Paul Whittles et al- A Comparitive Study Between Microwave and Microfluidic Reactivity to Offer Up...
Transcript of Paul Whittles et al- A Comparitive Study Between Microwave and Microfluidic Reactivity to Offer Up...
-
8/3/2019 Paul Whittles et al- A Comparitive Study Between Microwave and Microfluidic Reactivity to Offer Up Microreactors a
1/1
H-Cube - Continuous-flow
Hydrogenation
A flow of substrate is pumped into the reactor where it is combined with hydrogen,produced by the electrolysis of water
The substrate/hydrogen mixture is heated and/or pressurized, up to 100C and100 bars (1450 psi) respectively, and then passed through a catalyst cartridge(CatCart)
The reaction takes place on the catalyst and the generated product elutescontinuously into a collection vial.
EXPERIMENTALS
Paul Whittles, Niesz Krisztian, Richard Jones, Laszlo rge, Ferenc Darvas
ThalesNano, Inc., Zahony u. 7., Budapest, Hungary H-1031 [email protected]
SummaryThe above reactions demonstrate that the continuous-flow technology, H-Cube for hydrogenation and X-Cube for different type of chemical reactions can offer a viablesolution to the microwave scale up problem. These microreactors open the door to the new generation of reactions and scale-up applications combining the elavetedtemperature and pressure with the continuous-flow of reactants resulting higher yield than it can be achieved in microwave reeactors.
References: (1) Leadbeater, N. E.; Smith, R. J.; Org. Lett.; 2006; 8(20); 4589 - 4591. (2) Varma, R. S.; Dahiya, R.; Tetrahedron; 54 (23); 1998; 6293 - 6298.(3) Firoz, M. M.; Khakshoor O; Ghaffarzadeh M; J. Chem. Res. Synop. 12;
2001; 525-527, (4) Ju, Y.; Kumar, D.; Varma, R. S; J. Org. Chem.; 2006; 71(17); 6697 - 6700. (5) Gupta, R,; Paul, S.; Nanda, P.; J. Indian Chem. Soc.; 2005; 82(6); 573 - 574.
A Comparitive Study Between Microwave and Microfluidic Reactivityo Offer Up Microreactors as a Scale Up Alternative to Microwaves
The hydrogenation reactor, H-Cube, is acompact continuous-flow reactor whichperforms high pressure hydrogenationsthrough the use of a microfluidic reactionline, in-situ hydrogen generation and acatalyst cartridge system (CatCart).
INTRODUCTIONThe pharmaceutical and chemical industry is continuously searching for technologies that make synthesis easier and faster in large scale.
Microflow technology has many advantages highly efficient heat exchange is one of the most important. The flow of material through the
reactors is only a matter of minutes, so results can be achieved in a very short space of time. At ThalesNano Nanotechnology Inc., we havedeveloped a series continuous-flow reactors for organic synthesis. Below is a description of the H-Cube, a hydrogenation reactor, and the
X-Cube reactor for different type of organic reactions. The microreactors reactions can also be scaled-up easily by running many smallscale reactions in parallel, and/or for a longer time. With the microwave technology scale up is extremely difficult and fraught withcomplications. Therefore microreactors can offer a viable solution to the microwave scale up problem. The following reactions will
demonstrate that different type of reactions can be performed with the similar results as can achieve using microwave irradiation.
X-Cube - Continuous-flow organic reactions
Many application can prove theadvantages of the microwave assistedorganic synthesis. Using microwaveenergy the results of the reactions aregenerally better than in case ofconventional heating which means thathigher yields can be achieved because ofthe direct, focused heating if the reactionmixture instead of the vessel. The scale-up procedure eighter in bach or inmicrowave reactors is complicated
NHN
NH2
O
+
1. 2.
Reaction
No.Mode Catalyst/Reagent Conditions
Yield /
%
1 Microwave 1. Montmorillonte K10 clay
2. NaBH4-clay
MW irradiation
65C, MW irradiation
89
1 Flow 1% Ir/C Solvent: EtOH
c = 0,01 M
T = 70 C;
p = 70 bars
Flow rate: 0,5 mL/min
93
2 Microwave Triethylammonium
formate, formic acid
MW irradiation81
2 Flow FibreCat Ir Solvent: EtOH
C = 0,01 M
T = 100 C
p = 70 barsFlow rate: 0,3 mL/perc
94
NH
NH2
O
+
N NH
Reaction No. ModeCatalyst/Rea
gentConditions Yield / %
Azid synthesis Microwave NaN3 Solvent: H2O
120C 95Azid synthesis Flow Azid on
AmberlyteSolvent: Acetonitrilp = 40 barsT = 110CFlow rate: 0,2 mL/minc = 0,1 M
96
N-formylation Microwave Basic
alumina, H2O
36-38C
81
N-formylation Flow Titanium Solvent: EtOH:-HCOOH= 5:1p = 50 barsT = 200CFlow rate: 0,2 mL/minc = 0,1 M
90
Suzuki coupling Microwave DBU,Pd(OAc)2
Solvent: EtOH, H2O150C
55
Suzuki coupling Flow FibreCat1007;
Base: TBAF;Solvent: IPA;c= 0,01 M
p = 10 barsT = 80 C;
Flow rate: 0,3 mL/min;
70
Br N3
NH
N
O
B
HO OH
+
Br
O
O
The X-Cube allows organic reactions to beperformed in a flow manner, combining the use oftemperatures and pressures up to 200C and 150bars (2176 psi) respectively and acatalyst/reagent cartridge system (CatCart). Acontinuous-flow of reaction mixture may be fed by
a dual pump system or injected into the reactordirectly. All reagents are heterogeneous includingmany polymer bound reagents and catalysts.
The two reaction zones can be heated independently and multistep synthesis canbe carried out in one flow.
The high pressure/high temperature capability means many reactions progress tocompletion in minutes
Regulated gas can be introduced into the instrument from an external gas source toperform industrially important triphasic reactions.
Scale-up: Present and Future Perspective
Easier scale-upwith
similar results
Step 1.
Easier scale-upwith
similar results
Step 2.
BACKGROUND
The following reactions demonstrate that
different reactions can be performed withthe similar results can be achieved usingmicrowave irradiation, but the scale-upusing continuous flow mode is easierand have 3 ways
increasing the time of reactions
increasing the flow rate
using the soon available H-CubeMidi, Scale-up Hydrogenation Reactor
Reaction 1. (Microwave mode) Reaction 1. (Flow mode)
Reaction 2.
FibreCat is a trademark of Reaxa Ltd,.