Continuous deoxygenation of concentrated stearic acid

S. Lestari; J. Beltramini; M. Lu; P. Mäki-Arvela; H. Bernas; O. Simakova; K. Eränen; D. Murzin

Continuous deoxygenation of concentrated stearic acid

S. Lestari^*, J. Beltramini, M. Lu, P. Mäki-Arvela, H. Bernas, O. Simakova, K. Eränen, D. Murzin

^*Corresponding author for this work

Research output: Contribution to conference › Paper (not published) › peer-review

Abstract

Catalytic deoxygenation of concentrated stearic acid was studied at 300°C under 10 bar Ar or 5% H₂/Ar in a trickle bed reactor using mesoporous supported Pd/C beads as a catalyst. Stable catalyst performance giving about 15% conversion level of stearic acid was observed. The main liquid phase product was heptadecane. The main gaseous products were CO and CO₂. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montreal, Quebec, Canada 8/23-27/2009).

Original language	English
Pages	516e
Publication status	Published - 2009
MoE publication type	O2 Other
Event	8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering - Montreal, QC, Canada Duration: 23 Aug 2009 → 27 Aug 2009

Conference

Conference	8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering
Country/Territory	Canada
City	Montreal, QC
Period	23/08/09 → 27/08/09

Cite this

Lestari, S., Beltramini, J., Lu, M., Mäki-Arvela, P., Bernas, H., Simakova, O., Eränen, K., & Murzin, D. (2009). Continuous deoxygenation of concentrated stearic acid. 516e. Paper presented at 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering, Montreal, QC, Canada.

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title = "Continuous deoxygenation of concentrated stearic acid",

abstract = "Catalytic deoxygenation of concentrated stearic acid was studied at 300°C under 10 bar Ar or 5% H2/Ar in a trickle bed reactor using mesoporous supported Pd/C beads as a catalyst. Stable catalyst performance giving about 15% conversion level of stearic acid was observed. The main liquid phase product was heptadecane. The main gaseous products were CO and CO2. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montreal, Quebec, Canada 8/23-27/2009).",

author = "S. Lestari and J. Beltramini and M. Lu and P. M{\"a}ki-Arvela and H. Bernas and O. Simakova and K. Er{\"a}nen and D. Murzin",

note = "Copyright: Copyright 2010 Elsevier B.V., All rights reserved.; 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering ; Conference date: 23-08-2009 Through 27-08-2009",

year = "2009",

language = "English",

pages = "516e",

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Lestari, S, Beltramini, J, Lu, M, Mäki-Arvela, P, Bernas, H, Simakova, O, Eränen, K & Murzin, D 2009, 'Continuous deoxygenation of concentrated stearic acid', Paper presented at 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering, Montreal, QC, Canada, 23/08/09 - 27/08/09 pp. 516e.

Continuous deoxygenation of concentrated stearic acid. / Lestari, S.; Beltramini, J.; Lu, M. et al.
2009. 516e Paper presented at 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering, Montreal, QC, Canada.

Research output: Contribution to conference › Paper (not published) › peer-review

TY - CONF

T1 - Continuous deoxygenation of concentrated stearic acid

AU - Lestari, S.

AU - Beltramini, J.

AU - Lu, M.

AU - Mäki-Arvela, P.

AU - Bernas, H.

AU - Simakova, O.

AU - Eränen, K.

AU - Murzin, D.

PY - 2009

Y1 - 2009

N2 - Catalytic deoxygenation of concentrated stearic acid was studied at 300°C under 10 bar Ar or 5% H2/Ar in a trickle bed reactor using mesoporous supported Pd/C beads as a catalyst. Stable catalyst performance giving about 15% conversion level of stearic acid was observed. The main liquid phase product was heptadecane. The main gaseous products were CO and CO2. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montreal, Quebec, Canada 8/23-27/2009).

AB - Catalytic deoxygenation of concentrated stearic acid was studied at 300°C under 10 bar Ar or 5% H2/Ar in a trickle bed reactor using mesoporous supported Pd/C beads as a catalyst. Stable catalyst performance giving about 15% conversion level of stearic acid was observed. The main liquid phase product was heptadecane. The main gaseous products were CO and CO2. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montreal, Quebec, Canada 8/23-27/2009).

UR - http://www.scopus.com/inward/record.url?scp=77951600139&partnerID=8YFLogxK

M3 - Paper (not published)

AN - SCOPUS:77951600139

SP - 516e

T2 - 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering

Y2 - 23 August 2009 through 27 August 2009

ER -

Continuous deoxygenation of concentrated stearic acid

Abstract

Conference

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