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Creation of filaments for 3D printing via hot melt extrusion:
Evaluating different downstream technologies
T. Kipping1
, C. Makert2
, M. Richter3
, A. Geissler-Fichtner3
, N. Gottschalk4
, N. Di Gallo1
, A. G. Elia1
, A. N. Knuettel1
, F. Bauer1
© 2020 Merck KGaA, Darmstadt, Germany and/or its affiliates. All Rights Reserved.
MilliporeSigma, the Vibrant M, Parteck, extrex and SAFC are trademarks of Merck KGaA, Darmstadt, Germany or its ­
affiliates.
All other trademarks are the property of their respective owners. Detailed information on trademarks is available via publicly accessible resources.
Lit. No. MS_PS7016EN
11/2020
Objectives
The aim was to produce a Parteck®
MXP based filament with minor variation in
filament diameter and superior 3D printing capabilities as well as a significant
amount of API content. Different downstream technologies were assessed in
order to optimize the filament geometry and homo-geneity. A 3-axis laser
measurement device was used as an online in process control in order to assess
the homogeneity of the filament over the entire production (see Figure 1).
Figure 1: 
Schematic view of the 3-axis laser measurement ­
device used as an in-process control.
Purpose
For several years now 3D printing technology has been gaining increasing
attention within the pharmaceutical industry [1]. The number of publications
is rapidly increasing. One promising 3D printing technology is the fused
deposition modeling where a polymer strand is heated and extruded through
a small nozzle followed by a solidification on a build plate. The production
of the filaments itself is already described, but so far low focus is laid on
assessing the filament properties like varying filament diameter or break
tendencies. Our main goal was therefore to evaluate the production of
highly loaded (15% API load), highly homogeneous filaments which shall
provide excellent properties for 3D printing applications.
Y Z
X
Conveyor belt Laser measurement
Conveyor belt Laser measurement
Twin screw extruder
(Pharma 11)
Twin screw extruder
(Pharma 11)
Melt pump
(extrex®
PFS)
80 200 200 200 200 195 190
80 200 200 200 200 195 190 190
175
Feedrate: ~0.3 kg/h, rotation speed: 150 rpm
Feedrate: ~0.3 kg/h, rotation speed: 150 rpm
Target pressure:
~40 bar
Methods
Polyvinyl alcohol based Parteck®
MXP excipient from Merck KGaA, Darmstadt,
Germany was used as a polymer for the hot melt extrusion. The model drug
substance ketoconazole was purchased from LGM Pharma (Erlanger, KY 41018,
USA). in Figure 2. 3D printing was performed using an Ultimaker 3 (firmware
version: 4.0.1.20171023, UltFilaments for 3D printing with a target diameter of
1.75 mm were produced with an extrex®
PFS – 20GP Melt pump from Maag
Automatik GmbH (Groß-Ostheim, Germany) attached to a Pharma 11 twin-
screw extruder from Thermo Scientific (Karlsruhe, Germany). The diameter of
the filaments was measured with a 3-axis laser micrometer from Zumbach
(Orpund, Switzerland) ODAC Trio33. An overview of the filament manufacturing
process is presented imaker, Geldermalsen, Netherlands), which was modified
to enable printing of filament with a diameter of 1.75 mm. Nozzle diameter was
0.4 mm. Tablets were designed in Fusion 360 (Autodesk, Farnborough, United
Kingdom). Therefore, a cylinder shape was designed (diameter: 10 mm, height:
2.4 mm). Simplify 3D (version 4.0.1. Simplify 3D, Cincinnati, USA) was used for
slicing. Tablets were printed at 10 mm/s with an infill density of 100%. All
printing parameters were kept equal, except for printing temperatures. Parteck®
MXP was printed at 230 °C and Ketoconazole containing filaments at 210 °C.
Figure 2: 
Schematic view of the process setup evaluated for 3D printing.
Conclusions
Identifying the right down-stream equipment can be an important factor
for creating a homogenous filament. The use of a melt pump can improve
the consistency and ensures the safety of the process.
During production the pulsation of the melt flow could be drastically reduced.
Also a positive impact on the filament geometry can be assured.
For the evaluated samples both technologies pro-vided reliable material
properties for 3D printing. Variations in diameter were observed at an
extend where the geometry of the final dosage form was not negatively
affected.
It can be expected that at a larger production scale the benefits of a melt
pump are even more pronounced providing the basis for a further auto-
mation of the process.
Placebo – no melt pump
Placebo – with melt pump Ketoconazole – with melt pump
Ketoconazole – no melt pump
8
10
6
4
2
Diameter
[mm]
14
12
0
0.20
0.25
0.15
0.10
0.05
Mass
[g]
0.35
0.30
0.00
2.0
2.5
3.0
1.5
1.0
0.5
Height
[mm]
4.0
3.5
0.0
1.75
1.70
1.80
1.85
Diameter
[mm]
Time [Min]
1.50
10
0 1 2 3 4 5 6 7 8 9
X Axis
Y Axis
Z Axis
1.65
1.60
1.55
1.95
1.90
2.00
1.75
1.70
1.80
1.85
Diameter
[mm]
Time [Min]
1.50
10
0 1 2 3 4 5 6 7 8 9
X Axis
Y Axis
Z Axis
1.65
1.60
1.55
1.95
1.90
2.00
1.75
1.70
1.80
1.85
Diameter
[mm]
Time [Min]
1.50
10
0 1 2 3 4 5 6 7 8 9
X Axis
Y Axis
Z Axis
1.65
1.60
1.55
1.95
1.90
2.00
1.75
1.70
1.80
1.85
Diameter
[mm]
Time [Min]
1.50
10
0 1 2 3 4 5 6 7 8 9
X Axis
Y Axis
Z Axis
1.65
1.60
1.55
1.95
1.90
2.00
References
1.	
Jamróz W, Szafraniec J, Kurek M, Jachowicz R. 3D Printing in
Pharmaceutical and Medical Applications –Recent Achievements and Challenges.
Pharmaceutical research. 2018; 35 (9):176-
1
	MilliporeSigma: thomas.kipping@milliporesigma.com
2
	 Maag Automatik GmbH: christian.makert@maag.com
3
	 Thermo Fisher Scientific: margarethe.richter@thermofisher.com
4
	 EMD Serono: nadine.gottschalk@emdserono.com
Figure 3: 
Variation of diameter over time for Parteck®
MXP Placebo extrudates with integration of a melt
pump (left) and without the melt pump (right).
Figure 4: 
Variation of diameter over time for Parteck®
MXP extrudates loaded with 20% ketoconazole with
integration of a melt pump (left) and without the melt pump (right).
Figure 5: 
Characterization of 3D printed tablets: From left to right: Mass, diameter, height.
Results
The Integration of a melt pump reduces the pulsation of the melt and enhances
the precision of the targeted filament geometry for both placebo and drug
loaded filaments (Figure 3  4). It can be shown that the use of a melt pump
can increase the consistency and stability of the process. All printed samples
show a homogenous weight distribution of the tablets. In our first assessment
the geometry of the tablets was not affected by the different filament
manufacturing techniques (Figure 4). Independent from drug load or the
respective production method very reliable results concerning mass variation
and geometry could be achieved (Figure 5).
The Life Science business of Merck KGaA, Darmstadt, Germany operates as MilliporeSigma in the U.S. and Canada.
We provide information and advice to our customers on application technologies and
regulatory matters to the best of our knowledge and ability, but without obligation
or liability. ­
Existing laws and regulations are to be observed in all cases by our
customers. This also ­
applies in respect to any rights of third parties.
Our information and advice do not relieve our customers of their own
­
responsibility for checking the suitability of our products for the
envisaged purpose.

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Creation of filaments for 3D printing via hot melt extrusion - Evaluating different downstream technologies

  • 1. Creation of filaments for 3D printing via hot melt extrusion: Evaluating different downstream technologies T. Kipping1 , C. Makert2 , M. Richter3 , A. Geissler-Fichtner3 , N. Gottschalk4 , N. Di Gallo1 , A. G. Elia1 , A. N. Knuettel1 , F. Bauer1 © 2020 Merck KGaA, Darmstadt, Germany and/or its affiliates. All Rights Reserved. MilliporeSigma, the Vibrant M, Parteck, extrex and SAFC are trademarks of Merck KGaA, Darmstadt, Germany or its ­ affiliates. All other trademarks are the property of their respective owners. Detailed information on trademarks is available via publicly accessible resources. Lit. No. MS_PS7016EN 11/2020 Objectives The aim was to produce a Parteck® MXP based filament with minor variation in filament diameter and superior 3D printing capabilities as well as a significant amount of API content. Different downstream technologies were assessed in order to optimize the filament geometry and homo-geneity. A 3-axis laser measurement device was used as an online in process control in order to assess the homogeneity of the filament over the entire production (see Figure 1). Figure 1: Schematic view of the 3-axis laser measurement ­ device used as an in-process control. Purpose For several years now 3D printing technology has been gaining increasing attention within the pharmaceutical industry [1]. The number of publications is rapidly increasing. One promising 3D printing technology is the fused deposition modeling where a polymer strand is heated and extruded through a small nozzle followed by a solidification on a build plate. The production of the filaments itself is already described, but so far low focus is laid on assessing the filament properties like varying filament diameter or break tendencies. Our main goal was therefore to evaluate the production of highly loaded (15% API load), highly homogeneous filaments which shall provide excellent properties for 3D printing applications. Y Z X Conveyor belt Laser measurement Conveyor belt Laser measurement Twin screw extruder (Pharma 11) Twin screw extruder (Pharma 11) Melt pump (extrex® PFS) 80 200 200 200 200 195 190 80 200 200 200 200 195 190 190 175 Feedrate: ~0.3 kg/h, rotation speed: 150 rpm Feedrate: ~0.3 kg/h, rotation speed: 150 rpm Target pressure: ~40 bar Methods Polyvinyl alcohol based Parteck® MXP excipient from Merck KGaA, Darmstadt, Germany was used as a polymer for the hot melt extrusion. The model drug substance ketoconazole was purchased from LGM Pharma (Erlanger, KY 41018, USA). in Figure 2. 3D printing was performed using an Ultimaker 3 (firmware version: 4.0.1.20171023, UltFilaments for 3D printing with a target diameter of 1.75 mm were produced with an extrex® PFS – 20GP Melt pump from Maag Automatik GmbH (Groß-Ostheim, Germany) attached to a Pharma 11 twin- screw extruder from Thermo Scientific (Karlsruhe, Germany). The diameter of the filaments was measured with a 3-axis laser micrometer from Zumbach (Orpund, Switzerland) ODAC Trio33. An overview of the filament manufacturing process is presented imaker, Geldermalsen, Netherlands), which was modified to enable printing of filament with a diameter of 1.75 mm. Nozzle diameter was 0.4 mm. Tablets were designed in Fusion 360 (Autodesk, Farnborough, United Kingdom). Therefore, a cylinder shape was designed (diameter: 10 mm, height: 2.4 mm). Simplify 3D (version 4.0.1. Simplify 3D, Cincinnati, USA) was used for slicing. Tablets were printed at 10 mm/s with an infill density of 100%. All printing parameters were kept equal, except for printing temperatures. Parteck® MXP was printed at 230 °C and Ketoconazole containing filaments at 210 °C. Figure 2: Schematic view of the process setup evaluated for 3D printing. Conclusions Identifying the right down-stream equipment can be an important factor for creating a homogenous filament. The use of a melt pump can improve the consistency and ensures the safety of the process. During production the pulsation of the melt flow could be drastically reduced. Also a positive impact on the filament geometry can be assured. For the evaluated samples both technologies pro-vided reliable material properties for 3D printing. Variations in diameter were observed at an extend where the geometry of the final dosage form was not negatively affected. It can be expected that at a larger production scale the benefits of a melt pump are even more pronounced providing the basis for a further auto- mation of the process. Placebo – no melt pump Placebo – with melt pump Ketoconazole – with melt pump Ketoconazole – no melt pump 8 10 6 4 2 Diameter [mm] 14 12 0 0.20 0.25 0.15 0.10 0.05 Mass [g] 0.35 0.30 0.00 2.0 2.5 3.0 1.5 1.0 0.5 Height [mm] 4.0 3.5 0.0 1.75 1.70 1.80 1.85 Diameter [mm] Time [Min] 1.50 10 0 1 2 3 4 5 6 7 8 9 X Axis Y Axis Z Axis 1.65 1.60 1.55 1.95 1.90 2.00 1.75 1.70 1.80 1.85 Diameter [mm] Time [Min] 1.50 10 0 1 2 3 4 5 6 7 8 9 X Axis Y Axis Z Axis 1.65 1.60 1.55 1.95 1.90 2.00 1.75 1.70 1.80 1.85 Diameter [mm] Time [Min] 1.50 10 0 1 2 3 4 5 6 7 8 9 X Axis Y Axis Z Axis 1.65 1.60 1.55 1.95 1.90 2.00 1.75 1.70 1.80 1.85 Diameter [mm] Time [Min] 1.50 10 0 1 2 3 4 5 6 7 8 9 X Axis Y Axis Z Axis 1.65 1.60 1.55 1.95 1.90 2.00 References 1. Jamróz W, Szafraniec J, Kurek M, Jachowicz R. 3D Printing in Pharmaceutical and Medical Applications –Recent Achievements and Challenges. Pharmaceutical research. 2018; 35 (9):176- 1 MilliporeSigma: thomas.kipping@milliporesigma.com 2 Maag Automatik GmbH: christian.makert@maag.com 3 Thermo Fisher Scientific: margarethe.richter@thermofisher.com 4 EMD Serono: nadine.gottschalk@emdserono.com Figure 3: Variation of diameter over time for Parteck® MXP Placebo extrudates with integration of a melt pump (left) and without the melt pump (right). Figure 4: Variation of diameter over time for Parteck® MXP extrudates loaded with 20% ketoconazole with integration of a melt pump (left) and without the melt pump (right). Figure 5: Characterization of 3D printed tablets: From left to right: Mass, diameter, height. Results The Integration of a melt pump reduces the pulsation of the melt and enhances the precision of the targeted filament geometry for both placebo and drug loaded filaments (Figure 3 4). It can be shown that the use of a melt pump can increase the consistency and stability of the process. All printed samples show a homogenous weight distribution of the tablets. In our first assessment the geometry of the tablets was not affected by the different filament manufacturing techniques (Figure 4). Independent from drug load or the respective production method very reliable results concerning mass variation and geometry could be achieved (Figure 5). The Life Science business of Merck KGaA, Darmstadt, Germany operates as MilliporeSigma in the U.S. and Canada. We provide information and advice to our customers on application technologies and regulatory matters to the best of our knowledge and ability, but without obligation or liability. ­ Existing laws and regulations are to be observed in all cases by our customers. This also ­ applies in respect to any rights of third parties. Our information and advice do not relieve our customers of their own ­ responsibility for checking the suitability of our products for the envisaged purpose.