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Fuels & Lubricants Magazine

Issue No. 3, October 2018

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GREEN CORNER<br />

gases is needed. The relative relation and extent of the<br />

side reactions are calculated from the distribution of<br />

secondary products: carbon monoxide, carbon dioxide<br />

and methane.<br />

CO 2<br />

+ H 2<br />

—> CH 4<br />

+ H 2<br />

O (2)<br />

Hydrogen consumption during the decarboxylation<br />

or hydrodeoxygenation reaction has a major influence<br />

on product yield distribution, inhibition of catalysts, gas<br />

composition and heat balance.<br />

If all triglycerides are reacted by decarboxylation,<br />

seven moles of hydrogen will be consumed in contrast<br />

to sixteen moles of hydrogen to be consumed if triglycerides<br />

are converted by HDO mechanism, ie 63% lower<br />

hydrogen consumption. However, if all the carbon dioxide<br />

obtained is converted to carbon monoxide and then<br />

into methane, it will consume nineteen tons of hydrogen<br />

by decarboxylation, ie the consumption of hydrogen is<br />

19% higher [11].<br />

Therefore, the ratio of decarboxylation and hydrodeoxydation<br />

reaction mechanisms should be 65/35. The<br />

favourable relationship between the reaction mechanisms<br />

can be monitored by the analysis of the relative<br />

relation between n-C17 and n-C18 by the simulated<br />

distillation method. This relationship depends on the<br />

type of catalyst, the process conditions and the type of<br />

renewable feedstock.<br />

CONCLUSION<br />

The key parameters that show the quality of used cooking<br />

oil or waste animal fat for the hydrotreating process<br />

are the total acidity, water content, metal content and<br />

free fatty acids content.<br />

The used cooking oil is more suitable feedstock than<br />

animal fat due to lower acid number, kinematic viscosity<br />

and significantly lower metal content. Such properties<br />

make used cooking oil more suitable for direct coprocessing<br />

in refinery units by known conversion processes.<br />

The reactions of UCO hydrotreating are exothermic<br />

so during co-processing increasing of temperature in the<br />

catalyst layer should be noticed which could have the<br />

impact on duration of the catalyst.<br />

The key barrier for the independent processing of<br />

UCO and animal fats in refinery units is the limit availability<br />

of the feedstock. Also, for continuous co-processing,<br />

it is recommended to upgrade the hydrodesulfurization<br />

unit with isomerisation unit to have a possibility<br />

to convert the n-paraffins partly into iso-paraffins to<br />

improve low-temperature properties of the obtained<br />

diesel fuel.<br />

Hydrotreating of used cooking oil and animal fats for<br />

the production of hydrotreated vegetable oil used as<br />

a fuel in transport is a promising technology that will<br />

inevitably develop in the following years in European<br />

Union countries or in oil companies in order to replace<br />

part fossil fuels with renewable fuels in economically and<br />

environmentally effective way.<br />

LITERATURE<br />

[1] URL: http://eur-lex.europa.eu/legal-content/HR/<br />

TXT/PDF/?uri=CELEX:32015L1513&from=HR (access:<br />

June, 22th 2018)<br />

[2] M. Crocker, Thermochemical conversion of biomass<br />

to liquid fuels and chemicals, Royal Society of Chemistry,<br />

UK, 2010, p. 1-25.<br />

[3] D. Sperling, D. Gordon, Two Billion Cars: Driving Toward<br />

Sustainability, Oxford University Press, 2009, p. 6-7.<br />

[4] M. Guo, W. Song, J. Buhain, Bioenergy and biofuels:<br />

History, status, and perspective, Renew. Sust. Energ.<br />

Rev. 42 (2015) 712-725.<br />

[5] L. Zhang, G. Hu, Supply chain design and operational<br />

planning models for biomass to drop-in fuel production,<br />

Biomass Bioenerg 58 (2013) 238-250.<br />

[6] M. F. Ali, M. E. Ali Bassam, J. G. Speight, Handbook<br />

of Industrial Chemistry, Organic Chemicals, McGraw-<br />

Hill, New York, 2014, p. 528-537.<br />

[7] Izvješće o posebnim kategorijama otpada za 2016.<br />

godinu, Hrvatska agencija za okoliš i prirodu, travanj<br />

2018. p. 7 - 9<br />

[8] S. J. Miller, Production of Biofuels and Biolubricants<br />

From a Common Feedstock, US Patent Publication No.<br />

0084026, 2009, p. 1-2.<br />

[9] M. J. McCall; A. Anumakonda, A. Bhattacharyya, J.<br />

Kocal, Feed-Flexible Processing of Oil-Rich Crops to<br />

Jet Fuel, AIChE Meeting, Chicago, 2008.<br />

[10] B. Donnis; R. G. Egeberg, P. Blom, K. G. Knudsen,<br />

Hydroprocessing of Bio-Oils and Oxygenates to Hydrocarbons,<br />

Understanding the Reaction Routes, Topics in<br />

Catalysis 52 (3) (2009) 229-240.<br />

[11] R. G. Egeberg, N. H. Michaelsen, L. Skyum, Novel<br />

hydrotreating technology for production of green diesel,<br />

Haldor Topsoe, 2010, 6-9.<br />

28 <strong>Fuels</strong>&<strong>Lubricants</strong> No. 3 OCTOBER 2018

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