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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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 |
work_keys_str_mv |
AT vladimirvchesnokov formicacidasahydrogendonorforcatalytictransformationsoftar AT pavelpdik formicacidasahydrogendonorforcatalytictransformationsoftar AT aleksandraschichkan formicacidasahydrogendonorforcatalytictransformationsoftar |
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