EP1048891A3 - Verfahren zur Bereitstellung einer kontinuierlichen Erdgasversorgung - Google Patents

Verfahren zur Bereitstellung einer kontinuierlichen Erdgasversorgung Download PDF

Info

Publication number
EP1048891A3
EP1048891A3 EP00108331A EP00108331A EP1048891A3 EP 1048891 A3 EP1048891 A3 EP 1048891A3 EP 00108331 A EP00108331 A EP 00108331A EP 00108331 A EP00108331 A EP 00108331A EP 1048891 A3 EP1048891 A3 EP 1048891A3
Authority
EP
European Patent Office
Prior art keywords
natural gas
liquefied
providing
gas supply
pipeline network
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.)
Withdrawn
Application number
EP00108331A
Other languages
English (en)
French (fr)
Other versions
EP1048891A2 (de
Inventor
Franz Dr. Lürken
Hans-Jürgen Dr. Güdelhöfer
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.)
Messer Griesheim GmbH
Original Assignee
Messer Griesheim GmbH
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 Messer Griesheim GmbH filed Critical Messer Griesheim GmbH
Publication of EP1048891A2 publication Critical patent/EP1048891A2/de
Publication of EP1048891A3 publication Critical patent/EP1048891A3/de
Withdrawn legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
    • F25J1/0251—Intermittent or alternating process, so-called batch process, e.g. "peak-shaving"
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17D—PIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00—Pipe-line systems
    • F17D1/02—Pipe-line systems for gases or vapours
    • F17D1/04—Pipe-line systems for gases or vapours for distribution of gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022—Hydrocarbons, e.g. natural gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0221—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using the cold stored in an external cryogenic component in an open refrigeration loop
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0254—Operation; Control and regulation; Instrumentation controlling particular process parameter, e.g. pressure, temperature
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/42—Nitrogen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/50—Oxygen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/58—Argon
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/60—Details about pipelines, i.e. network, for feed or product distribution
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/62—Details of storing a fluid in a tank

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Bei einem Verfahren zur Bereitstellung einer kontinuierlichen Erdgasversorgung in einem Rohrleitungsnetz (1) wird Erdgas in Tageszeiten ohne sehr hohe Erdgasentnahme aus dem Rohrleitungsnetz entnommen (2) und verflüssigt mit Hilfe eines niedrig siedenden flüssigen Gases (9,11), insbesondere Stickstoff, Sauerstoff oder Argon. Das so verflüssigte Erdgas wird einem Vorratsbehälter (14) zugeführt und in Tageszeiten einer sehr hohen Erdgasentnahme wird das verflüssigte Erdgas aus dem Vorratsbehälter entnommen und dem Rohrleitungsnetz (15,17,19) wieder zugeführt. Das aus der Rohrleitung entnommene Erdgas wird gereinigt und mit einer Verflüssigungsvorrichtung verflüssigt, welche durch die Verwendung tiefkalter Gase eine sehr hohe Kondensationsleistung auf geringem Raum und zu geringen Investitionskosten darstellt.
EP00108331A 1999-04-30 2000-04-15 Verfahren zur Bereitstellung einer kontinuierlichen Erdgasversorgung Withdrawn EP1048891A3 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19919639 1999-04-30
DE19919639A DE19919639C1 (de) 1999-04-30 1999-04-30 Verfahren zur Bereitstellung einer kontinuierlichen Erdgasversorgung

Publications (2)

Publication Number Publication Date
EP1048891A2 EP1048891A2 (de) 2000-11-02
EP1048891A3 true EP1048891A3 (de) 2002-09-11

Family

ID=7906369

Family Applications (1)

Application Number Title Priority Date Filing Date
EP00108331A Withdrawn EP1048891A3 (de) 1999-04-30 2000-04-15 Verfahren zur Bereitstellung einer kontinuierlichen Erdgasversorgung

Country Status (2)

Country Link
EP (1) EP1048891A3 (de)
DE (1) DE19919639C1 (de)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102005056102A1 (de) * 2005-10-27 2007-05-03 Linde Ag Vorrichtung zur Gasdruckerhöhung
DE102006046246A1 (de) * 2006-08-08 2008-02-14 Griepentrog, Hartmut, Prof. Dr.-Ing. Verfahren und Anlage zum Verdampfen von verflüssigtem Erdgas und Entspannen von Erdgas
DE102010020476B4 (de) 2010-05-14 2023-05-04 Air Liquide Deutschland Gmbh Verwendung einer Vorrichtung zum Speichern, Umfüllen und/oder Transportieren von tiefkalt verflüssigtem brennbarem Gas in einem Fahrzeug
CN103867895A (zh) * 2012-12-10 2014-06-18 河南宇天化工有限公司 一种用于苯加氢装置的供气系统
DE102015206723A1 (de) * 2015-04-15 2016-10-20 Siemens Aktiengesellschaft Verfahren zum Betrieb einer Kraftwerksanlage an Standorten mit zu geringer Brennstoffversorgung
CN112944213A (zh) * 2021-03-17 2021-06-11 重庆渝微电子技术研究院有限公司 一种动态气液配气系统及方法

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3511058A (en) * 1966-05-27 1970-05-12 Linde Ag Liquefaction of natural gas for peak demands using split-stream refrigeration
US3661542A (en) * 1969-01-23 1972-05-09 Shell Oil Co Short term peak shaving of natural gas
US3760597A (en) * 1971-08-06 1973-09-25 Linde Ag Short term storage of natural gas
US4903496A (en) * 1988-03-04 1990-02-27 Sulzer Brothers Limited Plant and method for periodic charging and discharging of a gas reservoir
DE4205010A1 (de) * 1992-02-19 1993-08-26 Hansjuergen Dr Ing Richter Verfahren zur vergleichmaessigung des gasbezuges und rohrleitungssystem fuer die gasverteilung
DE4304673A1 (de) * 1993-01-05 1994-09-15 Rauscher Georg Verfahren zur Verflüssigung von Gasen, dadurch gekennzeichnet, daß flüssiges Gas bei hohem Druck verdampft, entspannt, verflüssigt, unterkühlt und im Wärmetauscher als Kühlmittel verwendet wird
DE19511383A1 (de) * 1995-03-28 1996-10-02 Linde Ag Kombination eines Erdgasverflüssigungsverfahrens mit einem Verdampfungsverfahren für kryogene Flüssigkeiten

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0949600A (ja) * 1995-05-31 1997-02-18 Osaka Gas Co Ltd 天然ガスの貯蔵送出方法およびその装置

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3511058A (en) * 1966-05-27 1970-05-12 Linde Ag Liquefaction of natural gas for peak demands using split-stream refrigeration
US3661542A (en) * 1969-01-23 1972-05-09 Shell Oil Co Short term peak shaving of natural gas
US3760597A (en) * 1971-08-06 1973-09-25 Linde Ag Short term storage of natural gas
US4903496A (en) * 1988-03-04 1990-02-27 Sulzer Brothers Limited Plant and method for periodic charging and discharging of a gas reservoir
DE4205010A1 (de) * 1992-02-19 1993-08-26 Hansjuergen Dr Ing Richter Verfahren zur vergleichmaessigung des gasbezuges und rohrleitungssystem fuer die gasverteilung
DE4304673A1 (de) * 1993-01-05 1994-09-15 Rauscher Georg Verfahren zur Verflüssigung von Gasen, dadurch gekennzeichnet, daß flüssiges Gas bei hohem Druck verdampft, entspannt, verflüssigt, unterkühlt und im Wärmetauscher als Kühlmittel verwendet wird
DE19511383A1 (de) * 1995-03-28 1996-10-02 Linde Ag Kombination eines Erdgasverflüssigungsverfahrens mit einem Verdampfungsverfahren für kryogene Flüssigkeiten

Also Published As

Publication number Publication date
EP1048891A2 (de) 2000-11-02
DE19919639C1 (de) 2000-11-16

Similar Documents

Publication Publication Date Title
Kruse et al. Calculating the consequences of a CO2-pipeline rupture
EP1048891A3 (de) Verfahren zur Bereitstellung einer kontinuierlichen Erdgasversorgung
GB2172388B (en) Gas and oil handling
EP0933583A3 (de) System zum Füllen eines Zylinders mit cryogenem Fluidum
ES2048382T5 (es) Sistema para suministro de gases a alta presion.
GB2412718B (en) Method and apparatus for delivering a high pressure gas from a cryogenic storage tank
TNSN99195A1 (fr) Procede ameliore pour la liquiquefaction du gaz naturel
ATE215211T1 (de) Verfahren zur xenongewinnung
DE69636545D1 (de) Gefrierkonservierte hepatocyten und verfahren für ihre herstellung
HK1003012A1 (en) A method and a sampling assembly for taking a representative fluid sample from a pressurised fluid system
Foerg History of cryogenics: the epoch of the pioneers from the beginning to the year 1911
EP1167860A3 (de) Mobile Füllanlage für Gasflaschen
AU573779B2 (en) Steel casting using a co2 gas protective shroud
WO2001024858A3 (de) Gassammeleinrichtung
ATE228224T1 (de) Messsystem für eine erdgastankstelle
Gifford The simple ATDL urban air pollution model
EP1004779B1 (de) Verfahren und Vorrichtung zur Gasversorgung und Gasrückgewinnung
JP2003270103A (ja) 流体供給設備での流体サンプリング方法
EP0926428A3 (de) Verfahren und Anordnung zur Entfernung von Brenngasen aus Gasnetzen
Ohmiya et al. The author's answer to the discussion by Prof. Yuji Hasemi.(Yuji HASEMI, J. Environ. Eng., AIJ, No. 566, 119-120, Apr., 2003).
KAJIHARA On the variation of the relative stem curve in even-aged forest stand of sugi
SU1555592A1 (ru) Способ наполнени баллонов газовой смесью под давлением
Rozenfeld et al. High-Effect Inhibitors of Corrosion and Hydrogen Saturation for the Gas and Petroleum Industry
DE531406C (de) Verfahren zur Versorgung der Abnehmer mit Druckgas
Schmid-Fetzer et al. Thermodynamic assessment of the V-N system

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: MESSER GRIESHEIM GMBH

AKX Designation fees paid
REG Reference to a national code

Ref country code: DE

Ref legal event code: 8566

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20030312

REG Reference to a national code

Ref country code: HK

Ref legal event code: WD

Ref document number: 1035936

Country of ref document: HK