HRP20190655T1 - Postupak i uređaj za proizvodnju ugljikovodika - Google Patents

Postupak i uređaj za proizvodnju ugljikovodika Download PDF

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Publication number
HRP20190655T1
HRP20190655T1 HRP20190655TT HRP20190655T HRP20190655T1 HR P20190655 T1 HRP20190655 T1 HR P20190655T1 HR P20190655T T HRP20190655T T HR P20190655TT HR P20190655 T HRP20190655 T HR P20190655T HR P20190655 T1 HRP20190655 T1 HR P20190655T1
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HR
Croatia
Prior art keywords
filter
discharge valve
fraction
system valves
mechanical
Prior art date
Application number
HRP20190655TT
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English (en)
Inventor
Steen Brummerstedt Iversen
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Steeper Energy Aps
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.)
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Publication date
Application filed by Steeper Energy Aps filed Critical Steeper Energy Aps
Publication of HRP20190655T1 publication Critical patent/HRP20190655T1/hr

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Classifications

    • 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/02Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
    • 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/002Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
    • 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
    • C10G31/00Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/09Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by filtration
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1011Biomass
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20Characteristics of the feedstock or the products
    • C10G2300/30Physical properties of feedstocks or products
    • C10G2300/302Viscosity
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40Characteristics of the process deviating from typical ways of processing
    • C10G2300/4012Pressure
    • 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
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock

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  • 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)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Claims (9)

1. Postupak proizvodnje tekućeg ugljikovodika prevođenjem ugljičnog materijala koji se nalazi u jednoj ili više sirovina, naznačen time što se postupak sastoji u – osiguravanju dovodnog materijala iz jedne ili više sirovina; – stlačivanju dovodnog materijala do zadanog tlaka obrade od najmanje 150 bara (15 MPa); – grijanju stlačenog dovodnog materijala do zadane temperature postupka od najmanje 370 stupnjeva; – reagiranju stlačenog i zagrijanog dovodnog materijala kroz zadani vremenski period; – hlađenje reagiranog dovodnog materijala do temperature ispod 200 °C; – mehaničkom odvajanju frakcije više viskoznosti od prevedenog dovodnog materijala pod radnim tlakom upotrebom mehaničkog filtra s filtarskim otvorima između 1 µm i 500 µm; – gdje se temperaturu filtara tako kontrolira da bude u rasponu od 40 do 200 °C; – gdje se mehanički odvojenu frakciju više viskoznosti ekstrahira iz postupka; – gdje se ekstrahiranje provodi mijenjanjem mehaničkih filtara između najmanje jednog uključenog i najmanje jednog isključenog filtra; – gdje se filtar uključi i tako otvori za dotok, a zatim se filtar isključi i tako zatvori za dotok otvaranjem odnosnom zatvaranjem sustavnih ventila uzvodno i nizvodno od filtra; – gdje se dodatno ispusni ventil nalazi između zatvorenih sustavnih ventila i uzvodno od filtarskog elementa, te se otvara prema području nižeg tlaka, radi ispuštanja mehanički odvojene visokoviskozne frakcije iz filtra i kroz ispusni ventil; – gdje je ispusni ventil zatvoren, a komoru se napuni nestlačivim fluidom prije stavljanja filtarske komore pod tlak otvaranjem sustavnih ventila; – transportiranju preostale prevedene dovodne mase kroz sustav za smanjivanje tlaka i dodatno kroz sustav za odvajanje.
2. Postupak u skladu s patentnim zahtjevom 1, naznačen time što se mehanički odvojenu i uzastopno ekstrahiranu frakciju više viskoznosti dodatno obrađuje.
3. Postupak u skladu s patentnim zahtjevom 1, naznačen time što mehanički odvojena frakcija ima viskoznost određenu kombinacijom karakteristika filtra, temperature i tlaka obrade.
4. Postupak u skladu s patentnim zahtjevom 3, naznačen time što se temperaturu filtara tako kontrolira da bude u rasponu od 40 do 150 °C, a po mogućnosti u rasponu od 50 do 120 °C, primjerice u rasponu od 60 do 100 °C.
5. Postupak u skladu s patentnim zahtjevom 1, naznačen time što se ispusni ventil otvara prema tlačnim uvjetima okoliša.
6. Uređaj namijenjen provođenju postupka u skladu s prethodnim patentnim zahtjevima, naznačen time što uređaj sadrži: – uređaj za stlačivanje, prilagođen za stlačivanje dovodne smjese; – uređaj za grijanje, prilagođen za grijanje stlačene dovodne smjese; – konverzijski spremnik, prilagođen za držanje stlačene i zagrijane dovodne smjese kroz zadano vrijeme obrade; – uređaj za hlađenje, prilagođen za u najmanju ruku djelomično hlađenje obrađene dovodne smjese; – uređaj za mehaničko filtriranje s rasponom filtarskih otvora između 1 µm i 500 µm, prilagođen za odvajanje frakcije više viskoznosti od obrađene dovodne smjese i dopuštanje da frakcija niže viskoznosti prođe kroz uređaj za filtriranje; – gdje je paralelno smješteno više filtara i gdje se sustavni ventili nalaze uzvodno i nizvodno od svakog od filtara; – gdje se sustavni ventili nalaze na uzvodnoj i nizvodnoj strani uređaja za mehaničko filtriranje; – gdje se ispusni ventil nalazi između sustavnih ventila; – gdje se ventil za dovod fluida nalazi između sustavnih ventila i prilagođen je da omogući dotok fluida kada su sustavni ventili i ispusni ventil zatvoreni; – uređaj za smanjivanje tlaka, prilagođen za u najmanju ruku djelomično smanjivanje tlaka obrađene dovodne smjese koja je prošla kroz uređaj za mehaničko filtriranje; – uređaj za odvajanje, namijenjen odvajanju komponenata obrađene dovodne smjese koja je prošla kroz uređaj za mehaničko filtriranje.
7. Uređaj u skladu s patentnim zahtjevom 6, naznačen time što je uređaj za mehaničko filtriranje filtar s rasponom filtarskih otvora između 10 µm i 250 µm.
8. Uređaj u skladu s patentnim zahtjevom 6, naznačen time što se ispusni ventil nalazi uzvodno od uređaja za odvajanje.
9. Uređaj u skladu s patentnim zahtjevom 6, naznačen time što se ventil za dovod fluida nalazi nizvodno od uređaja za odvajanje.
HRP20190655TT 2013-12-21 2019-04-05 Postupak i uređaj za proizvodnju ugljikovodika HRP20190655T1 (hr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DKPA201300715 2013-12-21
EP14831091.5A EP3083888B1 (en) 2013-12-21 2014-12-22 Process and apparatus for producing hydrocarbon
PCT/IB2014/067212 WO2015092773A1 (en) 2013-12-21 2014-12-22 Process and apparatus for producing hydrocarbon

Publications (1)

Publication Number Publication Date
HRP20190655T1 true HRP20190655T1 (hr) 2019-06-14

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Country Status (15)

Country Link
US (1) US10113118B2 (hr)
EP (1) EP3083888B1 (hr)
CA (1) CA2934697C (hr)
CY (1) CY1121548T1 (hr)
DK (1) DK3083888T3 (hr)
ES (1) ES2720727T3 (hr)
HR (1) HRP20190655T1 (hr)
HU (1) HUE043033T2 (hr)
LT (1) LT3083888T (hr)
PL (1) PL3083888T3 (hr)
PT (1) PT3083888T (hr)
RS (1) RS58686B1 (hr)
SI (1) SI3083888T1 (hr)
TR (1) TR201905755T4 (hr)
WO (1) WO2015092773A1 (hr)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20200255759A1 (en) * 2015-11-10 2020-08-13 Board Of Regents Of The Nevada System Of Higher Education On Behalf Of The University Of Nevada System for hydrothermal treatment of wet biomass
CA2935825A1 (en) 2016-07-11 2018-01-11 Steeper Energy Aps Process for producing low sulphur renewable oil
DK179391B1 (en) 2017-02-08 2018-05-28 Steeper Energy Aps Pressure reduction in high pressure processing system
DK179687B1 (en) * 2017-03-30 2019-03-25 Steeper Energy Aps High pressure treatment system separation system
DK201770842A1 (en) * 2017-11-09 2019-05-21 Steeper Energy Aps Modular processing system
EP3720926A1 (en) 2017-11-10 2020-10-14 Steeper Energy ApS Recovery system for high pressure processing system
CN110193221B (zh) * 2019-05-20 2021-11-09 中国石化长城能源化工(宁夏)有限公司 一种清洗聚四氢呋喃装置板框压滤机滤布的方法

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Also Published As

Publication number Publication date
US10113118B2 (en) 2018-10-30
EP3083888A1 (en) 2016-10-26
HUE043033T2 (hu) 2019-07-29
TR201905755T4 (tr) 2019-05-21
CY1121548T1 (el) 2020-05-29
EP3083888B1 (en) 2019-01-30
RS58686B1 (sr) 2019-06-28
LT3083888T (lt) 2019-05-10
SI3083888T1 (sl) 2019-06-28
PL3083888T3 (pl) 2019-07-31
DK3083888T3 (da) 2019-05-06
PT3083888T (pt) 2019-05-21
WO2015092773A1 (en) 2015-06-25
US20160333273A1 (en) 2016-11-17
CA2934697A1 (en) 2015-06-25
ES2720727T3 (es) 2019-07-24
CA2934697C (en) 2019-07-09

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