NO150079B - Fremgangsmaate for utvinning av etylen fra crackinggasser ved lavtemperaturfraksjonering - Google Patents

Fremgangsmaate for utvinning av etylen fra crackinggasser ved lavtemperaturfraksjonering Download PDF

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Publication number
NO150079B
NO150079B NO771073A NO771073A NO150079B NO 150079 B NO150079 B NO 150079B NO 771073 A NO771073 A NO 771073A NO 771073 A NO771073 A NO 771073A NO 150079 B NO150079 B NO 150079B
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Norway
Prior art keywords
modulation
low
amplifier
transistor
voltage
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Application number
NO771073A
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English (en)
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NO150079C (no
NO771073L (no
Inventor
Luigi Gazzi
Oronzo Sguera
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Snam Progetti
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Publication of NO771073L publication Critical patent/NO771073L/no
Publication of NO150079B publication Critical patent/NO150079B/no
Publication of NO150079C publication Critical patent/NO150079C/no

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0228Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0242Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 3 carbon atoms or more
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/143Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/09Purification; Separation; Use of additives by fractional condensation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/002Cooling of cracked gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0204Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
    • F25J3/0219Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
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    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0228Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0233Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 1 carbon atom or more
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
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    • F25J3/0228Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0238Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 2 carbon atoms or more
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    • F25J3/0228Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0252Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of hydrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/02Processes or apparatus using separation by rectification in a single pressure main column system
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    • F25J2200/70Refluxing the column with a condensed part of the feed stream, i.e. fractionator top is stripped or self-rectified
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    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/74Refluxing the column with at least a part of the partially condensed overhead gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F25J2200/78Refluxing the column with a liquid stream originating from an upstream or downstream fractionator column
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    • F25J2200/80Processes or apparatus using separation by rectification using integrated mass and heat exchange, i.e. non-adiabatic rectification in a reflux exchanger or dephlegmator
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    • F25J2205/02Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
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    • F25J2205/04Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
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    • F25J2210/12Refinery or petrochemical off-gas
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    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2215/00Processes characterised by the type or other details of the product stream
    • F25J2215/62Ethane or ethylene
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    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2235/00Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
    • F25J2235/60Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being (a mixture of) hydrocarbons
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    • F25J2240/02Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream
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    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2245/00Processes or apparatus involving steps for recycling of process streams
    • F25J2245/02Recycle of a stream in general, e.g. a by-pass stream
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    • F25J2260/00Coupling of processes or apparatus to other units; Integrated schemes
    • F25J2260/02Integration in an installation for exchanging heat, e.g. for waste heat recovery
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    • F25J2270/00Refrigeration techniques used
    • F25J2270/02Internal refrigeration with liquid vaporising loop
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F25J2270/04Internal refrigeration with work-producing gas expansion loop
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    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
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    • F25J2270/00Refrigeration techniques used
    • F25J2270/60Closed external refrigeration cycle with single component refrigerant [SCR], e.g. C1-, C2- or C3-hydrocarbons
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    • F25J2270/90External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
    • F25J2270/902Details about the refrigeration cycle used, e.g. composition of refrigerant, arrangement of compressors or cascade, make up sources, use of reflux exchangers etc.
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    • F25J2270/00Refrigeration techniques used
    • F25J2270/90External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
    • F25J2270/906External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by heat driven absorption chillers
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/40Ethylene production

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Water Supply & Treatment (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Investigating Or Analyzing Materials By The Use Of Fluid Adsorption Or Reactions (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

Amplitudemodulasjonskompressor.
Oppfinnelsen angår en amplitudemodulasjonskompressor for bærebølgeanlegg, hvor der fra en vekselstrømforsterkers utgangsspenning med en detektor, et lavpassfilter og en lavfrekvensforsterker fås et likespenningssignal som er proporsjonalt med vekselspenningens amplitude og varierer med lavfrekvensmodulasjonen, og som anvendes til negativ tilbakekobling.
Det ble allerede foreslått å anvende en negativ tilbakekobling for modulasjonsfre-kvensene, idet utgangsspenningen fra forsterkeren for amplitudemodulerte signaler demoduleres for å modulere den modulerte spenning med denne demodulerte spenning. For modulasjonen ble der benyttet en van-lig modulatorkrets. Ved en annen løsning blir like- og vekselspenningskomponentene av det demodulerte signal tilført en diode parallellkoblet med en avstemt svingekrets. Med denne diode ble inngangssignalet til den etterfølgende forsterker dempet av den påtrykte spenning og overensstemmende med dennes størrelse.
Begge løsninger har den ulempe at mo-dulasjonssignalet ved komprimeringen blir forvrengt for sterkt for mange formål.
Oppfinnelsens oppgave er å skaffe en forbedret amplitudemodulasjonskompressor som gjør det mulig å redusere modulasjonsgraden for en amplitudemodulert svingning med små forvrengninger.
Dette blir ifølge oppfinnelsen oppnådd ved at tilbakekoblingssignalet over en kondensator styrer basis-siden av en transistor hvis kollektorstrøm er en på en innstillbar likestrøm overlagret vekselstrøm som har formen av modulasjonen som skal komprimeres, og er i faseopposisjon til denne samt styrer en eller flere dioder hvis arbeidspunkt bestemmes ved den innstillbare like-strøm, og som er koblet som styrte dempningselementer for vekselstrømforsterke-ren, så dennes forsterkningsgrad blir proporsjonal med den differensielle motstand av diodene.
Oppfinnelsen er anskueliggjort på teg-ningen. Fig. 1 er et koblingsskjema for et ut-førelseseksempel, delvis i blokkform. Fig. 2 er et diagram som viser den relative forsterkning i avhengighet av den momentane modulasjonsverdi, og
fig. 3 viser en reguleringskarakteristikk.
I utførelsen på fig. 1 dannes hele kob-lingsanordningen av vekselspenningsfor-sterkeren V og mot-modulasjonsgrenen. Forsterkeren V består av en kaskadekob-ling av en første forsterkerdel VI, en transistor Tl, en bredtbåndtransformator ii og en annen forsterkerdel V2 samt to serie-koblede dioder Dl og D2, hvis forbindelses-punkt er koblet til kollektoren på transistoren Tl over en kondensator Cl. Emitteren på transistoren Tl er kobelt til jord, og pri-mærviklingen på transformatoren U er til-koblet spenningskildens positive pol. Den ene ende av sekundærviklingen på transformatoren ti er ført til jord, og den annen ende mater forsterkerdelen V2. De andre ender av dioden Dl og D2 er jordet over kondensatorer henholdsvis C2 og C3. Dess-uten er dioden Dl tilsluttet en spennings-kilde på + 30 V, mens dioden D2 er for-bundet med kollektoren på transistoren T2 i mot-modulasjonsgrenen. Mot-modulasjonsgrenen dannes av en detektor Dt, et lavpassfilter TP, en lavfrekvensforsterker V3, hvis forsterkning kan innstilles for hånden, og som har en utgang med lav ohmsk motstand, en kondensator C4 og transistoren T2 i kaskade. Transistoren T2 er anordnet som et motkoblet trinn, idet motstanden RI forbinder basis på transistoren T2 med + 6 V-kilden. Den innstillbare motstand R2 mellom emitteren på transistoren T2 og jord tjener til innstilling av motkoblingsgraden. Detektoren Dt er tilsluttet forsterkerens utgang.
Inngangen E til forsterkeren V får modulert høyfrekvensspenning tilført, og ved utgangen A uttas den forsterkede inn-gangsspenning med rediisert modulasjonsgrad. Herav danner detektoren Dt et mo-dulasjonssignal som er proporsjonalt med høyfrekvensspenningens amplitude, og som når inngangen til lavfrekvensforsterkeren V3 over lavpassfilteret TP, som tjener til å undertrykke resterende høyfrekvens. Utgangsspenningen fra lavfrekvensforsterkeren V3 passerer via kondensatoren C4 til basis på transistoren T2. Kondensatoren C4 sørger for at koblingen bare reagerer på modulasjonen. Basis på transistor T2 får forspenning fra + 6 V-klemmen over motstanden RI. Spenningen på emitteren hos transistoren T2 følger spenningen ved dennes basis. Da den innstillbare motkoblings-motstand R2 som ligger mellom emitteren på transistoren T2 og jord, gjennomflytes av kollektorstrømmen, blir denne proporsjonal med emitterspenningen og dermed også med basisspenningen. Med den innstillbare motstand R2 påvirkes foruten en-dringen av kollektorlikestrømmen også ba-sisvekselspenningen. Utgangsstrømmen fra kollektoren på transistoren T2 er en vek-selstrøm som er overlagret på den med R2 innstillbare likestrøm, og som har samme form som modulasjonen som skal komprimeres, og er i faseopposisjon til denne. Ut-gangsstrømmen fra kollektoren på transistoren T2 styrer diodene Dl og D2, hvis arbeidspunkt bestemmes av likestrømmen, og som tjener som styrt belastning for transistoren Tl, på den måte at det høyfrekvente inngangssignals modulasjonsgrad reduseres ved hjelp av styringen av høyfrekvensfor-sterkningen i takt med modulasjonen.
Under den forutsetning at den differensielle vekselstrømmotstand av reguler-ingsdiodene er meget mindre enn den pa-rallellkoblede impedans av den med inn-gangsimpedansen av forsterkerdelen V2 belastede transformator ti og av kollektor-motstanden av transistoren Tl, følger sam-menhengen mellom reguleringsstrømmen i og forsterkningen i det trinn som inne-holder transistoren Tl, loven
hvor V,, i, og k er konstanter. Forutsetnin-gen for en høy ohmsk kollektormotstand for transistoren Tl blir ved frekvenser over 1 megaherz oppfylt på en enkel måte hvis der for Tl anvendes en transistor av tetrode-typen. Uttrykket ^—^— jk svarer til forløpet av den différensielle gjennom-slipningsmotstand av en strømførende krystalldiode som funksjon av strømmen i.
Med hensyn til virkemåten av den be-skrevne koblingsanordning kan forholdet resymeres derhen at forsterkningsgraden av forsterkeren V ved momentant stor amplitude av vekselspenningen i transistoren Tl blir redusert overensstemmende med den i diodene Dl og D2 foreliggende sam-menheng mellom differensiell motstand og likestrømgjennomgang, hvorunder der til hver modulasjonsverdi svarer en bestemt forsterkning.
For modulasjonskompresjonen kan det av fig. 2 utledes hvorledes forsterkningen må være for hver momentan modulasjonsverdi mn foråt modulasjonsgraden m ved den eksempelvis viste sinusmodulasjon på n = 0,8 blir redusert med en konstant faktor. For en amplitudemodulasjonskompre-sjon med faktor 3 må f. eks. en momentanverdi av 1,6 (m0 = 0,6) komprimeres til 1,2 (m0 = 0,6/3 = 0,2), altså forsterkes med 0,75. En momentanverdi av 0,4 (mn = —0,6) må forsterkes til 0,8 (m0 = —0,2), altså med en faktor av 2,0. Den relative forsterkning vre i avhengighet av den momentane modulasjonsverdi er således for en eksakt modulasjonsgradskompresj,on en meget ik-ke-lineær karakteristikk, som fig. 2 viser. Sammenligner man denne konstruerte motmodulasjonskarakteristikk med fig. 3, hvor diodenes reguleringskarakteristikk er oppført i lineær målestokk i omgivelsen av f. eks. iR = 1 mA (jfr. formel for v), faller den store likhet av de to kurver i øynene selv om de følger helt forskjellige matema-tiske lover. Man kan følgelig få en approk-simasjon til mot-modulasjons-karakteri-stikken ved at man i området omkring en bestemt hvilestrøm (her f. eks. 1 mA) på-trykker reguleringen en vekselstrøm som
har formen av modulasjonen som skal
komprimeres, og er i faseopposisjon til den.
En modulert sinussvingning beholder altså
sin form efter en slik motregulering med
en sinusformet strøm og taper bare i modulasjonsgrad. Ved ikke faseren mot-modulasjon, f. eks. ved for sterk fasedreining
i lavpassfilteret TP, kan der eventuelt opp-tre sterke forvrengninger. Ved endring av
forsterkningen i motmodulasjonsgrenen
kan den ønskede kompresjonsgrad innstilles. For en konstant kompresjonsfaktor be-høver bare forholdet ioo/i0 å forbli konstant, hvor i0 er grunnstrømmen og icv> den
vekselstrøm som overlagres for en bestemt
modulasjon.

Claims (2)

1. Amplitudemodulas j onskompressor for bærebølgeanlegg, hvor der fra en vek-selstrømforsterkers utgangsspenning med en detektor, et lavpassfilter og en lavfrekvensforsterker fås et likespenningssignal som er proporsjonalt med vekselspenningens amplitude og varierer med lavfrekvensmodulasjonen, og som anvendes til negativ tilbakekobling, karakterisert ved at tilbakekoblingssignalet over en kondensator styrer basissiden av en transistor, hvis kollektorstrøm er en på en innstillbar likestrøm overlagret vekselstrøm som har formen av modulasjonen som skal komprimeres, og er i faseopposisjon til denne samt styrer en eller flere dioder hvis arbeidspunkt bestemmes ved den innstillbare likestrøm, og som er koblet som styrte dempningselementer for vekselstrømfor-sterkeren, så dennes forsterkningsgrad blir proporsjonal med den differensielle motstand av diodene.
2. Amplitudemodulasj onskompressor som angitt i påstand 1, karakterisert ved at kompresjonsf aktoren velges ved innstilling av lavfrekvensforsterkerens forsterkning.
NO771073A 1976-03-26 1977-03-25 Fremgangsmaate for utvinning av etylen fra crackinggasser ved lavtemperaturfraksjonering NO150079C (no)

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Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4143521A (en) * 1977-02-08 1979-03-13 Stone & Webster Engineering Corporation Process for the production of ethylene
IT1136894B (it) * 1981-07-07 1986-09-03 Snam Progetti Metodo per il recupero di condensati da una miscela gassosa di idrocarburi
EP0137744B2 (en) * 1983-09-20 1991-08-28 Costain Petrocarbon Limited Separation of hydrocarbon mixtures
GB2146751B (en) * 1983-09-20 1987-04-23 Petrocarbon Dev Ltd Separation of hydrocarbon mixtures
US4695303A (en) * 1986-07-08 1987-09-22 Mcdermott International, Inc. Method for recovery of natural gas liquids
US4720293A (en) * 1987-04-28 1988-01-19 Air Products And Chemicals, Inc. Process for the recovery and purification of ethylene
IT1241471B (it) * 1990-07-06 1994-01-17 Tpl Processo ed apparecchiatura per il massimo recupero dell'etilene e del propilene dal gas prodotto dalla pirolisi di idrocarburi.
RU2056018C1 (ru) * 1993-10-07 1996-03-10 Давид Павлович Синельников Способ обработки пирогаза перед газоразделением. способ получения технологического низкотемпературного холода в парокомпрессионной холодильной машине при обработке пирогаза перед газоразделением
US5379597A (en) * 1994-02-04 1995-01-10 Air Products And Chemicals, Inc. Mixed refrigerant cycle for ethylene recovery
US5361589A (en) * 1994-02-04 1994-11-08 Air Products And Chemicals, Inc. Precooling for ethylene recovery in dual demethanizer fractionation systems
US5377490A (en) * 1994-02-04 1995-01-03 Air Products And Chemicals, Inc. Open loop mixed refrigerant cycle for ethylene recovery
US5421167A (en) * 1994-04-01 1995-06-06 The M. W. Kellogg Company Enhanced olefin recovery method
CN100551885C (zh) * 2005-09-29 2009-10-21 中国石油化工集团公司 从制备烯烃的产品气中回收低碳烯烃的方法
DE102007063347A1 (de) * 2007-12-28 2009-07-02 Uhde Gmbh Verfahren zur Abtrennung von leichtsiedenden Komponenten aus einem Kohlenwasserstoffstrom
FR2939693B1 (fr) * 2008-12-16 2011-12-23 Inst Francais Du Petrole Nouveau procede de recuperation du co2 issu des fumees de regeneration d'une unite de craquage catalytique
DE102010020282A1 (de) * 2010-05-12 2011-11-17 Linde Aktiengesellschaft Stickstoff-Abtrennung aus Erdgas
BR112018012402A2 (pt) * 2015-12-18 2018-12-04 Bechtel Hydrocarbon Technology Solutions Inc sistema e método para recuperação de hidrocarbonetos leves.
IT202200007049A1 (it) * 2022-04-08 2023-10-08 Alessandro Bugli Impianto e processo per la separazione di idrogeno da gas naturale
EP4345406A1 (en) * 2022-09-29 2024-04-03 Sulzer Management AG Plant and method for separating liquified petroleum gas from fuel gas by cryogenic distillation

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2731810A (en) * 1949-01-04 1956-01-24 Qjivaiiov snoonilnod
US2775103A (en) * 1954-12-23 1956-12-25 Phillips Petroleum Co Hydrocarbon separation
US2823523A (en) * 1956-03-26 1958-02-18 Inst Gas Technology Separation of nitrogen from methane
GB869412A (en) * 1956-06-19 1961-05-31 Atomic Energy Authority Uk Improvements in or relating to apparatus for the production of deuterium-enriched hydrogen
US2909905A (en) * 1957-06-05 1959-10-27 Black Sivalls & Bryson Inc Method for processing a natural gas stream
FR1228051A (fr) * 1958-11-28 1960-08-26 Air Liquide Procédé de dégazage d'un liquide riche en éthylène
GB1012599A (en) * 1964-03-12 1965-12-08 Couch Internat Methane Ltd Regasifying liquified natural gas by fractionating gaseous mixtures
US3433026A (en) * 1966-11-07 1969-03-18 Judson S Swearingen Staged isenthalpic-isentropic expansion of gas from a pressurized liquefied state to a terminal storage state
US3756036A (en) * 1971-04-20 1973-09-04 Phillips Petroleum Co Demethanizing method and apparatus
US3938934A (en) * 1974-11-08 1976-02-17 Scm Corporation Fuel economizer process and apparatus

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IE45273B1 (en) 1982-07-28
FR2345412B1 (no) 1980-02-29
IT1058546B (it) 1982-05-10
DE2713359A1 (de) 1977-09-29
SE420915B (sv) 1981-11-09
SE7703479L (sv) 1977-09-27
NL173844B (nl) 1983-10-17
IS1055B6 (is) 1981-08-25
NO150079C (no) 1984-08-22
AR212989A1 (es) 1978-11-30
GB1571073A (en) 1980-07-09
FI770813A (no) 1977-09-27
NL7703283A (nl) 1977-09-28
CA1047386A (en) 1979-01-30
US4163652A (en) 1979-08-07
IE45273L (en) 1977-09-26
NO771073L (no) 1977-09-27
DK134077A (da) 1977-09-27
FR2345412A1 (fr) 1977-10-21
IS2381A7 (is) 1977-09-27
NL173844C (nl) 1984-03-16
DE2713359B2 (de) 1979-05-17
BE852922A (fr) 1977-09-26

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