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The invention discloses an inferior ethyl bridge – wuwu zirconium indene, Louis compound and its preparation method and application in the oligomerization of propylene. The invention of the ethylenedioxy-based hydrosilane – wuwu zirconium, Louis composition can be through the ethylenedioxy – fluorenylmethylchloroformate ligand compound hydrosilane-first with alkyl alkali metal in the organic medium reaction, then adding ZrCl4 Or HfCl4 Obtained by the method. The invention of the linen – wuwu zirconiumethyl bridge indene, Louis compound is a high-efficient catalyst, under a comparatively mild condition, used for catalytic oligomerization of propylene, with high catalytic activity, and of the untreated alkyl the alumina alkane helps can be high under the catalysis of the selectively containing the allyl group of acrylic oligomer; at the same time can be controlled by polymerization reaction conditions for the realization of aligned polymer molecular weight control, and has very high industrial application value. Its structure has the following general formula: (by machine translation)

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

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Pomegranate marcs (PM) and grape marcs (GM) were pyrolysed in a fixed bed reactor to investigate the effects of pyrolysis temperature (400, 500 and 600 C), heating rate (300 and 700 C/min) and pyrolysis atmosphere (nitrogen (N2) and vacuum (25 kPa)) on product yields and properties. Maximum bio-oil yields were obtained at a pyrolysis temperature of 500 and 600 C for PM and GM, respectively, with a heating rate of 700 C/min under vacuum in a non-catalytic procedure. The results show that the pyrolysis of PM yields more bio-oil (43.7 wt%) than that of the GM (27.4 wt%). Therefore, an analysis of variance (ANOVA) was performed to investigate pyrolysis parameters on the yields of the bio-oil and gas products. To study the catalytic upgrading of the pyrolysis vapors, biomass samples were pyrolysed at 500 C using 10 wt% Aluminum-MCM-41 (Al-MCM-41) as a catalyst. The yields and the quality of the bio-oil and gas were influenced using the Al-MCM-41. Based on the GC?MS results, the composition of pyrolysis oil was significantly affected by the presence of a catalyst. The formation of oxygenated compounds and fatty acids was inhibited by the Al-MCM-41, while the formation of aromatic hydrocarbons was promoted. In addition, the HHV (higher heating value) of the bio-oils and the yield of syngas increased using a catalyst. It was observed that the PM and GM bio-oils could be used as a substitute for fossil fuels to generate heat and chemicals and that syngas yields could be enhanced using a catalyst.

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

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Upon treatment with a combination of HFIP and an organic sulfonic acid, alkenes behave as Br°nsted bases and protonate to give carbocations which can be trapped by electron-rich arenes. The reaction constitutes a Friedel-Crafts hydroarylation which proceeds with Markovnikov selectivity and is orthogonal to traditional metal-catalyzed processes. Intermolecular transfer hydrogenation and hydrothiolation under analogous conditions are also demonstrated.

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

Archives for Chemistry Experiments of 2-Methyl-1H-indene

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The 1,2-aryl migration and fragmentation reactions of 1-indanylmethyl (1), 2-tetralyl (2), 2-indanylmethyl (3), 1-tetralyl (4), 2-methyl-1-indanyl (5), and 1-methyl-2-indanyl (6) radicals were studied by flash vacuum pyrolysis of the tert-butyl perester precursors at 327-627 deg C and 10-2 torr.Radicals 1 and 2 are interconverted via 1,2 aryl migration which is readily reversible at all temperatures.This equilibrium is depleted by beta scission of 1 and recyclization to 4 and by beta scission of 2 followed by recyclization to 2 or 3 in modest yields.The reverse neophyle-like rearrangement of 2 to 1 occurs with a lower activation barrier than beta-scission of 1 to form a 2-(o-vinylphenyl)ethyl radical.Enthalpies, entropies, and free energies of reactions were calculated for the above reactions from group additivity parameters, and activation energies were estimated from values reported for simple alkyl radicals.It is shown that the beta scission of 4 and recyclization to 1 is important only at very high temperatures (>500 deg C) as a mechanism for the isomerization of tetralin and related hydroaromatic structures to alkylindans and that the reverse neophyl-like rearrangement of 2 to 1 is the favored pathway for isomerizations observed during dissolution of coal in hydroaromatic media at elevated temperatures.

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

More research is needed about 2-Methyl-1H-indene

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Cinnamyl alcohol (1) and two derivatives 2 and 3 have been incorporated in dehydrated HMor and HZSM-5 zeolites with the aim to characterize spectroscopically the corresponding carbocations generated within the solids. Product studies of the supernatant liquid phase combined with diffuse reflectance UV-vis and IR spectroscopy provide unequivocal evidence for the carbocations. Thus, cinnamyl alcohol (1) affords the 1,5-diphenylpentadienyl cation in HMor and HZSM-5 as a persistent species. In the case of HMor with larger pore dimensions the bulkier 1-(2?-cinnamyl)-3-phenylpropenyl cation was also spectroscopically detected. No persistent carbocation was observed when the alpha-methylcinnamyl alcohol (2) was incorporated in the acid zeolites, wherein a complete cyclization to 2-methylindene takes place. Finally, incorporation of 2-methyl-4-tolyl-3-buten-2-ol (3) in HZSM-5 allowed detection of the gem-dimethyl-subsituted p-methylcinnamyl cation, with a lifetime of hours. This cation is not persistent enough in HMor to be characterized. The present study illustrates how structurally related allylic substrates may give distinct carbenium ions whose persistence depends on the host-guest fit in the interior of the acid zeolites.

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

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This study aims to examine the effect of various advanced catalysts on tire waste pyrolysis oil using a small pilot-scale pyrolysis reactor with a capacity of 20 L. The catalytic pyrolysis with activated alumina catalyst produced maximum liquid oil (32 wt.%) followed by activated calcium hydroxide (26 wt.%), natural zeolite (22 wt.%) and synthetic zeolite (20 wt.%) catalysts, whereas liquid oil yield of 40% was obtained without catalyst. The gas chromatography-mass spectrometry results confirmed the pyrolysis liquid oil produced without catalyst consist of up to 93.3% of mixed aromatic compounds. The use of catalysts decreased the concentration of aromatic compounds in liquid oil down to 60.9% with activated calcium hydroxide, 71.0% with natural zeolite, 84.6% with activated alumina, except for synthetic zeolite producing 93.7% aromatic compounds. The Fourier-transform infrared spectroscopy data revealed that the mixture of aromatic and aliphatic hydrocarbon compounds were found in all liquid oil samples, which further confirmed the gas chromatography results. The characteristics of pyrolysis liquid oil had viscosity (1.9 cSt), density (0.9 g/cm3), pour point (?2 C) and flash point (27 C), similar to conventional diesel. The liquid oil had higher heating values, key feature of a fuel, in the range of 42?43.5 MJ/kg that is same to conventional diesel (42.7 MJ/kg). However, liquid oil requires post-treatments, including refining and blending with conventional diesel to be used as a transport fuel, source of energy and value-added chemicals.

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

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Despite the prevalence of the N-H aziridine motif in bioactive natural products and the clear advantages of this unprotected parent structure over N-protected derivatives as a synthetic building block, no practical methods have emerged for direct synthesis of this compound class from unfunctionalized olefins. Here, we present a mild, versatile method for the direct stereospecific conversion of structurally diverse mono-, di-, tri-, and tetrasubstituted olefins to N-H aziridines using O-(2,4-dinitrophenyl)hydroxylamine (DPH) via homogeneous rhodium catalysis with no external oxidants. This method is operationally simple (i.e., one-pot), scalable, and fast at ambient temperature, furnishing N-H aziridines in good-to-excellent yields. Likewise, N-alkyl aziridines are prepared from N-alkylated DPH derivatives. Quantum-mechanical calculations suggest a plausible Rh-nitrene pathway.

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

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Palladium-Catalyzed Cyclization of Benzyl Halides and Related Electrophiles Containing Alkenes and Alkynes as a Novel Route to Carbocycles

Treatment of benzyl halides and related electrophiles containing alkene and alkyne groups with a catalytic amount of Pd complexes, such as Pd(PPh3)4, provides the corresponding cyclization products containing five- through seven-membered rings often with retention of the alkene regiochemistry.

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

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Chemistry is traditionally divided into organic and inorganic chemistry. Quality Control of: 2-Methyl-1H-indene. The former is the study of compounds containing at least one carbon-hydrogen bonds.In a patent,Which mentioned a new discovery about 2177-47-1

Stoichiometric synthesis of Fe/CaxO catalysts from tailored layered double hydroxide precursors for syngas production and tar removal in biomass gasification

A series of bi-functional Fe/CaxO catalysts with different Ca/Fe molar ratios (2/1, 3/1, 4/1, 5/1) were prepared from tailored single-source CaxFe-LDHs precursors and applied to the thermo-chemical catalytic conversion of biomass. The results of catalyst characterization using XRD, SEM and CO2-TPD techniques indicate that the Fe load has a significantly influence on the composition, particle size, alkalinity and CO2 adsorption capacity of resulting Fe/CaxO materials. As catalysts, the selectivity of H2 was increased and the selectivity of CO was reduced with increasing Fe load. The highest gasification yield of 48.3 wt.%, H2 yield of 37.48 vol.% and H2/CO ratio of 1.36 were obtained at an optimized composition of Ca/Fe = 2/1, with the gasification efficiency as high as 76.4%. GC?MS analysis of the condensable tar indicated that the as-synthesized Fe/CaxO catalysts were capable for selective phenolics production from biomass gasification, with the maximum phenolics yield as high as 90.06%. Moreover, based on the results of structure characteristics and catalytic activities, a synergistic catalytic mechanism was proposed that the Ca2Fe2O5 and Fe3O4 formed by partial reduction of Ca2Fe2O5 during biomass gasification are the main active site for catalytic cracking of tar, which can be further promoted by the in-situ CO2 absorption of CaO.

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Reference:
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI

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Biocatalytic asymmetric dihydroxylation of conjugated mono-and poly-alkenes to yield enantiopure cyclic cis-diols

Dioxygenase-catalysed asymmetric dihydroxylation, of a series of conjugated monoalkenes and polyenes, was found to yield the corresponding monols and 1,2-dihydrodiols. The diol metabolites were obtained from monosubstituted, gem-disubstituted, cis-disubstituted, and trisubstituted alkene substrates, using whole cells of Pseudomonas putida strains containing toluene and naphthalene dioxygenases. Dioxygenase selection and alkene type were established as important factors, in the preference for dioxygenase-catalysed 1,2-dihydroxylation of conjugated alkene or arene groups, and monohydroxylation at benzylic or allylic centres. Competition from allylic hydroxylation of methyl groups was observed only when naphthalene dioxygenase was used as biocatalyst. The structures, enantiomeric excess values and absolute configurations of the bioproducts, were determined by a combination of stereochemical correlation, spectroscopy (NMR and CD) and X-ray diffraction methods. cis-1,2-Diol metabolites from arenes, cyclic alkenes and dienes were generally observed to be enantiopure (> 98% ee), while 1,2-diols from acyclic alkenes had lower enantiomeric excess values (< 88% ee). The enantiopure cis-diol metabolite of a gem-disubstituted fulvene was used as precursor in a new chemoenzymatic route to a novel C2-symmetrical ketone. I hope this article can help some friends in scientific research. I am very proud of our efforts over the past few months and hope to 2177-47-1, help many people in the next few years.Formula: C10H10

Reference£º
Metal catalyst and ligand design,
Ligand Template Strategies for Catalyst Encapsulation – NCBI