of ⁇ sledney ⁇ a ⁇ gaz ⁇ v ⁇ y ⁇ azy with ⁇ sleduyuschey ⁇ ndensatsiey chas ⁇ i uglev ⁇ d ⁇ d ⁇ v (if ne ⁇ e ⁇ e ⁇ e ⁇ ab ⁇ i) in ⁇ chn ⁇ y chas ⁇ i s ⁇ uyn ⁇ g ⁇ a ⁇ a ⁇ a ⁇ a and magis ⁇ ali him.
- Condensed gases are compressed in the installation to pressure, and if they are used, they can be used for consumer technical needs.
- an active working fluid is a liquid medium, which is a hazardous product. This prevents pollution of the environment, since there is no release of gas into the atmosphere, which is hazardous to the environment.
- the cannon can be carried out by a large part. This is due to the fact that in this embodiment, there is a slight increase in the positive effect of the process and the operation of a vacuum-generating device.
- an additional impulse of a liquid working medium will increase the degree of compression of the pumped-out gas mixture.
- the indicated experimental methods were indicated, which are most expediently directed to a second or subsequent loss of liquid at a rate of 30% or less.
- the most efficient way of working is to relieve the pressure, when, because of the high pressure, the pressure is very high.
- the installation of a liquid product distillation works with the following process.
- the heated liquid product (in the case of non-transformers - non-crude raw materials) is supplied to the vacuum chamber 1 with a pressure of 10-60 mm r.h.
- ⁇ unit 6 with a pressure greater than 0, 1 1 ⁇ Pa the two-phase mixture is divided into a gas phase and a liquid medium.
- the inventive invention which is also inadequately processed, may be used in chemical, food, pharmaceutical, and other industrial applications.
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9523547A JP2000502599A (ja) | 1995-12-22 | 1996-10-11 | 液体製品蒸留ユニット |
DE69632741T DE69632741D1 (de) | 1995-12-22 | 1996-10-11 | Anlage zur destillation eines flussigen produktes |
CA002241160A CA2241160C (en) | 1995-12-22 | 1996-10-11 | Unit for distillation of a liquid product |
US09/091,286 US6086721A (en) | 1995-12-22 | 1996-10-11 | Facility for distilling a liquid product |
EP96935634A EP0882480B1 (en) | 1995-12-22 | 1996-10-11 | Facility for distilling a liquid product |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU95121523 | 1995-12-22 | ||
RU95121523/04A RU2091117C1 (ru) | 1995-12-22 | 1995-12-22 | Установка для перегонки жидкого продукта |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1997023262A1 true WO1997023262A1 (fr) | 1997-07-03 |
Family
ID=20174915
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/RU1996/000303 WO1997023262A1 (fr) | 1995-12-22 | 1996-10-11 | Installation pour la distillation de produits liquides |
Country Status (8)
Country | Link |
---|---|
US (1) | US6086721A (ru) |
EP (1) | EP0882480B1 (ru) |
JP (1) | JP2000502599A (ru) |
CA (1) | CA2241160C (ru) |
DE (1) | DE69632741D1 (ru) |
ES (1) | ES2221937T3 (ru) |
RU (1) | RU2091117C1 (ru) |
WO (1) | WO1997023262A1 (ru) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2550514C2 (ru) * | 2013-09-13 | 2015-05-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Уфимский государственный нефтяной технический университет" | Способ испарения многокомпонентных смесей и способ подачи горячей струи в ректификационные колонны |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6346173B2 (en) * | 1996-08-16 | 2002-02-12 | Evgueni D. Petroukhine | Method for the vacuum distillation of a liquid product, particularly oil stock, (variants) and system for realizing the same |
RU2108365C1 (ru) * | 1997-02-14 | 1998-04-10 | Сергей Анатольевич Попов | Установка для перегонки жидкого продукта (варианты) |
RU2114893C1 (ru) * | 1997-09-04 | 1998-07-10 | Сергей Анатольевич Попов | Способ перегонки многокомпонентной смеси и установка для его осуществления |
WO1999030792A1 (fr) * | 1997-12-16 | 1999-06-24 | Sergei Anatolievich Popov | Procede de generation de vide dans des colonnes d'echange de masses |
RU2135842C1 (ru) | 1998-01-27 | 1999-08-27 | Попов Сергей Анатольевич | Способ работы насосно-эжекторной установки и насосно-эжекторная установка для его осуществления |
RU2135843C1 (ru) | 1998-04-27 | 1999-08-27 | Попов Сергей Анатольевич | Способ работы насосно-эжекторной установки и установка для его осуществления |
RU2146778C1 (ru) * | 1998-08-25 | 2000-03-20 | Попов Сергей Анатольевич | Способ работы насосно-эжекторной установки и насосно-эжекторная установка для реализации способа ее работы |
US6817837B2 (en) | 2002-07-19 | 2004-11-16 | Walker-Dawson Interest, Inc. | Jet pump with recirculating motive fluid |
EP1540190A1 (en) * | 2002-07-19 | 2005-06-15 | Walker-Dawson Interests, Inc. | Recirculating jet pump and method of moving material |
RU2287355C1 (ru) * | 2005-12-27 | 2006-11-20 | Александр Владимирович Косс | Способ подготовки нефти и/или нефтепродуктов к переработке и установка для его осуществления |
RU2354430C1 (ru) * | 2007-12-20 | 2009-05-10 | Валерий Григорьевич Цегельский | Способ создания вакуума в вакуумной колонне перегонки нефтяного сырья и установка для осуществления способа |
MX2012011568A (es) * | 2010-04-09 | 2012-11-16 | Abaridy Pty Ltd | Sistema de absorcion de vapor. |
US20150184907A1 (en) * | 2014-01-02 | 2015-07-02 | Serguei Popov | Condensing and absorbing gas compression unit and variants thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3579307A (en) * | 1968-12-31 | 1971-05-18 | Asahi Chemical Ind | Apparatus for recovering acrylonitrile monomer in the production of a polymer |
SU1273379A1 (ru) * | 1985-03-15 | 1986-11-30 | Всесоюзный научно-исследовательский институт углеводородного сырья | Способ конденсации смеси паров вакуумной колонны процесса перегонки нефти |
EP0634198A1 (en) * | 1993-07-08 | 1995-01-18 | Agfa-Gevaert N.V. | Installation for controlling the underpressure in an evaporator apparatus |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1567429A (en) * | 1923-08-25 | 1925-12-29 | Alfred R Earl | Process for series separation of crude petroleum |
US2105935A (en) * | 1930-11-26 | 1938-01-18 | Foster Wheeler Corp | Oil treatment |
GB1109413A (en) * | 1967-03-13 | 1968-04-10 | Paul Alfred Johnson | Improvements in wall plaques, statuettes, advertising devices and the like |
JPS588281B2 (ja) * | 1979-02-13 | 1983-02-15 | 石川島播磨重工業株式会社 | 蒸留処理設備における熱回収方法及びその装置 |
US4695349A (en) * | 1984-03-07 | 1987-09-22 | Linde Aktiengesellschaft | Process and apparatus for distillation and/or stripping |
US5209828A (en) * | 1991-12-23 | 1993-05-11 | Mobil Oil Corporation | System for concentrating a spent caustic stream |
DE59610308D1 (de) * | 1996-11-19 | 2003-05-08 | Sulzer Chemtech Ag Winterthur | Destillationsanlage mit Wärmepumpe |
RU2108365C1 (ru) * | 1997-02-14 | 1998-04-10 | Сергей Анатольевич Попов | Установка для перегонки жидкого продукта (варианты) |
-
1995
- 1995-12-22 RU RU95121523/04A patent/RU2091117C1/ru active
-
1996
- 1996-10-11 DE DE69632741T patent/DE69632741D1/de not_active Expired - Lifetime
- 1996-10-11 CA CA002241160A patent/CA2241160C/en not_active Expired - Fee Related
- 1996-10-11 JP JP9523547A patent/JP2000502599A/ja active Pending
- 1996-10-11 ES ES96935634T patent/ES2221937T3/es not_active Expired - Lifetime
- 1996-10-11 US US09/091,286 patent/US6086721A/en not_active Expired - Lifetime
- 1996-10-11 EP EP96935634A patent/EP0882480B1/en not_active Expired - Lifetime
- 1996-10-11 WO PCT/RU1996/000303 patent/WO1997023262A1/ru active IP Right Grant
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3579307A (en) * | 1968-12-31 | 1971-05-18 | Asahi Chemical Ind | Apparatus for recovering acrylonitrile monomer in the production of a polymer |
SU1273379A1 (ru) * | 1985-03-15 | 1986-11-30 | Всесоюзный научно-исследовательский институт углеводородного сырья | Способ конденсации смеси паров вакуумной колонны процесса перегонки нефти |
EP0634198A1 (en) * | 1993-07-08 | 1995-01-18 | Agfa-Gevaert N.V. | Installation for controlling the underpressure in an evaporator apparatus |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2550514C2 (ru) * | 2013-09-13 | 2015-05-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Уфимский государственный нефтяной технический университет" | Способ испарения многокомпонентных смесей и способ подачи горячей струи в ректификационные колонны |
Also Published As
Publication number | Publication date |
---|---|
RU2091117C1 (ru) | 1997-09-27 |
EP0882480A1 (en) | 1998-12-09 |
ES2221937T3 (es) | 2005-01-16 |
EP0882480A4 (en) | 2000-08-16 |
DE69632741D1 (de) | 2004-07-22 |
EP0882480B1 (en) | 2004-06-16 |
JP2000502599A (ja) | 2000-03-07 |
CA2241160A1 (en) | 1997-07-03 |
CA2241160C (en) | 2003-07-08 |
US6086721A (en) | 2000-07-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO1997023262A1 (fr) | Installation pour la distillation de produits liquides | |
EP0783910A1 (en) | Process for the vacuum distillation of a liquid product, preferably crude petroleum, and a facility for carrying out the process | |
WO1998044262A1 (fr) | Mode de fonctionnement d'un appareil a jet | |
RU2113634C1 (ru) | Способ работы насосно-эжекторной установки для перегонки жидкого продукта (54) | |
US3548568A (en) | Methods of and apparatus for liquid-vapor contact and phase separation | |
US6120254A (en) | Jet pump for creating the vacuum conditions required for liquid product distillation | |
WO1998058176A1 (fr) | Appareil de pompage et d'ejection et variantes | |
WO1996016711A1 (fr) | Installation de distillation sous vide d'un produit liquide | |
WO1999008003A1 (fr) | Procede de generation de vide et appareil de pompage et d'ejection permettant de mettre en oeuvre ce procede | |
WO2000001952A1 (fr) | Procede de fonctionnement d'un appareil de pompage et d'ejection et appareil de pompage et d'ejection a plusieurs etages permettant de mettre en oeuvre ce procede | |
WO2000077406A2 (fr) | Procede de compression d'un milieu gazeux contenant des hydrocarbures | |
WO1999001670A1 (fr) | Installation de pompage et d'ejection | |
US6350351B1 (en) | Plant for the vacuum distillation of a liquid product | |
RU2073123C1 (ru) | Насосно-эжекторная установка | |
RU2095392C1 (ru) | Установка вакуумной перегонки жидкого продукта | |
US6106243A (en) | Jet pump installation for creating a vacuum during distillation of a liquid | |
RU2146778C1 (ru) | Способ работы насосно-эжекторной установки и насосно-эжекторная установка для реализации способа ее работы | |
RU2083638C1 (ru) | Способ вакуумной перегонки жидкого продукта и установка для его осуществления | |
RU2133385C1 (ru) | Насосно-эжекторная установка | |
WO1997020013A1 (fr) | Procede de distillation d'un produit liquide | |
SU866298A1 (ru) | Насосна установка | |
WO1999022148A1 (fr) | Procede de fonctionnement d'un installation de pompage et d'ejection, et installation s'y rapportant | |
RU2212569C1 (ru) | Способ создания вакуума в вакуумной колонне и установка создания вакуума (варианты) | |
US6277247B1 (en) | Operation method of a plant for distilling liquid products and plant for realizing the same | |
WO2001090276A1 (fr) | Procede de distillation de petrole |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): CA JP US |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 09091286 Country of ref document: US |
|
ENP | Entry into the national phase |
Ref document number: 2241160 Country of ref document: CA Ref country code: CA Ref document number: 2241160 Kind code of ref document: A Format of ref document f/p: F |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1996935634 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 1996935634 Country of ref document: EP |
|
WWG | Wipo information: grant in national office |
Ref document number: 1996935634 Country of ref document: EP |