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Electronic Supplementary Information · 2017-11-09 · experiment was carried out according to the...

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S1 Electronic Supplementary Information Design and 3D Printing of a Stainless Steel Reactor for Continuous Difluoromethylations Using Fluoroform Bernhard Gutmann, a,b Manuel Köckinger, a Gabriel Glotz, a Tania Ciaglia, a Eyke Slama, b Matej Zadravec, b Stefan Pfanner, c Manuel C. Maier d Heidrun Gruber-Wölfler, b,d and C. Oliver Kappe* a,b a Institute of Chemistry, University of Graz, NAWI Graz, Heinrichstrasse 28, 8010 Graz, Austria. Email: [email protected] b Center for Continuous Flow Synthesis and Processing (CC FLOW) Research Center Pharmaceutical Engineering GmbH (RCPE), Inffeldgasse 13, Graz, Austria c Anton Paar, Anton-Paar-Straße 20, 8054 Graz, Austria d Institute of Process and Particle Engineering, Graz University of Technology, Inffeldgasse 13, 8010 Graz, Austria Electronic Supplementary Material (ESI) for Reaction Chemistry & Engineering. This journal is © The Royal Society of Chemistry 2017
Transcript

S1  

Electronic Supplementary Information

Design and 3D Printing of a Stainless Steel Reactor for Continuous

Difluoromethylations Using Fluoroform

Bernhard Gutmann,a,b Manuel Köckinger,a Gabriel Glotz,a Tania Ciaglia,a Eyke Slama,b Matej Zadravec,b Stefan Pfanner,c Manuel C. Maierd Heidrun Gruber-Wölfler,b,d

and C. Oliver Kappe*a,b

a Institute of Chemistry, University of Graz, NAWI Graz, Heinrichstrasse 28, 8010 Graz, Austria. Email: [email protected]

b Center for Continuous Flow Synthesis and Processing (CC FLOW) Research Center Pharmaceutical Engineering GmbH (RCPE), Inffeldgasse 13, Graz, Austria

c Anton Paar, Anton-Paar-Straße 20, 8054 Graz, Austria d Institute of Process and Particle Engineering, Graz University of Technology, Inffeldgasse

13, 8010 Graz, Austria

Electronic Supplementary Material (ESI) for Reaction Chemistry & Engineering.This journal is © The Royal Society of Chemistry 2017

 

Fig. S1 3D CAD drrawing for ttest print (fofor the print see Fig. S2) .

S2 

 

Fig. S2 Unmolt

Microscopeten particles

e pictures os are fused o

of the test pron the top su

rint using 31urface of th

16L stainleshe channel.

ss steel powwder. (C1 an

S3 

nd C2)

 

Fig. S3 3D CAD drrawing of thhe continuoous flow reaactor.

S4 

 

Fig. S4 Green: r

Fig. S5 laser-sin

3D CAD drreaction of

EOS DMLntern (acces

rawing of thfeed A and

LS System (fssed Octobe

he continuoB. Red: Re

for details ser 20, 2017)

ous flow reaeaction with

see: http://w)).

actor. Blue: h feed C.

www.shapete

Pre-cooling

ec.at/kompe

g of feed A

etenzen/met

S5 

and B.

tall-

 

Table S

AnalysParticle DispersParticle WeighteAnalysisResultsConcenUniformSpecificD[3,2] D[4,3]

Fig. S6

S1 Particle s

is

sion medium absorptioned deviations model s ntration mity c surface

Particle siz

size distribu

Stainle

m Dry disn 3.792 n 1.00%

univers 0.00460.270 18.69 m41.1 µm45.7 µm

ze distributio

ution charac

ss steel spersion

sal

%

m2/Kg m m

on character

cteristics of

Particle refRefractionLaser Shascattering Sensitivity Width Uits Dv10 Dv50 Dv90

eristics of th

the 316L st

fraction ind index dispeding model

he 316L stai

tainless stee

ex ersion med

nless steel p

el powder.

2.75

ium 1.000.89Mie exte 0.87Volu28.143.566.2

powder.

S6 

7 0 %

nted

5 umes µm µm µm

S7  

Fig. S7 Step experiment: To determine the residence time distribution (RTD) in the reactor, a step experiment was performed. A 10-3 M aqueous solution of Rose Bengal was pumped through the reactor with a flow rate of 1 mL/min. A fast switch from the Rose Bengal solution to water was carried out by means of a three-way valve, while maintaining a flow rate of 1 mL/min. The concentration of Rose Bengal at the outlet was measured in-line with an in-house developed photomete .

Fig. S8 Determination of the retention time: Dimensionless exit age distribution Eϴ vs. dimensionless time ϴ (derived from data points presented in Fig. S7). The evaluation of the experiment was carried out according to the dispersion model by Levenspiel [Levenspiel, O., 1999. Chemical Reaction Engineering. Wiley, New York]. Exit age distribution in dimensionless form of the experiment and a fit with a Gaussian normal distribution can be seen. With the experimental data a Bodenstein number for the open-open vessel condition was found to be 31.44 and mean residence time was calculated to be 154.4 s (reactor plus feed lines) for the step experiment. The Bodenstein number and the narrow exit age distribution suggest moderate axial dispersion throughout the reactor, without channeling or unexpected dead volumes.

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0

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0 50 100 150 200 250 300 350

[Signal]

[s]

‐1

‐0,5

0

0,5

1

1,5

2

2,5

3

3,5

0 0,5 1 1,5 2

E Θ[‐]

Θ [‐]

Gaussian normal distribution

Step Experiment

 

1H-NNMR of difluoroomethyldiphenyllactonitrile (CDCCl3)

S

S8 

 

13C--NMR of difluorromethyldiphenyylactonitrile (CDDCl3)

S

S9 

 

19F-NNMR of difluoroomethyldiphenyylactonitrile (CDDCl3)

S1

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