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583-57-3

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583-57-3 Usage

Chemical Properties

clear colourless liquid

Check Digit Verification of cas no

The CAS Registry Mumber 583-57-3 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 5,8 and 3 respectively; the second part has 2 digits, 5 and 7 respectively.
Calculate Digit Verification of CAS Registry Number 583-57:
(5*5)+(4*8)+(3*3)+(2*5)+(1*7)=83
83 % 10 = 3
So 583-57-3 is a valid CAS Registry Number.
InChI:InChI=1/C8H16/c1-7-5-3-4-6-8(7)2/h7-8H,3-6H2,1-2H3/t7-,8-/m1/s1

583-57-3 Well-known Company Product Price

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  • (Code)Product description
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  • Aldrich

  • (D153001)  1,2-Dimethylcyclohexane,mixtureofcisandtrans  98%

  • 583-57-3

  • D153001-100G

  • 363.87CNY

  • Detail

583-57-3SDS

SAFETY DATA SHEETS

According to Globally Harmonized System of Classification and Labelling of Chemicals (GHS) - Sixth revised edition

Version: 1.0

Creation Date: Aug 12, 2017

Revision Date: Aug 12, 2017

1.Identification

1.1 GHS Product identifier

Product name 1,2-DIMETHYLCYCLOHEXANE

1.2 Other means of identification

Product number -
Other names o-Dimethylcyclohexane

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only.
Uses advised against no data available

1.4 Supplier's details

1.5 Emergency phone number

Emergency phone number -
Service hours Monday to Friday, 9am-5pm (Standard time zone: UTC/GMT +8 hours).

More Details:583-57-3 SDS

583-57-3Synthetic route

o-xylene
95-47-6

o-xylene

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
With hydrogen; [(norbornadiene)rhodium(I)chloride]2; phosphinated polydiacetylene In n-heptane at 30℃; under 60800 Torr; for 1.8h;100%
With Ti8O8(14+)*6C8H4O4(2-)*4O(2-)*3.3Li(1+)*0.7Co(2+)*0.7C4H8O*0.7H(1-); hydrogen In neat (no solvent) at 120℃; under 37503.8 Torr; for 18h;100%
With hydrogen In water at 100℃; under 15001.5 Torr; for 5h;99%
1,2-dimethylcyclohexene
1674-10-8

1,2-dimethylcyclohexene

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
With hydrogen; 1,5-hexadienerhodium(I)-chloride dimer In various solvent(s) for 6h; Ambient temperature; pH=7.6;79%
2-methyloct-7-enenitrile

2-methyloct-7-enenitrile

A

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

B

methylcycloheptane
4126-78-7

methylcycloheptane

Conditions
ConditionsYield
With potassium; tert-butyl alcohol In N,N,N,N,N,N-hexamethylphosphoric triamide; diethyl ether at 0℃; for 3h;A 71%
B 28%
1,6-dimethyl-1-cyclohexene
1759-64-4

1,6-dimethyl-1-cyclohexene

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
With hydrogen; 1,5-hexadienerhodium(I)-chloride dimer In various solvent(s) for 13h; Ambient temperature; pH=7.6;70%
o-xylene
95-47-6

o-xylene

A

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

B

1,2-dimethylcyclohexene
1674-10-8

1,2-dimethylcyclohexene

C

1,6-dimethyl-1-cyclohexene
1759-64-4

1,6-dimethyl-1-cyclohexene

Conditions
ConditionsYield
With hydrogen; 1-butyl-3-methylimidazolium Tetrafluoroborate; Rh nanoparticles stabilized by poly(NVP-co-VBIMCl) at 75℃; under 30402 Torr; for 12h; Product distribution;A 68%
B 16%
C 16%
C16H16O4

C16H16O4

A

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

B

3,4-dimethylcyclohexanol
5715-23-1

3,4-dimethylcyclohexanol

C

C8H16O2

C8H16O2

Conditions
ConditionsYield
With hydrogen; lanthanum(lll) triflate In isopropyl alcohol at 150℃; for 8h;A 33%
B 41%
C 61%
1-chloro-1,2-dimethyl-cyclohexane
1122-02-7

1-chloro-1,2-dimethyl-cyclohexane

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
With diethyl ether; sodium
Conditions
ConditionsYield
With nickel kieselguhr; hydrogen at 240 - 250℃; under 73550.8 Torr; optically inactive substance of uncertain configuration;
1,2-dimethylcyclohexanol
5402-29-9

1,2-dimethylcyclohexanol

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
With zinc(II) chloride Hydrierung des Reaktionsprodukts in Gegenwart von Nickel bei 150grad;
Multi-step reaction with 2 steps
1: PCl3
2: sodium; diethyl ether
View Scheme
3,4-dimethylcyclohexanol
5715-23-1

3,4-dimethylcyclohexanol

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
With hydrogen; vanadium(V) oxide; iron at 326.9℃; 1.5E5 Pa; Yield given;
1,7-Octadiene
3710-30-3

1,7-Octadiene

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
With zirconocene dichloride; dibutylmagnesium In diethyl ether for 24h; Mechanism; Product distribution; Ambient temperature; other dienes, other allyl magnesium compounds;100 % Chromat.
With zirconocene dichloride; dibutylmagnesium In diethyl ether for 24h; Ambient temperature;80 % Chromat.
propylcyclohexane
1678-92-8

propylcyclohexane

1,2-dimethylcyclohexane cation

1,2-dimethylcyclohexane cation

A

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

B

n-propyl cyclohexane cation

n-propyl cyclohexane cation

Conditions
ConditionsYield
at 61.9℃; Equilibrium constant; Irradiation;
1,3-dihydroisobenzofuran
496-14-0

1,3-dihydroisobenzofuran

copper oxide-chromium oxide

copper oxide-chromium oxide

A

8-oxabicyclo[4.3.0]nonane
4743-54-8

8-oxabicyclo[4.3.0]nonane

B

o-xylene
95-47-6

o-xylene

C

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

D

(2-Methylcyclohexyl)methanol
2105-40-0

(2-Methylcyclohexyl)methanol

Conditions
ConditionsYield
at 250℃; under 88260.9 Torr; Hydrogenation;
at 300℃; under 88260.9 Torr; Hydrogenation;
at 350℃; under 88260.9 Torr; Hydrogenation;
1-Methylnaphthalene
90-12-0

1-Methylnaphthalene

Raney nickel

Raney nickel

A

cyclohexane
110-82-7

cyclohexane

B

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
at 400℃; under 102971 Torr; Hydrogenation;
3,4-Dimethylphenol
95-65-8

3,4-Dimethylphenol

hydrogen

hydrogen

nickel / aluminium oxide

nickel / aluminium oxide

A

o-xylene
95-47-6

o-xylene

B

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

C

3,4-dimethylcyclohexanol
5715-23-1

3,4-dimethylcyclohexanol

D

3,4-dimethylcyclohexanone
5465-09-8

3,4-dimethylcyclohexanone

Conditions
ConditionsYield
at 150℃; Quantum yield;
at 200℃; Quantum yield;
at 250℃; Quantum yield;
(+/-)-trans,cis-decahydro-2-naphthol
36667-73-9

(+/-)-trans,cis-decahydro-2-naphthol

hydrogen iodide
10034-85-2

hydrogen iodide

A

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

B

trans-Decalin
493-02-7

trans-Decalin

C

methyl cyclohexane
82166-21-0

methyl cyclohexane

Conditions
ConditionsYield
at 290 - 340℃; im Rohr;
7-iodo-3-methyl-hept-1-ene

7-iodo-3-methyl-hept-1-ene

A

methylheptene
3404-75-9

methylheptene

B

3-methyl-1-heptene
4810-09-7

3-methyl-1-heptene

C

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

D

methylcycloheptane
4126-78-7

methylcycloheptane

Conditions
ConditionsYield
With 2,2'-azobis(isobutyronitrile); tris-(trimethylsilyl)silane In benzene Heating;
2-Methylcyclohexanone
583-60-8

2-Methylcyclohexanone

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

Conditions
ConditionsYield
Multi-step reaction with 2 steps
2: zinc chloride / Hydrierung des Reaktionsprodukts in Gegenwart von Nickel bei 150grad
View Scheme
methane
34557-54-5

methane

A

Isobutane
75-28-5

Isobutane

B

methylbutane
78-78-4

methylbutane

C

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

D

cis-1,3-dimethylcyclohexane
638-04-0

cis-1,3-dimethylcyclohexane

E

1,2,4-trimethylcyclohexane
2234-75-5

1,2,4-trimethylcyclohexane

F

1,3,5-trimethylcyclohexane
1839-63-0

1,3,5-trimethylcyclohexane

trans-1,3-dimethylcyclohexane
2207-03-6

trans-1,3-dimethylcyclohexane

H

methyl cyclohexane
82166-21-0

methyl cyclohexane

I

1,1,3-trimethylcyclohexane
3073-66-3, 150927-19-8, 150927-30-3

1,1,3-trimethylcyclohexane

Conditions
ConditionsYield
Stage #1: methane With aluminum tri-bromide; sodium bromide at 110℃; for 2h; Electrolysis;
Stage #2: at 200℃; for 0.5h;
o-xylene
95-47-6

o-xylene

A

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

B

1,2-dimethylcyclohexene
1674-10-8

1,2-dimethylcyclohexene

Conditions
ConditionsYield
With hydrogen In tetrahydrofuran at 120℃; under 7500.75 Torr; for 1h;
octane
111-65-9

octane

A

o-xylene
95-47-6

o-xylene

B

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

C

ethylbenzene
100-41-4

ethylbenzene

Conditions
ConditionsYield
With propene; (iPr4PCP)IrH4; para-xylene; 1,3,5-trimethyl-benzene at 165℃; under 760.051 Torr; for 120h;A 75 %Chromat.
B n/a
C 11 %Chromat.
1,2,3-propanetricarboxylic acid trimethyl ester
6138-26-7

1,2,3-propanetricarboxylic acid trimethyl ester

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

1-(2,3-dimethyl-cyclohexylidene)-propane-1,2,3-tricarboxylic acid trimethyl ester

1-(2,3-dimethyl-cyclohexylidene)-propane-1,2,3-tricarboxylic acid trimethyl ester

Conditions
ConditionsYield
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

o-xylene
95-47-6

o-xylene

Conditions
ConditionsYield
With platinum at 300 - 310℃;
platinum on activated charcoal at 126.9℃; for 24h; Rate constant;
With palladium 10% on activated carbon at 170 - 190℃;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

trans-1,3-dimethylcyclohexane
69685-68-3

trans-1,3-dimethylcyclohexane

Conditions
ConditionsYield
With aluminium trichloride trans-1.3-dimethyl-cyclohexane;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

cis-1,3-dimethylcyclohexane
638-04-0

cis-1,3-dimethylcyclohexane

Conditions
ConditionsYield
With aluminium trichloride at 56℃;
With aluminium trichloride cis-1.3-dimethyl-cyclohexane;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

1,2-dimethyl-1-nitro-cyclohexane

1,2-dimethyl-1-nitro-cyclohexane

Conditions
ConditionsYield
With aluminum(III) nitrate nonahydrate at 140℃;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

n-propyl cyclohexane cation

n-propyl cyclohexane cation

A

propylcyclohexane
1678-92-8

propylcyclohexane

B

1,2-dimethylcyclohexane cation

1,2-dimethylcyclohexane cation

Conditions
ConditionsYield
Equilibrium constant; Irradiation;
aluminium trichloride
7446-70-0

aluminium trichloride

1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

A

cis-1,3-dimethylcyclohexane
638-04-0

cis-1,3-dimethylcyclohexane

B

trans-1,4-dimethylcyclohexane
2207-04-7

trans-1,4-dimethylcyclohexane

C

cis-1,4-dimethylcyclohexane
624-29-3

cis-1,4-dimethylcyclohexane

Conditions
ConditionsYield
substance of uncertain configuration;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

steam

steam

carbon dioxide
124-38-9

carbon dioxide

Conditions
ConditionsYield
at 675 - 725℃; substance of uncertain configuration;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

oxygen

oxygen

A

2,7-octanedione
1626-09-1

2,7-octanedione

B

1,2-dimethylcyclohexanol
5402-29-9

1,2-dimethylcyclohexanol

C

acetic acid
64-19-7

acetic acid

D

hexyl-methyl-ketone
111-13-7

hexyl-methyl-ketone

Conditions
ConditionsYield
at 100℃; substance of uncertain configuration;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

oxygen

oxygen

A

formic acid
64-18-6

formic acid

B

5-ketohexanoic acid
3128-06-1

5-ketohexanoic acid

C

hexanoic acid
142-62-1

hexanoic acid

Conditions
ConditionsYield
at 100℃; substance of uncertain configuration;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

A

cis-1,4-dimethylcyclohexane
624-29-3

cis-1,4-dimethylcyclohexane

B

cis-1.3-dimethyl-cyclohexane; trans-1.4-dimethyl-cyclohexane

cis-1.3-dimethyl-cyclohexane; trans-1.4-dimethyl-cyclohexane

Conditions
ConditionsYield
With aluminium trichloride at 56℃;
1,2-Dimethyl-cyclohexane
583-57-3

1,2-Dimethyl-cyclohexane

A

trans-1,4-dimethylcyclohexane
2207-04-7

trans-1,4-dimethylcyclohexane

B

cis-1.4-dimethyl-cyclohexane, cis-1.3-dimethyl-cyclohexane

cis-1.4-dimethyl-cyclohexane, cis-1.3-dimethyl-cyclohexane

Conditions
ConditionsYield
With aluminium trichloride at 56℃;

583-57-3Relevant academic research and scientific papers

One-pot dual catalysis for the hydrogenation of heteroarenes and arenes

Chatterjee, Basujit,Kalsi, Deepti,Kaithal, Akash,Bordet, Alexis,Leitner, Walter,Gunanathan, Chidambaram

, p. 5163 - 5170 (2020/09/07)

A simple dinuclear monohydrido bridged ruthenium complex [{(η6-p-cymene)RuCl}2(μ-H-μ-Cl)] acts as an efficient and selective catalyst for the hydrogenation of various heteroarenes and arenes. The nature of the catalytically active species was investigated using a combination of techniques including in situ reaction monitoring, kinetic studies, quantitative poisoning experiments and electron microscopy, evidencing a dual reactivity. The results suggest that the hydrogenation of heteroarenes proceeds via molecular catalysis. In particular, monitoring the reaction progress by NMR spectroscopy indicates that [{(η6-p-cymene)RuCl}2(μ-H-μ-Cl)] is transformed into monomeric ruthenium intermediates, which upon subsequent activation of dihydrogen and hydride transfer accomplish the hydrogenation of heteroarenes under homogeneous conditions. In contrast, carbocyclic aryl motifs are hydrogenated via a heterogeneous pathway, by in situ generated ruthenium nanoparticles. Remarkably, these hydrogenation reactions can be performed using molecular hydrogen under solvent-free conditions or with 1,4-dioxane, and thus give access to a broad range of saturated heterocycles and carbocycles while generating no waste.

Ru subnanoparticles on N-doped carbon layer coated SBA-15 as efficient Catalysts for arene hydrogenation

Qian, Wei,Lin, Lina,Qiao, Yunxiang,Zhao,Xu, Zichen,Gong, Honghui,Li,Chen,Huang, Rong,Hou, Zhenshan

, (2019/08/12)

The N-doped carbon layer coated SBA-15 support has been accomplished via a pyrolysis process. The ultra-low loading Ru nanoparticles (ca. 0.1 wt.%) was incorporated into the support by impregnation and the sequential reduction. The images of HAADF-STEM revealed that the Ru particles with sub-1-nm size (0.2-0.7 nm) were uniformly dispersed on the support. The ultrafine Ru particles displayed the excellent activity for the hydrogenation of olefins, arenes, phenol derivatives and heteroarenes in aqueous phase. The aliphatic or alicyclic compounds were produced selectively without the hydrogenolysis of C–O and C–N bonds. The high turnover frequency (TOF) values can reach up to 10,000 h?1. Notably, the activity of these catalysts improved dramatically with decreasing the sizes of Ru particles. Meanwhile, the N-doped carbon layer coating endowed the high stability of the Ru catalysts and prevented the leaching of the Ru species owning to the strong interaction between doped-N atoms and the ultrafine Ru particles. Overall, this work provides a highly attractive strategy to construct the supported sub-1-nm Ru particles utilized for the aqueous hydrogenation.

Polyoxometalates Comprising Noble Metals and Corresponding Metal Clusters

-

Paragraph 0288-0292, (2019/02/13)

The invention relates to poly oxometalates represented by the formula (An)m+{M′s[M″M15X10OyRzHq]}m? or solvates thereof, corresponding supported poly-oxometalates, and processes for their preparation, as well as corresponding metal-clusters, optionally in the form of a dispersion in a liquid carrier medium or immobilized on a solid support, and processes for their preparation, as well as their use in reductive conversion of organic substrate.

Titanium(III)-Oxo Clusters in a Metal-Organic Framework Support Single-Site Co(II)-Hydride Catalysts for Arene Hydrogenation

Ji, Pengfei,Song, Yang,Drake, Tasha,Veroneau, Samuel S.,Lin, Zekai,Pan, Xiandao,Lin, Wenbin

, p. 433 - 440 (2018/01/17)

Titania (TiO2) is widely used in the chemical industry as an efficacious catalyst support, benefiting from its unique strong metal-support interaction. Many proposals have been made to rationalize this effect at the macroscopic level, yet the underlying molecular mechanism is not understood due to the presence of multiple catalytic species on the TiO2 surface. This challenge can be addressed with metal-organic frameworks (MOFs) featuring well-defined metal oxo/hydroxo clusters for supporting single-site catalysts. Herein we report that the Ti8(μ2-O)8(μ2-OH)4 node of the Ti-BDC MOF (MIL-125) provides a single-site model of the classical TiO2 support to enable CoII-hydride-catalyzed arene hydrogenation. The catalytic activity of the supported CoII-hydride is strongly dependent on the reduction of the Ti-oxo cluster, definitively proving the pivotal role of TiIII in the performance of the supported catalyst. This work thus provides a molecularly precise model of Ti-oxo clusters for understating the strong metal-support interaction of TiO2-supported heterogeneous catalysts.

Effect of the Crystallographic Phase of Ruthenium Nanosponges on Arene and Substituted-Arene Hydrogenation Activity

Ghosh, Sourav,Jagirdar, Balaji R.

, p. 3086 - 3095 (2018/05/29)

Identifying crystal structure sensitivity of a catalyst for a particular reaction is an important issue in heterogeneous catalysis. In this context, the activity of different phases of ruthenium catalysts for benzene hydrogenation has not yet been investigated. The synthesis of hcp and fcc phases of ruthenium nanosponges by chemical reduction method has been described. Reduction of ruthenium chloride using ammonia borane (AB) and tert-butylamine borane (TBAB) as reducing agents gave ruthenium nanosponge in its hcp phase. On the other hand, reduction using sodium borohydride (SB) afforded ruthenium nanosponge in its fcc phase. The as prepared hcp ruthenium nanosponge was found to be catalytically more active compared to the as prepared fcc ruthenium nanosponge for hydrogenation of benzene. The hcp ruthenium nanosponge was found to be thermally stable and recyclable over several cycles. This self-supported hcp ruthenium nanosponge shows excellent catalytic activity towards hydrogenation of various substituted benzenes. Moreover, the ruthenium nanosponge catalyst was found to bring about selective hydrogenation of aromatic cores of phenols and aryl ethers to the respective alicyclic products without hydrogenolysis of the C?O bond.

Nanoscale Ziegler catalysts based on bis(acetylacetonate)nickel in the arene hydrogenation reactions

Titova, Yuliya Yu.,Schmidt, Fedor K.

, p. 105 - 114 (2017/09/05)

The turnover frequencies of catalytic systems based on Ni(acac)2–AlEt3 or AlEt2(OEt) in the hydrogenation of benzene and its methyl-substituted homologs (toluene, three isomers of xylene, and 1,3,5-trimethylbenzene) have been determined at temperatures of 80–120 °C, initial PH2 = 15 bar, and different ratios of Al/Ni. The size and nature of the nanoparticles forming in the systems based on Ni(acac)2–AlEt3 or AlEt2(OEt) under the benzene hydrogenation condition shave been resolved by high-resolution electron microscopy and X-ray microanalysis. This study included the performance of competitive hydrogenation reactions of benzene with toluene or three xylene isomers. The relative adsorption constants of toluene and three xylene isomers have been determined and the stereochemistry of the hydrogen addition to the arene ring has also been elucidated.

A stable and practical nickel catalyst for the hydrogenolysis of C-O bonds

Cui, Xinjiang,Yuan, Hangkong,Junge, Kathrin,Topf, Christoph,Beller, Matthias,Shi, Feng

, p. 305 - 310 (2017/01/24)

The selective hydrogenolysis of C-O bonds constitutes a key step for the valorization of biomass including lignin fragments. Moreover, this defunctionalization process offers the possibility of producing interesting organic building blocks in a straightforward manner from oxygenated compounds. Herein, we demonstrate the reductive hydrogenolysis of a wide variety of ethers including diaryl, aryl-alkyl and aryl-benzyl derivatives catalyzed by a stable heterogeneous NiAlOx catalyst in the presence of a Lewis acid (LA). The special feature of this catalyst system is the formation of substituted cyclohexanols from the corresponding aryl ether.

Upgrading of aromatic compounds in bio-oil over ultrathin graphene encapsulated Ru nanoparticles

Shi, Juanjuan,Zhao, Mengsi,Wang, Yingyu,Fu, Jie,Lu, Xiuyang,Hou, Zhaoyin

supporting information, p. 5842 - 5848 (2016/05/24)

Fast pyrolysis of biomass for bio-oil production is a direct route to renewable liquid fuels, but raw bio-oil must be upgraded in order to remove easily polymerized compounds (such as phenols and furfurals). Herein, a synthesis strategy for graphene encapsulated Ru nanoparticles (NPs) on carbon sheets (denoted as Ru@G-CS) and their excellent performance for the upgrading of raw bio-oil were reported. Ru@G-CS composites were prepared via the direct pyrolysis of mixed glucose, melamine and RuCl3 at varied temperatures (500-800 °C). Characterization indicated that very fine Ru NPs (2.5 ± 1.0 nm) that were encapsulated within 1-2 layered N-doped graphene were fabricated on N-doped carbon sheets (CS) in Ru@G-CS-700 (pyrolysis at 700 °C). And the Ru@G-CS-700 composite was highly active and stable for hydrogenation of unstable components in bio-oil (31 samples including phenols, furfurals and aromatics) even in aqueous media under mild conditions. This work provides a new protocol to the utilization of biomass, especially for the upgrading of bio-oil.

Aromatic ring hydrogenation catalysed by nanoporous montmorillonite supported Ir(0)-nanoparticle composites under solvent free conditions

Das, Prabin,Sarmah, Podma Pollov,Borah, Bibek Jyoti,Saikia, Lakshi,Dutta, Dipak Kumar

, p. 2850 - 2855 (2016/03/22)

Ir(0)-nanoparticles (Ir-NPs) were synthesized into the nanopores of modified montmorillonite clay by incipient wetness impregnation of IrCl3 followed by reduction with ethylene glycol. The activation of the montmorillonite clay was carried out by treatment with HCl under controlled conditions to increase the surface area by generating nanopores which act as host for the metal nanoparticles. The synthesized Ir-NP-montmorillonite composites were characterized by N2-sorption, powder XRD, SEM, EDS, TEM, XPS, etc. The composites exhibit high surface area of 327 m2 g-1 and the Ir-NPs with size around 4 nm are uniformly distributed on the support. The Ir-NPs show efficient catalytic activity in aromatic ring hydrogenation under solvent free conditions with maximum conversion up to 100% and Turn Over Frequency (TOF) up to 79 h-1. The catalyst can be easily separated by simple filtration and remained active for several runs without significant loss of catalytic efficiency.

Enhancing the catalytic activity of Ru NPs deposited with carbon species in yolk-shell nanostructures

Guo, Miao,Lan, Guojun,Peng, Juan,Li, Mingrun,Yang, Qihua,Li, Can

, p. 10956 - 10963 (2016/07/21)

The synthesis of metal NPs with a well-defined size, shape and composition provides opportunities for tuning the catalytic performance of metal NPs. However, the presence of a stabilizer on the metal surface always blocks the active sites of metal NPs. Herein, we report an efficient method to remove the stabilizer on the metal surface via H2 pyrolysis with Ru-poly(amindoamine) encapsulated in silica-based yolk-shell nanostructures as an example. The CO uptake amount of Ru NPs increases sharply after H2 pyrolysis, indicating that the exposure degree of Ru NPs is increased. No aggregation of the colloidal Ru NPs occurs after H2 pyrolysis, which could be mainly assigned to the protection effect of C and N species formed on Ru NPs. The overall activity of Ru NPs in the yolk-shell nanostructure after the pyrolysis could reach as high as 20 300 mmol per mmol Ru per h in the hydrogenation of toluene, which is much higher than that of most reported Ru-based solid catalysts. It was found that the yolk-shell nanostructure could efficiently prevent the leaching of Ru NPs during the catalytic process. Ru NPs in the yolk-shell nanostructure could also catalyze the hydrogenation of benzoic acid and Levulinic acid with high activity and selectivity.

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