4032-93-3 Usage
Uses
Used in Fuel Industry:
2,3,6-Trimethylheptane is used as a fuel additive for its high octane rating, which enhances the performance and efficiency of gasoline engines. Its ability to improve combustion and reduce engine knocking makes it a valuable component in the production of high-octane gasoline.
Used in Chemical Production:
In the chemical industry, 2,3,6-Trimethylheptane serves as an intermediate in the synthesis of other chemicals. Its versatile chemical structure allows for its use in creating a variety of compounds, contributing to the development of new products and processes.
Used as a Solvent:
2,3,6-Trimethylheptane is also utilized as a solvent in various applications due to its ability to dissolve a wide range of substances. Its solvent properties make it suitable for use in industrial processes where the dissolution of certain materials is required.
Check Digit Verification of cas no
The CAS Registry Mumber 4032-93-3 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 4,0,3 and 2 respectively; the second part has 2 digits, 9 and 3 respectively.
Calculate Digit Verification of CAS Registry Number 4032-93:
(6*4)+(5*0)+(4*3)+(3*2)+(2*9)+(1*3)=63
63 % 10 = 3
So 4032-93-3 is a valid CAS Registry Number.
InChI:InChI=1/C10H22/c1-8(2)6-7-10(5)9(3)4/h8-10H,6-7H2,1-5H3
4032-93-3Relevant academic research and scientific papers
Paraffin alkylation
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Page/Page column 7, (2008/06/13)
A liquid acid process is disclosed in which a hydrocarbon component containing an olefin, an olefin precursor or mixture and an isoalkane and a liquid acid catalyst is fed to a downflow reaction zone containing a disperser, under conditions to induce pulse flow at or near the outlet to react the isoalkane and olefin to produce a reaction product and feeding the reaction product to a vaporization zone containing a disperser under conditions to induce pulse flow at or near the outlet of the vaporization zone. A pressure drop across the disperser in the vaporization zone causes partial vaporization of the hydrocarbon which quench es the heat reaction and cooling the unvaporized portion of said reaction product, which is recovered and allowed to separate into an acid phase and hydrocarbon phase containing the alkylate. The acid catalyst and hydrocarbons may be fractally fed to the reaction zone.
