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Search for "continuous-flow" in Full Text gives 177 result(s) in Beilstein Journal of Organic Chemistry.

Efficient and selective chemical transformations under flow conditions: The combination of supported catalysts and supercritical fluids

  • M. Isabel Burguete,
  • Eduardo García-Verdugo and
  • Santiago V. Luis

Beilstein J. Org. Chem. 2011, 7, 1347–1359, doi:10.3762/bjoc.7.159

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  • on solid supports or in liquid phases and supercritical fluids (scFs), to develop selective and enantioselective chemical transformations under continuous and semi-continuous flow conditions. The results presented have been selected to highlight how the combined use of those two elements can
  • to a limited number of fields, a significant development in this area can be envisaged for the near future due to the clear advantages of these systems over the conventional ones. Keywords: biphasic systems; continuous flow processes; enantioselective catalysis; immobilized catalysts; polymer
  • economic efficiency and in short time frames [1]. The use of flow systems clearly offers a simple approach towards addressing these last few issues. The main advantages of continuous flow systems using conventional or neoteric solvents have been highlighted in different books and reviews [2][3][4][5][6][7
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Review
Published 30 Sep 2011

Koch–Haaf reaction of adamantanols in an acid-tolerant hastelloy-made microreactor

  • Takahide Fukuyama,
  • Yu Mukai and
  • Ilhyong Ryu

Beilstein J. Org. Chem. 2011, 7, 1288–1293, doi:10.3762/bjoc.7.149

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  • : continuous flow system; hastelloy; Koch–Haaf reaction; microreactor; Introduction The recent evolution of microreactor technology has allowed synthetic chemists to use this precisely sophisticated reaction apparatus in place of the well-established glassware batch flask [1][2][3][4][5][6][7][8][9][10
  • % total yield (2c:2c':2c'' = 23:53:24). The batch reaction resulted in an inferior yield with more of the rearranged products (83% yield, 2c:2c':2c'' = 19:62:19). All results are summarized in Table 1. Multigram scale synthesis of 2a from 1a was carried out in a continuous flow reaction. When the reaction
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Letter
Published 15 Sep 2011

The Eschenmoser coupling reaction under continuous-flow conditions

  • Sukhdeep Singh,
  • J. Michael Köhler,
  • Andreas Schober and
  • G. Alexander Groß

Beilstein J. Org. Chem. 2011, 7, 1164–1172, doi:10.3762/bjoc.7.135

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Published 25 Aug 2011

Triple-channel microreactor for biphasic gas–liquid reactions: Photosensitized oxygenations

  • Ram Awatar Maurya,
  • Chan Pil Park and
  • Dong-Pyo Kim

Beilstein J. Org. Chem. 2011, 7, 1158–1163, doi:10.3762/bjoc.7.134

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  • context triple-channel microreactors could be quite useful as they comprise all the required elements for photosensitized oxygenations, namely continuous-flow processing, large gas–liquid interfacial area, short molecular diffusion distances, and very high surface illumination homogeneity. The middle
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Published 24 Aug 2011

Scaling up of continuous-flow, microwave-assisted, organic reactions by varying the size of Pd-functionalized catalytic monoliths

  • Ping He,
  • Stephen J. Haswell,
  • Paul D. I. Fletcher,
  • Stephen M. Kelly and
  • Andrew Mansfield

Beilstein J. Org. Chem. 2011, 7, 1150–1157, doi:10.3762/bjoc.7.133

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  • , respectively. Under optimal reaction conditions the quantity of product could be increased from 31 mg per hour to 340 mg per hour simply by changing the volumetric capacity of the monolith. Keywords: continuous flow; microwave heating; monolith; scaling-up; Suzuki–Miyaura reaction; Introduction Interest in
  • ][5][6][7]. Much of this work has focused on continuous-flow microreactor methodology for laboratory based organic synthesis, and has featured the development of inorganic and organic polymer based functionalized monolithic reactors that can operate at elevated temperatures and under high pressure [8
  • [12][13]. To this end, the use of microwave heating in conjunction with microporous monolithic reactors has attracted some interest for small-scale synthesis under continuous-flow conditions [14][15][16]. One obvious problem, however, when using microwaves to heat solvents/reagents and surface
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Published 23 Aug 2011

Evaluation of a commercial packed bed flow hydrogenator for reaction screening, optimization, and synthesis

  • Marian C. Bryan,
  • David Wernick,
  • Christopher D. Hein,
  • James V. Petersen,
  • John W. Eschelbach and
  • Elizabeth M. Doherty

Beilstein J. Org. Chem. 2011, 7, 1141–1149, doi:10.3762/bjoc.7.132

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  • H-Cube® and the effect of that dispersion on the reaction outcome [15]. As a result of that study, we generated a predictive correlation between non-steady state and continuous flow scale-up conditions for simple reductions. In this report, using the reduction of styrene to ethylbenzene over 10% Pd
  • (Figure 7). It should be noted that Kappe observed a “Pd mirror” due to soluble Pd leaching from a CatCart® during a continuous flow Mizorki–Heck reaction [24]. In comparison, the fine black precipitate seen in our wash experiment is more consistent with solid Pd/C catalyst. The experiment was repeated
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Published 22 Aug 2011

Continuous flow photolysis of aryl azides: Preparation of 3H-azepinones

  • Farhan R. Bou-Hamdan,
  • François Lévesque,
  • Alexander G. O'Brien and
  • Peter H. Seeberger

Beilstein J. Org. Chem. 2011, 7, 1124–1129, doi:10.3762/bjoc.7.129

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  • Berlin, Germany 10.3762/bjoc.7.129 Abstract Photolysis of aryl azides to give nitrenes, and their subsequent rearrangement in the presence of water to give 3H-azepinones, is performed in continuous flow in a photoreactor constructed of fluorinated ethylene polymer (FEP) tubing. Fine tuning of the
  • reaction conditions using the flow reactor allowed minimization of secondary photochemical reactions. Keywords: azepinones; azides; continuous flow; nitrenes; photochemistry; Findings Although photochemical rearrangements are an important class of reactions for heterocycle synthesis [1][2], their use is
  • often hindered by technical difficulties, both in research laboratories and in industry, particularly when large quantities of material are required [3][4]. In response, there has been a recent growth in the application of continuous flow techniques [5][6][7] for the deployment of photochemical
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Published 17 Aug 2011

Continuous gas/liquid–liquid/liquid flow synthesis of 4-fluoropyrazole derivatives by selective direct fluorination

  • Jessica R. Breen,
  • Graham Sandford,
  • Dmitrii S. Yufit,
  • Judith A. K. Howard,
  • Jonathan Fray and
  • Bhairavi Patel

Beilstein J. Org. Chem. 2011, 7, 1048–1054, doi:10.3762/bjoc.7.120

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  • : continuous flow reactions; fluorine; fluoropyrazole; gas-liquid flow reactor; selective direct fluorination; Introduction Organic systems which bear fluorine atoms are used in an ever widening range of applications in the life sciences. Many commercially significant pharmaceutical and agrochemical products
  • manufacturing, we developed continuous flow microreactor systems that enabled gas/liquid fluorination reactions between fluorine and various substrates to occur in very efficient processes [19][20][21]. Fluoro-carbonyl derivatives can, in principle, be utilised as building blocks for the preparation of more
  • established that, in both batch and continuous flow processes, 1,3-dicarbonyl derivatives are not equally reactive towards fluorine gas [12] and that the ease of selective direct fluorination depends on the nature and proximity of other functional groups. Substrates that have a high initial equilibrium enol
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Published 02 Aug 2011

Chemistry in flow systems II

  • Andreas Kirschning

Beilstein J. Org. Chem. 2011, 7, 1046–1047, doi:10.3762/bjoc.7.119

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  • promising results, and the lasting effects will certainly become apparent in the years to come. I am very pleased to say that this series contains representative examples of fields in organic synthesis where continuous flow conditions have already made a significant impact. In particular I would like to
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Editorial
Published 02 Aug 2011

Continuous flow hydrogenation using polysilane-supported palladium/alumina hybrid catalysts

  • Hidekazu Oyamada,
  • Takeshi Naito and
  • Shū Kobayashi

Beilstein J. Org. Chem. 2011, 7, 735–739, doi:10.3762/bjoc.7.83

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  • Hidekazu Oyamada Takeshi Naito Shu Kobayashi Department of Chemistry, School of Science and Graduate School of Pharmaceutical Sciences, The University of Tokyo, Hongo, Bunkyo-ku, Tokyo 113-0033, Japan 10.3762/bjoc.7.83 Abstract Continuous flow systems for hydrogenation using polysilane-supported
  • polymer-incarcerated (PI) catalysts, which have high catalytic activity without causing metal leaching [1]. Heterogeneous catalytic hydrogenation in a batch system has recently been applied to continuous flow hydrogenation systems for high-throughput synthesis [2][3][4][5][6][7][8][9][10]. There are
  • of catalysts (or inability for their re-use), the need for vigorous stirring to achieve catalytic activity, and the possible necessity for longer reaction times, which may lead to undesirable side reactions or harsh reaction conditions. Continuous flow systems have the potential to overcome these
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Published 31 May 2011

Unusual behavior in the reactivity of 5-substituted-1H-tetrazoles in a resistively heated microreactor

  • Bernhard Gutmann,
  • Toma N. Glasnov,
  • Tahseen Razzaq,
  • Walter Goessler,
  • Dominique M. Roberge and
  • C. Oliver Kappe

Beilstein J. Org. Chem. 2011, 7, 503–517, doi:10.3762/bjoc.7.59

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  • Chemistry, Karl-Franzens-University Graz, Universitätsplatz 1, A-8010 Graz, Austria Continuous Flow/Microreactor Technologies, Lonza AG, CH-3930 Visp, Switzerland 10.3762/bjoc.7.59 Abstract The decomposition of 5-benzhydryl-1H-tetrazole in an N-methyl-2-pyrrolidone/acetic acid/water mixture was
  • explanations for these highly unusual rate accelerations are presented. In addition, general aspects of reactor degradation, corrosion and contamination effects of importance to continuous flow chemistry are discussed. Keywords: flow chemistry; heterogeneous catalysis; microreactors; palladium; process
  • continuous flow processes is becoming increasingly important. In the past few years our research group [19][20][21][22][23][24][25] has reported a number of successful case studies where initial reaction optimization for a variety of synthetic transformations was performed under batch microwave conditions
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Published 21 Apr 2011

Studies on Pd/NiFe2O4 catalyzed ligand-free Suzuki reaction in aqueous phase: synthesis of biaryls, terphenyls and polyaryls

  • Sanjay R. Borhade and
  • Suresh B. Waghmode

Beilstein J. Org. Chem. 2011, 7, 310–319, doi:10.3762/bjoc.7.41

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  • continuous flow of hydrogen gas [43]. The scanning electron microscope image shows that particle size of the catalyst is ~100 to 300 nm (Supporting Information File 1). The X-ray photoemission spectra confirms the formation of metallic Pd(0) particles, the binding energy values were 335.3 and 340.5 eV for Pd
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Published 15 Mar 2011

About the activity and selectivity of less well-known metathesis catalysts during ADMET polymerizations

  • Hatice Mutlu,
  • Lucas Montero de Espinosa,
  • Oĝuz Türünç and
  • Michael A. R. Meier

Beilstein J. Org. Chem. 2010, 6, 1149–1158, doi:10.3762/bjoc.6.131

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  • from Radleys. Stirring was continued at the selected temperature under a continuous flow of nitrogen for 5 h. After 5 h reaction time, the reaction mixture was dissolved in 1 mL of THF and polymerization halted by the addition of 1 mL of ethyl vinyl ether. The mixture was then stirred for 30 min at
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Published 03 Dec 2010

Self-assembly and semiconductivity of an oligothiophene supergelator

  • Pampa Pratihar,
  • Suhrit Ghosh,
  • Vladimir Stepanenko,
  • Sameer Patwardhan,
  • Ferdinand C. Grozema,
  • Laurens D. A. Siebbeles and
  • Frank Würthner

Beilstein J. Org. Chem. 2010, 6, 1070–1078, doi:10.3762/bjoc.6.122

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  • , and then cooled to 0 °C in an ice-bath. To this solution, a solution of 2, 2´-bithiophene in dry THF (68.0 mg in 5 mL) was added dropwise under continuous flow of argon. A white solid precipitate was formed. The reaction mixture was stirred at room temperature for 1 h and then immersed in an ice-bath
  • product was dissolved in 20 mL dry DMF, compound 9 added and the flask evacuated, purged three times with argon and ~15 mg of the Pd-catalyst added under continuous flow of argon. The reaction mixture was then heated at 80 °C for 8 h under an argon atmosphere. It was observed that an orange precipitate
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Published 16 Nov 2010

Kinetics and mechanism of vanadium catalysed asymmetric cyanohydrin synthesis in propylene carbonate

  • Michael North and
  • Marta Omedes-Pujol

Beilstein J. Org. Chem. 2010, 6, 1043–1055, doi:10.3762/bjoc.6.119

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  • achieved at atmospheric pressure and room temperature [74][75][76][77], or in a gas-phase continuous flow reactor [78], thus facilitating the use of waste carbon dioxide in this process [79]. In this paper we give full details of the use of catalyst 2 in propylene carbonate, and describe kinetic studies
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Published 03 Nov 2010

Continuous flow enantioselective arylation of aldehydes with ArZnEt using triarylboroxins as the ultimate source of aryl groups

  • Julien Rolland,
  • Xacobe C. Cambeiro,
  • Carles Rodríguez-Escrich and
  • Miquel A. Pericàs

Beilstein J. Org. Chem. 2009, 5, No. 56, doi:10.3762/bjoc.5.56

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  • : asymmetric synthesis; continuous flow; diarylmethanols; solid-supported catalyst; triarylboroxins; Introduction Diarylmethanols constitute the basic scaffold in several important drugs such as antihistamines and muscle relaxants (R)-neobenodine, (R)-orphenadrine or (S)-carbinoxamine (Figure 1) [1]. Despite
  • -pass, continuous flow highly enantioselective ethylation of aldehydes characterized by very short residence times (down to 2.8 min) [23]. According to these precedents, we considered that 2 could be a good candidate for a planned continuous enantioselective production of diarylmethanols. When a large
  • continuous flow enantioselective processes [52] are still scarce [22][53][54][55][56][57] in spite of the enormous potential of this methodology. Herein, we report the development of a continuous flow system for the preparation of enantioenriched diarylmethanols using triarylboroxins as the ultimate aryl
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Published 15 Oct 2009

Acid- mediated reactions under microfluidic conditions: A new strategy for practical synthesis of biofunctional natural products

  • Katsunori Tanaka and
  • Koichi Fukase

Beilstein J. Org. Chem. 2009, 5, No. 40, doi:10.3762/bjoc.5.40

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  • prominent biological activity in a “practical” and a “industrial” manner. Keywords: acid-mediated reaction; microreactor; natural products synthesis; oligosaccharide; pristane; Introduction A continuous flow microreactor, an innovative technology, has been used to realize efficient mixing and fast heat
  • problems, we used a continuous flow microreactor. An application of the microfluidic system to the glycosylation reaction was first reported by Seeberger and co-workers on α-mannosylation [18]. We also have established an efficient microfluidic glycosylation in combination with the affinity separation
  • the synthetic procedure, therefore, we used a continuous flow microreactor. Optimal conditions for reductive opening of 4,6-O-benzylidene acetals by a microfluidic system, similar to the α-sialylation and the β-mannosylation protocols, were examined using the glucose 4,6-O-benzylidene acetal 7 (Table
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Published 20 Aug 2009

Gold film- catalysed benzannulation by Microwave- Assisted, Continuous Flow Organic Synthesis (MACOS)

  • Gjergji Shore,
  • Michael Tsimerman and
  • Michael G. Organ

Beilstein J. Org. Chem. 2009, 5, No. 35, doi:10.3762/bjoc.5.35

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  • of gold, copper, silver, and gold-on-silver were prepared and evaluated for their catalytic activity in the microwave-assisted, continuous flow benzannulation of aryl, alkyl and silylalkynes with alkynylbenzaldehydes. Only the gold-on-silver films possessed both the high level of catalytic activity
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Published 21 Jul 2009

Radical carbonylations using a continuous microflow system

  • Takahide Fukuyama,
  • Md. Taifur Rahman,
  • Naoya Kamata and
  • Ilhyong Ryu

Beilstein J. Org. Chem. 2009, 5, No. 34, doi:10.3762/bjoc.5.34

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  • pressurized carbon monoxide gas. Good to excellent yields of carbonylated products were obtained via radical formylation, carbonylative cyclization and three-component coupling reactions, using tributyltin hydride or TTMSS as a radical mediator. Keywords: continuous flow system; microreactor; radical
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Published 13 Jul 2009

Controlling hazardous chemicals in microreactors: Synthesis with iodine azide

  • Johan C. Brandt and
  • Thomas Wirth

Beilstein J. Org. Chem. 2009, 5, No. 30, doi:10.3762/bjoc.5.30

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  • Johan C. Brandt Thomas Wirth Cardiff University, School of Chemistry, Park Place, Cardiff CF10 3AT, UK. 10.3762/bjoc.5.30 Abstract Aromatic aldehydes have been converted into the corresponding carbamoyl azides using iodine azide. These reactions have been performed safely under continuous flow
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Published 12 Jun 2009

From discovery to production: Scale- out of continuous flow meso reactors

  • Peter Styring and
  • Ana I. R. Parracho

Beilstein J. Org. Chem. 2009, 5, No. 29, doi:10.3762/bjoc.5.29

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  • Peter Styring Ana I. R. Parracho Department of Chemical & Process Engineering, The University of Sheffield, Mappin Street, Sheffield S1 3JD, United Kingdom 10.3762/bjoc.5.29 Abstract A continuous flow parallel reactor system has been developed to provide a rapid and seamless transition from the
  • a full analysis. By replication of the single reactor in parallel, the same chemistry can be achieved on a larger scale, on a small footprint and without the mass and heat transport limitations of reactor scale-out in batch. Keywords: catalysis; continuous flow; Kumada reaction; parallel; scale-out
  • Suzuki and Heck coupling reactions at elevated temperatures while the nickel catalyst is active in the Kumada coupling [11][12] reaction at room temperature in batch (Scheme 1) and continuous flow reactors. In the latter, the catalyst is packed into a 3 mm diameter glass reactor tube of length 25 mm and
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Published 09 Jun 2009

The development and evaluation of a continuous flow process for the lipase- mediated oxidation of alkenes

  • Charlotte Wiles,
  • Marcus J. Hammond and
  • Paul Watts

Beilstein J. Org. Chem. 2009, 5, No. 27, doi:10.3762/bjoc.5.27

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  • lipase B, Novozym® 435, in a preliminary investigation into the development of a continuous flow reactor capable of performing the chemo-enzymatic oxidation of alkenes in high yield and purity, utilising the commercially available oxidant hydrogen peroxide (100 volumes). Initial investigations focussed
  • on the lipase-mediated oxidation of 1-methylcyclohexene, with the optimised reaction conditions subsequently employed for the epoxidation of an array of aromatic and aliphatic alkenes in 97.6 to 99.5% yield and quantitative purity. Keywords: Candida antarctica lipase B; continuous flow; epoxidation
  • alternative to traditional techniques. With this in mind, we report herein the development and evaluation of continuous flow technique for the enzyme-mediated synthesis of epoxides, employing the immobilised Candida antarctica lipase B, Novozym® 435 (4). This was recently found to be the most efficient
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Published 02 Jun 2009

Continuous flow based catch and release protocol for the synthesis of α-ketoesters

  • Alessandro Palmieri,
  • Steven V. Ley,
  • Anastasios Polyzos,
  • Mark Ladlow and
  • Ian R. Baxendale

Beilstein J. Org. Chem. 2009, 5, No. 23, doi:10.3762/bjoc.5.23

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  • chemical syntheses [38][39][40][41][42][43][44][45][46][47][48][49][50][51][52][53][54]. In this work we report the use of the Uniqsis FlowSyn™ continuous flow reactor [55] (Figure 1) to effect a flow-based preparation of α-ketoesters. The key feature of this process is the application of a catch and
  • promote the base-catalysed dehydration, affording the nitroolefinic esters 1 (Scheme 2) [105]. As we have deliberately constructed this sequence for implementation in a continuous flow process, the intermediate nitroalkanols 5 were not isolated and the nitroolefinic esters were used without further
  • Uniqsis FlowSyn™ unit to achieve multi-step organic synthesis under continuous flow-chemistry conditions. This was accomplished by adapting the device to incorporate immobilised reagents packed in flow tubes, enabling clean transformations without recourse to conventional product work-up or purification
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Published 20 May 2009

Polyionic polymers – heterogeneous media for metal nanoparticles as catalyst in Suzuki–Miyaura and Heck–Mizoroki reactions under flow conditions

  • Klaas Mennecke and
  • Andreas Kirschning

Beilstein J. Org. Chem. 2009, 5, No. 21, doi:10.3762/bjoc.5.21

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  • heterogeneous supports for palladium(0) nanoparticles is described. These functionalized polymers were incorporated inside a flow reactor and employed in Suzuki–Miyaura and Heck cross couplings under continuous flow conditions. Keywords: Heck–Mizoroki reaction; heterogeneous catalysis; ion exchange resin
  • heterogenization of transition metals. A major hurdle for industrial applications of heterogenized homogeneous metal catalyst is associated with keeping metal leaching down to a minimum. Immobilization can be regarded as one enabling technique in organic chemistry [5][6] that in conjunction with continuous flow
  • transition metals on solid phases inside monolithic flow reactors [9][10][11][12][13][14][15][16][17][18] we describe the preparation of palladium nanoparticles loaded on polyionic polymers and their use under continuous flow conditions in various C-C-cross-coupling reactions [19][20][21][22]. Results and
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Published 08 May 2009

Chemistry in flow systems

  • Andreas Kirschning

Beilstein J. Org. Chem. 2009, 5, No. 15, doi:10.3762/bjoc.5.15

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  • focus on the development of flow devices for laboratory use and hence for industrial applications. An important field of research is the optimization and adaptation of known reactions and reaction sequences for use in flow systems. Advantageously, continuous-flow processes can be further improved by
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Published 29 Apr 2009
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