Research Article | | Peer-Reviewed

Development of a Capsule Formulation Containing Dry Bark Extract of Annickia Polycarpa: Laboratory to Pilot Scale-up

Received: 9 August 2025     Accepted: 20 August 2025     Published: 11 September 2025
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Abstract

This study focuses on the development and scale-up of a capsule formulation based on the dry extract of Annickia polycarpa bark, a West African medicinal plant known for its antimalarial, antibacterial, and antioxidant properties. The objective was to adapt the process, initially optimized at laboratory scale, to a pilot scale for pharmaceutical valorization. Hot maceration followed by drying yielded a higher extraction rate at pilot scale (24%) compared to laboratory scale (18.46%). Powder characterization revealed very fine particles (Dx50 < 125 µm), residual moisture within pharmacopeial limits (4%), and good solubility (100-200 g/L). However, the powders exhibited poor flowability, requiring wet granulation with pregelatinized starch or carboxymethylcellulose as binders. This step significantly improved flow properties and particle cohesion. Capsules produced from the granules met uniformity of mass requirements according to the European Pharmacopeia and displayed a rapid disintegration time (< 7 minutes), ensuring efficient release of active compounds. The human equivalent dose (HED), extrapolated from animal studies, was estimated at 3,402 mg/day for a 70 kg adult, allowing the definition of capsule size 2 with 247-296 mg of extract per unit. Overall, these findings demonstrate the technical feasibility and robustness of the encapsulation process for Annickia polycarpa, providing promising perspectives for industrial development and the production of standardized phytomedicines. However, further studies on long-term stability, bioavailability, and clinical efficacy are required to ensure the quality, safety, and therapeutic effectiveness of the final product.

Published in Pharmaceutical Science and Technology (Volume 9, Issue 2)
DOI 10.11648/j.pst.20250902.12
Page(s) 53-63
Creative Commons

This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.

Copyright

Copyright © The Author(s), 2025. Published by Science Publishing Group

Keywords

Annickia Polycarpa, Pilot-Scale Extraction, Capsule Formulation, Phytomedicine

1. Introduction
The valorization of African plant resources for therapeutic purposes constitutes a strategic issue for the development of improved traditional medicines and phytomedicines. Annickia polycarpa (DC.) Setten & Maas (Annonaceae), commonly used in traditional pharmacopeias of West Africa, is renowned for its antimalarial, antibacterial, antifungal, antioxidant and anti-inflammatory properties . The barks of this plant contain alkaloids, flavonoids, terpenes and phenols, which justify its documented pharmacological activity .
The development of a phytomedicament requires rigorous control of the transformation process, from the extraction of bioactive compounds to the galenic formulation. The dry extract represents a stable and concentrated form, compatible with putting in capsules, which is one of the most common oral forms in herbal medicine for its acceptability, dosage accuracy and ease of packaging . However, the transition from small-scale production to pilot or industrial scale poses several technological challenges, particularly with regard to reproducibility of yield, stability of assets, physical characteristics of the powder (particle size, hygroscopicity, compressibility) and the suitability with the capsule packaging process .
The formulation of capsules is based on strict criteria, including the fluidity of the powder, the uniformity of the filling, the absence of reactions between excipients and active ingredients, as well as the stability of the content over time . Moreover, scaling up in the production line requires applying galenical engineering principles (such as respecting drying, grinding, mixing and encapsulation conditions), while maintaining the pharmaceutical specifications of the finished product .
The present study aims to develop a formulation in capsules based on dry extract of Annickia polycarpa bark, starting from the experimental conditions of the laboratory to adapt them to the pilot scale. It is part of an approach to the industrial valorization of traditional pharmacopoeia, by combining quality, stability and pharmaceutical compliance requirements.
2. Material and Methods
2.1. Material
2.1.1. Plant Material
The plant material was bark of Annickia polycarpa.
They were harvested about 75 km from Daloa on the way to Zoukougbeu, in the Classified forest of Haut Sassandra de Daloa on Sunday, August 22, 2021. The sample was authenticated by a morphological identification at the National Center of Floristics of the FELIX HOUPHOUËT-BOIGNY University (FHBU). The herbarium is kept there under number UCJ001184. The collected bark were dried at room temperature (25°C), away from the sun, for two weeks. They were then ground (Retsch GM 300 Mill) at 2000 rpm to obtain a fine powder.
2.1.2. Technical Equipment and Materials

1) Agitator KIKA WERKE

2) Bain marie

3) Precision balance O’HAUS

4) Beakers 3 liters

5) Timer

6) Sieve 100µ

7) Grinder Retsch GM 300

8) Granulometer MASTERSIZER 3000E

9) Manual capsule maker

10) Delitest PHARMATEST PTZ

1) Evaporator E1400v3 FF3

2) Tilting cooker (Reactor 80 L)

3) Porcelain tray

4) Rotavapor Heidolph

5) Filter 90µ in canvas

6) Homemade gas oven

7) Oven MEMMERT

8) Semi-automatic capsule maker MULTIGEL MS-6 AUT

9) Granulator ERWEKA FGS equipped with an engine ERWEKA AR400

2.2. Methods
2.2.1. Extraction Method by Hot Maceration, Followed by a Concentration by Evaporation and Drying
The hot maceration operation consisted of letting the Annickia polycarpa bark powder stay in water heated to 80°C for 1 hour 30 minutes and twice 1 hour, to extract the active metabolites.
The extraction yield was calculated according to the Equation:
Determination of dry extract yield:
The dry extract yield (EY%) was calculated from the following formula:
Equation (1): Extraction yield
EY%=mass of dry extractmass of bark powderx100(1)
(i). Laboratory Scale
100 g of Annickia polycarpa bark powder was placed in a beaker with a capacity greater than 3 L. The water bath was run up to 80°C. 800 mL of osmosis water was added to the beaker containing our sample, then placed in the water bath with stirring for 1 hour. Using a sieve, the resulting mixture was filtered.
Twice, 800 mL of 80°C RO water was added to the bark powder residue, and the same operation was carried out to exhaust the drug, this time with stirring for 1 hour.
The liquid extraction yield was calculated.
The resulting macerate was then concentrated to one-third volume using a rotavapor.
The concentrated liquid extract was dried in a MEMMERT oven at 50°C. The dry extract obtained was weighed and the extraction yield calculated.
(ii). Pilot-Scale Maceration
3000 g of Annickia polycarpa bark powder were placed in a tilting cooker filled with 80 L of osmosis water heated to 80°C. The mixture was stirred for 1 h 30 min, then filtered through a sieve with a mesh less than 90 µm in diameter.
Twice, we added 80 L of RO water to the bark powder residue and performed the same operation to exhaust the drug, this time stirring for 1 hr.
The filtrate obtained is concentrated in a vacuum evaporator to about 1/3 of its volume.
The concentrated liquid extract was dried in a gas oven at 80°C. The dry extract obtained was weighed and the extraction yield calculated.
2.2.2. Characterization of Extract Powders
The characterization of extract powders enabled us to compare the pharmaco technical properties of powdered extracts and to deduce the extract most suitable for galenic formulation.
Due to the low yield of extract obtained in the laboratory, we were only able to carry out tests that did not require a large quantity of extract. The table below shows all the tests carried out on each sample. The cages marked with a tick are the tests we carried out.
Our standards were obtained from the 9th edition of the European Pharmacopoeia.
NB: the flow test requires 100 g of powder.
Table 1. Tests carried out on the different powder samples.

Characterization tests of powders

Extracted at the laboratory scale oven

Extract at pilot scale

Macroscopic and organoleptic examination

X

X

Flowability test

X

Laser particle size analysis

X

X

Residual moisture test

X

X

Solubility test

X

X

(i). Macroscopic and Organoleptic Characterization of the Extracts
The organoleptic characteristics of the extracts were determined by an observation of color, taste and smell.
(ii). Flowability Test
100 g of powder was weighed and put into the standardized funnel previously plugged with the finger. The powder flow time was timed after clearing the funnel. The test was repeated 3 times. The results are expressed as flow times of 100 g of powder.
(iii). Laser Particle Size Analysis
The passage of the extracts to the MALVERN laser particle sizer type MASTERSIZER 3000 E made it possible to plot the histograms of the percentages of the simple masses and the cumulative percentages of the powders as a function of the size of the particles, to determine the particle size distribution profile of the powder, then the median particle size (50% of the powder). The fineness of the powders was defined according to the following table:
Table 2. Classification of powders according to their fineness.

Descriptive term

X50

Cumulative volume distribution Q3 (x)

Coarse

>355

Q3 (355) <0,50

Moderately fine

180-355

Q3 (180) <0,50 et Q3 (355) ≥0,50

Fine

125-180

Q3 (125) <0,50 et Q3 (180) ≥0,50

Very fine

≤125

Q3 (125) ≥0,50

(iv). Residual Moisture Test: Gravimetric Method
3 test shots of 1 to 3 g (m) of powder were introduced, respectively in 3 pre-calibrated watch glasses. The masses of the test shots plus the tares have been noted. After 2 hours in the oven at a temperature of 102±2°C, the test samples were weighed again. Mass constancy was checked by heating 1 h more each time, until the difference in mass is less than 0.5 mg. The mass of water contained in the powder of each watch glass was noted M and given by the formula: M = m-m’. The mass after drying is: m’ .
The residual moisture content (RM%) was calculated according to the Equation
RM%=m-m'mx100(2)
The standard states that it must be between 3 and 5%.
(v). Solubility Test
The method was that of the OECD (Organization for Economic Cooperation and Development) 105. Increasing volumes of water were gradually added to approximately 0.1 g of sample (sprayed), at room temperature, in a 10 ml graduated bottle closed with a glass stopper. After each addition of water, the mixture was stirred for 10 minutes. It was then visually checked if the sample was completely dissolved. If undissolved parts of the sample remained after adding 10 ml of water, the test should continue in a 100 ml graduated flask.
Table 3 below gives the volume of water that completely dissolves the sample, the approximate solubility. If the solubility is low, the time required to dissolve the substance may be long and at least 24 hours. If after 24 hours the substance is still not dissolved, it is necessary to wait up to 96 hours or proceed with further dilution.
Table 3. Different types of solubility according to the OECD.

ml of water for 0,1 g soluble

0,1

0,5

1

2

10

100

> 100

Approximate solubility (g/l)

> 1000

1000 à 200

200 à 100

100 à 50

50 à 10

10 à 1

< 1

2.2.3. Wet Granulation of the Extracts and Characterization
Determining the dose to be admintered
The determination of the dose to be administered was made using a factor-based dose approach. In this approach, the no observed adverse effect level (NOAEL) of the drug in the animal undergoes simple allometric extrapolation to obtain the Human Equivalent dose (HED). The United States Food and Drug Administration (FDA) has formulated a table of conversion factors (Table 4) that allow for proper calculation of the HED.
Table 4. Conversion factors in the determination of HED.

Species

HED (mg/kg) = Divide animal dose by…

HED (mg/kg) = Multiply animal dose by…

Mouse

12,3

0,081

Hamster

7,4

0,135

Rat

6,2

0,162

Guinea pig

4,6

0,216

Rabbit

3,1

0,324

Dog

1,8

0,541

Marmoset

6,2

0,162

Baboon

1,8

0,541

To account for size-independent effects of pharmacokinetics and pharmacodynamics, the DHE is then multiplied by the mass of a standard adult (70 kg) and divided by a safety factor equal to 10. The FDA approach uses 0.67 as an exponent to extrapolate doses between species.
Choice of excipients
The excipients were selected on the basis of the results of the rheological characterization, their availability and the fact that they were obtained from our natural resources.
Table 5. Excipients description.

Raw materials

Function

Proportion

Description

Carboxymethyl cellulose

Binder

2.5%

White, odorless, tasteless powder. Hygroscopic after drying

Pregelatinized corn starch

Binder

5%

White to off-white, medium-coarse to fine powder. It is painless and has a slight, characteristic taste

Osmosed water

Dampening solution

Sqt

Purer, odorless water, free of chlorine aftertaste and other undesirable, polluting substances.

Wet granulation was chosen because the flow of powder extract was infinite.
In view of the low yield of the powder extracts obtained in the laboratory, and given that after the various characterization tests, the two extracts presented practically the same characteristics (see results), we carried out wet granulation with the powder extract obtained on a pilot scale (720 g).
Wet granulation
It was carried out in the following stages:
1) Weighing: The various raw materials were crushed and weighed using a mortar and pestle combination and a precision balance.
2) Mixing: The raw materials required for the internal phase of the granules (dry extract + binder) were mixed. The binder was added dry, to optimize the amount of water required for wetting.
3) Wetting: Once the mixture was homogeneous, we proceeded to the wetting stage, a critical step in the granulation process. This involved adding osmosed water at 75°C to the mixture until a paste of optimum consistency was obtained.
4) Granule formation: This was carried out on the BONALS oscillating granulator. The wet mass was passed through a screen. The wet granulated mass was weighed.
5) Drying: The granulated mass obtained was placed in the MEMMERT oven for 48 h at 50°C.
Residual moisture was measured using the loss-on-drying method.
Two formulas were produced: formula 1 with 5% pregelatinized starch as binder, and formula 2 with 2.5% carboxymethyl cellulose.
Formula 1:
Table 6. Formula 1 (First granulation formula).

Raw materials

Function

Quantity

Annickia polycarpa bark extract

Active ingredient

20 g

Pregelatinized corn starch

Binder

5%

Osmosed water

Dampening solution

Sqt

Formula 2:
Table 7. Formula 2 (Second granulation formula).

Raw materials

Function

Quantity

Annickia polycarpa bark extract

Active ingredient

20 g

Carboxymethyl cellulose

Binder

2.5%

Osmosed water

Dampening solution

Sqt

We performed the following tests on formulas 1 and 2:
1) Particle size analysis: sieve method
2) Flow tests
3) Residual moisture test
(i). Particle Size Analysis: Sieve Method
The test was carried out using a sieve shaker with 7 sieves of mesh sizes 4000, 2000, 1000, 600, 300, 150, 100 and 50 μm on a sample of 25 to 100 g of powder. The powder was placed on the top sieve and agitated for 10 min at a speed of 40 vibrations per minute. The rejects from each sieve and the base were weighed. Histograms of single and cumulative mass percentages of powders as a function of particle size were plotted. D10, D50 and D90 deciles were determined. The classification of powders is shown in Table 2.
(ii). Flowability Test
100 g of granules were weighed and placed in the standardized funnel, which had previously been plugged with a finger. The time taken for the powder to flow was measured after the funnel had been cleared. The test was repeated 3 times. Results were expressed as flow times for 100 g of granules.
(iii). Residual Moisture Test: Gravimetric Method
3 test doses of 1 to 3 g (m) of granules were introduced into 3 pre-weighed watch glasses. The masses of the test samples plus the tares were noted. After 2 h in the oven at a temperature of 102±2°C, the test samples were weighed again. Mass consistency was checked by heating for a further 1 h each time, until the difference in mass was less than 0.5 mg (m'). The mass of water contained in the powder of each watch glass was noted M and given by the formula: M = m-m'. The mass of the test sample is: m.
2.2.4. Human Equivalent Dose of Annickia Polycarpa
An in vivo study evaluated the antimalarial activity of Annickia polycarpa extract in mice infected with Plasmodium berghei. The doses administered ranged from 200 to 600 mg/kg/day. At 600 mg/kg, parasitaemia was suppressed by 75.8%, with no apparent toxicity at oral doses of up to 4,000 mg/kg .
HED=Animal dose (mg/kg)Conversion factor animal/human(3)
Human Equivalent Dose (HED):
Animal dose = 600 mg/kg
Human body weight = 70 kg
Conversion factor (mouse → human) = 0,081 (see Table 4)
HED = 600 mg/kg× 0,081 = 48,6 mg/kg (human)
Total dose for 70 kg = 48,6 × 70 = 3 402 mg/day
2.2.5. Theoretical Extract Masses per Capsule
Formula 1
In 3000 mg of granules (2000 mg of extract + 1000 mg of binder), there are 2000 mg of plant extract.
For a size 2 capsule with a theoretical average weight of 370 mg, there are 247.67 mg of plant extract.
Formula 2
In 2500 mg of granules (2000 mg of extract + 500 mg of binder), there are 2000 mg of plant extract.
For a size 2 capsule with a theoretical average weight of 370 mg, there are 296 mg of plant extract.
2.2.6. Capsule Manufacturing and Capsule Control
The quantities required for capsule filling were determined using the filling table.
Formula: granules obtained from Formula 1 and Formula 2.
The extract dose per capsule was determined. Then, using the filling table, the amount of granule-excipient mixture required to fill 20 size 2 capsules was defined for both formulas. In a mortar, a homogeneous mixture was prepared and distributed into capsules by scraping level.
Capsule filling: The body of each capsule was opened and placed in the capsule filler, with the caps set aside. The capsules were filled by scraping level (without tamping). Once filling was complete, the capsule filler was gently tapped and carefully lowered, the upper part turned a quarter turn. The capsules were closed and ejected by turning the upper part of the capsule filler a quarter turn (same direction).
(i). Uniformity of Mass
Method: We individually weighed the 20 filled samples, then emptied and weighed the contents of each capsule, and finally weighed the cleaned empty capsule. We then determined:
1) Net weight.
2) Mean (X̄)
3) Confidence Interval (CI)
CI = X̄±PX̄ P = Acceptance limit
CC’ = X̄±2PX̄
(ii). Disintegration Test
Capsules were placed in each basket compartment, a disk was added (specific immersion medium: 37 ± 2°C), the test duration was set, and the device was started. At the specified time, the basket rack was lifted out of the liquid.
Upon complete disintegration, the soft mass contained no palpable core.
Table 8. Acceptance criteria for the disintegration test.

LEVEL

SAMPLES

Acceptance criteria (at the end of specific time)

Test 1

06

All units disintegrated: Test compliant

1 ou 2 units not disintegrated: Perform Test 2

More than 2 units not disintegrated: Test non-compliant

Test 2

12

16 out of 18 disintegrated

3. Results
3.1. Extraction Yield
Table 9. Drying results of the extracts at different scales.

Laboratory scale

Pilot scale

Powder quantity

100 g

3000 g

Extract mass obtained

18,46 g

720 g

Yield %

18,46%

24%

3.2. Characterization of Extract Powders
3.2.1. Macroscopic and Organoleptic Characterization
Both extracts were brown in color, in flake form, slightly bitter, with a characteristic plant odor.
Table 10. Macroscopic and organoleptic examination of the two extracts.

CHARACTERISTIC

RESULT

Color

Brown

Odor

Characteristic

Taste

Slightly bitter

Figure 1. Annickia polycarpa extract.
3.2.2. Flowability Test
Both extracts were classified as very fine powders based on Dx50 values below 125 µm. Both showed almost identical D10 values (1.60-1.61 µm), meaning that 10% of particles had a diameter below this size. The “pilot extract” had slightly finer particles (2.35 µm) and a narrower distribution (D90 = 5.78 µm) compared to the “oven extract” (D90 = 6.06 µm).
The “laboratory extract” had the largest mean particle size (3.35 µm), indicating overall larger particles.
Both extracts had D90/D10 ratios greater than 1, indicating heterogeneous size distribution, which may influence their rheological behavior.
Table 11. Particle size distribution of the different extracts.

PARAMETER

Laboratory Pilot

D10

1,61 μm 1,60 µm

Median: D50

2,39 μm 2,35 µm

D90

6,06 μm 5,78 µm

Mean

3,35 μm 3,24 µm

D90 / D10

3,78 3,61

3.2.3. Residual Moisture Content
Table 12. Residual moisture content test results.

SAMPLES

m (g)

After 2 h

After 3 h

RESULTS

m 1

m’

Oven extract

1,00

0,98

0,96

m-m’= 0.04 g

RM %= 04

Pilot extract

1,00

0,98

0,96

m-m’= 0.04 g

RM %= 04

The residual moisture content of both extracts complied with standards (3-5%) (Table 12).
3.2.4. Solubility Test
Both extracts were soluble in water, with an approximate solubility of 100-200 g/L, and showed similar solubility profiles.
Table 13. Solubility test.

SAMPLE

ml water dissolving 0,1 g

Approximate solubility (g/l)

Oven extract

1

100 à 200

Pilot extract

1

100 à 200

3.3. Wet Granulation
3.3.1. Determination of HED
1) Animal dose = 600 mg/kg (Annickia polycarpa)
2) Human weght = 70 kg
3) Conversion factor (mouse → human) = 0,081
4) HED = 600 mg/kg× 0,081 = 48,6 mg/kg (human)
5) Total dose for pour 70 kg = 48,6 × 70 = 3 402 mg/day
3.3.2. Particles Size Analysis Granules
Table 14. Particle size distribution of Annikia polycarpa.

D10

2,332

Є [100-200]

Median: D50

11,6

Є [300-600]

D90

20,988

Є [600-1000]

Mean

3.887

Standard deviation

3.993

3.3.3. Flowability Test
Table 15. Flowability test.

SAMPLES

Polycarpa

1st test

0,47 s

2nd test

0,45 s

3rd test

0,43 s

Both formulas exhibited excellent flow through the funnel, with complete discharge and flow times ≤ 10 s (0.45 s for Formula 1, 0.30 s for Formula 2). Flow occurred in a funnel-shaped stream..
3.3.4. Residual Moisture Content
The residual moisture content of the granules complied with the standard (between 3 and 5%). Formula 1 and Formula 2 granules had substantially equal values (04 and 03% respectively).
Table 16. Residual moisture content of Formulas 1 and 2.

Formula

m (g)

After 2 h

After 3 h

RESULT

m

m’

Formula 1

1

0,99

0,96

m-m’= 0.04 g

RM %= 04

Formula 2

1

0,99

0,97

m-m’= 0.03 g

RM %=03

3.3.5. Capsule Manufacturing and Quality Control
(i). Uniformity of Mass
No capsule mass fell outside the confidence interval. Capsules showed good uniformity of mass.
Table 17. Uniformity of mass.

Mass of the full capsules (mg)

Mass of the empty capsules (mg)

Mass of the content of the capsules (mg)

m1

370

55

315

m2

350

66

284

m3

350

60

290

m4

350

70

280

m5

370

55

315

m6

320

60

260

m7

350

66

284

m8

330

60

270

m9

320

61

259

m10

370

55

315

m11

340

67

273

m12

340

70

270

m13

360

60

300

m14

340

60

280

m15

350

56

294

m16

330

58

272

m17

390

55

335

m18

360

57

303

m19

350

55

295

m20

350

55

295

Total

6990

1201

5789

Mean

349,5

60,05

289,45

1) Mean (X̄): X̄=289,45 mg
2) Confident interval (CI)
a. CI = X̄±PX̄, P = Acceptance limit, P = 10% because X< 300 mg
b. CI = [260,54-318,36]
c. CI’ = X̄±2PX̄
d. CI’ = [231,56-347,34]
(ii). Disintegration Test
All 6 capsules disintegrated in less than 7 minutes (below the 15 min limit). Test passed.
Table 18. Disintegration test.

SAMPLE

A. polycarpa

1st test

6 min 30

2nd test

6 min 10

4. Discussion
4.1. Extraction Yield
The extraction yield was significantly higher at pilot scale (24%) than at laboratory scale (18.46%). This difference can be attributed to a more favorable solvent-to-material ratio, more homogeneous agitation, and better thermal control at the pilot scale, enabling more complete diffusion of active metabolites . Large-scale processes often benefit from optimized mass and heat transfer parameters, which favor the extraction of polar compounds such as alkaloids and flavonoids from A. polycarpa . Shorter drying times and controlled temperature at pilot scale also help limit thermal degradation of actives, as reported in several phyto-extraction studies .
4.2. Particles Size Characterization
Both extracts showed very fine particle sizes (D50 < 125 µm), with slightly finer particles and a narrower distribution at pilot scale (D90 = 5.78 µm) compared to laboratory scale (D90 = 6.06 µm). Finer particle sizes generally increase surface area and dissolution rate . However, heterogeneous size distribution (D90/D10 > 3) can affect blend uniformity and rheology, often requiring pre-processing such as granulation to improve flowability . Similar findings have been reported for polyphenol-rich plant powders, where excessive milling may cause electrostatic charging and poor flow .
4.3. Residual Moisture and Solubility
Residual moisture levels (4% for both extracts) complied with European Pharmacopoeia standards (3-5%), ensuring microbiological and chemical stability . Excess moisture can promote enzymatic degradation or microbial growth, while too little moisture can increase friability and dust formation . Solubility values (100-200 g/L) were favorable for oral bioavailability of hydrophilic extracts and consistent with the high alkaloid and polyphenol content reported in A. polycarpa .
4.4. Granulation and Flowability Improvement
Wet granulation transformed non-flowing powders into granules with excellent flow (≤ 0.45 s for 100 g). This is consistent with pharmaceutical engineering principles, where granulation increases bulk density, reduces interparticle cohesion, and improves flow . The choice of pregelatinized starch and carboxymethylcellulose as binders aligns with their ability to provide good interparticle cohesion while maintaining rapid disintegration . Post-granulation moisture content (3-4%) remained within recommended limits, ensuring granule stability .
4.5. Capsule Quality Control
Capsules met European Pharmacopoeia criteria for mass uniformity and disintegration (< 7 min, well below the 15 min limit ). These results reflect good filling performance, homogeneous blending, and excipient-extract compatibility . Rapid disintegration is essential for prompt release and absorption of active ingredients .
5. Conclusion
This study successfully developed a capsule formulation containing dry extract of Annickia polycarpa bark, scaling the process from laboratory to pilot production. The pilot-scale process achieved a higher extraction yield (24% vs. 18.46% at laboratory scale) while maintaining physicochemical quality, particularly in terms of residual moisture (4%), solubility (100-200 g/L), and fine particle size (D50 < 125 µm).
Wet granulation significantly improved powder flowability, ensuring uniform capsule filling and mass uniformity in line with European Pharmacopoeia standards. The capsules also showed short disintegration times (< 7 minutes), favorable for rapid release of active compounds.
From an industrial perspective, these results confirm the technical feasibility and robustness of the process, offering promising prospects for the pharmaceutical valorization of A. polycarpa. However, further studies on long-term stability, bioavailability, and clinical evaluation of antimalarial efficacy are required to finalize development into a phytomedicine that meets quality, safety, and efficacy standards.
Abbreviations

CI

Confidence Interval

Eq

Equation

EY%

Extraction Yield

FDA

Food and Drug Administration

FHB U

Felix Houphouët-Boigny University

HED

Human Equivalent Dose

NOAEL

Non Observed Adverse Effect Level

OECD

Organization for Economic Cooperation and Development

RM%

Residual Moisture Content

Sqt

Sufficient Quantity To

Author Contributions
Lia Gnahoré Jose Arthur: Conceptualization, Supervision, Validation, Writing – original draft, Writing – review & editing
Kone Sounan Serge Alain: Investigation, Writing – original draft
Dally Laba Ismaël: Supervision, Validation, Writing – review & editing
Conflicts of Interest
The authors declare no conflicts of interest.
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  • APA Style

    Arthur, L. G. J., Alain, K. S. S., Ismaël, D. L. (2025). Development of a Capsule Formulation Containing Dry Bark Extract of Annickia Polycarpa: Laboratory to Pilot Scale-up. Pharmaceutical Science and Technology, 9(2), 53-63. https://doi.org/10.11648/j.pst.20250902.12

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    ACS Style

    Arthur, L. G. J.; Alain, K. S. S.; Ismaël, D. L. Development of a Capsule Formulation Containing Dry Bark Extract of Annickia Polycarpa: Laboratory to Pilot Scale-up. Pharm. Sci. Technol. 2025, 9(2), 53-63. doi: 10.11648/j.pst.20250902.12

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    AMA Style

    Arthur LGJ, Alain KSS, Ismaël DL. Development of a Capsule Formulation Containing Dry Bark Extract of Annickia Polycarpa: Laboratory to Pilot Scale-up. Pharm Sci Technol. 2025;9(2):53-63. doi: 10.11648/j.pst.20250902.12

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  • @article{10.11648/j.pst.20250902.12,
      author = {Lia Gnahoré Jose Arthur and Kone Sounan Serge Alain and Dally Laba Ismaël},
      title = {Development of a Capsule Formulation Containing Dry Bark Extract of Annickia Polycarpa: Laboratory to Pilot Scale-up
    },
      journal = {Pharmaceutical Science and Technology},
      volume = {9},
      number = {2},
      pages = {53-63},
      doi = {10.11648/j.pst.20250902.12},
      url = {https://doi.org/10.11648/j.pst.20250902.12},
      eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.pst.20250902.12},
      abstract = {This study focuses on the development and scale-up of a capsule formulation based on the dry extract of Annickia polycarpa bark, a West African medicinal plant known for its antimalarial, antibacterial, and antioxidant properties. The objective was to adapt the process, initially optimized at laboratory scale, to a pilot scale for pharmaceutical valorization. Hot maceration followed by drying yielded a higher extraction rate at pilot scale (24%) compared to laboratory scale (18.46%). Powder characterization revealed very fine particles (Dx50 Annickia polycarpa, providing promising perspectives for industrial development and the production of standardized phytomedicines. However, further studies on long-term stability, bioavailability, and clinical efficacy are required to ensure the quality, safety, and therapeutic effectiveness of the final product.
    },
     year = {2025}
    }
    

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  • TY  - JOUR
    T1  - Development of a Capsule Formulation Containing Dry Bark Extract of Annickia Polycarpa: Laboratory to Pilot Scale-up
    
    AU  - Lia Gnahoré Jose Arthur
    AU  - Kone Sounan Serge Alain
    AU  - Dally Laba Ismaël
    Y1  - 2025/09/11
    PY  - 2025
    N1  - https://doi.org/10.11648/j.pst.20250902.12
    DO  - 10.11648/j.pst.20250902.12
    T2  - Pharmaceutical Science and Technology
    JF  - Pharmaceutical Science and Technology
    JO  - Pharmaceutical Science and Technology
    SP  - 53
    EP  - 63
    PB  - Science Publishing Group
    SN  - 2640-4540
    UR  - https://doi.org/10.11648/j.pst.20250902.12
    AB  - This study focuses on the development and scale-up of a capsule formulation based on the dry extract of Annickia polycarpa bark, a West African medicinal plant known for its antimalarial, antibacterial, and antioxidant properties. The objective was to adapt the process, initially optimized at laboratory scale, to a pilot scale for pharmaceutical valorization. Hot maceration followed by drying yielded a higher extraction rate at pilot scale (24%) compared to laboratory scale (18.46%). Powder characterization revealed very fine particles (Dx50 Annickia polycarpa, providing promising perspectives for industrial development and the production of standardized phytomedicines. However, further studies on long-term stability, bioavailability, and clinical efficacy are required to ensure the quality, safety, and therapeutic effectiveness of the final product.
    
    VL  - 9
    IS  - 2
    ER  - 

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    1. 1. Introduction
    2. 2. Material and Methods
    3. 3. Results
    4. 4. Discussion
    5. 5. Conclusion
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