Solvodynamic study on Solubility Enhanced Lovastatin in presence of Arginine as Cosolute

 

NF Zolkiflee1, MMR Meor Mohd Affandi1,3*, ABA Majeed2,3

1Department of Pharmaceutics, Faculty of Pharmacy, Universiti Teknologi MARA (UiTM),

Puncak Alam Campus, Bandar Puncak Alam, Selangor Darul Ehsan, Malaysia.

2Brain Research Laboratory, Faculty of Pharmacy, Universiti Teknologi MARA (UiTM) Selangor,

42300 Bandar Puncak Alam, Selangor Darul Ehsan, Malaysia.

3Pharmaceutical and Life Sciences CoRe, Universiti Teknologi MARA (UiTM), 40450 Shah Alam,

Selangor Darul Ehsan, Malaysia.

*Corresponding Author E-mail: meor@uitm.edu.my

 

ABSTRACT:

In this study, the solute-cosolute interaction, solute-solvent interaction involved in the solubilisation process of ARG solutions and LVS-ARG solution systems are illustrated. The sound velocity values of both solution systems were determined at varying concentrations of ARG (0.01-0.8 mol.dm-3) at 298.15 K. Next, the refractive index and the density of the solution systems was measured at temperature range from 298.15 to 313.15K. Acoustic and volumetric parameters such as isentropic compressibility (KS), apparent isentropic molar compressibility (KSΦ), relative association (RA), acoustic impedance (Z), internal pressure (πi), free volume (Vf), molar volume (Φv0), molar expansibility (ΦE0) were calculated from sound velocity and density data. From the study, an increasing trend in sound velocity was observed with the increase in ARG concentration while compressibility values showed opposite trend. Additionally, solute-solvent interaction and structural effects of water for ARG and LVS-ARG systems are discussed regarding the changes in acoustic parameters.

 

KEYWORDS: Acoustic Parameter, Arginine, Lovastatin, Refractive Index, Solute-Solvent Interactions, Sound Velocity.

 

 


INTRODUCTION:

In the development of effective drugs, one of the main factors emphasized by formulators is the aqueous solubility. This factor is, however, a challenge for lovastatin (LVS)1, a statin drug classified under Biopharmaceutical Classification System (BCS) Class II drugs which have low solubility despite being highly permeable2-4. The structure of LVS is shown in Figure 1. Numerous formulation strategies such as solid dispersion, particle size reduction, forming inclusion complex and some other novel methods have been applied and investigated in order to overcome this limitation5.

 

Figure 1: Chemical structure of LVS

 

Arginine (ARG) is a semi-essential amino acid obtained by hydrolysis of many proteins and found particularly abundant in protamines and histones6-8. Previous studies reported that ARG to be effective in suppressing protein aggregation and protein adsorption to a solid surface, facilitating desorption of bound proteins from various chromatographic columns, and enhancing the solubility of the highly insoluble wheat protein in phosphate buffer pH 7 as well as in water9-13. It has been indicated that ARG also undergoes weak hydrogen bonding to the protein surface and is possibly involved in the π electron-cation interaction9. From these facts we assume that ARG has the potential to improve the solubility of LVS.

 

Previously, we reported the 43-fold solubility enhancement of LVS in the presence of ARG as a cosolute14. In recent years, most studies are centred only on the solubility improvement and leaving out the fundamental properties that are vital information to understand the enhanced solubility mechanism of the drug. In this manuscript, the related thermodynamics and solute-solvent interactions of LVS-ARG are presented. Additionally, we further investigated the molecular interactions and dynamics, as well as related structural effects during solubilization by measuring the sound velocity, density, and refractive index. Data on functional properties were obtained by determining values of sound velocity, density, and refractive index.

 

MATERIAL AND METHODS:

Chemicals and reagents:

Materials used to prepare our solution systems were LVS and ARG, they were used without further purification. All materials used in the current study were of analytical grade and purchased from Sigma Aldrich (St. Louis, MO, USA). The chemical name, CAS number (CAS), supplier, purification method and purity are shown in Table 1. Ultrapure water (Select Bio O Purite: Oxfordshire, United Kingdom) was used to prepare the solutions.

 

Table 1: Source and Purity of Chemical Reagents Used in This Work.

Chemical Name

CAS No.

Abbreviation

Supplier

Mass Fraction Puritya

L-arginine

74-79-3

ARG

Sigma-Aldrich

≥99.5%

Lovastatin

75330-75-5

LVS

Sigma-Aldrich

≥99.5%

a The purities of compounds are provided by the suppliers.

 

Preparation of Solution Systems:

ARG and LVS-ARG solution systems were prepared according to the method described by Higuchi and Connors15. Chemicals were weighed on a Metler balance with a precision of 0.001mg and dissolved in 100mL purified water in a conical flask. ARG solutions with various concentrations (0.01-0.8 mol.dm-3) denoted as SB1 to SB7 were freshly prepared.

 

An excess amount of LVS was added to each flask containing the specified molar solutions of the ARG, denoted as SD1 to SD7 respectively. Separately, an excess amount of LVS was added to laboratory grade water to determine the respective intrinsic solubility, denoted as SD0. All conical flasks were placed in a mechanical water bath shaker at temperature of 308.15± 0.02K and shaken for a maximum period of 72 h. At the end of the incubation period, the suspensions were filtered through a 0.5µm membrane filter. Aliquots of the filtrates were subjected to viscosity estimation against the respective molar solutions of ARG as the blank. Each experiment was repeated at least three times and the results reported were the average values.

 

Refractive Index Measurement:

A 7 Abbemax digital refractometer (Misco, USA) was used to measure the refractive index. It is fitted with Microsoft windows software and the instrument was calibrated using reference solvents, provided by the supplier. The temperature of the system was maintained by the inbuilt peltier device, with a temperature uncertainty of ±0.01K. Meanwhile, uncertainties in refractive indices were ±0.000001.

 

Volumetric Study:

Density determination of the solutions (both blank and solutions containing saturated concentrations of LVS at four different temperatures ranging from 298.15K and 313.15K) was carried out by using Anton Paar digital density meter (Model DMA 60/602; Anton Paar, Austria). The temperature of water around the density meter cell was controlled by temperature bath (± 0.02K). Calibration of the density meter was done using dry air and pure water. All density measurements of the solutions were made with respect to pure water. Densities of pure water at the experimental temperatures were obtained from the literature16.

 

Sound Velocity:

The sound velocity through different samples at temperature 298.15 K was measured using a multifrequency electroacoustics spectrometer (Dispersion Tech Inc, USA) at frequency of 2 Mhz. The accuracy of the ultrasonic velocity measurement is within ± 0.5m/s. All the generated data were used to further calculate the thermo-physical parameters. The data were to be interpreted with respect to the solute solvent interactions and structural effects in order to provide more insights into solution dynamics.

 

RESULTS:

Refractive Index:

Triplicate measurements of refractive index (ηD) were taken and the values were averaged. Table 2 and Table 3 show the values of ηD and molar refractivity (RD) respectively, of water as well as varying molar concentrations of ARG and LVS-ARG recorded at 298.15, 303.15, 308.15 and 313K. To obtain the values of RD, Lorentz-Lorentz equation16-18 was used for calculation:

RD = [(nD2–1)/(nD2+1)](∑3i=1 xiMi/ρ)                            (1)

 

Where xi is the mole fraction while Mi is the molecular weight of the ith component of the mixture.

 


Table 2: Refractive Indices (nD) and Molar Refractive Indices (RD) of ARG Solution.

Sample/ mol.dm-3

T/K

298.15

303.15

308.15

313.15

nD

RD

 (x 10-3)

nD

RD

 (x 10-3)

nD

RD

(x 10-3)

nD

RD

(x 10-3)

SB0 

1.3326 ± 0.0003

0

1.3319 ± 0.0001

0

1.3312 ± 0.0001

0

1.3304 ± 0.0001

0

SB1 (0.01)

1.3329 ± 0.0019

6.4084

1.3312 ± 0.0019

6.4463

1.3306 ± 0.0016

6.4478

1.3300 ± 0.0012

6.4409

SB2 (0.03)

1.3336 ± 0.0001

19.3876

1.3330 ± 0.0001

19.4204

1.3323 ± 0.0001

19.4164

1.3315 ± 0.0001

19.3761

SB3 (0.09)

1.3358 ± 0.0002

58.3309

1.3351 ± 0.0002

58.3404

1.3343 ± 0.0002

58.4703

1.3335 ± 0.0002

58.2304

SB4 (0.27)

1.3414 ± 0.0004

175.7754

1.3407 ± 0.0004

175.7126

1.3400 ± 0.0004

177.0282

1.3393 ± 0.0003

175.4011

SB5 (0.50)

1.3489 ± 0.0007

327.0939

1.3482 ± 0.0007

327.2028

1.3473 ± 0.0007

330.0117

1.3461 ± 0.0006

326.3160

SB6 (0.70)

1.3542 ± 0.0008

458.7044

1.3535 ± 0.0009

458.9417

1.3528 ± 0.0007

462.2153

1.3522 ± 0.0004

458.4722

SB7 (0.80)

1.3552 ± 0.0031

522.5150

1.3561 ± 0.0025

524.8786

1.3551 ± 0.0025

526.5028

1.3538 ± 0.0026

523.0518

SB0 = purified water, SB1-SB7 = ARG solution ranging from 0.1 to 0.8 mol dm-3.

 

Table 3: Refractive Indices (nD) and Molar Refractive Indices (RD) of ARG Solution Saturated with LVS.

Sample/ mol.dm-3

T/K

298.15

303.15

308.15

313.15

nD

RD

 (x 10-3)

nD

RD

 (x 10-3)

nD

RD

(x 10-3)

nD

RD

(x 10-3)

SD0 

1.3326 ± 0.0001

1.7143

1.3319 ± 0.0001

1.7143

1.3313 ± 0.0002

1.7137

1.3306 ± 0.0001

1.7111

SD1(0.01)

1.3329 ± 0.0001

6.5943

1.3323 ± 0.0001

6.5966

1.3316 ± 0.0001

6.5906

1.3310 ± 0.0003

6.5828

SD2(0.03)

1.3336 ± 0.0001

20.1223

1.3330 ± 0.0001

20.1279

1.3323 ± 0.0001

20.1478

1.3315 ± 0.0001

20.0741

SD3(0.09)

1.3360 ± 0.0118

59.2752

1.3351 ± 0.0001

59.2817

1.3343 ± 0.0002

59.3858

1.3335 ± 0.0002

59.2489

SD4(0.27)

1.3416 ± 0.0001

176.6848

1.3409 ± 0.0002

176.7785

1.3401 ± 0.0002

178.2674

1.3390 ± 0.0008

176.2886

SD5(0.50)

1.3493 ± 0.0010

328.3082

1.3480 ± 0.0010

328.1923

1.3472 ± 0.0007

332.4537

1.3462 ± 0.0005

341.4808

SD6(0.70)

1.3542 ± 0.0016

460.2231

1.3544 ± 0.0017

461.4931

1.3536 ± 0.0019

467.1890

1.3529 ± 0.0024

460.4983

SD7(0.80)

1.3581 ± 0.0009

528.3047

1.3568 ± 0.0007

527.9455

1.3554 ± 0.0010

526.9387

1.3541 ± 0.0010

525.7482

SD0 = purified water, SD1-SD7 = ARG solution saturated with LVS ranging from 0.1 to 0.8 mol dm-3.

 


Volumetric Studies:

To get insight to solute-solvent interactions, it is crucial to evaluate limiting apparent molar volume (ΦV0) and limiting apparent molar expansibility (ΦE0) of ARG and LVS-ARG solution systems at 298.15, 303.15, 308.15 and 313.15 K by thorough analysis of the experimental data. The following relationships derived from experimentally measured densities were used to evaluate data given in Table 4:

 

ΦV = 1000 (Cd0) –1(d0d) + M2/d0                              (2)

 

ΦE = αΦV0 + (α – α0)1000/C                                          (3)

 

where C is the molar concentration of the solute, d0 is the density of pure water, d is the density of the solution, M2 is the molecular mass of the solute and α0 and α are the coefficients of expansion of the solvent and solution (with or without drug), respectively, and determined by means of the relation available in the literature.

 

Values of ΦV calculated by means of Eq. (2) were fitted by a method of least squares to Masson equation to obtain ΦV0 (limiting apparent molar volume) and the slope, SV

 

ΦV = ΦV0 + SVC1/2                                                          (4)

 

Values of ΦE from Eq (3) were also fitted by using least square method to get limiting apparent expansibility, ΦE0, and the slope SE.

 

ΦE = ΦE0 + SE/C                                                            (5)

 

The standard partial molar volumes, ΔtΦV0 were experimentally determined parameter using the following equation:

 

Move the equation number to the end of the line as such:

ΔtΦV0 = ΦV0 (in aqueous arginine solutions) – ΦV0 (in

water)                  

 

Table 4: Limiting Apparent Molar Volume (Φv0), Standard Partial Molar Volume (ΔtΦV0), Limiting Apparent Molar Expansibility (ΦE0), SV and SE Constant of ARG, and LVS-ARG Systems.

System

Temperature (K)

SV

(cm3.mol-1)

ΦV0

(cm9/2.mol-3/2)

ΔtΦV0

(cm9/2.mol-3/2)

SE

(cm3.mol-1 K)

ΦE0

(cm9/2.mol-3/2 K-1)

ARG

298.15

11.68

503.54

298.45

-312.38

952.69

LVS-ARG

298.15

22.44

345.61

140.52

0.70

13.80

ARG

303.15

6.18

359.03

153.94

-320.46

1025.80

LVS-ARG

303.15

8.55

357.26

152.17

0.32

8.24

ARG

308.15

3.96

361.07

155.98

-241.95

765.21

LVS-ARG

308.15

5.18

403.36

198.27

0.45

9.74

ARG

313.15

6.96

359.49

154.40

-234.62

721.68

LVS-ARG

313.15

19.52

369.75

164.66

0.51

10.25

 


Sound Velocity:

The results of the sound velocity (U) and density (d) were used to calculate the isentropic compressibility (KS) of the samples as

 

KS= 1/dU2                                                                       (7)

 

and the internal pressure as              

 

Пi = (KS0KS)                                                               (8)

 

where KS0 is the isentropic compressibility of water. The apparent isentropic molar compressibility KSՓ of the samples was calculated from Eq. (9):

 

KSՓ = (1000 KS/C) – KS0/d0(1000d/C) – M                   (9)

 

where KS0 is the isentropic compressibility and d0 is the density of water at 298.15 K. The values are shown in Table 5.

 


Table 5: Values of Sound Velocity (U), Density (ρ), Isentropic Compressibility (Ks) and Apparent Isentropic Compressibility (KsΦ) of Different Concentrations of ARG and LVS-ARG at 298.15 K.

Solution system

Ultrasonic parameter

Concentration/ mol.dm-3

0.01

(S1)

0.03

(S2)

0.09

(S3)

0.27

(S4)

0.50

(S5)

0.70

(S6)

0.80

(S7)

ARG

Sound velocity/m.s-1

1494.45

1493.65

1498.20

1520.05

1543.00

1560.30

1570.05

Density @298.15 K/ kg.m-3

0.9970

0.9990

1.0010

1.0083

1.0193

1.0277

1.0320

KS (10-7)/Pa-1

4.4910

4.4868

4.4507

4.2922

4.1205

3.9970

3.9309

KSΦ/10-5)

-15.3210

-4.2635

-1.1826

-2.2352

-2.0086

-1.4851

-1.3846

LVS-ARG

Sound velocity/m.s-1

1494.85

1494.25

1498.80

1521.57

1543.87

1564.20

1570.65

Density @298.15 K/ kg.m-3

0.9960

0.9980

1.0007

1.0090

1.0197

1.0277

1.0310

KS (10-7)/Pa-1

4.4931

4.4877

4.4486

4.2808

4.1145

3.9771

3.9317

KSΦ (10-5)

-12.1111

-3.5964

-.1.6227

-2.8912

-2.2224

-1.8140

-1.3563

 


The values of density and sound velocity were then used to estimate the magnitude of relative association (RA) from the relation19,20:

 

RA = d/d0 (U0/U)1/3                                                       (10)

 

where U0 is the sound velocity of water at 298.15 K. The acoustic impedance Z is determined from the relation19:

 

Z = Ud                                                                         (11)

 

The values of the KS, KS0, RA and Z of the samples are given in Table 5 and Table 6 respectively. Meanwhile, the value of free volume, Vf was calculated from the relation21:

 

Vf = Vmb                                                                   (12)

 

where Vm is the molar volume of the mixture and is given by   

 

Vm = Mav/d                                                                   (13)

 

and        

 

Mav = ∑nimi/∑ni                                                           (14)

 

where ni is the number of moles and mi is the molecular mass of the ith component in the mixture, while d is density of the corresponding aqueous solution systems.

 

In Eq.(12), b is the van der Waals constant and obtained from the relation:

 

b = [ Mav/ d [1- (RT/MavU2)]] × [1 + (MavU2/3RT)1/2]

 

where R is the universal gas constant, T (=298.15) K, and Mav is the average molecular mass of the mixture as given in Eq. (14). The values of Vf along with that of internal pressure, πi are given in Table 6.


 

Table 6: The Molar Volume (Vm), Free Volume (Vf), Internal Pressure (πi), Acoustic Impedance (Z) and Relative Association (RA) of Different Concentrations of ARG and LVS-ARG.

Solution system

Ultrasonic parameter

Concentration/ mol.dm-3

0.01

(S1)

0.03

(S2)

0.09

(S3)

0.27

(S4)

0.50

(S5)

0.70

(S6)

0.80

(S7)

ARG

Vm /m3

174.72

174.37

174.03

172.76

170.90

169.51

168.80

Vf (103) /m3mol-1

-39.6321

-39.6497

-39.6818

-39.7207

-39.8930

-39.9859

-40.2878

Πi (10-9) /Pa

1.8681

2.2869

5.8991

21.7469

38.9151

51.2695

57.8758

Z (102)/kgm-2S-1

14.8997

14.9216

14.9970

15.3272

15.7283

16.0347

16.2029

RA

1.0005

1.0027

1.0037

1.0061

1.0120

1.0165

1.0187

LVS-ARG

 

Vm /m3

174.90

174.55

174.08

172.65

170.84

169.51

168.96

Vf (103) /m3mol-1

-39.6116

-39.6658

-39.6808

-39.7405

-39.8607

-39.9956

-40.3710

Πi (10-9) /Pa

2.0004

2.5407

6.4499

23.2279

39.8549

53.6028

58.1378

Z (102) /kgm-2S-1

14.8887

14.9126

14.9980

15.3526

15.7423

16.0748

16.1934

RA

0.9993

1.0014

1.0031

1.0063

1.0121

1.0156

1.017

 


DISCUSSION:

Refractive Index:

It was observed that the values of ηD of water (SD0) at the experimental temperatures were slightly lower than the LVS-ARG (SD1-SD7) solution systems. Additionally, (Fig. 1) and (Fig. 2) show an upward trend of ηD value with an increase in concentration of both ARG and LVS-ARG solution systems. It could be deduced that an increased presence of tightly packed molecules resulted in high refractive indices since light would travel slower in the medium22. Meanwhile, ηD value decreased with an increase in temperature for LVS-ARG system where the ηD value for LVS-ARG system was greater than that of ARG at high concentration (SD7). This could be due to decreased interaction between component molecules with the rise in temperature23.


 

Fig. 1: Refractive Indices Reading (nD) against Concentration (mol/dm3) for ARG Solution at Temperature 298.15 K(♦), 303.15 K (■), 308.15 K (▲), 313.15 K (×).

 

 

Fig. 2: Refractive Indices Reading (nD) against Concentration (mol.dm-3) for LVS-ARG Complex at Temperature 298.15 K(♦), 303.15 K (■), 308.15 K (▲), 313.15 K (×).


The RD values for the studied system show the same trend as that of the ηD values where those of the LVS-ARG system are higher as compared to ARG. The refractive indices increase with an increase in the concentration of ARG molecules. An efficient packing of ions in the solution systems and the ion arrangement resulted in high refractive index values which proves that solubility for LVS in LVS-ARG system is enhanced in the presence of ARG24.

 

Since graphs of RD values against concentration gives out similar trend at all experimental temperature, only RD values at 303.15 K were illustrated to represent the relationship in (Fig. 3) and (Fig. 4) as a function of ARG and LVS-ARG systems, respectively.

 

Fig. 3: Molar Refractive Indices (RD) against Concentration (mol.dm-3) of ARG System.

 

 

Fig. 4: Molar Refractive Indices (RD) against Concentration (mol.dm-3) of LVS-ARG System.

 

Plots in (Fig. 3) and (Fig. 4) display a linear upward trend with an increase in ARG concentration in both solution systems. The slopes of the lines in both plots were very similar, thus indicating that the rate of change of molar refraction was almost identical. RD is directly proportional to the molecular polarizability17. This relation could be seen in (Fig. 3) and (Fig. 4) which revealed that the general polarizability of the ARG and LVS-ARG solution increased with the cosolute and solute content. Additionally, varying degree of tight packing resulted LVS-ARG to have maximum solute-solvent interaction as compared to ARG.

 

Volumetric Studies:

From Table 4 values of ΦV0 are observed to be positive at all experimental temperatures. It is a measure of solute-solvent interaction for LVS-ARG system and ion-solvent interaction for ARG system where the positive value indicates strong solute-solvent and ion-solvent interactions. With increase in temperature for both systems, the ion-solvent and the solute-solvent interactions also increase except at 311.15K. This phenomenon promotes the structure-making effects of the LVS in aqueous ARG systems.

 

The values of SV are observed to be negative at all experimental temperatures except at higher temperature for LVS-ARG system which indicated absence of ion-ion or solute-solute interaction in the system. SV values of ARG-LVS system were smaller as compared to that of ARG system. This suggested that the structure of the solvent was enhanced in presence of LVS, which follows our previous assumption.

 

At all experimental temperatures, the values of ΔtΦV0 are observed to be positive (Table 4). They however decrease as the temperature increases. Strong interactions between LVS and the solvent (water) are indicated by the positive values of ΔtΦV0. It could also be due to water molecules being withdrawn from ions (the cation and anion of the ARG) and drug (LVS) molecules. The values are decreased as the temperature increased indicating lesser net solvation caused by overlapping cospheres, effectively destroying the interactions. This might enlarge the drug (solute) volume and cause ARG to lose its effect on the water structure due to the strong interaction between LVS and ARG.

 

In Table 4, ΦE0 values for both ARG and ARG-LVS systems at all experimental temperatures are listed. From observation, values of SE were negative in ARG system without LVS and positive for ARG system with abundant LVS. Negative values of ΦE0 provide an indication of insignificant caging or packing effect, which indicate that the structure of solvent was enhanced.

 

Sound velocity:

Table 5 shows that the sound velocity, (U) increased with an increase in the concentration of the solute for both solution systems. The sound velocity value was, however, slightly higher in LVS-ARG compared to ARG solution. This indicated that there was higher presence of molecules and intermolecular hydrogen-bonding in the LVS-ARG solution system, the magnitude of the speed of sound through the liquid system was enhanced25,26. This could be supported by the higher density values of the LVS-ARG.

 

Table 5 also deduces that at a fixed temperature, KS values show a declining pattern with an increase in concentration of ARG in both ARG and LVS-ARG system. Since KS values are summation of contribution from solvent intrinsic and solute intrinsic, solute intrinsic which is dominant over solvent intrinsic gives the combined effect of solvation of ions and breaking of the structure of LVS molecules27. KS values for ARG were slightly higher than LVS-ARG except for S1, S2 and S7. It could be due to the dissociation of ARG and the following ion-pair formation and due to complex structure formation in the presence of LVS. KS also reflects the compactness of the hydration layers around the core of the solute, hence the isentropic compressibility may be decreased due to the reorientation of ARG molecules which then leads to self-association and formation of a cage that can fit a hydrophobic molecule, by reducing the effective hydrophobic surface, in this case the LVS molecule. In short, the presence of water insoluble LVS causes electrostriction on the medium as a result of decreased isentropic compressibility and internal pressure increase28. The apparent isentropic molar compressibility, KSՓ of the system is presented in Table 5. The values were negative for both systems. The negative values are associated with the strong attractive interactions between the solute and solvent due to solvation of the solute.

 

Acoustic impedance is the ratio of the instantaneous pressure excess on any solute/substance to its instantaneous velocity. When sound wave travels in a medium, variations of pressure from one particle to another occur. This occurrence is controlled by inertial and elastic properties of the medium29. Table 5 shows the calculated values of acoustic impedance, Z where the value increased with an increase in the concentration of ARG for both systems. This indicated that increase in concentration elevated the internal pressure and molecular interactions became stronger due to closer packing structure of solute and solvent molecules by the formation of H-bond in solutions29. This observation complied with the results of the internal pressure πi.

 

Table 6 also gives the values of internal pressure and free volume of the ARG and LVS-ARG solution system. The internal pressure is a parameter of solute-solvent interactions and indicates both the attractive and repulsive molecular interactions. Meanwhile, free volume is the effective volume accessible to the centre of a molecule in a liquid. Strong repulsive forces in the liquid along with the relatively weak attractive forces (which provide the internal pressure that holds the molecules together) are two factors that determine the structure of a liquid.

 

Internal pressure, πi is sensitive to attractive forces while free volume, Vf is responsive to the repulsive forces. Together, these factors determine the entropy (i.e., disorderliness) of the system. The values of πi were found to be positive and increased with an increase in the concentration. On the other hand, the values of Vf, were negative and decreased with an increase in ARG concentration for both systems. Strong intermolecular interaction is indicated by the positive values of πi which enhance the structure of water. Values of πi and isentropic compressibility correspond with each other. Meanwhile, Vf results showed negative values which suggested the weakening of cohesive forces that later caused disruption of the structure of water in systems that contains ARG molecules and LVS due to entrapment of water molecules in spaces created by aggregation of the LVS-ARG complex30.

 

The extent of association in solutions could be analysed using the relative association (RA) parameter. Generally RA values are governed by two factors that increase or decrease the value which are (i) breaking up solvent structure upon the addition of a solute which causes a declining pattern in RA values and (ii) successive solvation of solutes by solvent molecules will result in an inclining pattern in RA values. Table 6 shows RA values in both solution systems. It is known that slight addition of additive, i.e., structure breakers will increase the cohesion between molecules by breaking the open structure29. Hence in this case RA values rose with the increase in ARG concentration in both systems suggesting that the solute-solvent interaction is associated by solvation of solutes by solvent molecules.

 

CONCLUSION:

In this study, sound velocity was determined at 298.15 K (Table 5) and refractive index of various concentrations of ARG and LVS-ARG was determined at 298.15-313.15 K (Table 3 and Table 4). The nD of aqueous solutions of all systems was higher than that of water and increased with the concentration. The trend of RD values of the system was the same as that of the nD values where in the case of LVS-ARG was larger than ARG. nD and RD values indicated maximum interactions and polarizability within the systems and the results were in agreement with our solubility findings, where solubility of LVS was noticeably enhanced. The positive value of ΦV0 illustrates a strong solute-solvent and ion-solvent interaction in both ARG systems. The value of SV indicated solute-solvent interactions that prevail at the highest temperature for LVS-ARG system (Table 4).

 

The ultrasonic velocity (U) increased with the concentration in all systems. Aqueous solutions of LVS-ARG have higher values of U compared to ARG solution. Values of acoustic parameters such as isentropic compressibility (KS), internal pressure (πi), acoustic impedance (Z) and free volume (Vf) complement each other. The positive value of πi indicated that there was a strong intermolecular interaction leading to the enhanced structure of water. Values of Vf are negative and decrease with an increase in the cosolute/solute concentration. Values of RA in the case of ARG systems showed a regular pattern whereas that of LVS-ARG exhibited an irregular correlation with concentration. When compared among the systems, the presence of LVS, resulted in an increase of RA values suggesting that the solute solvent interactions were associated with the solvation of solutes by solvent molecules.

 

ACKNOWLEDGEMENT:

The authors are thankful to Faculty of Pharmacy, University Teknologi Mara (UiTM) for support and cooperation in the completion of this study. This study was supported by the Fundamental Research Grant Scheme (600-IRMI/FRGS 5/3 (19/2016)), Ministry of Higher Education, Government of Malaysia.

 

CONFLICT OF INTEREST:

The authors report no conflicts of interest. The authors alone are responsible for the content and writing of this article.

 

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Received on 13.08.2020           Modified on 16.10.2020

Accepted on 26.11.2020         © RJPT All right reserved

Research J. Pharm. and Tech. 2021; 14(7):3631-3638.

DOI: 10.52711/0974-360X.2021.00628