42806-77-9

Basic information

• Product Name: TRANS-1-METHYL-2-PROPYLCYCLOHEXANE
• Synonyms: TRANS-1-METHYL-2-PROPYLCYCLOHEXANE;trans-2-METHYL-2-PROPYLCYCLOHEXANE;Cyclohexane, 1-methyl-2-propyl-, trans-;Nsc73980;(1R,2R)-1-methyl-2-propylcyclohexane
• CAS NO: 42806-77-9
• Molecular Formula: C₁₀H₂₀
• Molecular Weight: 140.27
• Product Categories: Aromatics, Pharmaceuticals, Intermediates & Fine Chemicals
• Mol File: 42806-77-9.mol
• Article Data: 7

Chemical Properties

• Boiling Point: 174°C at 760 mmHg
• Flash Point: 47.7°C
• Appearance: /
• Density: 0.777g/cm³
• Vapor Pressure: 1.65mmHg at 25°C
• Refractive Index: 1.426
• CAS DataBase Reference: TRANS-1-METHYL-2-PROPYLCYCLOHEXANE(CAS DataBase Reference)
• NIST Chemistry Reference: TRANS-1-METHYL-2-PROPYLCYCLOHEXANE(42806-77-9)
• EPA Substance Registry System: TRANS-1-METHYL-2-PROPYLCYCLOHEXANE(42806-77-9)

Safety Data

• Hazardous Substances Data: 42806-77-9(Hazardous Substances Data)

Usage

Description

TRANS-1-METHYL-2-PROPYLCYCLOHEXANE is an organic compound with the molecular formula C10H20. It is a colorless liquid and is one of the chemical components found in petroleum solvents. TRANS-1-METHYL-2-PROPYLCYCLOHEXANE is characterized by its unique molecular structure, which consists of a cyclohexane ring with a methyl and a propyl group attached to opposite carbon atoms in a trans configuration.

Uses

Used in Petroleum Industry:
TRANS-1-METHYL-2-PROPYLCYCLOHEXANE is used as a component in petroleum solvents for various reasons. Its low toxicity, high solvency, and compatibility with a wide range of materials make it an ideal candidate for use in the petroleum industry. It is particularly useful in the formulation of solvents for cleaning, degreasing, and as additives in the production of fuels and lubricants.
Used in Chemical Synthesis:
In the field of chemical synthesis, TRANS-1-METHYL-2-PROPYLCYCLOHEXANE serves as an intermediate or building block for the production of various chemicals and materials. Its unique structure allows for further functionalization and modification, making it a versatile starting material for the synthesis of more complex organic compounds.
Used in Flavor and Fragrance Industry:
TRANS-1-METHYL-2-PROPYLCYCLOHEXANE is also utilized in the flavor and fragrance industry due to its distinct odor profile. It can be used as a component in the creation of various scent formulations, adding depth and complexity to the final product.
Used in Adhesives and Coatings:
TRANS-1-METHYL-2-PROPYLCYCLOHEXANE's solvency and compatibility with other materials make it suitable for use in the formulation of adhesives and coatings. It can be used as a solvent or a component in the production of various types of adhesives, sealants, and protective coatings for a wide range of applications, including automotive, construction, and packaging industries.

InChI:InChI=1/C10H20/c1-3-6-10-8-5-4-7-9(10)2/h9-10H,3-8H2,1-2H3/t9-,10-/m1/s1

Upstream product

• 1074-17-5 1-Methyl-2-propylbenzene 
• 994-66-1 tetrapropylsilane 
• 931-78-2 1-chloro-1-methylcyclohexane 
• 64-19-7 acetic acid 
• 91008-22-9 3-(6-Methyl-cyclohexyl-⁽³⁾)-propanol-⁽³⁾ 
• 103274-09-5 3-<6-Methyl-cyclohexenyl-(3)>-propen-(1)-ol-(3) 
• 103385-64-4 3-<6-Methyl-cyclohexenyl-(3)>-propin-(1)-ol-(3) 
• 89-94-1 6-methyl-3-cyclohexene-1-carbaldehyde 
• 91-17-8 decalin 
• 97-54-1 2-methoxy-4-propenylphenol 
• 2785-87-7 2-methoxy-4-n-propylphenol 
• 97-53-0 4-allylguaiacol 
• 4291-79-6 trans-1-Methyl-2-propylcyclohexan 
• 4291-79-6 cis-1-Methyl-2-propylcyclohexan 

Downstream Products

• 4291-79-6 trans-1-Methyl-2-propyl-cyclohexan 
• 4291-79-6 trans-1-methyl-2-propylcyclohexane 
• 4291-79-6 cis-1-Methyl-2-propyl-cyclohexan 

Relevant articles and documents

Efficient hydro-deoxygenation of lignin derived phenolic compounds over bifunctional catalysts with optimized acid/metal interactions

Efficient hydro-deoxygenation (HDO) of lignin derived phenolic compounds was a challenging task due to the incompatibility of the phenolic feedstock and the current hydro-processing catalysts. In this paper, hydro-deoxygenation of lignin derived phenolic compounds over a series of bifunctional catalysts with different metal/acid interactions was firstly carried out. It was found that the distance between the acidic site and noble metal played an important role in the catalytic performance of phenolic hydro-deoxygenation. A highly stable bifunctional catalyst for hydro-deoxygenation of lignin derived phenolic compounds was obtained through simple selective deposition of Pt on alumina in a commonly used Al2O3-ZSM-5 nanocomposite. The bifunctional catalyst retained its complete deoxygenation capacity for more than 500 h. The catalyst can also be used for the HDO of various phenolic model compounds and real bio-oil derived from lignin. A correction of the generally accepted the closer the better criterion in metal/acid bifunctional catalysts when used in bio-oxygenate HDO was also discussed.

Influence of iridium content on the behavior of Pt-Ir/Al2O 3 and Pt-Ir/TiO2 catalysts for selective ring opening of naphthenes

The influence of Ir content on the properties of Pt-Ir/Al2O 3 and Pt-Ir/TiO2 catalysts for selective ring opening of naphthenes was studied. It was found that these catalysts display a strong Pt-Ir interaction but only a weak metal-support interaction. Catalyst acidities depend on the metal loading, but opposite effects were observed on alumina (decrease) or titania (increase) as the metal loading increased. The results obtained from test reactions (cyclohexane dehydrogenation and cyclopentane hydrogenolysis) showed that titania supported catalysts were less active than their alumina supported counterparts. This behavior could be due to the partial blockage of metallic sites by migrated TiOx species and the sinterization of metallic phase during the reduction step. The methylcyclopentane ring opening reaction was found to occur through a partially selective mechanism, and an increase in activity as the Ir loading increased was observed. The selective mechanism was favored by higher total metal loadings, possibly due to an increase in the size of metallic aggregates. Alumina supported catalysts present higher ring opening selectivities. The activity for decalin ring opening increased both with metal loading and reaction temperature level.

Ring opening of decalin and methylcyclohexane over alumina-based monofunctional WO3/Al2O3 and Ir/Al 2O3 catalysts

Ring-opening reactions of decalin and MCH were studied over monofunctional acid (WO3/Al2O3) and metal (Ir/Al 2O3) catalysts containing, respectively, up to 5.3 at. W/nm2 and 1.8 wt% Ir. The catalysts were characterized by X-ray diffraction, Raman spectroscopy, low-temperature CO adsorption followed by infrared spectroscopy, and H2 chemisorption. A reaction network was proposed for both molecules and used to determine the kinetic parameters. Kinetic modeling allowed relating characterization results and catalytic performance. For WO3/Al2O3 catalysts, ring contraction precedes ring opening of both molecules. The evolution of ring contraction activity was consistent with the development of relatively strong Bronsted acid sites. Ring opening occurs according to a classic acid mechanism. For Ir/Al2O3 catalysts, only direct ring opening was observed. Ring opening proceeds mostly via dicarbene mechanism. Analysis of products indicated that monofunctional metal catalysts are better suited than acid solids for upgrading LCO.