The platform will undergo maintenance on Sep 14 at about 7:45 AM EST and will be unavailable for approximately 2 hours.
2014
DOI: 10.1016/j.tet.2014.02.057
|View full text |Cite
|
Sign up to set email alerts
|

Active Pd/Fe(OH) catalyst preparation for nitrobenzene hydrogenation by tracing aqueous phase chlorine concentrations in the washing step of catalyst precursors

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
5
0

Year Published

2014
2014
2021
2021

Publication Types

Select...
7

Relationship

0
7

Authors

Journals

citations
Cited by 8 publications
(5 citation statements)
references
References 29 publications
0
5
0
Order By: Relevance
“…In order to stimulate the maximum catalytic potential of the catalyst, the following methods are usually adopted: (1) preparation of catalysts with specific morphology for increasing the specific surface area and exposing more active sites of the catalysts; (2) loading the catalysts on the support to improve its stability, avoid the agglomeration, and extend the service life of the catalysts; and (3) adding the transition metal M (Ni, Co, Fe, Cu, Ag, etc.) to form the bimetal or multiple metal catalysts with Pd, thus reducing the consumption of noble metals, and some synergies will be achieved among the different metals that will substantially benefit the efficiency of the noble catalyst. At present, most of the catalysts used for hydrogenation of NB to AN are supported catalysts, and the impregnation and precipitation are the commonly used methods. Mark et al used Al 2 O 3 as a carrier to synthesize supported mono-(Pd or Ni) and bimetallic (Pd/Ni = 1:3, 1:1, and 3:1) catalysts by an equal volume impregnation method.…”
Section: Introductionmentioning
confidence: 99%
“…In order to stimulate the maximum catalytic potential of the catalyst, the following methods are usually adopted: (1) preparation of catalysts with specific morphology for increasing the specific surface area and exposing more active sites of the catalysts; (2) loading the catalysts on the support to improve its stability, avoid the agglomeration, and extend the service life of the catalysts; and (3) adding the transition metal M (Ni, Co, Fe, Cu, Ag, etc.) to form the bimetal or multiple metal catalysts with Pd, thus reducing the consumption of noble metals, and some synergies will be achieved among the different metals that will substantially benefit the efficiency of the noble catalyst. At present, most of the catalysts used for hydrogenation of NB to AN are supported catalysts, and the impregnation and precipitation are the commonly used methods. Mark et al used Al 2 O 3 as a carrier to synthesize supported mono-(Pd or Ni) and bimetallic (Pd/Ni = 1:3, 1:1, and 3:1) catalysts by an equal volume impregnation method.…”
Section: Introductionmentioning
confidence: 99%
“…However, reduced selectivity, over-reduction, and various side reactions were constantly observed with these highly active catalysts when reducible, labile, and strong leaving groups are typically involved in the nitroaromatics molecules. Therefore, Cu-, Ag-, and Au-based transition-metal catalysts were advanced for the selective transformation of nitroaromatics into aromatic amine at the expense of low hydrogenation activity and harsh reaction conditions. , In addition to metal catalysis, carbonaceous material-promoted metal-free reduction of nitroaromatics is of great interest in academic research.…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, Cu-, 9 Ag-, 10 and Au- 11 based transition-metal catalysts were advanced for the selective transformation of nitroaromatics into aromatic amine at the expense of low hydrogenation activity and harsh reaction conditions. 12,13 In addition to metal catalysis, carbonaceous material-promoted metal-free reduction of nitroaromatics is of great interest in academic research.…”
Section: Introductionmentioning
confidence: 99%
“…Palladium supported on Fe(OH)x has also been used for hydrogenation of nitroaromatics under atmospheric pressure. However, at slightly higher temperatures of ∼60 °C very high catalyst loading (∼41%) with respect to the substrate has been used (TOF ∼141 h −1 ) . Palladium supported on SiO 2 core shell catalyst and ligand capped Pt nano particles supported on carbon have shown hydrogenation at atmospheric pressure but at higher temperature with almost 100% and upto 80% nitrobenzene conversion respectively ,.…”
Section: Resultsmentioning
confidence: 99%