Synthetr Synthetron onTM · Flow chemistry offers significant advantages Current flow reactor...
Transcript of Synthetr Synthetron onTM · Flow chemistry offers significant advantages Current flow reactor...
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Synthetr
onTM
Flow Reactor Technology
SynthetronTM
©2012 KinetiChem, Inc. Irvine, CA Jeffrey C. Raber, Ph.D.
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Flow chemistry offers significant advantages
Current flow reactor technology does not meet all
possible reaction needs:
Precipitate and plugging concerns
Shortened diffusion path is not enough
Simple, rapid scale-up is most desired
Smaller plant footprint desirable
The Synthetron™ platform was conceived to over-come these limitations
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Formation of
thin flowing
films of
reagents
1. Line Contacting
The Synthetron incorporates two innovations
US Patents 7,125,527 & 7,534,404
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Forced Uniform
Molecular
Interdiffusion
2. FUMI
Disruption of molecular clusters enables more molecules to
be immediately available for reaction participation
Molecular clusters, groups of the same molecules together
in solution, slow down and impede potential reaction
rates
The Synthetron incorporates two innovations
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Molecular Clusters in Solutions
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Ideal flow reaction
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The Synthetron incorporates two innovations
Formation of
thin flowing
films of
reagents
1. Line Contacting
Forced Uniform
Molecular
Interdiffusion
2. FUMI
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Synthetron S3 Reactor
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Synthetron S3T1 Reactor
Easy to clean
Easy to assemble and inspect
Easy to re-machine the surfaces
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Broad material capabilities
Can mix and match materials
Flexibility of creating the right tool for the job
Options for making disks out of unique materials
PLASTICS METALS CERAMICS
PEEK® Hastelloy® SiC*
1 Watt/M - K 22 Watt/M - K 100 Watt/M - K
*not currently implemented
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Flexible and Scalable Technology Platform
Wide Range of Flow Rates are Possible
From 0.5 mL/min up to 400 mL/min on same device
Current Capabilities of Kilos-Per-Hour
Demonstrated with a 2.5” disk diameter
Scalability is based on increasing disk diameter
As disk diameter increases, reactive surface area
increases as a square function.
4 Kg/hr @ 2.5” disk diameter = 16 Kg/hr @ 5”!
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High Flow Rates = Production Capabilities
Broad Flow Rate Ranges Demonstrated
0.5 Kg/hr up to 8.0 Kg/hr in SAME DEVICE!
Tremendous Throughput
0.5 Kg/hr = 4Kg in 8 hour shift
8 Kg/hr = 64 Kg in 8 hour shift
KILO LAB IN A FUME HOOD!
Space and Time Savings
Energy Efficient
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High Flow Rates = New Options
Handling of precipitate formations
Particle Size Controls
Tremendous Throughput
Multiple Kg’s per hour possible with a reaction
volume of 0.2 mL
Enabling New Directions
New Applications
New Chemical Possibilities
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The Frequency Factor Impact
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Impacting a “SLOW” Reaction - ODS
Reactivity complementary to HDS – zero-levels not achieved
Oxidation occurs through peroxo-acid
Catalytic amounts of acid are required
Requires an aqueous oxidant to act on a substrate in the
organic phase
Translates into hours stirring at elevated temperatures!
How to improve and adapt this reaction to the Synthetron™
platform?
Otsuki, S. et al Energy & Fuels 2000, 14, 1232-1239
Kong, L. et al Catal. Lett. 2004, 92, 163-167
García-Gutiérrez, J. L. et al Appl. Catal A: General 2006, 305, 15-20
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Optimize Conditions with DOE
• Resolution IV experiment - Included 1 fold-over for a total of 29 trials
- 5 replicates of center point included
Parameter Low High
FR (mL/min) 0.3 2.0
gap size (µm) 25 150
RPM 740 6300
org:aq 1 10
% formic acid 2.5 5
temperature (˚C) 10 70
Shear Rate (sec-1)
16000 840000
Residence Time (sec)
1 53
• Bottom line: Discovered conditions that lead to ~60% removal
with a residence time of 80 seconds at only 10 C
• The same reaction with vigorous “traditional” stirring took
over 8 hours to reach the same extent conversion at 70 C
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Further Optimization Efforts
Higher flow rates were found to be effective
Residence Time is NOT an independent parameter
Recirculation = further ODS
Could use multiple reactors in-line as well
0
10
20
30
40
50
1 2 3
Pass Number
Percen
t d
eu
lfu
riz
ati
on
Seies 1
Series 2
Series 2 = smaller gap @
much higher shear rates
with lower oxidant ratios
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Reaction Examples
Traditional methods provided product in only 57%
yield and required difficult purification
How to improve and adapt this reaction to the
Synthetron™ platform?
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Reaction Examples
First Approach Second Approach
Feed 1 = Aniline/LHMDS Feed 1 = Nitroarene/Aniline
Feed 2 = Nitroarene Feed 2 = LHMDS
First Flow Rate = 60% First Flow Rate = 94%
Faster Flow Rate = 62% Faster Flow Rate = 96%
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Reaction Examples
Batch Synthetron
Add aniline to flask and cool to 0℃
Dropwise addition of LHMDS
Maintain 0℃, slowly add Nitroarene
Warm to r.t. over 12 hours
Equilibrate reactor at 25℃
Pump reagents as needed
Produce at 22.6 g/min or 1.36Kg/hr
57% Crude Yield 96% Crude Yield
Chromatography, Recrystallize recrystallization or direct use
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Reaction Examples: Organometallics
2.0M, r.t. Process Temp = 0°C 2.0M, r.t.
Batch Synthetron
30% Yield 98% Yield
Multiple side products 2 Kg/hr
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Reaction Examples: Organometallics
Batch CPC CLS-
microreactor Synthetron
76% Yield 90% Yield 98% Yield
50 g/hr 1.5 Kg/hr
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Reaction Examples: Gas-Liquid Efficiencies
Synthetron Process:
96.2% Purity @ 292 g/hr (unoptimized)
2.7% Biphenyl, 90% Isolated Yield
Only 1.75 equivalents of gas utilized!
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Reaction Examples: Precipitates
Complete Conversion of N-Boc-Phe
2880 g/h
Observed very small and fine particles
Others are studying particle formation
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Reaction Examples: Halogen/Lithium Exchange
Batch Synthetron
97% Yield 98% Yield
Variable results at scale 2.7 Kg/hr
Feed reagent concentrations of 2.0M, lithium products were quenched
with TMSCl and analyzed by GC.
Tet. Lett., 2010, 51, p. 4793.
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Reaction Examples: Halogen/Lithium Exchange
Batch Synthetron
85% Yield 92% Yield
Selectivity: 10 : 1 Selectivity: 104 : 1
Variable results at scale 3.5 Kg/hr
Feed reagent concentrations of 2.0M, lithium products were quenched
with TMSCl and analyzed by GC.
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Reaction Examples: Halogen/Lithium Exchange
Synthetron Process:
94% Conv., 2466 g/hr
400g produced in ~ 10 min reaction time.
A 50g batch process required ~40 min of
reagent addition time!
Tet. Lett., 2010, 51, p. 4793.
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Reaction Examples: Halogen/Lithium Exchange
Synthetron Process:
93% Conv., 1569 g/hr
Overall combined flow rate = 400 mL/min
Highly flexible synthetic platform for the
creation of diverse fine chemical building blocks
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Reaction Examples: Halogen/Lithium Exchange
Synthetron Process:
96% Conv., 2135 g/hr
Overall flow rate of 250 mL/min
Both solutions at 1.0M
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Comparisons
CPC CLS-microreactor Synthetron
100% Yield 97% Yield
177 g/hr 8602 g/hr
1.36 mol/hr† 44.8 mol/hr*
†Using Ethanol, www.cpc-
net.com/reactions/CPC01054.html
*Unoptimized Results, THP-Ether yield based
on crude 1H NMR
O
PhCH2OH+ +
O O Ph
Neat3 mol%HCl (conc.)
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CPC CLS-microreactor Synthetron
80% Yield 98% Yield
24 g/hr 2250 g/hr
0.237 mol/hr† 15.08 mol/hr*
†Using Propylamine, www.cpc-
net.com/reactions/CPC01017.html
*Unoptimized Results, Yield based on crude
1H NMR
Comparisons
NH2
O
O O+ N
H
O
Toluene
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Capabilities
OH
O
O O+ O
ONeat,
DMAP
(10 mol%) 96% 8.25 Kg/hr
98% 2.85 Kg/hr
ONH2
+NNeat
O
NC CN+
CN
CN
90% 5.24 Kg/hr
EtOH
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• Line contacting
• Forced Uniform
Molecular
Interdiffusion
1. High Throughput
• Gas/Liquid
reactions
• Precipitates
2. Flexible
• Take apart and clean
• Re-surface
• A forgiving reactor
3. Easy to use