Kinetic modelling of the aqueous-phase reforming of fischer-tropsch water over ceria-zirconia supported nickel-copper catalyst

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Kinetic modelling of the aqueous-phase reforming of fischer-tropsch water over ceria-zirconia supported nickel-copper catalyst. / Coronado, Irene; Arandia, Aitor; Reinikainen, Matti; Karinen, Reetta; Puurunen, Riikka L.; Lehtonen, Juha.

julkaisussa: CATALYSTS, Vuosikerta 9, Nro 11, 936, 01.11.2019.

Tutkimustuotos: Lehtiartikkelivertaisarvioitu

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@article{806319f15c024f368fc03a5d558fc2cd,
title = "Kinetic modelling of the aqueous-phase reforming of fischer-tropsch water over ceria-zirconia supported nickel-copper catalyst",
abstract = "In the Fischer–Tropsch (FT) synthesis, a mixture of CO and H2 is converted into hydrocarbons and water with diluted organics. This water fraction with oxygenated hydrocarbons can be processed through aqueous-phase reforming (APR) to produce H2. Therefore, the APR of FT water may decrease the environmental impact of organic waters and improve the efficiency of the FT process. This work aimed at developing a kinetic model for the APR of FT water. APR experiments were conducted with real FT water in a continuous packed-bed reactor at different operating conditions of temperature (210–240◦ C), pressure (3.2–4.5 MPa) and weight hourly space velocity (WHSV) (40–200 h−1) over a nickel-copper catalyst supported on ceria-zirconia. The kinetic model considered C1-C4 alcohols as reactants, H2, CO, CO2 and CH4 as the gaseous products, and acetic acid as the only liquid product. The kinetic model included seven reactions, the reaction rates of which were expressed with power law equations. The kinetic parameters were estimated with variances and confidence intervals that explain the accuracy of the model to estimate the outlet liquid composition resulting from the APR of FT water. The kinetic model developed in this work may facilitate the development of APR to be integrated in a FT synthesis process.",
keywords = "Aqueous-phase reforming, Fischer, Kinetic modelling, Nickel-based catalyst, Tropsch water",
author = "Irene Coronado and Aitor Arandia and Matti Reinikainen and Reetta Karinen and Puurunen, {Riikka L.} and Juha Lehtonen",
year = "2019",
month = "11",
day = "1",
doi = "10.3390/catal9110936",
language = "English",
volume = "9",
journal = "CATALYSTS",
issn = "2073-4344",
publisher = "MDPI AG",
number = "11",

}

RIS - Lataa

TY - JOUR

T1 - Kinetic modelling of the aqueous-phase reforming of fischer-tropsch water over ceria-zirconia supported nickel-copper catalyst

AU - Coronado, Irene

AU - Arandia, Aitor

AU - Reinikainen, Matti

AU - Karinen, Reetta

AU - Puurunen, Riikka L.

AU - Lehtonen, Juha

PY - 2019/11/1

Y1 - 2019/11/1

N2 - In the Fischer–Tropsch (FT) synthesis, a mixture of CO and H2 is converted into hydrocarbons and water with diluted organics. This water fraction with oxygenated hydrocarbons can be processed through aqueous-phase reforming (APR) to produce H2. Therefore, the APR of FT water may decrease the environmental impact of organic waters and improve the efficiency of the FT process. This work aimed at developing a kinetic model for the APR of FT water. APR experiments were conducted with real FT water in a continuous packed-bed reactor at different operating conditions of temperature (210–240◦ C), pressure (3.2–4.5 MPa) and weight hourly space velocity (WHSV) (40–200 h−1) over a nickel-copper catalyst supported on ceria-zirconia. The kinetic model considered C1-C4 alcohols as reactants, H2, CO, CO2 and CH4 as the gaseous products, and acetic acid as the only liquid product. The kinetic model included seven reactions, the reaction rates of which were expressed with power law equations. The kinetic parameters were estimated with variances and confidence intervals that explain the accuracy of the model to estimate the outlet liquid composition resulting from the APR of FT water. The kinetic model developed in this work may facilitate the development of APR to be integrated in a FT synthesis process.

AB - In the Fischer–Tropsch (FT) synthesis, a mixture of CO and H2 is converted into hydrocarbons and water with diluted organics. This water fraction with oxygenated hydrocarbons can be processed through aqueous-phase reforming (APR) to produce H2. Therefore, the APR of FT water may decrease the environmental impact of organic waters and improve the efficiency of the FT process. This work aimed at developing a kinetic model for the APR of FT water. APR experiments were conducted with real FT water in a continuous packed-bed reactor at different operating conditions of temperature (210–240◦ C), pressure (3.2–4.5 MPa) and weight hourly space velocity (WHSV) (40–200 h−1) over a nickel-copper catalyst supported on ceria-zirconia. The kinetic model considered C1-C4 alcohols as reactants, H2, CO, CO2 and CH4 as the gaseous products, and acetic acid as the only liquid product. The kinetic model included seven reactions, the reaction rates of which were expressed with power law equations. The kinetic parameters were estimated with variances and confidence intervals that explain the accuracy of the model to estimate the outlet liquid composition resulting from the APR of FT water. The kinetic model developed in this work may facilitate the development of APR to be integrated in a FT synthesis process.

KW - Aqueous-phase reforming

KW - Fischer

KW - Kinetic modelling

KW - Nickel-based catalyst

KW - Tropsch water

UR - http://www.scopus.com/inward/record.url?scp=85074683902&partnerID=8YFLogxK

U2 - 10.3390/catal9110936

DO - 10.3390/catal9110936

M3 - Article

VL - 9

JO - CATALYSTS

JF - CATALYSTS

SN - 2073-4344

IS - 11

M1 - 936

ER -

ID: 39406332