PL399654A1 - Manufacturing method of refined biocomponent for biofuels and refined biocomponent for biofuels - Google Patents

Manufacturing method of refined biocomponent for biofuels and refined biocomponent for biofuels

Info

Publication number
PL399654A1
PL399654A1 PL399654A PL39965412A PL399654A1 PL 399654 A1 PL399654 A1 PL 399654A1 PL 399654 A PL399654 A PL 399654A PL 39965412 A PL39965412 A PL 39965412A PL 399654 A1 PL399654 A1 PL 399654A1
Authority
PL
Poland
Prior art keywords
biocomponent
biofuels
refined
catalyst
catalytic depolymerization
Prior art date
Application number
PL399654A
Other languages
Polish (pl)
Inventor
Robert Kopaczel
Przemysław Mazurek
Original Assignee
Green Power Spólka Z Ograniczona Odpowiedzialnoscia Spólka W Organizacji
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 Green Power Spólka Z Ograniczona Odpowiedzialnoscia Spólka W Organizacji filed Critical Green Power Spólka Z Ograniczona Odpowiedzialnoscia Spólka W Organizacji
Priority to PL399654A priority Critical patent/PL399654A1/en
Priority to EP12183858.5A priority patent/EP2679655A1/en
Publication of PL399654A1 publication Critical patent/PL399654A1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/08—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
    • C10G1/086—Characterised by the catalyst used
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1003—Waste materials
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/04—Diesel oil

Abstract

Sposób wytwarzania uszlachetnionego biokomponentu do biopaliw w procesie katalitycznej depolimeryzacji, którym rozdrobnione odpady komunalne i/lub organiczne stanowiace surowiec wsadowy poddaje sie suszeniu, a nastepnie przetwarza sie w bloku separacji i wyparki polaczonym z turbina mieszajaca (110), w której nastepuje depolimeryzacja katalityczna, a zdepolimeryzowany surowiec destyluje sie w destylatorze (109) w celu otrzymania biokomponentu, przy czym czesc otrzymanego biokomponentu zuzywa sie do zasilania generatora spalinowo-elektrycznego. Depolimeryzacje katalityczna prowadzi sie w obecnosci glinokrzemianu sodu pelniacego role katalizatora, przy czym za pomoca bloku kontroli procesu technologicznego monitoruje sie automatycznie wskazania czujników powiazanych z poszczególnymi blokami procesu katalitycznej depolimeryzacji i w przypadku stwierdzenia odchylen wynikajacych z niedostatecznej ilosci katalizatora aktywuje sie automatyczny dozownik katalizatora, za którego pomoca dozuje sie do turbiny mieszajacej dawke katalizatora w ilosci od 5 kg do 35 kg na 1000 l biokomponentu w obiegu procesu, po czym powraca sie do monitorowania pracy poszczególnych bloków, natomiast do tak uzyskanego biokomponentu dodaje sie koloidalny roztwór nanoczastek dwutlenku ceru (CeO2) o wielkosci czastek od 6 nm do 8 nm w lekkich destylatach ropy naftowej w ilosci zapewniajacej stezenie koncowe nanoczastek dwutlenku ceru CeO2 w biokomponencie na poziomie od 5 ppm do 20 ppm. Przedmiotem zgloszenia jest równiez uszlachetniony biokomponent do biopaliw.A method of producing a refined biocomponent for biofuels in the process of catalytic depolymerization, which comminuted municipal and / or organic waste constituting the feedstock is dried, and then processed in a separation block and evaporator connected to a mixing turbine (110), in which catalytic depolymerization occurs. the depolymerised raw material is distilled in a distiller (109) in order to obtain a biocomponent, while part of the obtained biocomponent is used to power the diesel-electric generator. Catalytic depolymerization is carried out in the presence of sodium aluminosilicate acting as a catalyst, with the help of a technological process control block automatically monitoring the sensor indications associated with individual blocks of the catalytic depolymerization process and in the case of deviations resulting from insufficient amount of catalyst, an automatic catalyst feeder is activated. the catalyst dose is dosed into the mixing turbine in the amount of 5 kg to 35 kg per 1000 l of biocomponent in the process cycle, after which it returns to monitoring the operation of individual blocks, while to the biocomponent obtained in this way a colloidal solution of cerium dioxide nanoparticles (CeO2) is added particles from 6 nm to 8 nm in light petroleum distillates in an amount ensuring final concentration of CeO2 cerium dioxide nanoparticles in the biocomponent at a level from 5 ppm to 20 ppm. The subject of the application is also a refined biocomponent for biofuels.

PL399654A 2012-06-25 2012-06-25 Manufacturing method of refined biocomponent for biofuels and refined biocomponent for biofuels PL399654A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
PL399654A PL399654A1 (en) 2012-06-25 2012-06-25 Manufacturing method of refined biocomponent for biofuels and refined biocomponent for biofuels
EP12183858.5A EP2679655A1 (en) 2012-06-25 2012-09-11 Method for manufacturing treated biocomponent for biofuels and treated biocomponent for biofuels

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PL399654A PL399654A1 (en) 2012-06-25 2012-06-25 Manufacturing method of refined biocomponent for biofuels and refined biocomponent for biofuels

Publications (1)

Publication Number Publication Date
PL399654A1 true PL399654A1 (en) 2014-01-07

Family

ID=46880998

Family Applications (1)

Application Number Title Priority Date Filing Date
PL399654A PL399654A1 (en) 2012-06-25 2012-06-25 Manufacturing method of refined biocomponent for biofuels and refined biocomponent for biofuels

Country Status (2)

Country Link
EP (1) EP2679655A1 (en)
PL (1) PL399654A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019014778A1 (en) * 2017-07-21 2019-01-24 Roderick Michael Facey Enhanced distillate oil recovery from thermal processing and catalytic cracking of biomass slurry

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10049377C2 (en) 2000-10-05 2002-10-31 Evk Dr Oberlaender Gmbh & Co K Catalytic generation of diesel oil and petrol from hydrocarbon-containing waste and oils
GB0301599D0 (en) * 2003-01-23 2003-02-26 Oxonica Ltd Cerium oxide nanoparticles as fuel additives
DE10356245B4 (en) 2003-12-02 2007-01-25 Alphakat Gmbh Process for the production of diesel oil from hydrocarbon-containing residues and an apparatus for carrying out this process
DE102005040490A1 (en) * 2005-07-25 2007-02-08 Demir, Yaver Apparatus and Process for a Biofuel Refinery: Direct thermochemical conversion of organic substances to liquid fuels
DE102005056735B3 (en) 2005-11-29 2006-08-10 Koch, Christian, Dr. Preparation of diesel oil from hydrocarbon containing residual substances in an oil circulation with solid separation and product distillation, comprises providing heat through main energy carriers by one or more high speed mixing chambers
US20100139598A1 (en) 2008-07-17 2010-06-10 Wei Hua Wang Method of increasing the combustion efficiency of an internal combustion engine
GB2473500B (en) * 2009-09-15 2012-05-23 Ekotrend Sp Z O O Method and apparatus for producing diesel oil in a catalytic depolymerisation process and diesel oil
PL389069A1 (en) 2009-09-18 2011-03-28 Ekotrend Spółka Z Ograniczoną Odpowiedzialnością Method and system for producing fuel for diesel engines in the process of catalytic depolymerization and fuel for diesel engines

Also Published As

Publication number Publication date
EP2679655A1 (en) 2014-01-01

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