notes on formulation & evaluation of floating microspheres of an antibiotic drug
TRANSCRIPT
PREPARED BY:
Keyur Vasava…
1
“Formulation & Evaluation of floating microspheres of an antibiotic drug”
“Formulation & Evaluation of floating microspheres of an antibiotic drug”
Aim of present workObjectivesRationaleIntroductionMethodReview of literatureDrug profilePolymer profileExperimental workEvaluationconclusionReferences
2
Contents
3
AIM OF PRESENT WORK
Prevent degradation in alkaline pHTo maintain constant level of drug in the blood
plasma and minimize fluctuationremain buoyant to improve bioavailability.Prolonging gastric residence of a dosage form to
improve therapeutic value
4
Objectives Of Present Work
oral route: Ease of administrationMicrospheres(multiparticulate system):uniform
dosage formGRDDS: minimize fluctuationCephalexin ,BCS class ΙΙΙdrug has short half life
(80min) and low bioavailability hence it is suitable for gastroretentive system.
Method (W/O/W emulsion solvent evaporation method):simple ,economic & short processing time
Optimization: good % yield and good % drug release
5
Rationale
6
DrugCephalexin:
Antibiotic, BCS classш drug ,short half life,Low bioavailability
Gastro retentive Floating drug
delivery system
Floating Microspheres
spherical
Size range-10μm to 1000 μm
Introduction
The urinary tract is the body's filtering system for removal of liquid wastes.
Because have a shorter urinary tract, women are especially susceptible to bacteria that may invade the urinary tract and multiply -- resulting in infection known as a urinary tract infection, or UTI.
Fortunately, these infections are easily treated with antibiotics.
7
What is UTI???
8 Deshpandey.A A,Shah,Pharm res.1997 Atyabi,F.,Sharma H L,J control.Rel 1996
Approches toGRDDS
9 gaba Poonam,Floating microspheres a: Review,Volume 6 ,2008
Types of Gastroretentive drug Delivery system
10
Improves patient compliance Bioavailability enhancesGastric retention time is increased Drug releases in controlled manner for prolonged period. Superior to single unit floating dosage forms Avoidance of gastric irritationBetter therapeutic effect of short half-life drugs can be achieved.
Nayak Amit Kumar, Gastroretentive drug delivery systems: a review,
January-March 2010
Advantages of floating Microspheres
When Drugs are absorbed from specific site like from stomoch or upper GIT.
When such drugs are incorporated in SR system.
Only few drugs dissolve at absorption region and all other drug is going waste.
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Need for gastric Retention
12
Limitation of Floating Drug Delivery system
Criteria for selection of Drug
Criteria for selection of Drug
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Step 1 Preparation of aqueous phase
↓ Step 2 organic solvent (DCM:Acetone+ Polymer)W/O emulsion
↓ Step 3 primary emulsion poured to aq phase containing PVA(0.5%)
↓ Step 4 The resultant emulsion ( w/o/w type) was continually stirred ( 550 to 950 rpm)
↓ Step 5 fitration ,collection,washing and vaccum drying
Dr.Jose GR, Omidian H, Shah K. Pharm Tech 2003
Method of preparation of floating microspheres
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DRUG WORK DONE AUTHOR YEAR
Verapamil hydrochloride
preparation and evaluation of floating microspheres of verapamil hydrochloride for improving the drug bioavailability by prolongation of gastric residence time.
Tanwar Yuveraj Singh 2007
Glipizide Microspheres can be successfully designed for sustained delivery of Glipizide and to improve dosage form characteristics for easy formulation.
Phutane P 2010
Ketoprofen Microspheres developed for prolongation of gastric residence time.
GargRajeev et
2010
List of Review of related litereture
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Drug Work done Auther year
Piroxicame Microspheres with improvedmicromeritics property
RD Kale et al 2007
Famotidine Microsphreresto achieve an extended retention in the upper gastrointestinal tract, which may result in enhanced absorption and thereby improved bioavailability
Jain Abhishek Kumar
2009
Cimetidine Microspheres for prolongation of gastric residence time by the solvent evaporation method using polymers hydroxypropyl -methyl cellulose and ethyl cellulose.
Srivastava Anand kumar 2005
Ketorolac trometamol
Developed microspheres which can be prepared to improve the absorptionand bioavailability of ketorolac trometamol by retaining the system in to the stomach for prolonged period of time.
Barhate Shashikant
2009
DRUG WORK DONE AUTHER YEAR
Cefpodoxime proxatile
Developed microsphere in order to achieve an extended retention in the upper GIT, which may result in enhanced absorption and thereby improved bioavailability.
M.K.Deepa 2009
metformin Developed Microspheres may be used in clinic for prolonged drug release in stomach for at least 8 hrs, thereby improving the bioavailability and patient compliance.
Patel Asha et al 2006
diltiazem hydrochloride
microspheres developed ,The data obtained in this study thus suggest that a micro particulate floating dosage form of diltiazem hydrochloride can be successfully designed to give controlled delivery and improved oral bioavailability.
Gattani Yogesh S 2008
silymarin Microspheres developed for for prolonged gastric residence time and increased drug bioavailability.
Rajeev Garg 2010
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Name of Drug Cephalexin
Drug Category Anti-Bacterial Agents
Chemical Formula C16H17N3O4S
Chemical IUPAC Name (6R,7R)-7-[[(2R)-2-amino-2-phenylacetyl]amino]-3-methyl-8-oxo-5-thia-1-azabicyclo[4.2.0]oct-2-ene-2-carboxylic acid.
Chemical structure:
BCS class Class ш
Introduction to Cephalexin
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Cephalexin Dose for Bacterial Infections 65mg
Administration Orally
Half Life : 1 hour
Protein Binding 14%
Mechanism of Action : Cephalexin, like the penicillins, is a beta-lactam antibiotic. By binding to specific penicillin-binding proteins (PBPs) located inside the bacterial cell wall, it inhibits the third and last stage of bacterial cell wall synthesis.
Absorption : Well absorbed from the gastrointestinal tract.
Metabolism: 80% excreted unchanged in urine within 6 hours of administration
Excreation: Renal
Toxicity: diarrhea, nausea, upper abdominal pain, and vomiting.
Clinical use to treat urinary tract infections, respiratory tract infections, and skin and soft tissue infections. It is also sometimes used to treat acne.
Side-effects diarrhea, dizziness, headache, indigestion, joint pain, stomach pain and tiredness.
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Ethyl Cellulose:Functional Category Coating agent; flavoring agent; tablet
binder; tablet filler; viscosity increasing agent. Description Ethyl cellulose is a tasteless, free-flowing, white to
light tan-colored powder. Density (bulk): 0.4 g/cm3 Glass transition temperature: 129–133˚C Solubility Ethyl cellulose is freely soluble in chloroform, ethanol
( 95%), ethyl acetate, methanol, and toluene,acetone.Specific gravity: 1.12–1.15 g/cm3.
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1.Materials and Equipments2.Priliminary study2.1Spectrophotometric analysis of cephalexin2.2Drug–Excipients COMPABILITY Study2.3IN Process Optimization 3.Application of Full factorial design layout4.Characterization of Micromeritics property 5.Other evaluation parameters6.Formulation and evaluation of check point batch S107.Fiting to kinetic model8.Stability Study
22
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MATERIALS sources
Cephalexin Innova captab Ltd(chandigadh)
Ethyl cellulose(EC)
(18-24cps)
Qualikems Finechem
pvt.ltd,Nandesari,vadodara
Acetone Aatur Instra chem,Vadodara
Dichloromethane Suvidhinath laboratories,vadodara
Polyvinyl alcohol
(25-32cp)
Qualikems Finechem
pvt.ltd,Nandesari,vadodara
Hydrochloric acid IP Finar chemicals Ltd
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Equipments Sources
Digital electronic balance Scaletec mechatronics pvt.Ltd
Propeller stirrer Remimotor Ltd
Optical microscope USICO, india
Tap density Tester Electrolab , USP ETD: 1020
UV spectrophotometer Shimadzu , UV-1700, Pharmaspec
Dissolution Test apparatus Electrolab,TDT-08L
2.1Spectrophotometric analysis of cephalexin2.2Drug–Excipients COMPABILITY Study2.3IN Process Optimization
Determination of absorption maxima (λmax) of Cephalexin
λmax for cephalexin is 257 nm.
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Calibration curve
No of sample
Concentration(μg/ml)
Abs
1 10 0.109
2 20 0.25
3 30 0.357
4 40 0.465
5 50 0.567
6 60 0.668
7 70 0.791
8 80 0.901
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Conc (μg/ml) vs Abs
FT-IR spectra of drug
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Functional group
O-H Β-Lactom Amide -COOH -COOH
Standard Cephalexin
3148.13 1758.31 1689.43 1595.00 1399.94
FT-IR Spectra of Drug+polymer(E.C+PVA)
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Functional group
O-H Β-Lactom
Amide -COOH -COOH
CFL+EC+PVA 3168.49 1758.36 1689.36 1595.90 1399.01
There is no chemical interaction between Cephalexin and other excipients.
A. Volume of aqueous phase for primary emulsion
B. Volume of organic phase
C. Acetone : Dichloromethane
D. Stirring rate
E. Polymer:Drug
30
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A. VOLUME OF AQUEOUS PHASE FOR PRIMARY EMULSION
Volume of the organic phase 10 ml
Acetone: DCM ratio 1:1
Stirring rate 550 rpm
Concentration of PVA 0.5% w/v
Batch No. Volume of the aqueous
Phase
characteristic
A1 5 ml Thick emulsion(Not
easily pourable)
A2 10 ml Proper amount to
form emulsion
A3 15 ml Break down of
emulsion
Optimization of volume of aqueous phase for primary emulsion
Volume of the aqueous phase 10 ml
Acetone:DCM ratio 1:1
Stirring rate 550 rpm
Concentration of PVA 0.5 % w/v
32
B.VOLUME OF ORGANIC PHASE
Optimization of volume of the organic phase
Batch No. Volume of the organic
Phase
Product characteristic
B1 10 ml Aggregated lump
B2 20 ml Spherical microspheres
B3 30 ml Coarse, not complete
spherical
Volume of the aqueous phase 10 ml
Volume of the organic phase 20 ml
Stirring rate 550 rpm
Concentration of PVA 0. 5 % W/V
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C.ACETONE:DICHLOROMETHANE
Optimization of Acetone:Dichloromethane ratio
Batch No. ACT:DCM ratio Product characteristic Aggregation
C1 3:1 Spherical microspheres ++
C2 2:1 Spherical microspheres +
C3 1:1 Irregular microspheres ++
C4 1:2 Spherical microspheres +++
C5 1:3 Spherical microspheres +++
Volume of the aqueous phase 10 ml
Volume of the organic phase 20 ml
Acetone: DCM ratio 2:1
Concentration of PVA 0.5 % W/V
34
Batch No. Stirring rate Product characteristic Aggregation
D1 350 rpm Very large size particles +++
D2 550 rpm Larger size,Nearly
spherical
++
D3 750 rpm Small size, spherical ++
D4 950 rpm Small size microparticles +
D5 1150rpm very small,breakdown of
microparticles
++
Optimization of stirring rate
Batch No. Polymer:
drug ratio
Product
characteristic
Aggregation % yield
P1 6:1 Spherical + 78.93%
P2 5:1 Spherical + 70.28%
P3 4:1 Spherical + 63.95%
P4 3:1 spherical + 59.41%
P5 2:1 Spherical + 55.81%
P6 1:1 Spherical ++ 53.89%
P7 1:1.5 Spherical ++ 49.45%
P8 1:2 Irregular +++ -----
35+++:high aggregation
Parameter Selected batch Specification
Volume of aqueous phase A2 10 ml of aqueous phase
Volume of organic phase B3 20 ml of organic phase
Acetone : DCM ratio C2 2:1 ratio of ACT:DCM
Stirring rate D3 550rpm
750rpm
950 rpm36
OPTIMIZED BATCH
32 FACTORIAL DESIGNIndependent variables X1:Polymer concentration
X2: Stirring speed
Dependable variablesY1:particle size(μm)
Y2:% Drug encapsulation efficiency
Y3:t80%(min)
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3. APPLICATION OF FULL FACTORIAL DESIGN
level INDEPENDENT VARIABLES
X1(polymer concentration)(%)
X2(stirring speed)(rpm)
Low 8.33 550
Medium 10.43 750
high 12.50 950
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Batch code X1 (%) X2(rpm)
S1
8.33 550
S2
10.43 550
S3
12.50 550
S4
8.33 750
S5
10.43 750
S6
12.50 750
S7
8.33 950
S8
10.43 950
S9
12.50 95039
32 DESIGN LAYOUT
Micromeritics propertyScanning Electron Microscopy% buyovancyEvaluation of dependent variables
i. Particle size
ii.% drug Encapsulation efficiency
iii.t80%
TAPPED DENSITYBULK DENSITYCOMPRESSIBILITY INDEXANGLE OF REPOSE
41
4.MICROMERITICS PROPERTY
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Characterization of microspheres
FORMULATION CODE
BULK DENSITY(gm/cm)
TAPPED DENSITY(gm/cm)
COMPRESSIBILITY INDEX
ANGLE OF REPOSE
S1 0.350±0.013 0.394±0.006 11.16±0.231 19.29±0.22
S2 0.375±0.009 0.434±0.009 13.59±0.942 21.00±0.34
S3 0.400±0.110 0.450±0.003 11.11±0.620 22.19±0.29
S4 0.412±0.050 0.471±0.005 12.61±0.742 18.67±0.18
S5 0.437±0.060 0.507±0.010 13.80±0.426 22.58±0.65
S6 0.462±0.007 0.521±0.007 11.32±0.378 24.95±0.22
S7 0.487±0.060 0.557±0.015 12.59±0.672 19.29±0.65
S8 0.525±0.090 0.583±0.009 10.17±0.722 25.17±0.54
S9 0.562±0.030 0.633±0.016 11.21±0.465 27.11±0.27
Micromeritics property shows good flowability and packagability
Mean ± S.D., n=3
Spherical and uniform in shape,porous in nature and rough surface,shows good floating characteristics and flowability to the dosage form.
43
Scanning electron Microscopy
Buoyancy (% ) = ( Qf * 100 ) / ( Qf + Qs )
Formulation code % buoyancy(%)
S1 97±1.71
S2 88±1.81
S3 84±3.07
S4 91±2.65
S5 85±1.85
S6 81±2.85
S7 83±5.43
S8 81±4.41
S9 80±2.91
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Good %buoyancy shows good floating ability for prolong period of time.
Mean ± S.D., n=3
Formulation code
Particle size (µm)
%encapsulation efficiency(%)
t80% (min)
S1 475±1.32 67.95±3.75 657±7.02
S2 481±1.53 74.28±4.00 660±3.05
S3 491±0.95 81.93±4.39 695±6.00
S4 375±0.99 64.74±3.51 573±6.43
S5 385±1.17 72.33±2.63 586±5.03
S6 390±1.11 77.45±4.32 600±2.31
S7 239±1.56 59.52±3.21 521±2.30
S8 250±0.99 70.47±2.75 527±2.00
S9 275+1.56 74.16±2.42 566±3.50
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6.EVALUATION OF DEPENDABLE VARIABLES
Mean ± S.D., n=3
Batch code
Particle size(µm)
S1 475±1.32
S2 481±1.53
S3 491±0.95
S4 375±0.99
S5 385±1.17
S6 390±1.11
S7 239±1.56
S8 250±0.99
S9 275+1.56
46
EFFECT OF X1 AND X2 ON PARTICLE SIZE
Mean ± S.D., n=3
Contour plot Response Surface plot
47
Graphical representation of Effect of FactorX1 & X2 On particle size
Conclusion: As Polymer concentration increases particle size increases,and with incresing stirring speed it will decreases.
By Design expert version 8.0.5.2
Design-Expert® SoftwareFactor Coding: Actualparticle size
Design Points491
239
X1 = A: polymer concentrationX2 = B: stirring speed
8.33 9.02 9.72 10.41 11.11 11.81 12.50
550.00
630.00
710.00
790.00
870.00
950.00particle size
X1: A: polymer concentrationX2: B: stirring speed
300
350
400
450
Design-Expert® SoftwareFactor Coding: Actualparticle size
Design points above predicted valueDesign points below predicted value491
239
X1 = A: polymer concentrationX2 = B: stirring speed
550.00
630.00
710.00
790.00
870.00
950.00
8.33
9.02
9.72
10.41
11.11
11.81
12.50
200
250
300
350
400
450
500
par
ticle
siz
e
A: polymer concentration
B: stirring speed
Table – Out put of regression analysis for Effect of X1 and X2 on PARTICLE SIZE
Regression statistics
R Square 0.9922
Adjusted R Square 0.9896
Standard error 3.99
Coefficients
Coefficient coefficient Value P-value
Intercept 373.44 < 0.0001
X1 11.17 0.0360
X2 -113.83 < 0.0001
Equation: Y1==+381.89+11.17X1-113.83X2+5.00 X1X2+2.17X12-14.83X2
2
SUMMURY OUT PUT OF REGRESSION ANALYASIS
P value <0.05 indicats model is significant and +sign of coefficient of X1—if polymer concentration increases,particle size increases- Sign of coefficient of X2 shows if stirring speed decreases,particle size increases
Batch code Y2 (%encapsulationefficiency)
S1 67.95±3.75
S2 74.28±4.00
S3 81.93±4.39
S4 64.74±3.51
S5 72.33±2.63
S6 77.45±4.32
S7 59.52±3.21
S8 70.47±2.75
S9 74.16±2.42
49
EFFECT OF X1 AND X2 ON ENCAPSULATION EFFICIENCY(Y2)
Contour plot Response surface plot
Conclusion :As Polymer concentration increases % encapsulation efficiency increases,and with incresing stirring speed %encapsulation efficiency decreases.
50
EFFECT OF X1 AND X2 ON %Encapsulation efficiency (Y2)
By Design expert version 8.0.5.2
Design-Expert® SoftwareFactor Coding: Actual%encapsulation efficiency
Design Points81.93
59.52
X1 = A: polymer concentrationX2 = B: stirring speed
8.33 9.02 9.72 10.41 11.11 11.81 12.50
550.00
630.00
710.00
790.00
870.00
950.00%encapsulation efficiency
X1: A: polymer concentrationX2: B: stirring speed
65
70 75
80
Design-Expert® SoftwareFactor Coding: Actual%encapsulation efficiency
Design points above predicted valueDesign points below predicted value81.93
59.52
X1 = A: polymer concentrationX2 = B: stirring speed
550.00
630.00
710.00
790.00
870.00
950.00
8.33
9.02
9.72
10.41
11.11
11.81
12.50
55
60
65
70
75
80
85
%en
caps
ulat
ion
effic
ienc
y
A: polymer concentration B: stirring speed
Table – Out put of regression analysis for Effect of X1 and X2 on % ENCAPSULATION EFFICIENCY.
Regression statistics
R Square 0.9694
Adjusted R Square 0.9592
Standard error 0.45
Coefficients
Coefficient coefficient Value P-value
Intercept 71.43 < 0.0090
X1 6.89 < 0.0001
X2 -3.34 0.0010
Equation: Y1=72.44+6.89 X1-3.34X2+0.17X1X2-1.40X12-0.12 X2
2
SUMMURY OUT PUT OF REGRESSION ANALYSIS
P value <0.05 indicats model is significant and
+sign of coefficient of X1—if polymer concentration increases,% encapsulation efficiency increases
- Sign of coefficient of X2 shows if stirring speed decreases,%encapsulation efficiency increases
Batch code t80% (min)
S1 657±7.02
S2 660±3.05
S3 695±6.00
S4 573±6.43
S5 586±5.03
S6 600±2.31
S7 521±2.30
S8 527±2.00
S9 566±3.50
52
EFFECT OF X1 AND X2 ON t80%(Y3)
Contour plot Response surface plot
Conclusion :As Polymer conc increases ,t80% increases & t80% decreases with increasing stirring speed. 53
EFFECT OF X1 AND X2 ON t80%(Y3)
By Design expert version 8.0.5.2
Design-Expert® SoftwareFactor Coding: Actualt80%
Design Points725.62
586.22
X1 = A: polymer concentrationX2 = B: stirring speed
8.33 9.02 9.72 10.41 11.11 11.81 12.50
550.00
630.00
710.00
790.00
870.00
950.00t80%
X1: A: polymer concentrationX2: B: stirring speed
600
620
640
660
680
700
720
Design-Expert® SoftwareFactor Coding: Actualt80%
Design points above predicted valueDesign points below predicted value725.62
586.22
X1 = A: polymer concentrationX2 = B: stirring speed
550.00
630.00
710.00
790.00
870.00
950.00
8.33
9.02
9.72
10.41
11.11
11.81
12.50
580
600
620
640
660
680
700
720
740
t80
%
A: polymer concentration
B: stirring speed
Table – Out put of regression analysis for Effect of X1 and X2 on t80%
Regression statistics
R Square 0.9633
Adjusted R Square 0.9511
Standard error 4.48
Coefficients
Coefficient coefficient Value P-value
Intercept 598.33 < 0.0031
X1 18.33 0.0005
X2 -66.33 < 0.007
Equation: Y1==+644.42+13.69X1-57.98X2-3.23X1X2+2.76X12+5.93X2
2
SUMMURY OUT PUT OF REGRESSION ANALYSIS
P value <0.05 indicats model is significant and +sign of coefficient of X1—if polymer concentration increases,t80% increases- Sign of coefficient of X2 shows if stirring speed decreases,t80% increases
55
The overlay plot of the responses generates an optimized area, as per the desired criteria. The polymer concentration value was targeted 12.44 and Stirring speed was set to 950.15
Overlay plot for Optimization
By Design expert version 8.0.5.2
Design-Expert® SoftwareFactor Coding: ActualOverlay Plot
particle size%encapsulation efficiencyt80%
Design Points
X1 = A: polymer concentrationX2 = B: stirring speed
8.33 9.02 9.72 10.41 11.11 11.81 12.50
550.00
630.00
710.00
790.00
870.00
950.00Overlay Plot
X1: A: polymer concentrationX2: B: stirring speed
particle size: 299.191
particle size: 400.000
t80%: 605.140particle size 271.014%encapsula74.5152t80%: 605.153X1 12.44X2 950.00
FORMULATION INGREDIENT FORMULATION BATCH F10
Volume of aqueous phase 10 ml of aqueous phase
Volume of organic phase 20 ml of organic phase
Aceton:DCM 2:1 ratio of ACT:DCM
Stirring speed 605.15 rpm
Cephalexin 200mg
Polymer concentration 12.44%
PVA 0.5%
56
6.Formulation and evaluation of check point batch
TEST PARAMETERSBATCH S10 % Error
PREDICTED ACTUAL
Particle size 271μm 275μm 0.014%
% Encapsulation Efficiency
74.51% 73.21% 0.017%
t80% 605.15min 599.27min 0.0097%
TIME(hr) S1
S2
S3
S4 S5 S6 S7 S8 S9
0min 0 0 0 0 0 0 0 0 0
0.5min 1.97 0.987 0.074 3.94 2.96 1.97 6.9 4.93 2.96
1hr 8.92 6.92 4.93 6.99 7.93 4.93 10.94 8.92 7.93
2hr 16.02 12.99 9.86 11.09 11.09 10.01 18.08 14.07 13.42
3hr 23.27 18.21 13.2 20.2 18.98 18.89 27.34 24.26 23.18
4hr 30.67 26.49 16.13 29.51 24.32 22.26 36.8 33.65 31.57
5hr 38.22 32.96 23.38 37.04 34.7 32.6 44.48 42.25 39.14
6hr 46.91 38.58 29.79 45.71 42.34 41.18 53.3 52.01 47.85
7hr 53.79 46.28 36.33 54.54 51.11 48.94 60.31 58.02 54.76
8hr 60.81 53.15 42.02 61.57 59.07 57.85 67.71 64.13 63.77
9hr 67.95 61.93 58.75 69.73 68.42 64.95 76.7 74.3 71.96
10hr 72.26 68.27 64.86 77.04 77.04 73.16 81.18 81.74 79.32
11hr 78.61 74.57 71.08 83.5 82.15 79.55 89.8 88.28 86.8
12hr 84.1 84.1 79.38 89.5 86.74 84.1 98.17 96.91 93.22
57
58
%cumulative drug release of Batch S1 to S9
59
%cumulative drug release of Batch S10
TIME(hr) Batch S10
0min 0
0.5min 4.934
1hr 9.974
2hr 14.136
3hr 25.290
4hr 32.733
5hr 39.339
6hr 48.048
7hr 56.928
8hr 64.994
9hr 74.196
10hr 84.556
11hr 92.149
12hr 98.885
Results of Model Fitting of optimized Batch
Intercept Slope R2
Zero order plot 8.24 0.322 0.998
First order plot 0.0125 0.753 0.773
Higuchi 30.48 19.21 0.920
Korsmeyer peppas 1.17 0.749 0.828
60
7.Fitting to kinetic model
n > 0.749 > 1.0 indicates Drug release mechanism was non-fickian transport
Stability Study
Days Particle Size(µm) %drug Encapsulation efficiency(%)
t80%(min)
Before Storage
0 Days 275±0.23 73.21±1.23 599.27±3.65
After storage
7days 275±0.84 72.13±0.21 597.33±5.43
15days 273±0.43 71.09±1.23 595.45±3.25
30days 271±0.32 70.32±2.21 592.25±5.21
*Storage at 40 and 75%RH for 1month,mean±SD;n=3
61
8.Stability Study
Conclusion: Stability studies indicated that there was no significant difference observed between the release pattern of microspheres at 40ºC and 75% RH for one months
The results of a 32 full factorial design revealed that
the polymer ratio (X1) and stirring speed (X2)
significantly affected the dependent variablesThe microspheres of the check point batch (F10) exhibited
73.21% drug encapsulation efficiency, mean particle size of 275 µm and 599.27 min t80% which were nearer to predicted values obtained from overlay contour plot
of all the responses.These result shows a good relationship between the
experimental & predicted values,which confirms the practicability of the model.
62
conclusion
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