17302-32-8

Basic information

• Product Name: Nonane,3,7-dimethyl-
• Synonyms: Nonane,3,7-dimethyl-
• CAS NO: 17302-32-8
• Molecular Formula: C₁₁H₂₄
• Molecular Weight: 156.31
• Mol File: 17302-32-8.mol
• Article Data: 1

Chemical Properties

• Melting Point: -57.06°C (estimate)
• Boiling Point: 184°C
• Flash Point: 110.2°C
• Appearance: /
• Density: 0.7435
• Vapor Pressure: 1.06mmHg at 25°C
• Refractive Index: 1.4176
• CAS DataBase Reference: Nonane,3,7-dimethyl-(CAS DataBase Reference)
• NIST Chemistry Reference: Nonane,3,7-dimethyl-(17302-32-8)
• EPA Substance Registry System: Nonane,3,7-dimethyl-(17302-32-8)

Safety Data

• Hazardous Substances Data: 17302-32-8(Hazardous Substances Data)

Usage

Uses

3,7-Dimethylnonane is a research chemical of interest in the isomerization of n-dodecane

InChI:InChI=1/C11H24/c1-5-10(3)8-7-9-11(4)6-2/h10-11H,5-9H2,1-4H3

Upstream product

• 64-17-5 ethanol 

Relevant articles and documents

Synthesis of mesoporous ZSM-5 zeolites and catalytic cracking of ethanol and oleic acid into light olefins

Conversion of biomass-derived chemicals into light olefins is a promising method to maintain sustainable development of light olefin industry. In this study, three mesoporous ZSM-5 zeolites (MZSM-5-A, MZSM-5-B and MZSM-5-C) with major pore diameter about 4.8 nm, 16 nm and 22 nm were synthesized using a hydrothermal method by utilizing different templates. The catalytic activity of catalysts was studied by catalytic cracking of ethanol and oleic acid. The influence of reaction temperature on conversion and product selectivity was investigated. The characterization of ZSM-5 samples showed that the orders of the external surface area and mesopore volume were MZSM-5-C > MZSM-5-B > MZSM-5-A > conventional HZSM-5. In ethanol to light olefin reaction, MZSM-5-C achieved the highest light olefin yield (318.3 mL g?1) and ethylene selectivity (42.3%) at 400 °C. In oleic acid to light olefin reaction, MZSM-5-B achieved a complete conversion of oleic acid at 500 °C, and obtained the highest light olefin selectivity (38.1%) at 550 °C. The difference may be relevant to the size and chemical structure of feedstock molecular as well as the acidity of catalysts. Regardless of ethanol or oleic acid as feedstock, introduction of mesopore in zeolites significantly enhanced the light olefin yield and selectivity.