PL412988A1 - Technological line for producing biofuels and fuel biocomponents and method for producing biofuels and fuel biocomponents - Google Patents

Technological line for producing biofuels and fuel biocomponents and method for producing biofuels and fuel biocomponents

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Publication number
PL412988A1
PL412988A1 PL412988A PL41298815A PL412988A1 PL 412988 A1 PL412988 A1 PL 412988A1 PL 412988 A PL412988 A PL 412988A PL 41298815 A PL41298815 A PL 41298815A PL 412988 A1 PL412988 A1 PL 412988A1
Authority
PL
Poland
Prior art keywords
biocomponents
output
fuel
technological line
reactor
Prior art date
Application number
PL412988A
Other languages
Polish (pl)
Other versions
PL229547B1 (en
Inventor
Lech Hys
Sławomir Kownacki
Original Assignee
Lech Hys
Sławomir Kownacki
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 Lech Hys, Sławomir Kownacki filed Critical Lech Hys
Priority to PL412988A priority Critical patent/PL229547B1/en
Publication of PL412988A1 publication Critical patent/PL412988A1/en
Publication of PL229547B1 publication Critical patent/PL229547B1/en

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  • Liquid Carbonaceous Fuels (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Fats And Perfumes (AREA)

Abstract

Zgłoszenie rozwiązuje zagadnienie opracowania linii technologicznej i sposobu otrzymywania finalnego produktu bez odpadów i bez konieczności używania katalizatorów. Linia technologiczna do wytwarzania biopaliw i biokomponentów paliw, charakteryzuje się tym, że ma zbiornik surowca (1) połączony z hydrodynamicznym kawitatorem (3) oraz zbiornik alkoholu (4) połączony z tym kawitatorem, którego wyjście połączone jest ze zbiornikiem buforowym (6) emulsji, gdzie na wyjściu jest pompa wysokociśnieniowa (7) tłocząca do reaktora rurowego (8). Wyjście tego reaktora połączone jest z chłodnicą rurową (10), na której wyjściu jest zawór rozprężny (12), separator kolumnowy (13) połączony z kondensatorem (14), a w dolnej części ma zbiorniki produktów (15 i 16), zaś w górnej części wyjście kondensatora (14) połączone jest ze zbiornikiem alkoholu (4). Sposób, charakteryzuje się tym, że surowiec w proporcji 0,25 - 2,0 obj. wprowadza się do hydrodynamicznego pola kawitacyjnego i prowadzi proces kawitacji, aż do chwili utworzenia stabilnej emulsji, następnie zdyspergowaną mieszaninę przetłacza się pod ciśnieniem 20 MPa - 45 MPa, w czasie 120 s - 3600 s oraz w temperaturze 200°C - 450°C przez reaktor usytuowany w polu promieniowania podczerwonego, po czym przereagowana mieszanina wprowadzana jest do strefy intensywnego chłodzenia i chłodzona do osiągnięcia temperatury 20°C - 150°C.The application solves the issue of developing a technological line and how to obtain the final product without waste and without the need for catalysts. The technological line for the production of biofuels and biocomponents of fuels is characterized by the fact that it has a raw material tank (1) connected to a hydrodynamic cavitator (3) and an alcohol tank (4) connected to this cavitator, whose output is connected to the buffer tank (6) of the emulsion, where the output is a high pressure pump (7) conveying to the tubular reactor (8). The outlet of this reactor is connected to a tubular cooler (10), at the output of which is an expansion valve (12), a column separator (13) connected to a condenser (14), and in the bottom part there are product tanks (15 and 16), and in the top part the capacitor output (14) is connected to the alcohol tank (4). The method is characterized in that the raw material in the proportion of 0.25 - 2.0 vol. is introduced into the hydrodynamic cavitation field and conducts the cavitation process until a stable emulsion is formed, then the dispersed mixture is forced under a pressure of 20 MPa - 45 MPa, during 120 s - 3600 s and at a temperature of 200 ° C - 450 ° C through the reactor located in the infrared radiation field, after which the reacted mixture is introduced into the zone of intensive cooling and cooled until reaching a temperature of 20 ° C - 150 ° C.

PL412988A 2015-07-02 2015-07-02 Technological line for producing biofuels and fuel biocomponents and method for producing biofuels and fuel biocomponents PL229547B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL412988A PL229547B1 (en) 2015-07-02 2015-07-02 Technological line for producing biofuels and fuel biocomponents and method for producing biofuels and fuel biocomponents

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PL412988A PL229547B1 (en) 2015-07-02 2015-07-02 Technological line for producing biofuels and fuel biocomponents and method for producing biofuels and fuel biocomponents

Publications (2)

Publication Number Publication Date
PL412988A1 true PL412988A1 (en) 2017-01-16
PL229547B1 PL229547B1 (en) 2018-07-31

Family

ID=57756395

Family Applications (1)

Application Number Title Priority Date Filing Date
PL412988A PL229547B1 (en) 2015-07-02 2015-07-02 Technological line for producing biofuels and fuel biocomponents and method for producing biofuels and fuel biocomponents

Country Status (1)

Country Link
PL (1) PL229547B1 (en)

Also Published As

Publication number Publication date
PL229547B1 (en) 2018-07-31

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