CA2219244A1 - Procede et dispositif de fabrication d'un hydrocarbure, et produit ainsi fabrique - Google Patents

Procede et dispositif de fabrication d'un hydrocarbure, et produit ainsi fabrique Download PDF

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Publication number
CA2219244A1
CA2219244A1 CA 2219244 CA2219244A CA2219244A1 CA 2219244 A1 CA2219244 A1 CA 2219244A1 CA 2219244 CA2219244 CA 2219244 CA 2219244 A CA2219244 A CA 2219244A CA 2219244 A1 CA2219244 A1 CA 2219244A1
Authority
CA
Canada
Prior art keywords
hydrate
cooling
product
water
hydrocarbon
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.)
Abandoned
Application number
CA 2219244
Other languages
English (en)
Inventor
Otto Skovholt
Geir B. Lorentzen
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.)
Equinor ASA
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 CA2219244A1 publication Critical patent/CA2219244A1/fr
Abandoned legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10—Working-up natural gas or synthetic natural gas
    • C10L3/108—Production of gas hydrates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006—Controlling or regulating processes
    • B01J19/0013—Controlling the temperature of the process
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1862—Stationary reactors having moving elements inside placed in series
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/04—Pressure vessels, e.g. autoclaves
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C11/00—Use of gas-solvents or gas-sorbents in vessels
    • F17C11/007—Use of gas-solvents or gas-sorbents in vessels for hydrocarbon gases, such as methane or natural gas, propane, butane or mixtures thereof [LPG]
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00121—Controlling the temperature by direct heating or cooling
    • B01J2219/00123—Controlling the temperature by direct heating or cooling adding a temperature modifying medium to the reactants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/0015—Controlling the temperature by thermal insulation means
    • B01J2219/00155—Controlling the temperature by thermal insulation means using insulating materials or refractories
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00162—Controlling or regulating processes controlling the pressure
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/18—Details relating to the spatial orientation of the reactor
    • B01J2219/185—Details relating to the spatial orientation of the reactor vertical
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/19—Details relating to the geometry of the reactor
    • B01J2219/194—Details relating to the geometry of the reactor round
    • B01J2219/1941—Details relating to the geometry of the reactor round circular or disk-shaped
    • B01J2219/1943—Details relating to the geometry of the reactor round circular or disk-shaped cylindrical

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

On décrit un procédé de production d'un hydrocarbure stable, sous la forme d'hydrate d'au moins un hydrocarbure à formation d'hydrate, entouré d'un liquide contenant un hydrocarbure, ou en suspension dans celui-ci. L'invention concerne ce produit, un procédé de fabrication ainsi que l'installation de production de celui-ci. Le procédé comprend les étapes suivantes: a) dans une zone (1) de production d'hydrate, on met ensemble des hydrocarbures à formation d'hydrate et de l'eau, que l'on soumet aux conditions du processus de formation d'hydrate. On enlève de cette zone l'énergie thermique libérée lors de la formation d'hydrate, par refroidissement direct à l'aide d'un premier milieu de refroidissement. On obtient ainsi un premier produit intermédiaire, lequel possède une température moyenne égale ou supérieure à celle du point de congélation de l'eau. b) On enlève du premier produit intermédiaire toute l'eau présente et non transformée, obtenant ainsi un second produit intermédiaire, pratiquement dépourvu d'eau non transformée. c) Puis, dans une zone (80) de refroidissement, on refroidit ce second produit par contact direct avec un second milieu de refroidissement contenant des hydrocarbures, jusqu'à l'obtention d'une température se situant en moyenne en dessous du point de congélation de l'eau. Le produit terminal est composé d'un matériau solide, particulaire, contenant l'hydrate, entouré d'un milieu porteur liquide à base d'hydrocarbure, ou en suspension dans celui-ci, à une pression de vapeur inférieure à la pression finale existant à la température finale.
CA 2219244 1995-04-28 1996-04-26 Procede et dispositif de fabrication d'un hydrocarbure, et produit ainsi fabrique Abandoned CA2219244A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NO951669A NO951669L (no) 1995-04-28 1995-04-28 Fremgangsmåte og apparat for fremstilling av et hydrokarbonprodukt
NO951669 1995-04-28

Publications (1)

Publication Number Publication Date
CA2219244A1 true CA2219244A1 (fr) 1996-10-31

Family

ID=19898155

Family Applications (1)

Application Number Title Priority Date Filing Date
CA 2219244 Abandoned CA2219244A1 (fr) 1995-04-28 1996-04-26 Procede et dispositif de fabrication d'un hydrocarbure, et produit ainsi fabrique

Country Status (5)

Country Link
AU (1) AU5705296A (fr)
CA (1) CA2219244A1 (fr)
GB (1) GB2315773A (fr)
NO (1) NO951669L (fr)
WO (1) WO1996034226A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110898785A (zh) * 2019-11-29 2020-03-24 湖北新海鸿化工有限公司 一种201甲基硅油的连续生产工艺及装置

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9601030D0 (en) * 1996-01-18 1996-03-20 British Gas Plc a method of producing gas hydrate
NO311381B1 (no) * 1996-10-25 2001-11-19 Norske Stats Oljeselskap Fremgangsmåte og apparater for fremstilling, lagring og regassifisering av et hydrokarbonprodukt, det fremstilte produktog anvendelse derav
CA2300521C (fr) * 1999-03-15 2004-11-30 Takahiro Kimura Methode et dispositif de production d'hydrates
GB2356619A (en) * 1999-11-25 2001-05-30 British Gas Plc Transporting and storing a hydrate slurry
MY164866A (en) * 2007-03-13 2018-01-30 Mitsui Shipbuilding Eng Method of producing gas hydrate
CN103278374B (zh) * 2013-06-14 2015-04-22 中国科学院广州能源研究所 一种原位拉曼分析的水合物表征装置及水合物样品原位拉曼的分析方法

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2363529A (en) * 1941-05-06 1944-11-28 Fluor Corp Fractionation of hydrate-forming hydrocarbons
US2356407A (en) * 1941-08-15 1944-08-22 Fluor Corp System for forming and storing hydrocarbon hydrates
US3514274A (en) * 1965-02-18 1970-05-26 Exxon Research Engineering Co Transportation of natural gas as a hydrate
SU477917A1 (ru) * 1973-03-12 1975-07-25 Якутский Филиал Со Ан Ссср Способ трубопроводного транспорта природного газа
FR2625527B1 (fr) * 1987-12-30 1995-12-01 Inst Francais Du Petrole Procede de transport d'un fluide formant des hydrates
NO175656C (no) * 1992-06-29 1994-11-09 Norske Stats Oljeselskap Fremgangsmåte for lagring av gass, samt anlegg for gjennomföring av fremgangsmåten

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110898785A (zh) * 2019-11-29 2020-03-24 湖北新海鸿化工有限公司 一种201甲基硅油的连续生产工艺及装置

Also Published As

Publication number Publication date
GB9722661D0 (en) 1997-12-24
GB2315773A (en) 1998-02-11
NO951669D0 (no) 1995-04-28
AU5705296A (en) 1996-11-18
WO1996034226A1 (fr) 1996-10-31
NO951669L (no) 1996-10-29

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