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5435-64-3

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5435-64-3 Usage

Chemical Properties

3,5,5-Trimethylhexanal has an aldehydic odor.

Uses

3,5,5-Trimethylhexanal was used in preparation of gem-dithiols via reaction with hydrogen sulfide.

Preparation

From diisobutylene via the oxo reaction.

Flammability and Explosibility

Flammable

Check Digit Verification of cas no

The CAS Registry Mumber 5435-64-3 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 5,4,3 and 5 respectively; the second part has 2 digits, 6 and 4 respectively.
Calculate Digit Verification of CAS Registry Number 5435-64:
(6*5)+(5*4)+(4*3)+(3*5)+(2*6)+(1*4)=93
93 % 10 = 3
So 5435-64-3 is a valid CAS Registry Number.
InChI:InChI=1/C9H18O/c1-8(5-6-10)7-9(2,3)4/h6,8H,5,7H2,1-4H3

5435-64-3SDS

SAFETY DATA SHEETS

According to Globally Harmonized System of Classification and Labelling of Chemicals (GHS) - Sixth revised edition

Version: 1.0

Creation Date: Aug 12, 2017

Revision Date: Aug 12, 2017

1.Identification

1.1 GHS Product identifier

Product name 3,5,5-Trimethylhexanal

1.2 Other means of identification

Product number -
Other names 3,5,5-TRIMETHYLHEXANAL

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Food additives -> Flavoring Agents
Uses advised against no data available

1.4 Supplier's details

1.5 Emergency phone number

Emergency phone number -
Service hours Monday to Friday, 9am-5pm (Standard time zone: UTC/GMT +8 hours).

More Details:5435-64-3 SDS

5435-64-3Relevant articles and documents

Pd-Catalyzed Dehydrogenative Oxidation of Alcohols to Functionalized Molecules

Mori, Takamichi,Ishii, Chihiro,Kimura, Masanari

supporting information, p. 1709 - 1717 (2019/09/04)

A dehydrogenative oxidation reaction of primary alcohols to aldehydes catalyzed by a simple Pd/Xantphos catalytic system was developed under an argon or nitrogen atmosphere without oxidizing agents or hydrogen acceptors. The reaction product could be easily changed: under aerobic conditions, esters were obtained in aprotic solvents, whereas the corresponding carboxylic acids were produced in aqueous media. These oxidizing processes were applicable to the efficient synthesis of useful nitrogen-containing heterocyclic compounds such as indole, quinazoline, and benzimidazole via intramolecular versions of this reaction from amino alcohols.

Selective hydroformylation of olefins over the rhodium supported large porous metal-organic framework MIL-101

Van Vu, Toan,Kosslick, Hendrik,Schulz, Axel,Harloff, Joerg,Paetzold, Eckhard,Schneider, Mathias,Radnik, Joerg,Steinfeldt, Norbert,Fulda, Gerhard,Kragl, Udo

, p. 410 - 417 (2013/10/22)

Highly porous and crystalline metal-organic framework MIL-101 has been synthesized and used for the preparation of rhodium supported catalyst. Acetylacetonato(1,5-cyclooctadiene)rhodium(I) has been used as catalyst precursor. The material has been characterized by XRD, XPS, SAXS, FTIR, SEM, TEM, AAS, and nitrogen adsorption. The catalytic properties of Rh@MIL-101 have been investigated in the hydroformylation of olefins with different structure and chain length to the corresponding aldehydes. High conversion and selectivity to n-aldehydes have been achieved in the hydroformylation of n-alk-1-enes. The obtained results show that the rhodium species are highly dispersed and preferentially located at internal and less accessible sites at the supertetrahedral units.

PROCESS AND DEVICE FOR THE OXIDATION OF ORGANIC COMPOUNDS

-

Page/Page column 6, (2011/04/25)

The invention relates to a process for the oxidation of organic compounds by means of oxygen, in which, in a first step, the organic compound and at least part of the oxygen required for the oxidation are introduced into a first reaction zone which is operated isothermally and with backmixing and, in a second step, the reaction mixture from the first reaction zone is introduced into a second reaction zone which is operated adiabatically. The invention further relates to a reactor for carrying out the process, which comprises at least one isothermal reaction zone (3, 5) and an adiabatic reaction zone (7) which are arranged in a reactor shell (8), with each isothermal reaction zone (3, 5) being configured in the form of a jet loop reactor and the adiabatic reaction zone (7) being configured as a bubble column.

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