Formic Acid as a Hydrogen Donor for Catalytic Transformations of Tar

Specific features of the catalytic tar cracking in the presence of formic acid, BEA zeolite and 8% Ni-2.5% Mo/Sibunit catalyst were studied at 350 °C and 1.0 MPa pressure. The obtained results evidenced that formic acid can be used as a hydrogen donor during catalytic reactions. The formic acid addi...

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Main Authors: Vladimir V. Chesnokov, Pavel P. Dik, Aleksandra S. Chichkan
Format: Article
Language:English
Published: MDPI AG 2020-09-01
Series:Energies
Subjects:
tar
Online Access:https://www.mdpi.com/1996-1073/13/17/4515
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spelling doaj-9c860c02ce6042c5a82c09555951fef32020-11-25T03:02:51ZengMDPI AGEnergies1996-10732020-09-01134515451510.3390/en13174515Formic Acid as a Hydrogen Donor for Catalytic Transformations of TarVladimir V. Chesnokov0Pavel P. Dik1Aleksandra S. Chichkan2Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, 630090 Novosibirsk, RussiaBoreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, 630090 Novosibirsk, RussiaBoreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, 630090 Novosibirsk, RussiaSpecific features of the catalytic tar cracking in the presence of formic acid, BEA zeolite and 8% Ni-2.5% Mo/Sibunit catalyst were studied at 350 °C and 1.0 MPa pressure. The obtained results evidenced that formic acid can be used as a hydrogen donor during catalytic reactions. The formic acid addition made it possible to perform efficient hydrocracking of heavy feed such as tar. It was found that both the tar conversion and selectivity to light (gasoline-diesel) fractions grew in the sequence: tar < (tar - formic acid) < (tar - formic acid - BEA zeolite) < (tar - formic acid - BEA zeolite - 8% Ni-2.5% Mo/Sibunit catalyst). Furthermore, significantly lower concentrations of impurities containing sulfur and nitrogen were observed for the (tar - formic acid - BEA zeolite - 8% Ni-2.5% Mo/Sibunit catalyst) system. For example, the sulfur and nitrogen concentrations in the tar precursor were 1.50% and 0.86%, respectively. Meanwhile, their concentrations in the liquid products after the catalytic cracking were 0.73% and 0.18%, respectively.https://www.mdpi.com/1996-1073/13/17/4515hydrocrackingtarformic acidnickelzeolitehydrogen donor
collection DOAJ
language English
format Article
sources DOAJ
author Vladimir V. Chesnokov
Pavel P. Dik
Aleksandra S. Chichkan
spellingShingle Vladimir V. Chesnokov
Pavel P. Dik
Aleksandra S. Chichkan
Formic Acid as a Hydrogen Donor for Catalytic Transformations of Tar
Energies
hydrocracking
tar
formic acid
nickel
zeolite
hydrogen donor
author_facet Vladimir V. Chesnokov
Pavel P. Dik
Aleksandra S. Chichkan
author_sort Vladimir V. Chesnokov
title Formic Acid as a Hydrogen Donor for Catalytic Transformations of Tar
title_short Formic Acid as a Hydrogen Donor for Catalytic Transformations of Tar
title_full Formic Acid as a Hydrogen Donor for Catalytic Transformations of Tar
title_fullStr Formic Acid as a Hydrogen Donor for Catalytic Transformations of Tar
title_full_unstemmed Formic Acid as a Hydrogen Donor for Catalytic Transformations of Tar
title_sort formic acid as a hydrogen donor for catalytic transformations of tar
publisher MDPI AG
series Energies
issn 1996-1073
publishDate 2020-09-01
description Specific features of the catalytic tar cracking in the presence of formic acid, BEA zeolite and 8% Ni-2.5% Mo/Sibunit catalyst were studied at 350 °C and 1.0 MPa pressure. The obtained results evidenced that formic acid can be used as a hydrogen donor during catalytic reactions. The formic acid addition made it possible to perform efficient hydrocracking of heavy feed such as tar. It was found that both the tar conversion and selectivity to light (gasoline-diesel) fractions grew in the sequence: tar < (tar - formic acid) < (tar - formic acid - BEA zeolite) < (tar - formic acid - BEA zeolite - 8% Ni-2.5% Mo/Sibunit catalyst). Furthermore, significantly lower concentrations of impurities containing sulfur and nitrogen were observed for the (tar - formic acid - BEA zeolite - 8% Ni-2.5% Mo/Sibunit catalyst) system. For example, the sulfur and nitrogen concentrations in the tar precursor were 1.50% and 0.86%, respectively. Meanwhile, their concentrations in the liquid products after the catalytic cracking were 0.73% and 0.18%, respectively.
topic hydrocracking
tar
formic acid
nickel
zeolite
hydrogen donor
url https://www.mdpi.com/1996-1073/13/17/4515
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