Co-reporter:Mengshuai Liu, Kunqi Gao, Lin Liang, Jianmin Sun, Li Sheng and Masahiko Arai
Catalysis Science & Technology 2016 vol. 6(Issue 16) pp:6406-6416
Publication Date(Web):02 Jun 2016
DOI:10.1039/C6CY00725B
The combination of a metal-modified SBA-15 catalyst with potassium iodide was developed as heterogeneous dual catalysts for chemical fixation of CO2 to cyclic carbonates. It was observed that the binary Zn-SBA-15/KI catalysts were the most efficient among various metal-modified SBA-15/KI catalysts and showed an excellent synergetic effect in promoting the reaction under mild conditions. Moreover, the effects of reaction parameters on cycloaddition of CO2 with propylene oxide (PO) to propylene carbonate (PC) were optimized. Under the optimal conditions determined, the Zn-SBA-15/KI catalytic system was also versatile in CO2 cycloaddition with other epoxides. Additionally, the mechanistic details for the fixation of CO2 into a cyclic carbonate catalyzed by SBA-15/KI and Zn-SBA-15/KI were also contrastively elucidated using the density functional theory (DFT) method. The DFT results suggested that the zinc-modified and unmodified catalysts showed different coupling modes of CO2, and the ring-opening reaction was the rate-determining step in the SBA-15/KI catalyzed cycloaddition reaction, but the zinc-modified SBA-15/KI catalysts could enhance the CO2 cycloaddition, as the formation of a stable complex was beneficial to CO2 trapping. As a result, the ring-closing reaction became the rate-determining step in the Zn-SBA-15/KI catalyzed cycloaddition reaction, which was a promising result to guide the catalyst design for CO2 conversion.
Co-reporter:Shin-ichiro Fujita, Sayaka Asano, Masahiko Arai
Journal of Molecular Catalysis A: Chemical 2016 Volume 423() pp:181-184
Publication Date(Web):November 2016
DOI:10.1016/j.molcata.2016.06.022
•Phenylacetylene can be reduced with hydrazine over N-doped carbon catalyst.•Coexisting nitrobenzene assists the reduction of phenylacetylene with hydrazine.•There are interactions between phenylacetylene and nitrobenzene on N-doped carbon.A nitrogen-doped activated carbon (AC) can catalyze the reduction of nitrobenzene with hydrazine but not phenylacetylene. When nitrobenzene coexists in the reaction mixture, however, phenylacetylene can also be reduced. Nitrobenzene is likely to assist the adsorption of phenylacetylene on the surface of AC catalyst through molecular interactions between the two substrates, allowing their simultaneous reduction to aniline and styrene. For these interactions to occur, nitrogen and/or oxygen species doped on the surface of AC are involved. The results demonstrate a new interesting catalytic function of nitrogen- and oxygen-doped metal-free carbon materials.The reduction of phenylacetylene by hydrazine over nitrogen- and oxygen-doped AC catalyst can be assisted by coexisting reducible nitrobenzene.
Co-reporter:Hiroyuki Watanabe, Sayaka Asano, Shin-ichiro Fujita, Hiroshi Yoshida, and Masahiko Arai
ACS Catalysis 2015 Volume 5(Issue 5) pp:2886
Publication Date(Web):March 23, 2015
DOI:10.1021/acscatal.5b00375
Various nitrogen-doped carbon materials were prepared via treatments of an activated carbon (AC) with ammonia and hydrogen peroxide, and their catalytic performance was tested for aerobic oxidation of several alcohols in ethanol. The amount and nature of doped nitrogen-species were examined by X-ray photoelectron spectroscopy to discuss the genesis of active species by nitrogen doping. The nitrogen-doped AC catalysts are active for the oxidation of such alcohols as benzyl alcohol, cinnamyl alcohol, and 5-(hydroxymethyl)-2-furaldehyde, and in some cases, they are even more selective to the oxidation of the hydroxyl group compared with conventional Pt/C and Ru/C catalysts, for which coupling products with the ethanol solvent are formed at low conversion levels. Graphite-type doped nitrogen species are significant for the formation of active sites on the surface of AC. The present results demonstrate the potential of nitrogen-doped AC materials as metal-free, carbon-based catalysts useable for organic synthetic reactions.Keywords: activated carbon; alcohol; metal-free carbon catalyst; nitrogen doping; oxidation
Co-reporter:Ashvini Bhosale, Hiroshi Yoshida, Shin-ichiro Fujita and Masahiko Arai
Green Chemistry 2015 vol. 17(Issue 2) pp:1299-1307
Publication Date(Web):28 Nov 2014
DOI:10.1039/C4GC02118E
The selective hydrogenation of benzyl cyanide (BC) to the primary amine of 2-phenylethylamine (PEA) was investigated with a Pd/Al2O3 catalyst in different multiphase reaction media including n-hexane, water, and/or CO2. In neat n-hexane, the hydrogenation of BC occurs at a large rate but no PEA was formed and the secondary amine of N,N-bis(2-phenylethyl)amine (BPEA) was produced as the main product. The pressurization of n-hexane with CO2 decreased the rate of hydrogenation and the main product was BPEA. In this n-hexane–CO2 medium, the catalyst lost its activity during the reaction. When a similar volume of water was added to n-hexane, the rate of hydrogenation did not change so much but a small amount of the primary amine was detected to form in addition to the main product of BPEA. In contrast to these reaction media, a high PEA selectivity of >90% was obtained and no catalyst deactivation occurred in an n-hexane–water–CO2 medium. The rate of hydrogenation was smaller than that in neat n-hexane but comparable to those in n-hexane–water and n-hexane–CO2 media. Those results show that synergistic effects appear on the selective hydrogenation of BC to PEA when both water and CO2 are included in the reaction medium. Possible roles and actions of water and CO2 have been discussed on the basis of the results of hydrogenation runs under different conditions and in situ ambient and high pressure Fourier transform infrared spectroscopy measurements that give insights into molecular interactions of CO2 with reacting species.
Co-reporter:Hiroshi Yoshida, Yuichi Onodera, Shin-ichiro Fujita, Hiroki Kawamori and Masahiko Arai
Green Chemistry 2015 vol. 17(Issue 3) pp:1877-1883
Publication Date(Web):22 Jan 2015
DOI:10.1039/C4GC02211D
Selective hydrogenation of acetophenone (AP) to 1-phenylethanol (PhE) was investigated over Rh/Al2O3 and Rh/C catalysts in 13 solvents including water and conventional organic solvents. Strong solvent effects on the overall rate of AP conversion were observed in different manners depending on the catalysts used. The conversion obtained is correlated with hydrogen-bond-donation (HBD) capability for Rh/C but with hydrogen-bond-acceptance (HBA) capacity for Rh/Al2O3. The solvent effects should result from interactions between the carbonyl group of AP and the solvent molecules through hydrogen bonding for Rh/C and from those between the solvent molecules and the catalyst surface for Rh/Al2O3 having HBD hydroxyl groups on its surface. Water is the most effective functional solvent in the selective hydrogenation of AP for C and Al2O3-supported Rh catalysts due to its high HBD capability (α) and low HBA capability (β), respectively. For the hydrogenation with Rh/Al2O3 in water, its large polarity/polarizability index (π*) may contribute to the high selectivity to PhE.
Co-reporter:H. Yoshida, N. Iwasa, H. Akamatsu, M. Arai
International Journal of Hydrogen Energy 2015 Volume 40(Issue 16) pp:5624-5627
Publication Date(Web):4 May 2015
DOI:10.1016/j.ijhydene.2015.02.111
Co-reporter:Hiroshi Yoshida;Naoya Igarashi;Shin-ichiro Fujita
Catalysis Letters 2015 Volume 145( Issue 2) pp:606-611
Publication Date(Web):2015 February
DOI:10.1007/s10562-014-1404-4
Supported Pt catalysts were prepared using several kinds of TiO2 supports different in the crystallite size in the range of 10–500 nm and their catalytic activity was tested for the liquid-phase hydrogenation of 3-nitrostyrene, nitrobenzene, and styrene. With Pt on smaller TiO2 crystallites (nanocrystals), the selectivity to vinylaniline was improved in the hydrogenation of 3-nitrostyrene (regioselective hydrogenation) and the selectivity to aniline was promoted in the hydrogenation of a mixture of nitrobenzene and styrene (chemoselective hydrogenation). The effects of TiO2 crystallite size were discussed on the basis of the results of turnover frequency and FTIR of CO adsorbed on dispersed Pt particles. Low coordinated and/or electron-rich Pt sites should be formed on the surface of nanocrystal TiO2 supports. Nanocrystal TiO2 support is an important factor for controlling and improving the catalytic performance of dispersed Pt particles.
Co-reporter:Dr. Shin-ichiro Fujita;Ayaka Katagiri;Hiroyuki Watanabe;Sayaka Asano;Dr. Hiroshi Yoshida ;Dr. Masahiko Arai
ChemCatChem 2015 Volume 7( Issue 18) pp:2965-2970
Publication Date(Web):
DOI:10.1002/cctc.201500337
Abstract
N-doped carbon (N carbon) materials were prepared from a commercial polyacrylonitrile (PAN) by calcination and subsequent ammoxidation and these were used for a model reaction of Knoevenagel condensation of benzaldehyde and ethyl cyanoacetate. The catalytic activity of the calcined PAN for the reaction was very low, but it was greatly enhanced by the ammoxidation and the enhancement depended on both the calcination and ammoxidation temperatures. X-ray photoelectron spectra indicated the presence of pyridine-type and pyrrole-/pyridone-type N species and the amount of the former N species was well correlated with the catalytic activity. It was suggested that the presence of pyridine-type N in the graphene structure is significant for the emergence of the catalytic activity. The most active N-carbon catalyst prepared in the present study was much more active than solid-based catalysts reported so far including N carbon derived from activated carbon, N-doped carbon nanotubes, and a few metal oxide based catalysts.
Co-reporter:Shin-ichiro Fujita, Masahiro Tanaka and Masahiko Arai
Catalysis Science & Technology 2014 vol. 4(Issue 6) pp:1563-1569
Publication Date(Web):06 Jan 2014
DOI:10.1039/C3CY00977G
A series of magnesium containing mesoporous smectites has been prepared with and without incorporation of alkali hydroxide (NaOH, KOH or LiOH) and employed for the reaction of CO2 with aminobenzonitrile to produce quinazoline-2,4(1H,3H)-dione. The effects of the quantity and kind of the incorporated alkali atoms on the catalytic properties of the smectites were investigated. Characterization of the smectites has shown that the incorporation of alkali atoms reduces their surface area and total pore volume but enhances the amount and strength of their basic sites. The product yield increases with the amount of alkali atoms incorporated. The incorporation of Li was less effective than that of Na and K for the enhancement of the yield. It has been suggested that weak and/or moderate base sites are responsible for the reaction. The active sites should be alkali hydroxide particles existing between the smectite layers for the alkali incorporated smectites, while for the un-incorporated smectite, the active sites should be the Mg atoms and/or the neighboring O atoms. The Na incorporated smectite was deactivated by repeated catalyst recycling, while such deactivation was not observed with the un-incorporated smectite. The reason for the deactivation was discussed in connection with the structures of the active sites and the actions of the reaction intermediate.
Co-reporter:Hiroshi Yoshida, Akitoshi Tomizawa, Hiroto Tachikawa, Shin-ichiro Fujita and Masahiko Arai
Physical Chemistry Chemical Physics 2014 vol. 16(Issue 35) pp:18955-18965
Publication Date(Web):23 Jul 2014
DOI:10.1039/C4CP02114B
The catalytic hydrogenation of 2,4-dinitroaniline using a 0.5 wt% Pt/TiO2 catalyst was investigated in a multiphase medium of tetrahydrofuran (THF) pressurized by CO2 at different pressures and at 323 K. When CO2 pressure was increased, the overall rate of hydrogenation simply decreased but the selectivity to the desired product of 4-nitro-1,2-phenylenediamine increased. The noticeable enhancement of the selectivity to 4-nitro-1,2-phenylenediamine can be explained by chemical reactivities of CO2 molecules. In situ high-pressure FTIR and molecular simulations demonstrate that the dissolved CO2 molecules may interact with amino groups of the substrate and weaken the intra-hydrogen bonding between the amino and 2-nitro groups, which results in the change in the relative reactivity of the two nitro groups, yielding the desired product in a higher selectivity. The change in the intra- and inter-molecular interactions between the substrate and CO2 molecules was theoretically examined by DFT calculations.
Co-reporter:Hiroshi Yoshida, Toshiaki Zama, Shin-ichiro Fujita, Joongjai Panpranot and Masahiko Arai
RSC Advances 2014 vol. 4(Issue 47) pp:24922-24928
Publication Date(Web):27 May 2014
DOI:10.1039/C4RA02220C
Liquid-phase hydrogenation of phenylacetylene was investigated with Pd and PdZn alloy catalysts in toluene compressed by CO2. The influence of alloying and dense phase CO2 on the rate of conversion and the product selectivity was examined. With either Pd or PdZn the partially hydrogenated product of styrene was produced in high selectivity but the selectivity to styrene obtained with the latter was larger than that with the former when compared at the same conversion level. After the initial substrate was fully consumed, the styrene was fully hydrogenated to ethylbenzene for both catalysts but more slowly with the PdZn alloy catalyst. The presence of a dense phase of CO2 (1.5 MPa) enhanced the rate of phenylacetylene hydrogenation and the selectivity to styrene for the Pd and PdZn catalysts. Possible reasons for the positive effects of alloying and dense phase CO2 on the partial hydrogenation of phenylacetylene to styrene are discussed.
Co-reporter:Shin-ichiro Fujita, Hiroyuki Watanabe, Ayaka Katagiri, Hiroshi Yoshida, Masahiko Arai
Journal of Molecular Catalysis A: Chemical 2014 Volume 393() pp:257-262
Publication Date(Web):1 November 2014
DOI:10.1016/j.molcata.2014.06.021
•Doping of nitrogen and oxygen is effective for the preparation of carbon catalysts.•The carbon catalysts prepared are active for transfer hydrogenation with hydrazine.•The catalysts are chemoselective for nitrobenzene, styrene, and 3-nitrostyrene.•The adsorption of nitro and vinyl groups depends on the catalyst surface properties.•The carbon materials prepared can serve as metal free hydrogenation catalysts.An activated carbon (AC) was treated by hydrogen peroxide and ammonia to dope oxygen and nitrogen on its surface. The surface-functionalized AC catalysts were used for the transfer reduction of nitrobenzene, styrene, and 3-nitrostyrene by hydrazine hydrate. The reduction of nitrobenzene and 3-nitrostyrene was promoted over the oxygen- and nitrogen-doped catalysts compared to the parent AC catalyst. Those were less active for the reduction of styrene but active for the reduction of vinyl group of 3-nitrostyrene. However, the nitrogen dopant suppressed the reduction of vinyl group of 3-vinylaniline. The functionalized AC catalysts are likely to facilitate the adsorption and activation of nitro group of the nitro substrates through interactions with polarized surface induced by the oxygen and nitrogen hetero dopants. This should make it possible to reduce the vinyl group of 3-nitrostyrene on the surface. The nitrogen dopant hindered the reduction of the vinyl group of 3-vinylaniline because the adsorption through its amino group should become difficult on the surface of basic nature induced by the nitrogen doping. The AC serves as an electrical conductor and its performance should be enhanced by the surface functionalization and this would contribute to the formation of reducing species such as diimide and proton from hydrazine on the surface. The present results show that oxygen- and/or nitrogen-doped, functionalized carbon materials could be promising as metal-free multi-task catalysts.
Co-reporter:Sumonrat Riyapan, Yuttanant Boonyongmaneerat, Okorn Mekasuwandumrong, Hiroshi Yoshida, Shin-Ichiro Fujita, Masahiko Arai, Joongjai Panpranot
Journal of Molecular Catalysis A: Chemical 2014 Volumes 383–384() pp:182-187
Publication Date(Web):March 2014
DOI:10.1016/j.molcata.2013.12.003
•Calcination of sol–gel TiO2 under H2 created more surface Ti3+ than in air.•Catalyst performance in selective acetylene hydrogenation improved using TiO2-H2.•Higher Pd dispersion and more isolated adsorption sites were obtained on TiO2-H2.•The catalysts were prepared by impregnation and electroless deposition techniques.•The effectiveness of TiO2-H2 was confirmed for both methods and Pd 0.5–1 wt.%.The anatase nanocrystalline TiO2 samples were synthesized by a sol–gel method with a thermal treatment under air and H2 atmospheres at 350 °C and employed as the supports for preparation of Pd/TiO2 catalysts by impregnation and electroless deposition methods. The surface Ti3+ defects on the TiO2 significantly increased when treated under H2, compared to air, with no changes in the average crystallite size, specific surface area, and pore structure. The CO chemisorption and IR of adsorbed CO results showed that the use of H2-treated TiO2 resulted in higher Pd dispersion and the formation of more isolated adsorption sites, hence improving the catalytic performance in terms of both acetylene conversion and ethylene selectivity.
Co-reporter:Ruixia Liu, Yu Wang, Haiyang Cheng, Yancun Yu, Fengyu Zhao, Masahiko Arai
Journal of Molecular Catalysis A: Chemical 2013 Volume 366() pp:315-320
Publication Date(Web):January 2013
DOI:10.1016/j.molcata.2012.10.010
The reduction of an α,β-unsaturated aldehyde, citral, was investigated over a 10 wt% Pd catalyst under transfer hydrogenation (TH) conditions in a closed system with microwave assistance. Surprisingly, it was found that hydrogen was produced quite fast under the microwave irradiation during the reaction, and the reduction of citral was proved to go mainly through consecutive pathways of hydrogen production – hydrogenation rather than those commonly considered for TH reactions. Similar reaction pathways were also observed with a homogeneous catalyst of [RuCl2(C6H6)]2 and other typical hydrogen donors like formate salts and isopropanol, which are usually used in the typical transfer hydrogenations.Graphical abstractUnusual reaction mechanisms are proved for selective reduction of an α,β-unsaturated aldehyde of citral under typical transfer hydrogenation (TH) reaction conditions. The reaction goes through consecutive pathways of hydrogen production – hydrogenation than those commonly considered for TH reactions.Highlights► Hydrogen is produced promptly from HCOONa and H2O over Pd/C under microwave assistant. ► Citral was hydrogenated by the hydrogen produced in situ efficiently. ► A consecutive hydrogen production and hydrogenation process was confirmed.
Co-reporter:Hiroshi Yoshida, Satomi Narisawa, Shin-ichiro Fujita, Liu Ruixia and Masahiko Arai
Physical Chemistry Chemical Physics 2012 vol. 14(Issue 14) pp:4724-4733
Publication Date(Web):15 Feb 2012
DOI:10.1039/C2CP23590K
The formation and adsorption of CO from CO2 and H2 at high pressures were studied over alumina-supported noble metal catalysts (Pt, Pd, Rh, Ru) by in situ FTIR measurements. To examine the effects of surface structure of supported metal particles and water vapor on the CO adsorption, FTIR spectra were collected at 323 K with untreated and heat (673 K) treated catalysts in the absence and presence of water (H2O, D2O). It was observed that the adsorption of CO occurred on all the metal catalysts at high pressures, some CO species still remained adsorbed under ambient conditions after the high pressure FTIR measurements, and the frequencies of the adsorbed CO species were lower either for the heat treated samples or in the presence of water vapor. It is assumed that the CO absorption bands on atomically smoother surfaces appear at lower frequencies and that water molecules are adsorbed more preferentially on atomically rough surfaces rather than CO species.
Co-reporter:Xiangchun Meng, Haiyang Cheng, Shin-ichiro Fujita, Yancun Yu, Fengyu Zhao and Masahiko Arai
Green Chemistry 2011 vol. 13(Issue 3) pp:570-572
Publication Date(Web):31 Jan 2011
DOI:10.1039/C0GC00246A
Chemoselective hydrogenation of water-insoluble aromatic nitro compounds can be achieved over Ni catalysts in a H2O–compressed CO2 system at 35–50 °C without using any environmentally harmful solvent. The effective CO2 pressure is much lower than the critical pressure of CO2. The hydrogenation of nitro group should be the rate-determining step.
Co-reporter:Hiroshi Yoshida ; Katsumasa Kato ; Jinyao Wang ; Xiangchun Meng ; Satomi Narisawa ; Shin-ichiro Fujita ; Zhijian Wu ; Fengyu Zhao
The Journal of Physical Chemistry C 2011 Volume 115(Issue 5) pp:2257-2267
Publication Date(Web):January 5, 2011
DOI:10.1021/jp1105339
Hydrogenation of nitrostyrene (NS) was studied with a Pt/TiO2 catalyst in CO2-dissolved ethanol and toluene phases at 323 K. The effects of CO2 pressure and organic solvents on the total conversion and the product distribution were examined. The conversion simply decreases with CO2 pressure in the both expanded solvents. The pressurization with CO2 varies the product selectivity in the nonpolar solvent but not in the polar solvent. The interactions among the substrate, solvent, and CO2 molecules were measured by in situ high-pressure FTIR methods in transmittance and attenuated total reflection modes. The reactivity of the nitro group of NS is lowered by interactions with CO2, which is responsible for the change in the product distribution. The local structures of an NS molecule in the expanded solvents are discussed from the results of FTIR and molecular dynamics simulations. The change in the product distribution is explained by the change of the local composition around the substrate molecule depending on CO2 pressure. The local composition is likely to change in the toluene but not in the ethanol, in accordance with the changes in the product selectivity in these two solvents. The substrate−CO2 interactions are important in toluene while those between the substrate and the solvent are predominant in ethanol even at high CO2 pressures.
Co-reporter:Naokatsu Kan-nari;Shuhei Okamura;Shin-ichiro Fujita;Jun-ichi Ozaki
Advanced Synthesis & Catalysis 2010 Volume 352( Issue 9) pp:1476-1484
Publication Date(Web):
DOI:10.1002/adsc.201000029
Abstract
Nitrogen-doped carbon materials were prepared by ammoxidation of commercial carbon sources (carbon black and activated carbon) and applied as base catalysts for Knoevenagel and transesterification reactions. It was shown that these carbon materials were active and the activities were different depending on the ammoxidation conditions (temperature and ammonia concentration in air) and carbon sources used. The bulk, textural, and surface properties of the nitrogen-doped carbon materials were examined by several methods to clarify possible factors determining their final catalytic activities. The activated carbon-derived catalysts were more active than the carbon black-derived ones. The surface area and porosity were not responsible for this difference between the two carbon sources but the difference in the reactivity with oxygen was important. The reactivity of carbon sources with oxygen should influence the doping of nitrogen onto their surfaces by ammoxidation with ammonia and air and the resulting activities as base catalysts. The catalytic activity increases with the amount of nitrogen doped and, therefore, the nitrogen doped should be responsible for the catalytic activities. In addition, the activities are maximal at a ratio of nitrogen to oxygen of around 1, suggesting the importance of cooperative functions of nitrogen and oxygen on the surface of carbons.
Co-reporter:Nobuhiro Iwasa, Toshiyuki Yamane, Masaaki Takei, Jun-ichi Ozaki, Masahiko Arai
International Journal of Hydrogen Energy 2010 Volume 35(Issue 1) pp:110-117
Publication Date(Web):January 2010
DOI:10.1016/j.ijhydene.2009.10.053
The activities of various metal catalysts were tested in steam reforming of acetic acid for the production of H2, using conventional metal oxides and transition metal-incorporated mesoporous smectite-like materials as supports. It has been found that Pt is superior to Ni, Co, and Fe among Al2O3 supported catalysts, Al2O3 is more effective than ZrO2 and SiO2 as support for Pt, Ni incorporated smectite (SM(Ni)) support is more effective than Fe and Co incorporated ones for Pt, and SM(Ni) is also active in the absence of Pt. The total activity for the conversion of acetic acid is in the order of Pt/Al2O3 > Pt/SM(Ni) > SM(Ni) but the ability of H2 production is comparable among these catalysts. These catalysts (and the other ones) were observed to lose their activities during the reforming reactions. The activity of Pt/Al2O3 decreased during the whole course of reaction up to 10 h. In contrast, the activity of SM(Ni) also decreased within 2 h but it showed a stable activity in the following stage of reaction. The initial activity of the used Pt/SM(Ni) and SM(Ni) was able to be almost completely restored by thermal treatment with H2 but less effectively for the used Pt/Al2O3. The catalyst deactivation was shown to occur by the formation and deposition of carbon materials on the catalysts (XRD, TEM, thermal analysis). The properties of carbon deposits formed on Pt/Al2O3 and SM(Ni) catalysts should be different and this may be responsible for the differences in the extent of deactivation and in the regeneration behavior between the two catalysts.
Co-reporter:Shin-ichiro Fujita, Takuya Yamada, Yoshinari Akiyama, Haiyang Cheng, Fengyu Zhao, Masahiko Arai
The Journal of Supercritical Fluids 2010 Volume 54(Issue 2) pp:190-201
Publication Date(Web):August 2010
DOI:10.1016/j.supflu.2010.05.008
Hydrogenation of phenol to cyclohexanone and cyclohexanol in/under compressed CO2 was examined using commercial Rh/C and Rh/Al2O3 catalysts to investigate the effects of CO2 pressurization on the total conversion and the product selectivity. Although the total rate of phenol hydrogenation with Rh/C was lowered by the presence of CO2, the selectivity to cyclohexanone was improved at high conversion levels >70%. On the other hand, the activity of Rh/Al2O3 was completely lost in an early stage of reaction. The features of these multiphase catalytic hydrogenation reactions using compressed CO2 were studied in detail by phase behavior and solubility measurements, in situ high-pressure FTIR for molecular interactions of CO2 with reacting species and formation/adsorption of CO on the catalysts, and simulation of reaction kinetics using a simple model. The CO2 pressurization was shown to suppress the hydrogenation of cyclohexanone to cyclohexanol, improving the selectivity to cyclohexanone. The formation and adsorption of CO were observed for the two catalysts at high CO2 pressures in the presence of H2, which was one of important factors retarding the rate of hydrogenation in the presence of CO2. It was further indicated that the adsorption of CO on Rh/Al2O3 was strong and caused the complete loss of its activity.
Co-reporter:Y. Akiyama, X. Meng, S. Fujita, Y.-C. Chen, N. Lu, H. Cheng, F. Zhao, M. Arai
The Journal of Supercritical Fluids 2009 Volume 51(Issue 2) pp:209-216
Publication Date(Web):December 2009
DOI:10.1016/j.supflu.2009.08.006
The Heck reaction of iodobenzene and methyl acrylate was investigated with CO2-philic Pd complex catalysts having fluorous ponytails and the organic base triethylamine (Et3N) in the presence of CO2 under solventless conditions at 80 °C. The catalysts are not soluble in the organic phase in the absence of CO2 and the reaction occurs in a solid–liquid biphasic system. When the organic liquid mixture is pressurized by CO2, CO2 is dissolved into the organic phase and this promotes the dissolution of the Pd complex catalysts. As a result, the Heck reaction occurs homogeneously in the organic phase, which enhances the rate of reaction. This positive effect of CO2 pressurization competes with the negative effect that the reacting species are diluted by an increasing amount of CO2 molecules dissolved. Thus, the maximum conversion appears at a CO2 pressure of around 4 MPa under the present reaction conditions. The catalysts are separated in the solid granules by depressurization and are recyclable without loss of activity after washing with n-hexane and/or water. When the washing is made with hexane alone, the catalytic activity tends to increase on the repeated Heck reactions, probably due to the accumulation of such a base adduct as Et3NHI on the catalysts. When the washing is further made with water, however, the base adduct is taken off from the catalysts and they show similar activity levels in the repeated runs. The potential of CO2 pressure tunable heterogeneous/homogeneous reaction system has also been investigated for Sonogashira reactions of iodobenzene and phenylacetylene under similar conditions.
Co-reporter:Masahiko Arai, Shin-ichiro Fujita, Masayuki Shirai
The Journal of Supercritical Fluids 2009 Volume 47(Issue 3) pp:351-356
Publication Date(Web):January 2009
DOI:10.1016/j.supflu.2008.08.012
This contribution reviews several catalytic reactions in multiphase systems including dense phase CO2 and other counter liquid or solid phases such as organic liquids, poly(ethylene glycol), water, ionic liquids, fluorous liquids, solid acid/bases powders, and supported metal particles. The features and potentials of dense phase CO2 for the multiphase catalytic reaction and separation will be presented.This contribution reviews several catalytic reactions in multiphase systems including dense phase CO2 and other counter liquid or solid phases such as organic liquids, poly(ethylene glycol), water, ionic liquids, fluorous liquids, solid acid/bases powders, and supported metal particles.
Co-reporter:Guozhi Fan;Shin-ichiro Fujita;Bing Zou;Masahiro Nishiura
Catalysis Letters 2009 Volume 133( Issue 3-4) pp:
Publication Date(Web):2009 December
DOI:10.1007/s10562-009-0189-3
Diphenyl carbonate (DPC) was synthesized from phenol and dense phase CO2 in the presence of CCl4 and K2CO3 using different catalysts of ZnCl2, ZnBr2, Lewis acid ionic liquids including 1-butyl-3-methylimidazolium chloride (BMIMCl) and bromide (BMIMBr). It was found that K2CO3 was not required, ZnCl2 and ZnBr2 were similar in the catalytic performance, and the use of BMIMCl and BMIMBr was not effective for the production of DPC. For the reactions with ZnCl2 in CCl4, the effects of such reaction variables as temperature, CO2 pressure, the amount of ZnCl2, and the volume of CCl4 were studied in detail. It was shown that the pressure was less influential while a larger amount of ZnCl2, a smaller volume of CCl4, and a low temperature of around 100°C were beneficial for the synthesis of DPC. On the basis of the results obtained, possible reaction mechanisms were discussed.
Co-reporter:A. P. Singh;N. Torita;S. Shylesh;N. Iwasa;M. Arai
Catalysis Letters 2009 Volume 132( Issue 3-4) pp:
Publication Date(Web):2009 October
DOI:10.1007/s10562-009-0121-x
Chromium-containing ethane-bridged hybrid periodic mesoporous organosilicas (Cr-PMO) were synthesized using 1,2-bis(triethoxysilyl)ethane (BTEE) and tetraethyl orthosilicate (TEOS) as silica sources and alkyltrimethyl ammonium salts as surfactants by two different synthesis routes. PXRD and N2 adsorption–desorption analysis shows that the original structure of the materials is maintained after chromium substitution while spectroscopic study proves the incorporation of chromium in the frame wall positions and show the existence of Cr2O3 species in the mixed silica source (BTEE-TEOS) synthesized chromium samples. The catalytic activity of the newly developed chromium samples was evaluated in the liquid phase oxidation of cyclohexane and ethylbenzene using air as an oxidant. Further, the Cr-PMO samples exhibited better cyclohexane conversion and cyclohexanone selectivity than the conventional Cr-MCM-41 and other metal-containing MCM-41 samples. The exceptional activity of the new chromium-containing molecular sieves is attributed to the hydrophobicity of the materials and to the complementary structural features that facilitates the accessibility of substrate to the active framework chromium sites.
Co-reporter:Rajendra Srivastava;Shin-Ichiro Fujita
Reaction Kinetics, Mechanisms and Catalysis 2009 Volume 96( Issue 1) pp:
Publication Date(Web):2009 February
DOI:10.1007/s11144-009-5422-y
Alkylation of aromatic compounds with various alkylating agents such as benzyl chloride, benzyl alcohol and isopropyl chloride were investigated using ZnCl2 based ionic liquid (ILs) Lewis acid catalysts. Multi-component Lewis acid catalysts of ZnCl2 and ionic liquids such as 1-butyl-3-methylimidazolium bromide, 1-butylpyridinium bromide, cholin chloride and tetrabutylammonium bromide were prepared, supported on silica gel, and compared for alkylation reactions with various alkylating agents. Among the IL-based catalysts, 1-butyl-3-methyl imidazolium-bromide-ZnCl2 and 1-butylpyridinium bromide-ZnCl2 are highly active.
Co-reporter:S. Fujita;T. Tanaka;Y. Akiyama;K. Asai;J. Hao;F. Zhao;M. Arai
Advanced Synthesis & Catalysis 2008 Volume 350( Issue 10) pp:1615-1625
Publication Date(Web):
DOI:10.1002/adsc.200800212
Abstract
Heck coupling reactions of methyl acrylate with various aryl bromides have been investigated using a Pd/TPP catalyst in toluene under pressurized CO2 conditions up to 13 MPa. Although CO2 is not a reactant, the pressurization of the reaction liquid phase with CO2 has positive and negative impacts on the rate of Heck coupling depending on the structures of the substrates examined. In the case of either 2-bromoacetophenone or 2-bromocinnamate, the conversion has a maximum at a CO2 pressure of about 3 MPa; for the former, it is much larger by a factor of 3 compared with that under ambient pressure. For 2-bromobenzene, in contrast, the conversion is minimized at a similar CO2 pressure, being half compared with that at ambient pressure. In the other substrates, including the other isomers of these three aryl bromides, the conversion simply decreases or does not change so much with the CO2 pressure. To examine the factors responsible for the effects of CO2 pressurization, the phase behavior and the molecular interactions with dense phase CO2 have also been studied by visual observation and in situ high pressure FT-IR spectroscopy. In addition, impact of CO2 pressurization was also studied for the Diels–Alder reactions of isoprene with a few dienophiles like methyl acrylate, methyl vinyl ketone, and acrolein in the same solvent, toluene, but a heterogeneous silica-alumina catalyst was used (the reaction system was liquid-solid biphasic). When the CO2 pressure is raised, the conversion monotonously decreases for the three dienophiles; however, the product selectivity changes with the pressure, in particular for acrolein. The FT-IR spectroscopic measurements suggest that its reactivity is altered by interactions with CO2 molecules under pressurized conditions.
Co-reporter:Rajendra Srivastava Dr.;Nobuhiro Iwasa Dr.;Shin-ichiro Fujita Dr.
Chemistry - A European Journal 2008 Volume 14( Issue 31) pp:9507-9511
Publication Date(Web):
DOI:10.1002/chem.200801113
Co-reporter:Y. Akiyama, S. Fujita, H. Senboku, C.M. Rayner, S.A. Brough, M. Arai
The Journal of Supercritical Fluids 2008 Volume 46(Issue 2) pp:197-205
Publication Date(Web):September 2008
DOI:10.1016/j.supflu.2008.03.009
The interactions between a variety of carbonyl compounds (ketones, esters, and amides) and dense phase CO2 have been investigated by in situ high pressure FTIR measurements. The gas and liquid phase spectra of these compounds have also been measured to provide accurate reference data, and these have been compared with those obtained in n-hexane and dense phase CO2 at a variety of pressures. The frequency of the carbonyl IR absorption is a measure of the strength of the carbonyl bond, and in the dense CO2 medium, is in between that observed in the gaseous and liquid phases. The substituent effect on the ν(CO) absorption bands is the same for the gas, liquid, and dense CO2 spectra and it is related to the electron donating nature of the substituents. When solutions of carbonyl compounds in n-hexane are diluted, the ν(CO) absorption bands are blue-shifted. In contrast, these bands in dense CO2 are red-shifted with increasing pressure (dilution by CO2). The red shift with increasing CO2 pressure is larger in amides > esters > ketones.
Co-reporter:Jianmin Sun, Shin-ichiro Fujita, Masahiko Arai
Journal of Organometallic Chemistry 2005 Volume 690(Issue 15) pp:3490-3497
Publication Date(Web):1 August 2005
DOI:10.1016/j.jorganchem.2005.02.011
This brief review presents the recent development in the synthesis of cyclic carbonate from carbon dioxide (CO2) using ionic liquids as catalyst and/or reaction medium. The synthesis of cyclic carbonate includes three aspects: catalytic reaction of CO2 and epoxide, electrochemical reaction of CO2 and epoxide, and oxidative carboxylation of olefin. Some ionic liquids are suitable catalysts and/or solvents to the CO2 fixation to produce cyclic carbonate. The activity of ionic liquid is greatly enhanced by the addition of Lewis acidic compounds of metal halides or metal complexes that have no or low activity by themselves. Using ionic liquids for the electrochemical synthesis of the cyclic carbonate can avoid harmful organic solvents, supporting electrolytes and catalysts, which are necessary for conventional electrochemical reaction systems. Although the ionic liquid is better for the oxidative carboxylation of olefin than the ordinary catalysts reported previously, this reaction system is at a preliminary stage. Using the ionic liquids, the synthesis process will become greener and simpler because of easy product separation and catalyst recycling and unnecessary use of volatile and harmful organic solvents.A short review is given on the synthesis of cyclic carbonates from CO2 using ionic liquids as catalyst and/or reaction medium: chemical and electrochemical cycloaddition of CO2 to epoxides and oxidative carboxylation of olefins. The reaction systems using ionic liquids will contribute to the development of green processes of CO2 fixation and production of valuable organic compounds.
Co-reporter:Jianmin Sun, Shin-ichiro Fujita, Fengyu Zhao and Masahiko Arai
Green Chemistry 2004 vol. 6(Issue 12) pp:613-616
Publication Date(Web):26 Oct 2004
DOI:10.1039/B413229G
The synthesis of styrene carbonate (SC) from styrene oxide (SO) and CO2 has been studied with various catalyst systems including metal halides and ionic liquids. The total conversion of SO and the selectivity for SC strongly depend on the catalyst systems used. The highest SC yield of 93% can be achieved at a low temperature of 80 °C for 1 h with a catalyst system of ZnBr2 and [C4-mim]Cl at a molar ratio of 1 ∶ 2. A CO2 pressure of 4 MPa is optimal but elevated pressures have no positive effects on this SC synthesis.
Co-reporter:Bhalchandra M. Bhanage, Shin-ichiro Fujita, Yutaka Ikushima and Masahiko Arai
Green Chemistry 2004 vol. 6(Issue 2) pp:78-80
Publication Date(Web):09 Dec 2003
DOI:10.1039/B310115K
Clean synthesis to cyclic urea and cyclic urethane compounds using direct reaction of urea with diamine, amino alcohol or amino phenol has been achieved at 150 °C without any catalyst.
Co-reporter:Fengyu Zhao, Shin-ichio Fujita, Jianmin Sun, Yutaka Ikushima and Masahiko Arai
Chemical Communications 2004 (Issue 20) pp:2326-2327
Publication Date(Web):07 Sep 2004
DOI:10.1039/B408434A
It has been shown that CO2-expanded cinnamaldehyde liquid phase is a unique and effective medium for cinnamaldehyde hydrogenation to cinnamyl alcohol, due to interactions between the CO group of the substrate and CO2 molecules and increased solubility of H2.
Co-reporter:Bhalchandra M. Bhanage, Shin-ichiro Fujita, Yutaka Ikushima and Masahiko Arai
Green Chemistry 2003 vol. 5(Issue 4) pp:429-432
Publication Date(Web):09 Jun 2003
DOI:10.1039/B304182D
Two-step synthesis of dimethyl carbonate (DMC) from urea has been investigated with various solid catalysts. The first step involves reaction of urea with ethylene glycol (EG) to form ethylene carbonate (EC) and the second step transesterification of EC formed with methanol to give DMC and EG. It has been found that ZnO is highly active and selective for the two steps, of which the former should be conducted under reduced pressure. At around ambient pressure, 2-oxazolidone and ethyleneurea are formed in the first step. Similar to EG, other glycols such as 1,2- and 1,3-propanediols can also be transformed to corresponding cyclic carbonates.
Co-reporter:Fengyu Zhao, Yutaka Ikushima and Masahiko Arai
Green Chemistry 2003 vol. 5(Issue 5) pp:656-658
Publication Date(Web):21 Aug 2003
DOI:10.1039/B306560J
Hydrogenation of 2-butyne-1,4-diol to butane-1,4-diol has been successfully conducted in supercritical carbon dioxide at 323 K with a high selectivity of 84% for butane-1,4-diol at 100% conversion. No catalysts are needed since the reaction is promoted by the stainless steel reactor wall.
Co-reporter:Bhalchandra M. Bhanage, Shin-ichiro Fujita, Yutaka Ikushima and Masahiko Arai
Green Chemistry 2003 vol. 5(Issue 3) pp:340-342
Publication Date(Web):09 May 2003
DOI:10.1039/B300778B
Clean synthesis to imidazolidone and oxazolidone compounds using direct reaction of carbon dioxide with diamine or amino alcohols can be achieved at 6 MPa CO2 and 150 °C without use of any catalyst.
Co-reporter:Bhalchandra M. Bhanage, Shin-ichiro Fujita, Yutaka Ikushima, Kazuo Torii and Masahiko Arai
Green Chemistry 2003 vol. 5(Issue 1) pp:71-75
Publication Date(Web):18 Nov 2002
DOI:10.1039/B207750G
This paper reports the effect of various reaction variables on the activity and selectivity performance on a two-step synthesis of dimethyl carbonate (DMC) and glycol from propylene oxide, carbon dioxide and methanol using a heterogeneous Mg containing smectite catalyst. The first step, the reaction of propylene oxide with CO2 to form propylene carbonate, and the second step, the transesterification reaction of the cyclic carbonate such as ethylene carbonate with methanol to DMC and ethylene glycol, have been studied. The catalyst was found to be effective for one-pot synthesis of DMC, i.e. the sequential reaction of the epoxide, CO2 and methanol.
Co-reporter:Bhalchandra M Bhanage, Shin-ichiro Fujita, Masahiko Arai
Journal of Organometallic Chemistry 2003 Volume 687(Issue 2) pp:211-218
Publication Date(Web):7 December 2003
DOI:10.1016/j.jorganchem.2003.09.006
The application of multiphase catalytic systems for palladium catalyzed Heck reactions brings several benefits such as easy catalyst–product separation and catalyst recycling. The effective multiphase Heck systems can be prepared by using different types of catalyst phases, including biphasic catalysis and supported liquid phase catalysts, and a new generation solvent of supercritical carbon dioxide.Homogeneous and multiphase organo– and metal–palladium catalysts have been applied for Heck coupling reaction and separation using different types of catalysts and solvents including supercritical carbon dioxide.
Co-reporter:Nobuhiro Iwasa, Masayoshi Yoshikawa and Masahiko Arai
Physical Chemistry Chemical Physics 2002 vol. 4(Issue 21) pp:5414-5420
Publication Date(Web):01 Oct 2002
DOI:10.1039/B206916B
Gas phase hydrogenation of acetonitrile has been studied with various Pd-based catalysts using several supports, ZrO2, CeO2, MgO, SiO2, Al2O3, ZnO, Ga2O3 and In2O3. The catalysts may be divided into two groups, one of which includes ZnO, Ga2O3, and In2O3-supported catalysts and another group includes the other catalysts. The catalysts of the former group are less active but selective to the formation of ethylamine (MEA) and diethylamine (DEA). In particular, MEA is preferentially produced with the Pd/ZnO catalyst. These catalytic features may be ascribed to the formation of such Pd alloys as PdZn, Ga5Pd, Ga2Pd5, and In0.52Pd0.48 as confirmed by X-ray diffraction. Compared with these Pd alloy catalysts, the other catalysts including metallic Pd only are more active but less selective to MEA and DEA, similar to Pd black. The activity of Pd alloy catalysts can be improved by preparing the alloys on the surface of CeO2 support while maintaining their higher selectivity to MEA and DEA.
Co-reporter:Shin-ichiro Fujita, Shinya Fujisawa, Bhalchandra M. Bhanage, Yutaka Ikushima and Masahiko Arai
New Journal of Chemistry 2002 vol. 26(Issue 10) pp:1479-1484
Publication Date(Web):16 Sep 2002
DOI:10.1039/B203657F
Rhodium-catalyzed hydroformylation of 1-hexene was investigated in compressed CO2 and organic solvents using different fluorinated phosphine compounds as ligands at a temperature of 333 K. The reaction runs were conducted under conditions where the reaction mixtures were homogeneous in order to examine the activity of the rhodium complexes in different media. The effects of phosphine ligand, CO2 pressure, syngas (H2/CO) pressure and solvent on the hydroformylation activity were studied, along with FTIR examination of reaction mixtures. Such phosphine compounds as diphenyl(pentafluorophenyl)phosphine (II), bis(pentafluorophenyl)phenylphosphine (III), and tris(p-trifluoromethylphenyl)phosphine (VI) are effective ligands in scCO2. Compound II is better since with it the undesirable isomerization side reaction is avoided. The n/iso ratio (heptanal/2-methylhexanal) does not change so much with the phosphine ligand used. It is interesting that the aldehyde yield goes through a minimum at about 9 MPa with increasing CO2 pressure, and it tends to increase with an increase in the syngas pressure. The catalytic activities in scCO2 are comparable with those in toluene and it is suggested that scCO2 has some positive effects in promoting the hydroformylation.
Co-reporter:Shin-ichiro Fujita, Bhalchandra M. Bhanage, Yutaka Ikushima and Masahiko Arai
Green Chemistry 2001 vol. 3(Issue 2) pp:87-91
Publication Date(Web):26 Mar 2001
DOI:10.1039/B100363L
The synthesis of dimethyl carbonate (DMC) from methanol and
CO2 was studied in the presence of methyl iodide and various
base catalysts. Among the catalysts used, potassium carbonate was found to
be most active. Dimethyl ether (DME) is formed as a byproduct. When the
reaction was carried out at various pressure of CO2, two maxima
in DMC formation were observed at 4.5 and 8 MPa, while DME formation
decreased monotonically with increasing the CO2 pressure. The
effects of the amounts of methyl iodide and potassium carbonate on the DMC
and DME formation were also investigated. Mechanistic studies suggest that
DMC and DME are produced in parallel pathways and methyl iodide is involved
in the formation of both DMC and DME. Other alcohols show less reactivity
than methanol.
Co-reporter:Masayuki Shirai, Tomonari Tanaka, Masahiko Arai
Journal of Molecular Catalysis A: Chemical 2001 Volume 168(1–2) pp:99-103
Publication Date(Web):1 March 2001
DOI:10.1016/S1381-1169(00)00473-8
Hydrogenation of an α, β-unsaturated aldehyde, cinnamaldehyde (CAL), was carried out with silica-supported platinum catalysts in ethanol under pressurized hydrogen atmosphere up to 12 MPa at 50°C. The initial rate of reaction (CAL consumption) was proportional to hydrogen pressure and independent of CAL concentration. Increasing hydrogen pressure decreased the selectivity of cinnamyl alcohol (COL) but increased that of hydrocinnamaldehyde (HCAL). The COL selectivity increased with CAL concentration. The effect of hydrogen pressure on the selectivity in ethanol is different from that observed previously in a solvent of supercritical carbon dioxide.
Co-reporter:Shin-ichiro Fujita, Yuki Yamanishi, Masahiko Arai
Journal of Catalysis (January 2013) Volume 297() pp:137-141
Publication Date(Web):1 January 2013
DOI:10.1016/j.jcat.2012.10.001
Zinc-containing solid catalysts (zinc oxide, smectite, hydrotalcite) and several inorganic zinc salts were used to produce glycerol carbonate from glycerol and urea under solvent-free conditions at 130 °C and at a reduced pressure of 3 kPa. The leaching of Zn species was observed to occur for the solid catalysts, and the carbonate yield was shown to be correlated with the amount of zinc species dissolved into the liquid phase with a single relationship in common for all the catalysts employed. The reaction was also indicated to continue in the liquid phase alone, after the solid catalysts were removed from the reaction mixtures by filtration. The results obtained reveal that the reaction takes place homogeneously in the liquid phase irrespective of the parent solid catalysts used. Possible structure of active Zn species was discussed from the results of reaction runs under different conditions and Fourier transform infrared spectroscopy measurements of the liquid phase after the reaction.Graphical abstractThe reaction proceeds homogeneously with active Zn species in the liquid phase derived from the parent solid catalysts.Download high-res image (41KB)Download full-size imageHighlights► Three zinc-based solid catalysts are active for the glycerol carbonate synthesis. ► Glycerol carbonate is formed homogeneously by zinc complex species in liquid phase. ► The active zinc complex is the same irrespective of the parent pre-catalysts.
Co-reporter:R. Srivastava, S. Fujita, M. Arai
Applied Clay Science (January 2009) Volume 43(Issue 1) pp:1-8
Publication Date(Web):January 2009
DOI:10.1016/j.clay.2008.06.015
Co-reporter:Shin-ichiro Fujita, Hiroki Kawamori, Daisuke Honda, Hiroshi Yoshida, Masahiko Arai
Applied Catalysis B: Environmental (February 2016) Volume 181() pp:818-824
Publication Date(Web):February 2016
DOI:10.1016/j.apcatb.2015.08.048
Co-reporter:Ashvini Bhosale, Hiroshi Yoshida, Shin-ichiro Fujita, Masahiko Arai
Journal of CO2 Utilization (December 2016) Volume 16() pp:371-374
Publication Date(Web):1 December 2016
DOI:10.1016/j.jcou.2016.09.006
•CO2H2O multiphase medium is useful for selective hydrogenation of nitriles.•The effectiveness of CO2H2O medium depends on nitrile substrates used.•Molecular interactions with CO2 decrease the reactivity of CN of nitriles.The effectiveness of a multiphase medium including CO2 and water was studied for the selective hydrogenation of various nitriles of 2-phenylethyl cyanide (PEC), cinnamonitrile, n-hexanenitrile (HN) and 4-cyanobiphenyl with a conventional Pd/Al2O3 catalyst. Such a multiphase reaction medium was observed to have different impacts changing from one nitrile to another and the selective production of primary amine was achieved with PEC and HN but not with the other nitriles. Possible reasons for the substrate-dependent effects of CO2 and water were discussed.The desired product of primary amines can selectively be produced in hydrogenation of nitriles using a multiphase reaction medium including both CO2 and H2O.Download high-res image (72KB)Download full-size image
Co-reporter:Xiangchun Meng, Haiyang Cheng, Yoshinari Akiyama, Yufen Hao, Weibin Qiao, Yancun Yu, Fengyu Zhao, Shin-ichiro Fujita, Masahiko Arai
Journal of Catalysis (15 May 2009) Volume 264(Issue 1) pp:1-10
Publication Date(Web):15 May 2009
DOI:10.1016/j.jcat.2009.03.008
The selective hydrogenation of nitrobenzene (NB) over Ni/γ-Al2O3 catalysts was investigated using different media of dense phase CO2, ethanol, and n-hexane. In dense phase CO2, the total rate of NB hydrogenation was larger than that in organic solvents under similar reaction conditions; the selectivity to the desired product, aniline, was almost 100% over the whole conversion range of 0–100%. The phase behavior of the reactant mixture in/under dense phase CO2 was examined at reaction conditions. In situ high-pressure Fourier transform infrared measurements were made to study the molecular interactions of CO2 with the following reactant and reaction intermediates: NB, nitrosobenzene (NSB), and N-phenylhydroxylamine (PHA). Dense phase CO2 strongly interacts with NB, NSB, and PHA, modifying the reactivity of each species and contributing to positive effects on the reaction rate and the selectivity to aniline. A possible reaction pathway for the hydrogenation of NB in/under dense phase CO2 over Ni/γ-Al2O3 is also proposed.The complete selective hydrogenation of nitrobenzene to aniline can be achieved over conventional supported Ni catalysts under mild conditions in the presence of dense phase CO2.Download high-res image (81KB)Download full-size image
Co-reporter:Hironori Inomata, Masahide Shimokawabe, Masahiko Arai
Applied Catalysis A: General (1 November 2007) Volume 332(Issue 1) pp:146-152
Publication Date(Web):1 November 2007
DOI:10.1016/j.apcata.2007.08.013
Co-reporter:Ruixia Liu, Yancun Yu, Kazuki Yoshida, Guiming Li, Haoxi Jiang, Minhua Zhang, Fengyu Zhao, Shin-ichiro Fujita, Masahiko Arai
Journal of Catalysis (1 January 2010) Volume 269(Issue 1) pp:191-200
Publication Date(Web):1 January 2010
DOI:10.1016/j.jcat.2009.11.007
The selective hydrogenation of citral was studied with various TiO2-supported monometallic and bimetallic Pd and Au catalysts and their physical mixtures in supercritical CO2 (scCO2). Significant synergistic effects appeared when active Pd species was chemically or physically mixed with less active Au species. The total rate of conversion was greatly enhanced and the selectivity to citronellal (CAL) was improved. The physical properties of those catalysts were characterized by TEM, HRTEM-EDS, XPS, and UV/Vis and their features of H2 desorption were examined by TPD. The physical and chemical characterization results were used to discuss the reasons for the unexpected synergistic effects observed. The same selective hydrogenation was also conducted in a conventional non-polar organic solvent of n-hexane to examine the roles of scCO2. The use of scCO2 was effective for accelerating the hydrogenation of citral and improving the selectivity to CAL.The synergistic effects between Pd and Au or TiO2 make the chemically and physically mixed Pd/TO2 and Au/TiO2 present unexpected high reaction rate and selectivity in citral hydrogenation in scCO2.Download high-res image (64KB)Download full-size image
Co-reporter:Xiangchun Meng, Haiyang Cheng, Shin-ichiro Fujita, Yufen Hao, Yanjiao Shang, Yancun Yu, Shuxia Cai, Fengyu Zhao, Masahiko Arai
Journal of Catalysis (1 January 2010) Volume 269(Issue 1) pp:131-139
Publication Date(Web):1 January 2010
DOI:10.1016/j.jcat.2009.10.024
The hydrogenation of chloronitrobenzene to chloroaniline was investigated over Ni/TiO2 at 35 °C in supercritical CO2 (scCO2), ethanol, and n-hexane. The reaction rate followed the order of scCO2 > n-hexane > ethanol. In scCO2, the selectivity to chloroaniline and to aniline over Ni/TiO2 were 97–99.5% and <1%, respectively, in the conversion range of 9–100%. The high chemoselectivity to chloroaniline cannot be achieved over Ni/TiO2 in ethanol and n-hexane. In situ high-pressure Fourier transform infrared measurements were made to study the molecular interactions of CO2 with the following reactant and reaction intermediates: chloronitrobenzene, chloronitrosobenzene, and N-chlorophenylhydroxylamine. The molecular interaction modifies the reactivity of each species and accordingly the reaction rate and the selectivity. The influence of Cl substituent on the interaction modes of CO2 with these reacting species is discussed. Possible reaction pathways for the hydrogenation of chloronitrobenzene in scCO2 over Ni/TiO2 are also proposed.The chemoselective hydrogenation of chloronitrobenzene to chloroaniline can be achieved at any conversion levels up to 100% over Ni/TiO2 in scCO2 at 35 °C.Download high-res image (52KB)Download full-size image
Co-reporter:Hiroshi Yoshida, Satomi Narisawa, Shin-ichiro Fujita, Liu Ruixia and Masahiko Arai
Physical Chemistry Chemical Physics 2012 - vol. 14(Issue 14) pp:NaN4733-4733
Publication Date(Web):2012/02/15
DOI:10.1039/C2CP23590K
The formation and adsorption of CO from CO2 and H2 at high pressures were studied over alumina-supported noble metal catalysts (Pt, Pd, Rh, Ru) by in situ FTIR measurements. To examine the effects of surface structure of supported metal particles and water vapor on the CO adsorption, FTIR spectra were collected at 323 K with untreated and heat (673 K) treated catalysts in the absence and presence of water (H2O, D2O). It was observed that the adsorption of CO occurred on all the metal catalysts at high pressures, some CO species still remained adsorbed under ambient conditions after the high pressure FTIR measurements, and the frequencies of the adsorbed CO species were lower either for the heat treated samples or in the presence of water vapor. It is assumed that the CO absorption bands on atomically smoother surfaces appear at lower frequencies and that water molecules are adsorbed more preferentially on atomically rough surfaces rather than CO species.
Co-reporter:Mengshuai Liu, Kunqi Gao, Lin Liang, Jianmin Sun, Li Sheng and Masahiko Arai
Catalysis Science & Technology (2011-Present) 2016 - vol. 6(Issue 16) pp:NaN6416-6416
Publication Date(Web):2016/06/02
DOI:10.1039/C6CY00725B
The combination of a metal-modified SBA-15 catalyst with potassium iodide was developed as heterogeneous dual catalysts for chemical fixation of CO2 to cyclic carbonates. It was observed that the binary Zn-SBA-15/KI catalysts were the most efficient among various metal-modified SBA-15/KI catalysts and showed an excellent synergetic effect in promoting the reaction under mild conditions. Moreover, the effects of reaction parameters on cycloaddition of CO2 with propylene oxide (PO) to propylene carbonate (PC) were optimized. Under the optimal conditions determined, the Zn-SBA-15/KI catalytic system was also versatile in CO2 cycloaddition with other epoxides. Additionally, the mechanistic details for the fixation of CO2 into a cyclic carbonate catalyzed by SBA-15/KI and Zn-SBA-15/KI were also contrastively elucidated using the density functional theory (DFT) method. The DFT results suggested that the zinc-modified and unmodified catalysts showed different coupling modes of CO2, and the ring-opening reaction was the rate-determining step in the SBA-15/KI catalyzed cycloaddition reaction, but the zinc-modified SBA-15/KI catalysts could enhance the CO2 cycloaddition, as the formation of a stable complex was beneficial to CO2 trapping. As a result, the ring-closing reaction became the rate-determining step in the Zn-SBA-15/KI catalyzed cycloaddition reaction, which was a promising result to guide the catalyst design for CO2 conversion.
Co-reporter:Hiroshi Yoshida, Akitoshi Tomizawa, Hiroto Tachikawa, Shin-ichiro Fujita and Masahiko Arai
Physical Chemistry Chemical Physics 2014 - vol. 16(Issue 35) pp:NaN18965-18965
Publication Date(Web):2014/07/23
DOI:10.1039/C4CP02114B
The catalytic hydrogenation of 2,4-dinitroaniline using a 0.5 wt% Pt/TiO2 catalyst was investigated in a multiphase medium of tetrahydrofuran (THF) pressurized by CO2 at different pressures and at 323 K. When CO2 pressure was increased, the overall rate of hydrogenation simply decreased but the selectivity to the desired product of 4-nitro-1,2-phenylenediamine increased. The noticeable enhancement of the selectivity to 4-nitro-1,2-phenylenediamine can be explained by chemical reactivities of CO2 molecules. In situ high-pressure FTIR and molecular simulations demonstrate that the dissolved CO2 molecules may interact with amino groups of the substrate and weaken the intra-hydrogen bonding between the amino and 2-nitro groups, which results in the change in the relative reactivity of the two nitro groups, yielding the desired product in a higher selectivity. The change in the intra- and inter-molecular interactions between the substrate and CO2 molecules was theoretically examined by DFT calculations.
Co-reporter:Shin-ichiro Fujita, Masahiro Tanaka and Masahiko Arai
Catalysis Science & Technology (2011-Present) 2014 - vol. 4(Issue 6) pp:NaN1569-1569
Publication Date(Web):2014/01/06
DOI:10.1039/C3CY00977G
A series of magnesium containing mesoporous smectites has been prepared with and without incorporation of alkali hydroxide (NaOH, KOH or LiOH) and employed for the reaction of CO2 with aminobenzonitrile to produce quinazoline-2,4(1H,3H)-dione. The effects of the quantity and kind of the incorporated alkali atoms on the catalytic properties of the smectites were investigated. Characterization of the smectites has shown that the incorporation of alkali atoms reduces their surface area and total pore volume but enhances the amount and strength of their basic sites. The product yield increases with the amount of alkali atoms incorporated. The incorporation of Li was less effective than that of Na and K for the enhancement of the yield. It has been suggested that weak and/or moderate base sites are responsible for the reaction. The active sites should be alkali hydroxide particles existing between the smectite layers for the alkali incorporated smectites, while for the un-incorporated smectite, the active sites should be the Mg atoms and/or the neighboring O atoms. The Na incorporated smectite was deactivated by repeated catalyst recycling, while such deactivation was not observed with the un-incorporated smectite. The reason for the deactivation was discussed in connection with the structures of the active sites and the actions of the reaction intermediate.