WO2002057392A1 - Procede de fabrication de produits petroliers legers et installation correspondante - Google Patents
Procede de fabrication de produits petroliers legers et installation correspondante Download PDFInfo
- Publication number
- WO2002057392A1 WO2002057392A1 PCT/RU2002/000008 RU0200008W WO02057392A1 WO 2002057392 A1 WO2002057392 A1 WO 2002057392A1 RU 0200008 W RU0200008 W RU 0200008W WO 02057392 A1 WO02057392 A1 WO 02057392A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gasoline
- syρya
- products
- ποdachi
- τemπeρaτuρu
- Prior art date
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
- C10G7/00—Distillation of hydrocarbon oils
Definitions
- the inventive group of inventions is subject to the processing of carbohydrate raw materials and each of them is not used for the use of petroleum, it is not loaded.
- the predominantly advantageous product is the supply of hydrocarbons from warm raw materials that produce heavy gasoline - at (35 ⁇ 40) ° C, diesel oil at 120 ° C (- 30 ° C), (-1 ° C), ⁇ 1.5) ° ⁇ , with simultaneous cooling of the specified products at (145 ⁇ 150) ° ⁇ , (225 ⁇ 230) ° ⁇ , (240 ⁇ 245) ° ⁇ , (5 ⁇ 6) ° ⁇ , respectively, and after that, it has an excellent heating of raw materials with an electric furnace for (10 ⁇ 20) ° ⁇ , the temperature of light gasoline is allowed to cool down yu ⁇ eg ⁇ to (85 ⁇ 95) ° C v ⁇ d ⁇ y with ⁇ e ⁇ e ⁇ ad ⁇ m ⁇ em ⁇ e ⁇ a ⁇ u ⁇ y (25 ⁇ 30) ° C, ⁇ em ⁇ e ⁇ a ⁇ u ⁇ u in ⁇ ub ⁇ v ⁇ y em ⁇ s ⁇ i v ⁇ y ⁇ e ⁇ i ⁇ atsi ⁇ nn
- FIG. 1 An simplified installation diagram for the implementation of the process of lighting of non-food products is shown.
- the following parameters must be changed at least: the temperature of raw materials at the input and the exit of the heat exchanger 4 6 vse ⁇ e ⁇ a ⁇ a ⁇ ⁇ d ⁇ g ⁇ eva, ⁇ em ⁇ e ⁇ a ⁇ u ⁇ u ⁇ dyaschi ⁇ ⁇ du ⁇ v on v ⁇ da ⁇ and vy ⁇ da ⁇ ⁇ e ⁇ l ⁇ bmenni ⁇ v 4-6 on vse ⁇ e ⁇ a ⁇ a ⁇ ⁇ d ⁇ g ⁇ eva, ⁇ em ⁇ e ⁇ a ⁇ u ⁇ u on v ⁇ da ⁇ and vy ⁇ da ⁇ and u ⁇ ven ⁇ du ⁇ v in ⁇ echa ⁇ 11-13, 17-19, on ⁇ em ⁇ e ⁇ a ⁇ u ⁇ u v ⁇ da ⁇ and vy ⁇ da ⁇ ⁇ e ⁇ i ⁇ i ⁇ atsi ⁇ nny ⁇ ⁇ l ⁇ nn 14-16 , 20, on carts and in cubic tanks of the latest,
- gas-dense raw materials in the case of heat exchangers 4-6, 8-10 for the specified stages of the temperature, are at a temperature of 98 °, , in case of temperature transients, corresponding to 148.6 ° ⁇ , 228.6 ° ⁇ , 243.6 ° ⁇ , 5.6 ° ⁇ ,
- Vapors of the separated liquid are discharged from the vaporizer (cubic tank) to the reactive section of the cart, where it is separated from them.
- the supply of raw materials and its successive process through the exchange of 4-6 may be subject to a single service.
- Vapors of light gasoline from the compartments of 14-16 are available for exchanges of 8-10 and further to the refrigerators of 28-30, and the cubicals are supplied to the customers (raw materials are supplied to 20).
- 340 ° C eliminates the second major reversal 20. Maintaining a predetermined healthy balance at an accelerating rate of 300 is an The products of the separation of the partition 20 are:
- the products are dielectrics and this allows the use of electric heaters.
- the specific space In case of a decrease in the transmission coefficient, the specific space must also be cleared, i.e., the specific space, i.e. increased area of active heat transfer.
- the use of heaters with a closed cylinder would entail the creation of a compulsory circuit with a complex circuit for the exclusion of heaters.
- the transmission rate of the purchased heaters is much lower than that of the waste heaters, which leads to an even larger increase in its area.
- a simpler short-term heating of the heater might be to account for its inactivity, which is not unimportant in the automation of the industrial process.
- the assessment of the probability of occurrence of an emergency situation is carried out by examining the group of events from an end-user system.
- V is the sign of the event (association) of events; ⁇ - sign of multiplication (intersection) of events; ⁇ (C) - probability of event C; C is an event, an important incident of C;
- Bulgaria ⁇ V ⁇ V ⁇ > at the same time, the product can be used: -- ⁇ - in the installation part of the installation, or ⁇ 2 - outside of the device.
- ⁇ 3 ⁇ 3 V ⁇ 4 .
- ⁇ 4 ( ⁇
- ⁇ ( ⁇ V ⁇ 2 ) ⁇ ⁇ ; You may take advantage of the following conditions: -- ⁇ - to cool down comfortably, or ⁇ 2 - out of the box, more than 50% is compatible, ⁇ . ⁇ . The process is ideal with an excess pressure of more than 2 atm, and ⁇ - of the conversion of pipes.
- ⁇ ⁇ , ⁇ 0 2 .
- ⁇ flower ⁇ may be used only if the heater is off: -- ⁇ - turning off the heater, and 0 2 - turning off the heater.
- ⁇ on a site may happen: ⁇ - in the hardware part of the site, or ⁇ 2 - out of the appliance part.
- ⁇ ⁇ V ⁇ 2 .
- ⁇ ⁇ ⁇ ⁇ 2 .
- C ⁇ ⁇ ⁇ ⁇ 2 .
- ⁇ 3 the presence of a source of ignition, or B - self-ignition (for example, at temperatures above 250 ° C).
- C 2 ⁇ 3 V ⁇ 4 .
- ⁇ 3 ⁇ ⁇ ⁇ 2 .
- ⁇ ( ⁇ > h) 0.1211;
- Event ⁇ 7 is comprised of: ⁇ - Failure to shut off heat due to overpressure, and 2 ⁇ 2 - Failure to shut off heat when overheat.
- ⁇ 4 ⁇ admir ⁇ ⁇ 2 .
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)
- Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
Abstract
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EA200300808A EA005227B1 (ru) | 2001-01-17 | 2002-01-16 | Способ получения светлых нефтепродуктов и установка для его осуществления |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU2001101378 | 2001-01-17 | ||
RU2001101378/04A RU2184136C1 (ru) | 2001-01-17 | 2001-01-17 | Способ получения светлых нефтепродуктов и установка для его осуществления |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002057392A1 true WO2002057392A1 (fr) | 2002-07-25 |
Family
ID=20244922
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/RU2002/000008 WO2002057392A1 (fr) | 2001-01-17 | 2002-01-16 | Procede de fabrication de produits petroliers legers et installation correspondante |
Country Status (3)
Country | Link |
---|---|
EA (1) | EA005227B1 (fr) |
RU (1) | RU2184136C1 (fr) |
WO (1) | WO2002057392A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10356245B4 (de) * | 2003-12-02 | 2007-01-25 | Alphakat Gmbh | Verfahren zur Erzeugung von Dieselöl aus kohlenwasserstoffhaltigen Reststoffen sowie eine Vorrichtung zur Durchführung dieses Verfahrens |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9663721B2 (en) * | 2014-09-04 | 2017-05-30 | Uop Llc | Heat recovery from a naphtha fractionation column |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4087354A (en) * | 1976-11-18 | 1978-05-02 | Uop Inc. | Integrated heat exchange on crude oil and vacuum columns |
US4292140A (en) * | 1979-02-13 | 1981-09-29 | Ishikawajima-Harima Jukogyo Kabushiki Kaisha | Process for recovering heat in distillation process |
RU2058368C1 (ru) * | 1993-08-02 | 1996-04-20 | Талгат Галеевич Умергалин | Способ фракционирования нефти |
RU2100403C1 (ru) * | 1996-05-12 | 1997-12-27 | Валерий Георгиевич Леонтьевский | Способ фракционирования нефти и установка для его осуществления |
-
2001
- 2001-01-17 RU RU2001101378/04A patent/RU2184136C1/ru not_active IP Right Cessation
-
2002
- 2002-01-16 WO PCT/RU2002/000008 patent/WO2002057392A1/fr not_active Application Discontinuation
- 2002-01-16 EA EA200300808A patent/EA005227B1/ru not_active IP Right Cessation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4087354A (en) * | 1976-11-18 | 1978-05-02 | Uop Inc. | Integrated heat exchange on crude oil and vacuum columns |
US4292140A (en) * | 1979-02-13 | 1981-09-29 | Ishikawajima-Harima Jukogyo Kabushiki Kaisha | Process for recovering heat in distillation process |
RU2058368C1 (ru) * | 1993-08-02 | 1996-04-20 | Талгат Галеевич Умергалин | Способ фракционирования нефти |
RU2100403C1 (ru) * | 1996-05-12 | 1997-12-27 | Валерий Георгиевич Леонтьевский | Способ фракционирования нефти и установка для его осуществления |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10356245B4 (de) * | 2003-12-02 | 2007-01-25 | Alphakat Gmbh | Verfahren zur Erzeugung von Dieselöl aus kohlenwasserstoffhaltigen Reststoffen sowie eine Vorrichtung zur Durchführung dieses Verfahrens |
Also Published As
Publication number | Publication date |
---|---|
EA200300808A1 (ru) | 2004-06-24 |
RU2184136C1 (ru) | 2002-06-27 |
EA005227B1 (ru) | 2004-12-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3332925B2 (ja) | 改質方法および装置 | |
TW393509B (en) | Apparatus and process for reclaiming fuel oil from waste oil | |
CN108350759A (zh) | 使用独立双有机物兰金循环由柴油加氢处理-加氢裂化和常压蒸馏-石脑油加氢处理-芳烃设备中的废热***发电 | |
CN108350757B (zh) | 一种发电***和回收由石化精炼***产生的热能的方法 | |
CA2907885C (fr) | Traitement de carburant diesel a partir d'huile usagee | |
CN100531842C (zh) | 用于对混合流体进行分离的小型蒸馏装置和这类混合流体分离的蒸馏方法 | |
CN116261586A (zh) | 将混合塑料废物升级改造为清洁汽油和柴油燃料及其他产品的整合的连续转化和分离方法 | |
WO2002057392A1 (fr) | Procede de fabrication de produits petroliers legers et installation correspondante | |
HRPK20160331B3 (hr) | Postupak proizvodnje goriva za energetiku i uređaj za proizvodnju goriva | |
US20100242499A1 (en) | Method for re-gasification of liquid natural gas | |
US5286349A (en) | Apparatus for reclaiming useful oil products from waste oil | |
WO1983001070A1 (fr) | Appareil de rectification de solutions fermentees et procede de commande automatique de cet appareil | |
US20160160130A1 (en) | Integrated Vacuum Distillate Recovery Process | |
JPS59157179A (ja) | 水素と炭化水素を含有するガス混合物の化学処理用装置 | |
WO1997043355A1 (fr) | Procede et installations de fractionnement du petrole brut | |
US1524340A (en) | Process of heat application and apparatus therefor | |
CN101691498B (zh) | 一种用于降低焦化装置循环比的重蜡油溶剂脱沥青工艺 | |
RU2058368C1 (ru) | Способ фракционирования нефти | |
WO2004076595A1 (fr) | Procede de recyclage de dechets de caoutchouc | |
US2335727A (en) | Waste heat recovery system | |
RU2525984C1 (ru) | Электрообессоливающая установка | |
US2058355A (en) | Method and apparatus for transporting hydrocarbon liquids | |
RU2254897C1 (ru) | Установка атмосферной перегонки нефти | |
RU61151U1 (ru) | Установка фракционирования углеводородного сырья | |
RU2657445C1 (ru) | Блочно-комплектная абсорбционная установка улавливания легких фракций углеводородов |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
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: 200300808 Country of ref document: EA |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
32PN | Ep: public notification in the ep bulletin as address of the adressee cannot be established |
Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 69(1)EPC, EPO FORM 1205A OF 01.12.2003. |
|
122 | Ep: pct application non-entry in european phase | ||
NENP | Non-entry into the national phase |
Ref country code: JP |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: JP |