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Trans,trans,trans-2,10-Dimethyl-bicyclo<4.4.0>decan is a complex organic compound with the molecular formula C12H22. It is a bicyclic molecule, meaning it consists of two carbon rings fused together. The compound is characterized by three methyl groups (CH3) attached to the carbon atoms at positions 2 and 10, and the double bonds between the carbon atoms are in the trans configuration, which means they are on opposite sides of the molecule. This specific arrangement of the double bonds and methyl groups gives the compound its unique chemical properties and reactivity. It is an example of a strained hydrocarbon due to the trans,trans,trans configuration, which can affect its stability and potential applications in various chemical processes.

3604-13-5

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3604-13-5 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 3604-13-5 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 3,6,0 and 4 respectively; the second part has 2 digits, 1 and 3 respectively.
Calculate Digit Verification of CAS Registry Number 3604-13:
(6*3)+(5*6)+(4*0)+(3*4)+(2*1)+(1*3)=65
65 % 10 = 5
So 3604-13-5 is a valid CAS Registry Number.

3604-13-5Upstream product

3604-13-5Downstream Products

3604-13-5Relevant academic research and scientific papers

Synthesis of nickel-tungsten sulfide hydrodearomatization catalysts by the decomposition of oil-soluble precursors

Sizova,Kulikov,Onishchenko,Serdyukov,Maksimov

, p. 44 - 50 (2016/02/03)

Nickel-tungsten sulfide catalysts for the hydrogenation of aromatic hydrocarbons have been prepared by the in situ decomposition of an oil-soluble tungsten hexacarbonyl precursor in a hydrocarbon feedstock using oil-soluble nickel salt nickel(II) 2-ethylhexanoate as a source of nickel. The in situ synthesized Ni-W-S catalyst has been characterized by X-ray photoelectron spectroscopy. The activity of the resulting catalysts has been studied in the hydrogenation of bicyclic aromatic hydrocarbons and dibenzothiophene conversion in a batch reactor at a temperature of 350°C and a hydrogen pressure of 5.0 MPa. It has been shown that the optimum W: Ni molar ratio is 1: 2. Using the example of the hydrofining of feedstock with high sulfur and aromatics contents, it has been shown that the synthesized catalyst exhibits high activity in the hydrogenation of aromatic hydrocarbons.

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