142-96-1Relevant articles and documents
Hudson,Mc Adoo
, p. 109,111, 113 (1979)
Etherification of n-butanol to di-n-butyl ether over Keggin-, wells-Dawson-, and preyssler-type heteropolyacid catalysts
Kim, Jeong Kwon,Choi, Jung Ho,Park, Dong Ryul,Song, In Kyu
, p. 8121 - 8126 (2013)
Etherification of n-butanol to di-n-butyl ether was carried out over various structural classes of heteropolyacid (HPA) catalysts, including Keggin- (H3PW12O40), Wells-Dawson- (H6P2W18O62), and Preyssler-type (H14[NaP5W30O110]) HPA catalysts. Successful formation of HPA catalysts was well confirmed by FT-IR, 31P NMR, and ICP-AES analyses. Acid properties of HPA catalysts were determined by NH3-TPD (temperature-programmed desorption) measurements. Acid strength of the catalysts increased in the order of H14 [NaP5W30O110] 6P2W18O62 3PW12O40. The catalytic performance of HPA catalysts was closely related to the acid strength of the catalysts. In the etherification of n-butanol to di-n-butyl ether over various structural classes of HPA catalysts, Conversion of n-butanol and yield for di-n-butyl ether increased with increasing acid strength of HPA catalysts. Among the catalysts tested, Keggin-type (H3PW12O40) HPA catalyst with the strongest acid strength showed the best catalytic performance. Acid strength of HPAs served as an important factor determining the catalytic performance in the etherification of n-butanol to di-n-butyl ether. Copyright
Etherification of n-butanol to di-n-butyl ether over HnXW 12O40 (XCo2+, B3+, Si4+, and P5+) Keggin heteropolyacid catalysts
Kim, Jeong Kwon,Choi, Jung Ho,Song, Ji Hwan,Yi, Jongheop,Song, In Kyu
, p. 5 - 8 (2012)
Etherification of n-butanol to di-n-butyl ether was carried out over heteroatom-substituted HnXW12O40 (XCo 2+, B3+, Si4+, and P5+) Keggin heteropolyacid (HPA) catalysts. Acid properties of HPA catalysts were determined by NH3-TPD measurements. Acid strength of HnXW 12O40 Keggin HPA catalysts increased in the order of H6CoW12O40 5BW 12O40 4SiW12O40 3PW12O40. Yield for di-n-butyl ether increased with increasing acid strength of the catalysts. Acid strength of HPAs served as an important factor determining the catalytic performance in the etherification of n-butanol to di-n-butyl ether.
Kobylinski,Pines
, p. 384 (1970)
AQUIVION perfluorosulfonic acid resin for butyl levulinate production from furfuryl alcohol
Bernal, Hilda Gómez,Oldani, Claudio,Funaioli, Tiziana,Raspolli Galletti, Anna Maria
, p. 14694 - 14700 (2019)
This study reports the sustainable production of butyl levulinate (BL) from furfuryl alcohol (FA), a highly abundant biomass derived platform obtained from C5 sugars in hemicellulose. FA upgrading is performed adopting a robust and easily recyclable commercial perfluorosulfonic acid resin, Aquivion P87S, used as cylinder shaped pellets. This approach avoids the use of corrosive and harmful mineral acids allowing a simple separation of the catalyst from the reaction mixture, reducing the cost of equipment materials and disposal or neutralization issues, also resulting in reduced solvent dehydration. Moreover, FA alcoholysis to BL involves butanol as a sustainable reaction medium, also readily obtained from biomass. The catalyst remains stable up to 6 recycles. Furthermore, the absence of heavy by-products and the stability of the catalyst allowed us to perform successive additions of the substrate to the reaction medium to increase the BL concentrations up to 0.66 M (13 wt%).
Polymer-supported catalysts for clean preparation of n-butanol
Jiang, Haibin,Lu, Shuliang,Zhang, Xiaohong,Peng, Hui,Dai, Wei,Qiao, Jinliang
, p. 2499 - 2503 (2014)
A new type of RANEY metal catalyst supported by polymer was developed for the clean preparation of n-butanol. Unlike traditional supported catalysts, the newly developed alkalescent polyamide 6 (PA6) supported RANEY nickel catalyst provided a 100.0% conversion of n-butyraldehyde without producing any detectable n-butyl ether, the main byproduct in industry. The significantly enhanced catalyst selectivity of the polymer-supported RANEY metal catalyst was attributed to the elimination of the acid-catalyzed side reaction associated with RANEY metals and traditional catalyst supports, such as Al2O3 and SiO2. By eliminating acid-catalyzed side reactions, therefore, green chemistry could be achieved through reducing resources and energy consumption in chemical reactions. Furthermore, the preparation and recycling of the polymer-supported catalysts are also much more eco-friendly than for traditional Al2O3-/SiO 2-supported catalysts. The methodology developed in this study to use alkalescent polymers as the catalyst support could be applied to the whole catalyst family, including a series of important RANEY metal catalysts (e.g., RANEY nickel, RANEY cobalt, RANEY copper) used routinely in the chemical industry.
The Guanidine-Promoted Direct Synthesis of Open-Chained Carbonates
Shang, Yuhan,Zheng, Mai,Zhang, Haibo,Zhou, Xiaohai
, p. 933 - 938 (2019)
In order to reduce CO2 accumulation in the atmosphere, chemical fixation methodologies were developed and proved to be promising. In general, CO2 was turned into cyclic carbonates by cycloaddition with epoxides. However, the cyclic carbonates need to be converted into open-chained carbonates by transesterification for industrial usage, which results in wasted energy and materials. Herein, we report a process catalyzed by tetramethylguanidine (TMG) to afford linear carbonates directly. This process is greener and shows potential for industrial applications.
Silver(I)-Catalyzed Reductive Cross-Coupling of Aldehydes to Structurally Diverse Cyclic and Acyclic Ethers
Dong, Guichao,Li, Chuang,Liang, Ting,Xu, Xin,Xu, Zhou
supporting information, p. 1817 - 1821 (2022/03/16)
A range of medium-sized cyclic ethers (5 to 11 membered) have been effectively synthesized through intramolecular reductive coupling of dialdehydes initiated by 50 ppm to 0.5% of AgNTf2 with hydrosilane at 25 °C. The catalytic system is also suitable for the coupling of two different monoaldehydes to provide unsymmetrical ethers. This protocol features broad functional group compatibility, high product diversity, high efficiency, and utility in the late-stage modification of complex biorelevant molecules.
Transition Metal-Free Direct Hydrogenation of Esters via a Frustrated Lewis Pair
Sapsford, Joshua S.,Csókás, Dániel,Turnell-Ritson, Roland C.,Parkin, Liam A.,Crawford, Andrew D.,Pápai, Imre,Ashley, Andrew E.
, p. 9143 - 9150 (2021/07/31)
"Frustrated Lewis pairs"(FLPs) continue to exhibit unique reactivity for the reduction of organic substrates, yet to date, the catalytic hydrogenation of an ester functionality has not been demonstrated. Here, we report that iPr3SnNTf2 (1-NTf2; Tf = SO2CF3) is a more potent Lewis acid than the previously studied iPr3SnOTf; in an FLP with 2,4,6-collidine/2,6-lutidine (col/lut), this translates to faster H2 activation and the catalytic hydrogenolysis of an ester bond by a main-group compound, furnishing alcohol and ether (minor) products. The reaction outcome is sensitive to the steric and electronic properties of the substrate; CF3CO2Et and simple formates (HCO2Me and HCO2Et) are catalytically reduced, whereas related esters CF3CO2nBu and CH3CO2Et show only stoichiometric reactivity. A computational case study on the hydrogenation of CF3CO2Et and CH3CO2Et reveals that both share a common mechanistic pathway; however, key differences in the energies of a Sn-acetal intermediate and transition states emerge, favoring CF3CO2Et reduction. The alcohol products reversibly inhibit 1-NTf2/lut via formation of resting-state species 1-OR/[1·(1-OR)]+[NTf2]- however, the extra energy required to regenerate 1-NTf2/lut exacerbates the unfavorable reduction energy profile for CH3CO2Et, ultimately preventing turnover. These findings will assist the design of future main-group catalysts for ester hydrogenation, with improved performance.
SATURATED HOMOETHER MANUFACTURING METHOD FROM UNSATURATED CARBONYL COMPOUND
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Paragraph 0045-0046, (2020/05/14)
PROBLEM TO BE SOLVED: To provide a method for manufacturing saturated homoether from an unsaturated carboxyl compound at good efficiency. SOLUTION: There is provided a manufacturing method of saturated homoether using an unsaturated carboxyl compound and hydrogen as raw materials, and a catalyst in which a metal is carried on an acidic catalyst carrier. The metal of the catalyst is for example palladium, and the carrier of the catalyst is alumina, silica, silica-alumina, or the like. The unsaturated carbonyl compound as the raw material is 2-butenal, 2-ethyl-2-hexenal, 2-ethyl-2-butenal, 2-hexenal, and manufactured saturated homoether is dibuthylether, bis(2-ethylhexyl)ether, bis(2-ethylbuty)ether, dihexylether, or the like. SELECTED DRAWING: None COPYRIGHT: (C)2020,JPO&INPIT