Example of Applied Catalysis A: General format
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Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format
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Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format Example of Applied Catalysis A: General format
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Applied Catalysis A: General — Template for authors

Publisher: Elsevier
Categories Rank Trend in last 3 yrs
Process Chemistry and Technology #10 of 59 down down by 6 ranks
Catalysis #18 of 57 down down by 5 ranks
journal-quality-icon Journal quality:
High
calendar-icon Last 4 years overview: 1568 Published Papers | 14145 Citations
indexed-in-icon Indexed in: Scopus
last-updated-icon Last updated: 12/06/2020
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Related Journals

open access Open Access
recommended Recommended

Elsevier

Quality:  
High
CiteRatio: 30.2
SJR: 4.672
SNIP: 2.784
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Quality:  
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CiteRatio: 7.3
SJR: 0.8
SNIP: 0.868
recommended Recommended

Royal Society of Chemistry

Quality:  
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SJR: 4.322
SNIP: 2.101
open access Open Access
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American Chemical Society

Quality:  
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CiteRatio: 19.8
SJR: 4.898
SNIP: 2.2

Journal Performance & Insights

Impact Factor

CiteRatio

Determines the importance of a journal by taking a measure of frequency with which the average article in a journal has been cited in a particular year.

A measure of average citations received per peer-reviewed paper published in the journal.

5.006

8% from 2018

Impact factor for Applied Catalysis A: General from 2016 - 2019
Year Value
2019 5.006
2018 4.63
2017 4.521
2016 4.339
graph view Graph view
table view Table view

9.0

6% from 2019

CiteRatio for Applied Catalysis A: General from 2016 - 2020
Year Value
2020 9.0
2019 8.5
2018 8.5
2017 8.4
2016 7.4
graph view Graph view
table view Table view

insights Insights

  • Impact factor of this journal has increased by 8% in last year.
  • This journal’s impact factor is in the top 10 percentile category.

insights Insights

  • CiteRatio of this journal has increased by 6% in last years.
  • This journal’s CiteRatio is in the top 10 percentile category.

SCImago Journal Rank (SJR)

Source Normalized Impact per Paper (SNIP)

Measures weighted citations received by the journal. Citation weighting depends on the categories and prestige of the citing journal.

Measures actual citations received relative to citations expected for the journal's category.

1.265

9% from 2019

SJR for Applied Catalysis A: General from 2016 - 2020
Year Value
2020 1.265
2019 1.163
2018 1.211
2017 1.237
2016 1.202
graph view Graph view
table view Table view

1.374

3% from 2019

SNIP for Applied Catalysis A: General from 2016 - 2020
Year Value
2020 1.374
2019 1.34
2018 1.322
2017 1.265
2016 1.321
graph view Graph view
table view Table view

insights Insights

  • SJR of this journal has increased by 9% in last years.
  • This journal’s SJR is in the top 10 percentile category.

insights Insights

  • SNIP of this journal has increased by 3% in last years.
  • This journal’s SNIP is in the top 10 percentile category.

Applied Catalysis A: General

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Elsevier

Applied Catalysis A: General

Applied Catalysis A: General publishes novel papers on all aspects of catalysis of basic and practical interest. The scope of Applied Catalysis A: General includes the following: •Scientific understanding of any catalytic phenomenon. Phenomena of relevance to current indu...... Read More

Process Chemistry and Technology

Catalysis

Chemical Engineering

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Last updated on
12 Jun 2020
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ISSN
0926-860X
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Impact Factor
High - 1.526
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Open Access
No
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Sherpa RoMEO Archiving Policy
Green faq
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Plagiarism Check
Available via Turnitin
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Endnote Style
Download Available
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Bibliography Name
elsarticle-num
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Citation Type
Numbered
[25]
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Bibliography Example
G. E. Blonder, M. Tinkham, T. M. Klapwijk, Transition from metallic to tunneling regimes in superconducting microconstrictions: Excess current, charge imbalance, and supercurrent conversion, Phys. Rev. B 25 (7) (1982) 4515–4532. URL 10.1103/PhysRevB.25.4515

Top papers written in this journal

Journal Article DOI: 10.1016/S0926-860X(00)00843-7
Mechanisms of catalyst deactivation
Calvin H. Bartholomew1

Abstract:

The literature treating mechanisms of catalyst deactivation is reviewed. Intrinsic mechanisms of catalyst deactivation are many; nevertheless, they can be classified into six distinct types: (i) poisoning, (ii) fouling, (iii) thermal degradation, (iv) vapor compound formation accompanied by transport, (v) vapor-solid and/or s... The literature treating mechanisms of catalyst deactivation is reviewed. Intrinsic mechanisms of catalyst deactivation are many; nevertheless, they can be classified into six distinct types: (i) poisoning, (ii) fouling, (iii) thermal degradation, (iv) vapor compound formation accompanied by transport, (v) vapor-solid and/or solid-solid reactions, and (vi) attrition/crushing. As (i), (iv), and (v) are chemical in nature and (ii) and (v) are mechanical, the causes of deactivation are basically three-fold: chemical, mechanical and thermal. Each of these six mechanisms is defined and its features are illustrated by data and examples from the literature. The status of knowledge and needs for further work are also summarized for each type of deactivation mechanism. The development during the past two decades of more sophisticated surface spectroscopies and powerful computer technologies provides opportunities for obtaining substantially better understanding of deactivation mechanisms and building this understanding into comprehensive mathematical models that will enable more effective design and optimization of processes involving deactivating catalysts. © 2001 Elsevier Science B.V. All rights reserved. read more read less

Topics:

Catalyst poisoning (55%)55% related to the paper
View PDF
2,526 Citations
Journal Article DOI: 10.1016/S0926-860X(03)00549-0
Carbon nanotubes and nanofibers in catalysis
Philippe Serp1

Abstract:

This review analyses the literature from the early 1990s until the beginning of 2003 and covers the use of carbon nanotubes (CNT) and nanofibers as catalysts and catalysts supports. The article is composed of three sections, the first one explains why these materials can be suitable for these applications, the second describe... This review analyses the literature from the early 1990s until the beginning of 2003 and covers the use of carbon nanotubes (CNT) and nanofibers as catalysts and catalysts supports. The article is composed of three sections, the first one explains why these materials can be suitable for these applications, the second describes the different preparation methods for supporting metallic catalysts on these supports, and the last one details the catalytic results obtained with nanotubes or nanofibers based catalysts. When possible, the results were compared to those obtained on classical carbonaceous supports and explanations are proposed to clarify the different behaviors observed. read more read less

Topics:

Catalyst support (54%)54% related to the paper, Carbon nanotube (53%)53% related to the paper, Nanofiber (52%)52% related to the paper
1,742 Citations
Journal Article DOI: 10.1016/J.APCATA.2011.08.046
A review of catalytic upgrading of bio-oil to engine fuels

Abstract:

As the oil reserves are depleting the need of an alternative fuel source is becoming increasingly apparent. One prospective method for producing fuels in the future is conversion of biomass into bio-oil and then upgrading the bio-oil over a catalyst, this method is the focus of this review article. Bio-oil production can be f... As the oil reserves are depleting the need of an alternative fuel source is becoming increasingly apparent. One prospective method for producing fuels in the future is conversion of biomass into bio-oil and then upgrading the bio-oil over a catalyst, this method is the focus of this review article. Bio-oil production can be facilitated through flash pyrolysis, which has been identified as one of the most feasible routes. The bio-oil has a high oxygen content and therefore low stability over time and a low heating value. Upgrading is desirable to remove the oxygen and in this way make it resemble crude oil. Two general routes for bio-oil upgrading have been considered: hydrodeoxygenation (HDO) and zeolite cracking. HDO is a high pressure operation where hydrogen is used to exclude oxygen from the bio-oil, giving a high grade oil product equivalent to crude oil. Catalysts for the reaction are traditional hydrodesulphurization (HDS) catalysts, such as Co–MoS2/Al2O3, or metal catalysts, as for example Pd/C. However, catalyst lifetimes of much more than 200 h have not been achieved with any current catalyst due to carbon deposition. Zeolite cracking is an alternative path, where zeolites, e.g. HZSM-5, are used as catalysts for the deoxygenation reaction. In these systems hydrogen is not a requirement, so operation is performed at atmospheric pressure. However, extensive carbon deposition results in very short catalyst lifetimes. Furthermore a general restriction in the hydrogen content of the bio-oil results in a low H/C ratio of the oil product as no additional hydrogen is supplied. Overall, oil from zeolite cracking is of a low grade, with heating values approximately 25% lower than that of crude oil. Of the two mentioned routes, HDO appears to have the best potential, as zeolite cracking cannot produce fuels of acceptable grade for the current infrastructure. HDO is evaluated as being a path to fuels in a grade and at a price equivalent to present fossil fuels, but several tasks still have to be addressed within this process. Catalyst development, understanding of the carbon forming mechanisms, understanding of the kinetics, elucidation of sulphur as a source of deactivation, evaluation of the requirement for high pressure, and sustainable sources for hydrogen are all areas which have to be elucidated before commercialisation of the process. read more read less

Topics:

Fossil fuel (55%)55% related to the paper, Hydrodeoxygenation (55%)55% related to the paper, Catalysis (51%)51% related to the paper, Pyrolysis (50%)50% related to the paper, Cracking (50%)50% related to the paper
1,487 Citations
Journal Article DOI: 10.1016/J.APCATA.2009.10.008
Ionic liquids and catalysis: Recent progress from knowledge to applications

Abstract:

This review gives a survey on the latest most representative developments and progress concerning ionic liquids, from their fundamental properties to their applications in catalytic processes. It also highlights their emerging use for biomass treatment and transformation. This review gives a survey on the latest most representative developments and progress concerning ionic liquids, from their fundamental properties to their applications in catalytic processes. It also highlights their emerging use for biomass treatment and transformation. read more read less

Topics:

Ionic liquid (51%)51% related to the paper
1,471 Citations
Journal Article DOI: 10.1016/S0926-860X(97)00186-5
Design, synthesis, and use of cobalt-based Fischer-Tropsch synthesis catalysts
Enrique Iglesia1

Abstract:

Catalyst productivity and selectivity to C5+ hydrocarbons are critical design criteria in the choice of Fischer-Tropsch synthesis (FTS) catalysts and reactors. Cobalt-based catalysts appear to provide the best compromise between performance and cost for the synthesis of hydrocarbons from CO/H2 mixtures. Optimum catalysts with... Catalyst productivity and selectivity to C5+ hydrocarbons are critical design criteria in the choice of Fischer-Tropsch synthesis (FTS) catalysts and reactors. Cobalt-based catalysts appear to provide the best compromise between performance and cost for the synthesis of hydrocarbons from CO/H2 mixtures. Optimum catalysts with high cobalt concentration and site density can be prepared by controlled reduction of nitrate precursors introduced via melt or aqueous impregnation methods. FTS turnover rates are independent of Co dispersion and support identity over the accessible dispersion range (0.01–0.12) at typical FTS conditions. At low reactant pressures or conversions, water increases FTS reaction rates and the selectivity to olefins and to C5+ hydrocarbons. These water effects depend on the identity of the support and lead to support effects on turnover rates at low CO conversions. Turnover rates increase when small amounts of Ru (Ru/Co<0.008 at.) are added to Co catalysts. C5+ selectivity increases with increasing Co site density because diffusion-enhanced readsorption of α-olefins reverses, β-hydrogen abstraction steps and inhibits chain termination. Severe diffusional restrictions, however, can also deplete CO within catalyst pellets and decrease chain growth probabilities. Therefore, optimum C5+ selectivities are obtained on catalysts with moderate diffusional restrictions. Diffusional constraints depend on pellet size and porosity and on the density and radial location of Co sites within catalyst pellets. Slurry bubble column reactors and the use of eggshell catalyst pellets in packed-bed reactors introduce design flexibility by decoupling the characteristic diffusion distance in catalyst pellets from pressure drop and other reactor constraints. read more read less

Topics:

Catalyst support (60%)60% related to the paper, Catalysis (51%)51% related to the paper, Cobalt (51%)51% related to the paper, Heterogeneous catalysis (51%)51% related to the paper, Fischer–Tropsch process (51%)51% related to the paper
1,366 Citations
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Applied Catalysis A: General format uses elsarticle-num citation style.

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Of course! We support all the top citation styles, such as APA style, MLA style, Vancouver style, Harvard style, and Chicago style. For example, when you write your paper and hit autoformat, our system will automatically update your article as per the Applied Catalysis A: General citation style.

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To be honest, the answer is no. The impact factor is one of the many elements that determine the quality of a journal. Few of these factors include review board, rejection rates, frequency of inclusion in indexes, and Eigenfactor. You need to assess all these factors before you make your final call.

13. What is Sherpa RoMEO Archiving Policy for Applied Catalysis A: General?

SHERPA/RoMEO Database

We extracted this data from Sherpa Romeo to help researchers understand the access level of this journal in accordance with the Sherpa Romeo Archiving Policy for Applied Catalysis A: General. The table below indicates the level of access a journal has as per Sherpa Romeo's archiving policy.

RoMEO Colour Archiving policy
Green Can archive pre-print and post-print or publisher's version/PDF
Blue Can archive post-print (ie final draft post-refereeing) or publisher's version/PDF
Yellow Can archive pre-print (ie pre-refereeing)
White Archiving not formally supported
FYI:
  1. Pre-prints as being the version of the paper before peer review and
  2. Post-prints as being the version of the paper after peer-review, with revisions having been made.

14. What are the most common citation types In Applied Catalysis A: General?

The 5 most common citation types in order of usage for Applied Catalysis A: General are:.

S. No. Citation Style Type
1. Author Year
2. Numbered
3. Numbered (Superscripted)
4. Author Year (Cited Pages)
5. Footnote

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