2016
DOI: 10.1039/c6cy00169f
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Towards rational design of core–shell catalytic nanoreactor with high performance catalytic hydrogenation of levulinic acid

Abstract: Core–shell catalytic nanoreactor was designed, exhibiting high catalytic activity for levulinic acid hydrogenation.

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Cited by 50 publications
(26 citation statements)
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“…Compared with the homogenous analogues, including complexes bis‐NHC‐Ir 4a , bis‐NHC‐Pd 5 , and NHC‐Ru 6 , POMP‐NHC‐Ir 1d , POMP‐NHC‐Pd 2 , and POMP‐NHC‐Ru 3 exhibited much higher catalytic activities under otherwise identical reaction conditions (17% vs 99%, 18% vs 82%, and 56% vs 81%, Figure a). It has to be pointed out, there are few reports on Pd‐catalyzed hydrogenation of LA to GVL under hydrogen atmosphere, and good result and enhanced catalytic activity could be achieved by POMP‐NHC‐Pd 2 even at 130 ppm catalyst loadings. Furthermore, other privileged and commercially available catalysts ( 10‐12 ) were also employed in this transformation, only trace to inferior yields were obtained under optimal reaction conditions (Figure a).…”
Section: Fabrication Of Pomp‐nhc‐m By Direct Knitting With Different mentioning
confidence: 99%
“…Compared with the homogenous analogues, including complexes bis‐NHC‐Ir 4a , bis‐NHC‐Pd 5 , and NHC‐Ru 6 , POMP‐NHC‐Ir 1d , POMP‐NHC‐Pd 2 , and POMP‐NHC‐Ru 3 exhibited much higher catalytic activities under otherwise identical reaction conditions (17% vs 99%, 18% vs 82%, and 56% vs 81%, Figure a). It has to be pointed out, there are few reports on Pd‐catalyzed hydrogenation of LA to GVL under hydrogen atmosphere, and good result and enhanced catalytic activity could be achieved by POMP‐NHC‐Pd 2 even at 130 ppm catalyst loadings. Furthermore, other privileged and commercially available catalysts ( 10‐12 ) were also employed in this transformation, only trace to inferior yields were obtained under optimal reaction conditions (Figure a).…”
Section: Fabrication Of Pomp‐nhc‐m By Direct Knitting With Different mentioning
confidence: 99%
“…However, the GVL selectivity decreased dramatically from 95 % to 64 % upon raising the temperature further to 150 °C (Table , entries 16–18). Coke deposition, caused by some unexpected adverse reactions such as over‐hydrogenation or hydrogenolysis, was responsible for this reduced GVL selectivity (Figure ) …”
Section: Catalytic Conditionsmentioning
confidence: 99%
“…The GVL selectivity of Pd@C decreased markedly from 95 % to 70 % upon raising the temperature from 100 °C to 120 °C, and a similar decrease in GVL selectivity (from 95 % to 64 %) under the action of Pd@SiO 2 was also observed upon increasing the temperature from 120 °C to 150 °C. These results were attributed to the coverage of active sites by coke deposits on the catalyst surface …”
Section: Stability Of Catalystsmentioning
confidence: 99%
“…However, the as‐prepared catalysts in this work showed dramatic differences in stability; the optimal Ru/ZSM‐5C (commercial support by wet impregnation) can still achieve 95 % conversion at the 10th cycle (conv. >95 %, yield >85 %), which is as stable as the latest core–shell silica‐based nanocatalyst (used for 10 runs) . However, Ru/ZSM‐5S (supercritical CO 2 ‐assisted homogeneous deposition in commercial support) deactivated sharply at the 4th cycle, with its conversion rate dropped to 25 %, and similar deactivation also took place in Ru/ZSM‐5M (mesoporous support by wet impregnation).…”
Section: Introductionmentioning
confidence: 98%