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1031246-31-7

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1031246-31-7 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 1031246-31-7 includes 10 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 7 digits, 1,0,3,1,2,4 and 6 respectively; the second part has 2 digits, 3 and 1 respectively.
Calculate Digit Verification of CAS Registry Number 1031246-31:
(9*1)+(8*0)+(7*3)+(6*1)+(5*2)+(4*4)+(3*6)+(2*3)+(1*1)=87
87 % 10 = 7
So 1031246-31-7 is a valid CAS Registry Number.

1031246-31-7Relevant articles and documents

Heterogeneously Catalyzed Selective Decarbonylation of Aldehydes by CeO2-Supported Highly Dispersed Non-Electron-Rich Ni(0) Nanospecies

Matsuyama, Takehiro,Yatabe, Takafumi,Yabe, Tomohiro,Yamaguchi, Kazuya

, p. 13745 - 13751 (2021/11/17)

Aldehyde decarbonylation has been extensively investigated, primarily using noble-metal catalysts; however, nonprecious-base-metal-catalyzed aldehyde decarbonylation has been hardly reported. We have established an efficient selective aldehyde decarbonylation reaction with a broad substrate scope and functional group tolerance utilizing a heterogeneous Ni(0) nanospecies catalyst supported on CeO2. The high catalytic performance is attributable to the highly dispersed and non-electron-rich Ni(0) nanospecies, which possibly suppress a side reaction producing esters and adsorbed CO-derived inhibition of the catalytic turnover, according to detailed catalyst characterization and kinetic evaluation.

Acceptorless Dehydrogenative Synthesis of Pyrimidines from Alcohols and Amidines Catalyzed by Supported Platinum Nanoparticles

Sultana Poly, Sharmin,Siddiki, S. M. A. Hakim,Touchy, Abeda S.,Ting, Kah Wei,Toyao, Takashi,Maeno, Zen,Kanda, Yasuharu,Shimizu, Ken-Ichi

, p. 11330 - 11341 (2019/01/03)

A one-pot, acceptorless dehydrogenative method, using a carbon-supported Pt catalyst (Pt/C) along with KOtBu, has been developed for the synthesis of 2,4,6-trisubstituted pyrimidines from secondary and primary alcohols, and amidines. The reaction takes place efficiently using a wide range of substrate scopes (32 examples with isolated yields up to 92%). The Pt/C catalyst that promotes this process is reusable and has a higher turnover number (TON) than those employed in previously reported methods. The results of mechanistic studies suggest that the process takes place through a pathway that begins with Pt-catalyzed acceptorless dehydrogenation of the alcohol substrate, which is followed by sequential condensation, cyclization, and dehydrogenation. Measurements of the turnover frequency combined with the results of density functional theory calculations on different metal surfaces suggest that the adsorption energy of H on the Pt surface is optimal for the acceptorless dehydrogenation process, which causes the higher catalytic activity of Pt over those of other metals.

Synthetic method of rosuvastatin calcium key intermediate

-

, (2016/10/10)

The invention discloses a synthetic method of a rosuvastatin calcium key intermediate. The synthetic method particularly comprises the following steps: carrying out a condensation reaction between fluoroacetophenone and ethyl isobutyrate under the condition of using sodium as alkali by using isopropyl alcohol as a solvent to prepare 1-(4-fluorophenyl)-4-methyl amyl-1,3-diketone; then carrying out a ring closing reaction between the 1-(4-fluorophenyl)-4-methyl amyl-1,3-diketone and methylguanidine hydrochloride by using isopropanol as a solvent to obtain 4-(4-fluorophenyl)-6-isopropyl-N-methyl pyrimidine-2-amine; carrying out a substitution reaction between the 4-(4-fluorophenyl)-6-isopropyl-N-methyl pyrimidine-2-amine and methanesulfonyl chloride by using dichloromethane as a solvent to obtain 4-(4-fluorophenyl)-6-isopropyl-2-[(N-methyl-N-methanesulfonyl) amino] pyrimidine; finally, carrying out a Vilsmeier reaction between the 4-(4-fluorophenyl)-6-isopropyl-2-[(N-methyl-N-methanesulfonyl) amidogen] pyrimidine and DMF (Dimethyl Formamide) as well as phosphoryl chloride to obtain a target compound. The method disclosed by the invention has the advantages of being simple to operate, low in raw material price, high in availability of used raw materials, mild in reaction conditions, low in equipment requirements and production cost, easy for scale production and the like, and has significance industrial application value.

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