[go: up one dir, main page]

WO1999031198A2 - Installation permettant d'eliminer le dioxyde de carbone contenu dans des gaz et procede d'exploitation de cette installation - Google Patents

Installation permettant d'eliminer le dioxyde de carbone contenu dans des gaz et procede d'exploitation de cette installation Download PDF

Info

Publication number
WO1999031198A2
WO1999031198A2 PCT/RU1998/000416 RU9800416W WO9931198A2 WO 1999031198 A2 WO1999031198 A2 WO 1999031198A2 RU 9800416 W RU9800416 W RU 9800416W WO 9931198 A2 WO9931198 A2 WO 9931198A2
Authority
WO
WIPO (PCT)
Prior art keywords
ugleροda
gas
gases
diοκsida
dioxide
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/RU1998/000416
Other languages
English (en)
Russian (ru)
Other versions
WO1999031198A3 (fr
Inventor
Oleg Vianorovich Dogadin
Ludmila Alexeevna Goden
Lev Alexeevich Uvarov
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
Priority claimed from RU97121165/03A external-priority patent/RU97121165A/ru
Application filed by Individual filed Critical Individual
Publication of WO1999031198A2 publication Critical patent/WO1999031198A2/fr
Publication of WO1999031198A3 publication Critical patent/WO1999031198A3/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34—Arrangements for separating materials produced by the well
    • E21B43/40—Separation associated with re-injection of separated materials
    • 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2

Definitions

  • ⁇ ⁇ _U are known for the installation and the means for pumping liquid carbon dioxide and water saturated with carbon dioxide into the product, for the purpose of displacing the noise in order to increase the efficiency of the process.
  • Ne ⁇ ⁇ yan ⁇ y gas ⁇ sle se ⁇ a ⁇ a ⁇ ii is ⁇ lzuyu ⁇ in ⁇ aches ⁇ ve ⁇ a d ⁇ lni ⁇ eln ⁇ g ⁇ ⁇ m ⁇ imi ⁇ vaniya for the purpose z.a ⁇ ach ⁇ i in ⁇ las ⁇ with ⁇ mez ⁇ u ⁇ chn ⁇ y ⁇ sush ⁇ y di ⁇ sida ugle ⁇ da between s ⁇ u ⁇ enyami ⁇ m ⁇ essii ⁇ ie ⁇ ilengli ⁇ lem.
  • the cost of the base product is that it is supplied with CO 2 in an inactive gas up to 20 units. It is disposed of in the atmosphere and as a result of this occurs the contamination of the medium.
  • D ⁇ ugim ned ⁇ s ⁇ a ⁇ m s ⁇ s ⁇ ba and u ⁇ azann ⁇ y us ⁇ a- n ⁇ v ⁇ i yavlyae ⁇ sya is ⁇ lz ⁇ vanie bl ⁇ a amin ⁇ v ⁇ y ⁇ chis ⁇ i and ⁇ i- e ⁇ ilengli ⁇ lev ⁇ y ⁇ mezhu ⁇ chn ⁇ y ⁇ sush ⁇ i di ⁇ sida ugle ⁇ da in ⁇ tsesse d ⁇ lni ⁇ eln ⁇ g ⁇ ⁇ m ⁇ emi ⁇ vaniya for za ⁇ ach ⁇ i in ⁇ las ⁇ and s ⁇ ve ⁇ s ⁇ venn ⁇ , ne ⁇ b ⁇ dim ⁇ s ⁇ znachi ⁇ elny ⁇ ⁇ a ⁇ i- ⁇ alny
  • ⁇ - ⁇ ye is ⁇ lzuyu ⁇ sya in ⁇ m ⁇ le ⁇ sny ⁇ ene ⁇ g ⁇ e ⁇ n ⁇ l ⁇ giches ⁇ i ⁇ us ⁇ an ⁇ v ⁇ a ⁇ with ⁇ edva ⁇ i ⁇ eln ⁇ y ⁇ chis ⁇ y szha ⁇ y ⁇ dym ⁇ vy ⁇ gaz ⁇ v ⁇ di ⁇ sida ugle ⁇ da, and glub ⁇ im ⁇ lazhdeniem ⁇ chischen- ny ⁇ dym ⁇ vy ⁇ gaz ⁇ v, in u ⁇ dyaschi ⁇ atmosphere.
  • the proposed method is carried out as follows.
  • the combustion chamber I which is used for the generation of compressed flue gases, fumes are combusted and fumes are exhausted with a pressure of 0.3%, which is emitted.
  • Combustion exhaust chambers I compressed flue gases have a temperature of about 20 ° ⁇ and contain about 9% »of carbon dioxide.
  • ⁇ na ⁇ n ⁇ m e ⁇ n ⁇ mayze ⁇ e 2 e ⁇ i gases ⁇ lazhdayu ⁇ sya v ⁇ d ⁇ y, is ⁇ lzuem ⁇ y at ⁇ ebi ⁇ elya ⁇ e ⁇ la, d ⁇ ⁇ em ⁇ e ⁇ a ⁇ u ⁇ y ⁇ l ⁇ 50 ° C, and Part v ⁇ dyany ⁇ ⁇ a ⁇ v, s ⁇ de ⁇ zh, aschi ⁇ sya in szha ⁇ y ⁇ dym ⁇ vy ⁇ gaza ⁇ , ⁇ ndensi ⁇ ue ⁇ sya with allocation s ⁇ y ⁇ y ⁇ e ⁇ l ⁇ - ⁇ y ⁇ ndensatsii ⁇ a ⁇ v v ⁇ dy ⁇ b ⁇ az ⁇ vaniem ⁇ a ⁇ eln ⁇ m and moisture.
  • the flue gases are exhausted to a suitable regeneration 4, and the product is cooled to a com Further ⁇ asshi ⁇ yayu ⁇ sya gases in pressure ⁇ u ⁇ b ⁇ de ⁇ ande ⁇ e 7 d ⁇ bzhz ⁇ g ⁇ ⁇ a ⁇ ⁇ m ⁇ s ⁇ e ⁇ n ⁇ mu, ⁇ i e ⁇ m i ⁇ ⁇ em ⁇ e ⁇ a ⁇ u ⁇ a snizhae ⁇ sya d ⁇ « ⁇ 0 ⁇ C.
  • the latches 16 and 25 are turned off and with the help of the exhaust pipe 22, the liquefier is filled with hot water from the temperature of 18 ° C from the base 18 ° C. Panel 20, which was switched off by the prisone, in tank 18, pressure of about 0.2 PS is maintained. Then, the latches 26 and 16 are shut off and delivered to the suspension of the complete melting of the carbon dioxide.
  • P ⁇ i s ⁇ n ⁇ shenii 1 1 by weight and v ⁇ dy di ⁇ sida ugle ⁇ da, na ⁇ dyaschi ⁇ sya in ⁇ zhizhi ⁇ ele, Naya ⁇ nech- ⁇ avn ⁇ vesnaya ⁇ em ⁇ e ⁇ a ⁇ u ⁇ a ⁇ b ⁇ azuyuscheysya mixture s ⁇ s ⁇ avlya- e ⁇ ⁇ l ⁇ ⁇ 0 ⁇ C.
  • the latches 16 and 26 are turned off and the water from the fluidizer is burnt to the tank of cold water, and the gate 12 is turned off.
  • the system is located in the original condition of the above-mentioned processors and, starting with the loading of the fluidizer, is in use. In order to equalize all the operating processes, it is necessary to equalize

Landscapes

  • Geology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mining & Mineral Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • Physics & Mathematics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Gas Separation By Absorption (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Radio Relay Systems (AREA)

Abstract

Cette invention se rapporte à l'extraction du pétrole et du gaz à partir de puits de forage, et concerne plus précisément le traitement et l'exploitation de gisements pétroliers terrestres ou maritimes ainsi que la séparation de gaz pétroliers tout en tenant compte de la réinjection des matériaux séparés. Cette invention peut être utilisée dans l'industrie du gaz et du pétrole afin d'éliminer le dioxyde de carbone contenu dans les gaz. Cette installation comprend les éléments suivants connectés en série: une chambre de combustion (1), un économiseur sous pression (2), un séparateur d'humidité (3) ainsi qu'un régénérateur de réfrigération (4). Le régénérateur (4) est connecté par l'intermédiaire de la conduite (5) du flux de gaz direct à un turbo-détendeur (7), puis à un séparateur (8) de dioxyde de carbone solide. Le séparateur (8) est connecté au régénérateur et à un conduit de fumées (9) par l'intermédiaire de la conduite (6) du flux en retour; il est également connecté à un liquéfacteur (13) par l'intermédiaire de la conduite (10) de dioxyde de carbone solide et d'un dispositif à vis sans fin (11). Le liquéfacteur (13) est connecté à la vis sans fin (11), à un accumulateur (14) et à une pompe (23) par l'intermédiaire de clapets (12, 13, 17). Des réservoirs (18, 19) d'eau chaude et d'eau froide comportent une admission de vapeur et une admission d'eau provenant d'un conduit d'eau chaude. Les gaz comprimés et de type fumée qui se forment dans la chambre de combustion (1) sont refroidis dans l'économiseur sous pression (2) de manière à séparer les gouttelettes d'humidité, ainsi que dans le régénérateur de réfrigération (4). Les gaz sont ensuite détendus dans le turbo-détendeur (7) et refroidis jusqu'à ce que l'on atteigne la température de formation de dioxyde de carbone solide. On procède enfin à la fusion du dioxyde de carbone solide une fois celui-ci séparé dans le séparateur (8) et chargé dans le liquéfacteur (13).
PCT/RU1998/000416 1997-12-18 1998-12-17 Installation permettant d'eliminer le dioxyde de carbone contenu dans des gaz et procede d'exploitation de cette installation Ceased WO1999031198A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU97121165/03A RU97121165A (ru) 1997-12-18 Установка для очистки газов от диоксида углерода и способ ее эксплуатации
RU97121165 1997-12-18

Publications (2)

Publication Number Publication Date
WO1999031198A2 true WO1999031198A2 (fr) 1999-06-24
WO1999031198A3 WO1999031198A3 (fr) 1999-09-10

Family

ID=20200245

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/RU1998/000416 Ceased WO1999031198A2 (fr) 1997-12-18 1998-12-17 Installation permettant d'eliminer le dioxyde de carbone contenu dans des gaz et procede d'exploitation de cette installation

Country Status (1)

Country Link
WO (1) WO1999031198A2 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102257341A (zh) * 2008-12-19 2011-11-23 乔治洛德方法研究和开发液化空气有限公司 通过低温冷凝捕集二氧化碳的方法
CN102519299A (zh) * 2011-12-15 2012-06-27 东南大学 一种降低空气含湿量来提高冷却塔冷却效果的系统

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU572632A1 (ru) * 1975-07-11 1977-09-15 Всесоюзный Научно-Исследовательский Институт Холодильной Промышленности Способ получени жидкой двуокиси углерода и сухого льда
SU939895A1 (ru) * 1979-08-17 1982-06-30 Всесоюзный Научно-Исследовательский Институт Холодильной Промышленности Установка дл получени жидкой и газообразной двуокиси углерода
SU998820A1 (ru) * 1981-05-27 1983-02-23 Всесоюзный Научно-Исследовательский И Проектный Институт По Переработке Газа Способ отделени диоксида углерода от углеводородных смесей
FR2514071B1 (fr) * 1981-10-06 1986-09-26 Chaudot Gerard Procede de production de gisements d'hydrocarbure avec reinjection d'effluents dans le gisement ou dans le ou les puits et installation pour la mise en oeuvre dudit procede
SU1263980A1 (ru) * 1985-04-08 1986-10-15 Северо-Западное Отделение Всесоюзного Государственного Научно-Исследовательского И Проектно-Конструкторского Института "Внипиэнергопром" Способ ожижени твердой двуокиси углерода
US4765407A (en) * 1986-08-28 1988-08-23 Amoco Corporation Method of producing gas condensate and other reservoirs
SU1677465A1 (ru) * 1989-01-04 1991-09-15 Всесоюзный Научно-Исследовательский И Проектный Институт По Переработке Газа Способ отделени диоксида углерода от углеводородных смесей
RU2117519C1 (ru) * 1996-09-26 1998-08-20 Валерий Казимирович Корнев Способ уменьшения токсичных выбросов устройств, сжигающих органическое топливо

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102257341A (zh) * 2008-12-19 2011-11-23 乔治洛德方法研究和开发液化空气有限公司 通过低温冷凝捕集二氧化碳的方法
CN102519299A (zh) * 2011-12-15 2012-06-27 东南大学 一种降低空气含湿量来提高冷却塔冷却效果的系统

Also Published As

Publication number Publication date
WO1999031198A3 (fr) 1999-09-10

Similar Documents

Publication Publication Date Title
US8887504B2 (en) Non-to-minimally fractionalized biomass-fueled renewable energy
US4546829A (en) Enhanced oil recovery process
US4499946A (en) Enhanced oil recovery process and apparatus
CN101283220B (zh) 允许俘获产生的所有二氧化碳的氧化燃烧法
WO2002075112A1 (fr) Procede de mise en valeur de reserves d'hydrocarbures (et variantes) et complexe destine a sa mise en oeuvre (et variantes)
US7669418B2 (en) Heat energy supply system and method, and reconstruction method of the system
US6079222A (en) Method for preparing deep-frozen liquid gas
EA024378B1 (ru) Способ для гидравлического разрыва подземного пласта
MX2008011856A (es) Metodo y aparato para recuperar y transportar gas metano.
US20040261952A1 (en) Portable brine evaporator unit, process, and system
CN102132098B (zh) 将煤炭输送到热电厂用于燃烧的方法
CN109386316A (zh) 一种lng冷能和bog燃烧能联合利用系统及方法
CN108251148A (zh) 一种危废、固废含油泥砂热解析综合利用处置方法
US20220389866A1 (en) Thermal energy storage system comprising a packed-bed heat storage unit and a packed-bed cold storage unit, and method for operating a thermal energy storage system
US20060010865A1 (en) Produced water disposal method
Mazumder et al. Integrated ejector‐based flare gas recovery and on‐site desalination of produced water in Shale gas production
US8820080B2 (en) Nonfractionalized biomass-fueled refrigerant-based cogeneration
WO1999031198A2 (fr) Installation permettant d'eliminer le dioxyde de carbone contenu dans des gaz et procede d'exploitation de cette installation
US6971238B1 (en) Method for disposal of produced water
CN209242904U (zh) 一种防止污泥干化装置混合废气冷凝的装置
Nguyen et al. Development of gas turbine steam injection water recovery (SIWR) system
Rettenberger Utilization of landfill gas and safety measures
WO1996036472A1 (fr) Procede de recyclage de dechets caoutchouteux
CN109399890A (zh) 一种防止污泥干化装置混合废气冷凝的装置及方法
CN214693827U (zh) 一种含油污泥处理装置

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A2

Designated state(s): CA JP US

AL Designated countries for regional patents

Kind code of ref document: A2

Designated state(s): 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

121 Ep: the epo has been informed by wipo that ep was designated in this application
AK Designated states

Kind code of ref document: A3

Designated state(s): CA JP US

AL Designated countries for regional patents

Kind code of ref document: A3

Designated state(s): 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

122 Ep: pct application non-entry in european phase