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CAS

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4032-93-3

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4032-93-3 Usage

General Description

2,3,6-Trimethylheptane is a chemical compound with the molecular formula C10H22. It is a hydrocarbon with seven carbon atoms and three methyl (CH3) groups attached to different carbon atoms. 2,3,6-Trimethylheptane is a colorless, flammable liquid with a strong, gasoline-like odor. It is commonly used as a fuel additive and in the production of high-octane gasoline. 2,3,6-Trimethylheptane has a high octane rating, making it valuable for improving the performance and efficiency of gasoline engines. Additionally, it is used as a solvent and an intermediate in the synthesis of other chemicals. Overall, 2,3,6-Trimethylheptane is an important industrial compound with applications in fuel and chemical production.

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

4032-93-3Downstream Products

4032-93-3Relevant articles and documents

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.

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