Determination and modeling of caffeine solubility in N-methyl-2-pyrrolidone + propylene glycol mixtures

https://doi.org/10.1016/j.molliq.2021.117613Get rights and content

Highlights

  • Solubility of caffeine solubility in NMP + PG at different temperatures.

  • Correlation/back-calculation of the solubility data by some cosolvency models.

  • Calculation of thermodynamic parameters by using the van’t Hoff and Gibbs equations.

Abstract

The thermodynamics and solubilization behavior of caffeine in non-aqueous binary mixtures of N-methyl-2-pyrrolidone (NMP) and propylene glycol (PG) at temperatures ranged from 293.2 to 313.2 K are measured using a shake-flask method and the obtained solubility data are mathematically represented by using some cosolvency models (e.g. Jouyban-Acree, Jouyban-Acree-van’t Hoff, the mixture response surface, the double log–log and the modified Wilson) and their accuracy is investigated by computation of the mean relative deviations (MRD%) for back-calculated data. The density values of caffeine saturated solutions are determined and represented by Jouyban-Acree equation. Moreover, the apparent thermodynamic parameters of the caffeine dissolution process in the binary mixture of NMP and PG are computed using the Gibbs and van’t Hoff equations at mean harmonic temperature and discussed.

Introduction

Caffeine (3,7-dihydro-1,3,7-trimethyl-1H-purine-2,6-dione, Fig. 1) is a naturally occurring compound that is categorized as a psychoactive drug and mild stimulant [1]. Caffeine enhances visuospatial reasoning, memory and reaction time task performance in the elderly [2]. It is a factor in people's well-being, good physical performance and positive mood due to the secretion of dopamine in the brain [3], [4]. Caffeine is available as ampoule, tablet, gum, and capsule in the pharmaceutical market. It is also naturally found in the fruits, leaves and seeds of > 63 plant species worldwide including cocoa, Yaupon Holly, guarana and yerba mate. Diet pills and cosmetic manufacturers are considered the largest consumers of caffeine. Moreover, it is also employed in manufacturing body wash, lip balm, soap and facial scrub [5]. Various methodologies have been developed to extract caffeine from its natural sources such as water extraction, supercritical carbon dioxide extraction and organic solvent extraction. The extraction is performed by simply adding a portion of solvent to the liquid which contains dissolved caffeine. However, water is the most widely used liquid in the liquid–liquid extraction procedure, the use of organic solvents also has a special place and wide consumption [5]. Moreover, it is proved that coffee and beverages without caffeine is associated with many unique health benefits, including increased longevity and decreased risk of multiple cancers and chronic diseases. So, decaffeination can be a useful procedure for these productions. The conventional decaffeination process is extracting caffeine with an organic solvent that is based on the solubility property of caffeine or their ingredients in the used solvents. Knowing caffeine solubility can be helpful for these procedures and with the more information database available about caffeine solubility, pharmacists, chemists, and engineers will be able to make the right decision about the best solvent/antisolvent system for caffeine extraction [6], [7].

So far, the solubility profile of caffeine has been studied in monosolvents of chloroform, ethyl acetate, ethanol, carbon tetrachloride, water, dichloromethane, methanol and acetone at 298–323 K [8], 1-propanol, ethyl acetate, ethanol, methanol at 288.15 to 328.15 K [9], aqueous mixture of polyethylene glycol 400 at 298.2 K [10], dioxane at 298.2 K [11], and N,N-dimethylformamide (DMF) at 298.2 K [12] and non-aqueous mixtures of (carbitol + ethanol), (N-methyl-2-pyrrolidone (NMP) + ethanol), (NMP + 2-propanol), (NMP + 1-propanol), and (NMP + ethylene glycol) that are our previous works. But there is no report for the solubility of caffeine in the binary mixture of NMP and propylene glycol (PG). Caffeine is available in two crystalline forms (i,e. anhydrous and mono hydrated) that the used form of caffeine in the current study is anhydrous. NMP as a cosolvent in this work is categorized in class 2 of residual solvents with limited usage in drug substances, excipients, and drug products [13].

To provide a solubility database for caffeine in the cosolvency systems, the goals of this study are to (1) investigate the solubility and density of caffeine saturated solutions in the mixed solutions of NMP and PG at different temperatures; (2) correlate the data with reported cosolvency models; and (3) calculate the apparent thermodynamic properties for caffeine dissolution process in the mixed solvents of NMP and PG.

Section snippets

Materials

Caffeine (mass fraction purity of 0.997, Dana Pharmaceutical Company, Iran), NMP (mass fraction purity of 0.980, Merck, Germany), PG with mass fraction purity of 0.999 (Merck, Germany) are the materials used in the preparation of the saturated mixtures. Ethanol with mass fraction purity of 0.935 (Jahan Alcohol Teb, Arak, Iran) is employed for dilution purposes before spectrophotometric measurements.

X-ray power diffraction (XRPD) analysis

The crystal of caffeine is confirmed by XRPD carried on PHILIPS PW1730 (Holland). The XRPD data

Solubility profile of caffeine in the mixtures of NMP and PG and data modeling

The solubility data of caffeine in the non-aqueous mixture of NMP and PG measured at different temperatures (293.2–313.2 K) along with the standard deviation of replicated determinations are listed in Table 1. As can be seen, the solubility of caffeine will be raised by increasing both the mass fraction of NMP and the temperature; so that the lowest value is observed in neat PG at 293.2 K (xm = 9.88 × 10–4) and the highest one is observed for neat NMP at 313.2 K (xm = 1.90 × 10–2).

Additionally,

Conclusions

In the study ahead, experimental mole fraction solubility data of caffeine in the binary non-aqueous mixtures of NMP and PG at various temperatures are determined and correlated with some reported cosolvency models. Obtained MRDs% for all used models are < 11.0 indicating the capability of these models for correlating/predicting of solubility data. The apparent thermodynamic parameters for the caffeine dissolution process are also determined based on Gibbs and van't Hoff equations. The results

CRediT authorship contribution statement

Homa Rezaei: Investigation. Elaheh Rahimpour: Data curation, Writing – review & editing. Hongkun Zhao: Data curation. Fleming Martinez: Data curation, Writing – original draft. Abolghasem Jouyban: Supervision, Writing – review & editing.

Declaration of Competing Interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Acknowledgements

The research protocol was approved and supported by the Student Research Committee under grant number 67496 Faculty of Pharmacy, Tabriz University of Medical Sciences, Tabriz, Iran.

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