Continuous Manufacturing - Issues and Answers

MilliporeSigma 737 views 53 slides Nov 12, 2021
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About This Presentation

In this webinar, you will learn:

- The key issues in continuous manufacturing concerning excipients
- How those issues can be addressed

Detailed description:

Continuous manufacturing is a major trend in solid dose formulation. It shows economic and quality benefits, however, hurdles and challenge...


Slide Content

The life science business of Merck KGaA,
Darmstadt, Germany operates as
MilliporeSigma in the U.S. and Canada.
Continuous
Manufacturing
Dr. Leo Ohrem
Issues and Answers

The life science business
of Merck KGaA, Darmstadt,
Germany operates as
MilliporeSigma in the U.S.
and Canada

BAE
Solubility & Bioavailability
Enhancement
Now
Sustainingportfolio development on
excipients for solubility enhancement
(i.e. Parteck
®
SLC, Parteck
®
MXP).
Continuous Manufacturing
(Powder to Tablet)
Medium-term
Incrementalevolution of
specialty excipients for the
specific needs of continuous
manufacturing technologies
Additive Manufacturing
(3DPill Printing)
Long-term
Breakthrough innovation
on novel excipients for
existing and future additive
manufacturing technologies
CM
A&F Solid Formulation R&D Activity Focus
The right mix of incremental & breakthrough R&D
3
3D-
Printing
Research
Development

Poll Question
4

1.Are you currently working on continuous
manufacturing in solid dose?
a.No
b.No but in the near future
c.Yes, with focus on direct compression
d.Yes, with focus on wet granulation
e.Yes, with all above and will include dry granulation
f.Yes, for immediate release
g.Yes for controlled release
h.Yes, for ODT formulations
i.Yes, for low soluble drugs

Whatsnew?
Continuous Manufacturing | Sept 20216
Single Unit operations(UO) havebeencontinuous:
•Tablet compression
•Roller compaction
•Hot meltextrusion
New istheinterconnectionofseveral
UO without intermediate handling,
storage, analytics

7
From powder to tablet
in <5 minutes
APIExcipients
Blending
Lubricant
Blending
Tabletting
Excipients
Excipients
Coating
Final analytics
Continuous direct compression

8
From powder
to tablet
in < 25minutes
in continuous
wet granulation
APIExcipients
Blending
Excipients
Excipients
Lubricant
Blending
Tabletting
Coating
Final analytics
Granulation & drying
APIExcipients
Blending
Excipients
Excipients
Including wet granulation or
roller compaction

9
Why Continuous Manufacturing in solid dose?
Quantifiable evidence for increased efficiency demonstrated

Pharmacompaniesin themarketwith
registered drugsusingCM
Vertex Okambi(lumocaftor/Ivacaftor)
Jansen, Prezista(darunavir)
Eli Lilly, Versenio(abemaciclib)
Vertex Symdeko(Tezecaftor)
Pfizer Daurismo(glasdegib)
10
Who isactivelyworkingon Continuousmanufacturing?
Actively supported
by authorities:
US-FDA, EMA,
PMDA

Consequenceson excipients?
Quality constraints?
New products?
Flow!
Dosability!
Numberofcomponents!
Content Uniformity!
Batch-Batch Consistency!
What‘s in it for us?
11

Poll Questions
12

2. How many components will you
have to feed into a proposed
continuous process?
a.2-3
b.3-5
c.5-10
d.more

3. which components do you expect to
be difficult to be fed to the process?
a.API
b.Filler
c.Binder
d.Disintegrant
e.Lubricant
f.Glidant
g.sweetener
h.Flavors

Impressions from the real world
15
Hopper Emptying Test (Coarse Concave Screw)
M200 PMIC
MT-S not possible
MgSt
Wrong initial fill weight
KT20
ZD12FB
CF
CF_adp
MT-S
For poorly flowing µ-APAP in small scale feeders
almost immediate flow stagnation observed
Mass flow [kg/h] Mass flow [kg/h] Mass flow [kg/h]
15

Our Answer

Excipientchallenges in CM
Our Concept
17
1
DC Mannitol Parteck® M as multifunctional
excipient
2
Binary Premixes off the shelf ready to use
3
Customized premixes as individual projects
17

Parteck
®
M as
Multifuctional
Excipient

Why Mannitol?
Vegetable origin
Acceptance byauthorities& customers
Lowest water content & hygroscopicity
Inert to APIs & humans
Noimpurities4
19

Moisture
content and
hygroscopicity

Substance Watercontent
Starch < 15 %
MCC < 7 %
Isomalt < 7 %
Excipient System A < 5.75 %
Excipient System B < 3.5 %
Excipient System C < 3 %
Lactosemonohydrate < 1 %
DC-Mannitol < 0.3 %
Excipients systems A-C
are ready-to-use
systems of the
following composition:
A: lactose
monohydrate,
povidone,
crospovidone
B: lactose
monohydrate,
cellulose
C: lactose
monohydrate, maize
starch
Moisture Content
Watercontentofexcipientsmatters
21
Mannitol is the best choice to use with moisture sensitive APIs
Rowe, R. C., P. J. Sheskey, et al., Eds. (2009). Handbook of Pharmaceutical Excipients.
6th Edition. London, Washington DC, Pharmaceutical Press and American Pharmacists
Association or manufacturer’s information.
21

Hygroscopicity
Comparison offillerexcipients
22
Least hygroscopicity for mannitol
Even sorbitol may work well, if humidity can be controlled
22

Inertness
Impurities

Keep itsimple!
Whatyouleaveout, youdo not needtoworryabout
Impurities
Excipientsandtheirimpurities
24
MCC Water, glucose (reducing sugar), hydrogen bonding
(-> retardation), aldehydes, free radicals/peroxides
Glucose, Lactose Water, aldehydes, formic acid, reducing sugar
Starch Water, reducingsugar, aldehydes
HPMC Water, reducingsugar, retardation, aldehydes
PEG, Tween Aldehydes, peroxides
Povidone Peroxides, aldehydes, retardation
Crospovidone Peroxides, aldehydes
Wu Y, Levons J, NarangAS, RaghavanK, Rao VM. ReactiveImpuritiesin Excipients: Profiling, IdentificationandMitigationofDrug–ExcipientIncompatibility.AAPS
PharmSciTech. 2011;12(4):1248-1263. doi:10.1208/s12249-011-9677-z.

Impurities
Reducingsugarsarecauseforinstabilityandbrowning
(Maillardreaction)
25
How to minimize:
Commercial standard according to pharmacopoeia limits for
polyols (mannitol, sorbitol)
Ph. Eur. max. 0.10 %
USP max. 0.30 %
Is this limit sufficient for API stability?

Unwanted related substance from the reaction of API impurity (amine) and the reducing
sugars in the mannitol
MannitolAwithAPI, testedafter storage(60°C, 7 days),
The contentofthe targetimpurityis1.91%
MannitolA & API, testedafter blending
Mannitol B & API, tested after blending
MannitolB withAPI, testedafter storage(60°C, 7 days),
The contentofthe targetimpurityis0.57%
min
signal
Impurities
Reaction of API impurity with reducing sugars in mannitol
26
Impurity levels can be different between suppliers of the
same type of excipient

Impurities
Formulation of mannitolsfrom different suppliers using direct
compression
27
DC Formulation with
MannitolA
•Unwanted degradation
product of API: 6.5%
DC Formulation with MannitolB
•Unwanted API degradation
product of API: 1.5%
•Many fewer types of
impurities identified
The choice of excipient and the respective level of
impurities are critical factors influencing API stability
27

Impurities
Example: Reducingsugars in Parteck
®
M batch to
batch
28
Typical Values of an impurity are never the same as the
specification limits
28

Why Parteck
®
M?
Large & structured surface area
leadsto goodcontentuniformity
Perfect flow
Noaerosil
®
needed
Perfectcompressibility
Nobinderneeded
gooddisintegration
Nodisintegrantneeded
29
4

30
Granulation process
Statistical mixturevsorderedmixture
Common
knowledge:
Homogenous
mixtures only
possible for similar
particle sizes
30

Granulation process
Statistical mixture vs ordered mixture
3131

Spray-driedMannitolA
+ 1% AscorbicAcid< 10µm
Spray-driedMannitolB
+ 1% AscorbicAcid< 10µm
Granulation process
Statistical mixture vs ordered mixture
32
Large structuredsurfaceenablesorderedmixturesbyadsorptionof
the API
32

Compression force
Evaluation ofdifferent excipientsfordirectcompression
33
0
100
200
300
400
500
600
0 5 10 15 20 25 30 35
Tablet
hardness
[N]
Compactionforce[kN]
Calcium diphosphate anhydrate
Calcium diphosphate dihydrate
Lactose monohydrate
Mannitol, granulated
Mannitol, spray-dried A
Microcrystalline cellulose
Sorbitol
Sorbitol, spray-dried
Sorbitolandspray-driedmannitoldeliversuperiorcompressibility
33

Compressionforce
ParticleEngineering createscompressibility
34
SEM ofDC-Mannitol SEM ofParteck
®
M
Large surface areas show great compressibility
34

35
Polymorph and BET -surfaceParteck™ M 100 beta 3
Parteck™ M 200 beta 3
Mannitol 100 (SD) alpha 0.6
Mannitol 200 (SD) alpha 0.5
Mannitol 300 beta 0.5
Mannitol 400 beta 0.4
Mannitol 500 beta 0.3
Mannitol SD EZ alpha 0.5
Mannitol DC Granul. A beta 0.3
Mannitol DC Granul. B 2080beta 0.5
Mannitol DC granul. C 3215beta 0.4

36
Compressibilityofmannitols
tablet hardness[N]
0
100
200
300
400
0 5 10 15 20 25 30 35
compression force [kN]
Parteck
®
M 200
Mannitol SD
Gran. Mannitol
Method
Formulation:
99% testmaterial + 1%
magnesiumstearate; 5 min.
mixing
Compression:
singlepunchpress (Korsch
EK0 DMS, rpm:54, punch:
11mm, flat, facetted)
Tablet weight:
500 mg (rel. S.D.:0.5)
Mannitol A andB are
commerciallyavailable
mannitolgrades fordirect
compression.

37
0
20
40
60
80
Parteck
®
M DC-Mannitol Lactose/starch-
granules
Tablettose
tablet hardness (N)
Parteck
®
M: High compressibility
Formulation:
98,5% Mannit; 1,5% Mg-Stearat, Compr. Force 15 KN
99% Lactose, 1% Mg-Stearat, Compr. Force 15 KN

38
0
10
20
30
Parteck
®
M DC-Mannitol Lactose/starch-
granules
Tablettose
Disintegration time (min)
Parteck
®
M: Fast Disintegration
Formulation:
98,5% Mannit; 1,5% Mg-Stearat, Compr. Force 15 KN
99% Lactose, 1% Mg-Stearat, Compr. Force 15 KN

Whattype ofgranulationshallbeused?
39
Direct
compression
Wet
granulation
Dry
Granulation
Roller
compaction
All shall be possible!
Parteck
®
M fits all purposes

40
Direct
compression
Parteck® SRP 80
Parteck® ODT
Parteck® PLX
188
Parteck® M
Parteck® L M

41
Wet
Granulation
Parteck
®
Delta M
Parteck
®
M

42
WetGranulation vsDirectCompression
How to select an enabling technology?
Wet
Granulation
(beta
Mannitol)
Wet
Granulation
(delta
Mannitol)
Parteck
®
M
for Direct
Compression
After
Granulation
Betaform
mannitol
Betaform
mannitol
After
Granulation
Betaform
mannitol
Betaform
mannitol
Deltaform
mannitol

Wet Granulation vs Direct Compression
Results: Select the best enabling technology
43
Wet Granulation
Crystalline
Beta Mannitol
Wet Granulation
Parteck
®
Delta
Mannitol
Direct
Compression
Parteck
®
M 200
Results:
Wet Granulation
Results:
Direct Compression
Punching
Pressure:
29 kN
Tablet weight:541 mg
Tablet
hardness
34 N
Friability: bad
Disintegration:9 Min
50Sec
Punching
Pressure:
12 kN
Tablet weight: 505 mg
Tablet hardness 210 N
Friability: 0,20
Disintegration: 4 Min 23
Sec
Punching
Pressure:
12 kN
Tablet weight: 484 mg
Tablet hardness 111 N
Friability: 0,29
Disintegration: 4 Min
15 Sec



Important
Important

Poll Question
44

4. How do you appreciate premixes
and or coprocessedexcipients?
a.No, not at all –only straight pharmacopoeia
materials
b.Premixes most likely but coprocessednot
c.Coprocessedpreferred

Binary premixes
off the shelf
ready to use

Excipent System
New concept
47
DC-Mannitol
Lubricant
Mg Stearate
Parteck
®
LM
2 grades

48
•NoneedfordosageofsmallbadflowingcomponentMg-Stearate
•Guaranteedcontentuniformity
•Provenflowand processingperformance
•Provenlubricationfunctionality
Advantages
Resultspublishedat AAPS 2020
(Poster available)

49
•NoneedfordosageofsmallbadflowingcomponentNa-
croscarmellose
•provencontentuniformity& stabilityoverlonghaulsupplychain
•Provenflowand processingperformance
•Provendisintegrationfunctionality
•Registered in EU aspediatricdrug
Parteck
®
ODT
Established2009 goodtrack record

Customized
premixes

51
Individual customized premixes
Project business case
Open for any excipients of customers choice –no API
Analyt. Methods to be developed (& validated)
3
2
1
Content uniformity & stability to be proven
(segregation?)
Exclusivity –no off the shelf product, made to
order
4
5

The vibrant M, SAFC and Emprove are trademarks of Merck KGaA, Darmstadt, Germany or its affiliates. All other trademarks are theproperty of their respective owners.
Detailed information on trademarks is available via publicly accessible resources.
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