New Processes to Extract Pure Betacarotenes Molecules Using Acetic Acid Solvent
Andry Tahina Rabeharitsara, Phandry Nomena Ndjiva Rabearimihaja
Department Chemical Engineering of E.S.P.A, Antananarivo University, Antananarivo, Madagascar
To cite this article:
Andry Tahina Rabeharitsara, Phandry Nomena Ndjiva Rabearimihaja. New Processes to Extract Pure Betacarotenes Molecules Using Acetic Acid Solvent. American Journal of Applied Chemistry. Vol. 4, No. 2, 2016, pp. 64-70. doi: 10.11648/j.ajac.20160402.15
Received: February 23, 2016; Accepted: March 10, 2016; Published:March 28, 2016
Abstract: Betacarotenes molecules extractions using acetic acid (99% of purity) as solvent followed by distillated water neutralization or hexane solvent to get back betacarotenes. To obtain pure betacarotenes molecules, distillation step is necessary for the second process which use hexane solvent; however for the first process which use distillated water neutralization, decantation step is enough. The first process is energetically profitable. Unrefined palm oil which contains betacarotenes molecules with triglycerides and grease acids is used as model product for betacarotenes extraction. Both of the two processes have extraction rate more than 27% which increases proportionally with the weight of unrefined palm oil used for extraction.
Keywords: Extraction, Betacarotenes, Acetic Acid, Hydrogen Bond, Process, Neutralization, Decantation
Betacarotenes molecules have been widely used in food and pharmaceutical industries. They were seen in many natural products such as: palm grains, carrots, tomatoes, spinach, etc.… . Betacarotenes molecules have been obtained by chemical synthesis or by extraction. This paper show two news processes to extract betacarotenes molecules. The main of these processes is the first step which use acetic acid 99% purity like solvent extraction. Then, the first process use distillated water to obtain pure betacarotenes molecules after decantation whereas solvent hexane is used for the second process and distillation is necessary to separate pure betacarotenes molecules. The first process is energetically profitable than the second process which need energy to evaporate the solvent "hexane" under vacuum for getting back the pure betacarotenes molecules. Unrefined palm oil which contains betacarotenes molecules with triglycerides and grease acids is used as model product for betacarotenes extraction. Both of the two processes have extraction rate of pure betacarotenes more than 27% which increases proportionally with the weight of unrefined palm oil used for extraction.
2. Acetic Acid Extraction Followed by Water Neutralization
2.1. Principle of the Process Betacarotenes Extraction with Acetic Acid Followed by Water Neutralization
It was shown that hydrogen bond link  exist between betacarotenes molecules and animal’s grease or betacarotenes molecules and vegetable’s grease. The hydrogen bond is an attractive interaction between a hydrogen atom from a molecule or a molecular fragment X–H in which X is more electronegative than H, and an atom or a group of atoms in the same or a different molecule, in which there is evidence of bond formation. A typical hydrogen bond may be depicted as X–H … Y–Z, where the three dots denote the bond. X–H represents the hydrogen bond donor. The acceptor may be an atom or an anion Y, or a fragment or a molecule Y–Z, where Y is bonded to Z. In some cases, X and Y are the same. In more specific cases, X and Y are the same and X–H and Y–H distances are the same as well leading to symmetric hydrogen bonds. In any event, the acceptor is an electron rich region such as, but not limited to, a lone pair of Y or π-bonded pair of Y–Z. . That is why carotenoids are soluble in animal’s grease and vegetable’s grease . During their transfers between the various levels of the trophic networks, the carotenoid pigments are not appeared as isolated molecules: they are often related to other molecules which allow their integration in the cellular structures of the living matter, and thus they are met integrated in lipoproteins, caroténoprotéines or caroténolipoprotéines. They play also a part in the pigmentation, coloring, but also in the reproduction and seem to be at the origin of the visual pigments . Unrefined Palm oil contents are betacarotenes, grease acids and Triglycerides. That is why the color of the unrefined palm oil "Fig. 1".
The goal of this extraction process is to break the hydrogen bond links between betacarotenes molecules and triglycerides or grease molecules by acetic acids molecules. At the end, betacarotenes molecules will be on hydrogen bond link with acetic acids molecules. Next, distilled water is added progressively. Betacarotenes molecules, which are insoluble in water, became on top up to gather. Underneath, there is acid acetic solution which are up to gather because of hydrogen bond link: cycle dimer of acetic acid [6-7], the molecules form pairs (dimers), being connected by hydrogen bonds. The dimers can also be detected in the vapor at 120°C (248°F) . Dimers also occur in the liquid phase in dilute solutions in non-hydrogen-bonding solvents , and a certain extent in pure acetic acid but are disrupted by hydrogen-bonding solvents. The dissociation enthalpy of the dimer is estimated at 65.0–66.0 kJ/mole, and the dissociation entropy at 154–157 J mol−1 K−1 . Other lower carboxylic acids dimerize in a similar fashion .
2.2. Details of the Process Betacarotenes Extraction with Acetic Acid Followed by Water Neutralization
2.2.1. Step 1 Reagents Preparation
Unrefined palm oil is weighed then put in the beaker. Next, acetic acid 99% of purity is added "Fig. 7". Its pH is equivalent to pH = 3.27. The majority of the acetic acid molecules (pKa = 4.76) are on not dissociated (R-COOH) acid form "Fig. 2" [10-11-12-13-14-15-16].
2.2.2. Step 2 Mixing Reactants
Unrefined palm oil and acetic acid are mixed for few minutes "Fig. 7". Hydrogen bond links between triglycerides molecules or grease acids molecules and betacarotenes molecules are broken "Fig. 3" by the acetic acid solvent. From this moment, steric attraction begin between acetic acid molecules and betacarotenes molecules and supports their hydrogen bond links. Steric attraction occurs when molecules have shapes or geometries that are optimized for interaction with one another. In these cases molecules will react with each other most often in specific arrangements .
2.2.3. Step 3 Formation of Hydrogen Bond Links Between Betacarotenes Molecules and Acetic Acids Molecules
Transvase the mixed solution in the funnel, and let it rest during thirty minutes "Fig. 7". Hydrogen bond links between acetic acid molecules and betacarotenes molecules have taken seat "Fig. 4".
Two phases are observed. Betacarotenes molecules with acetic acid are underneath and on top there were triglycerides molecules and grease acids molecules "Fig. 5". Next, we take off the underneath phase which was rich on betacarotenes. To improve the betacarotenes extraction, we have added acetic acid in the rest of on top phase which became rich on triglycerides and grease acids molecules, then we take off the underneath phase. We repeat this action twice and get back together the acetic acid-betacarotenes solution. Liquid acetic acid is a hydrophilic (polar) protic solvent, similar to ethanol and water.
With a moderate relative static permittivity (dielectric constant) of 6.2, it dissolves not only polar compounds such as inorganic salts and sugars, but also non-polar compounds such as oils and elements such as sulfur and iodine. It readily mixes with other polar and non-polar solvents such as water, chloroform, and hexane. With higher alkanes (starting with octane), acetic acid is not completely miscible anymore, and its miscibility continues to decline with longer n-alkanes . This dissolving property and miscibility of acetic acid makes it a widely used industrial chemical, for example, as a solvent in the production of dimethyl terephthalate .
2.2.4. Step 4 Water Neutralization of the up to Gather Phase Rich on Betacarotenes
Distillated water is added progressively in the up to gather phase rich on betacarotenes which are soluble in acetic acids 99% "Fig. 7". The water play the basic role (H2O/H3O+) [20-21]. In the same time, the acetic acids-betacarotenes solution will be diluted in water and the pH of the solution increase progressively to seven. This is the neutralization step by distillated water. The acetic acid (pKa=4.76)  will be dissociated [R-COO-/H+] and soluble in water because hydrogen bond links between betacarotenes molecules and acetic acid molecules was broken "Fig. 6-a". Betacarotenes molecules which are insoluble in water became on top to gather. At last, we get back the betacarotenes "Fig. 6-b" by decantation process "Fig. 7".
2.3. Flow-Sheet of the Process Betacarotenes Extraction with Acetic Acid Followed by Water Neutralization
The β-Carotene extracted is a strongly colored red-orange "Fig. 8-a". It is a pigment abundant in plants and fruits. Beta-carotene is a well-known antioxidant . Eating a diet rich in them is often recommended. Benefits from taking supplements are not supported [25-26]. It is an organic compound and chemically is classified as a hydrocarbon and specifically as a terpenoid (isoprenoid). The structure was deduced by Karrer et al. in 1930 with eleven double combined connections  "Fig. 8-b". The chemical formula of betacarotenes is C40H56. It is insoluble in water with 1.05 [g.ml-1] density. Its molar mass is equal to 536.8726 [g. mol-1]. And its boiling point is 654.7 [°C] at 760 [mmHg]. Betacarotenes are soluble in hexane solvent.
The experimental results of beta-carotene solubilities in binary mixed solvents formed by cyclohexane, n-hexane, 1-hexene and toluene with 2,5,8-trioxanonane, acetone, and cyclohexanone are reported. The solubility of beta-carotene in pure solvents increases in the order: 2,5,8-trioxanonane < acetone < n-hexane <1-hexene < cyclohexanone < cyclohexane < toluene. In the mixed solvents studied a maximum of beta-carotene solubility is observed, except for the mixed solvents containing toluene. The reported solubility data for binary solvents were smoothed by means of Myers and Scott rational type equation. These results together with our previous results for hydrocarbon polar non-associating component are interpreted in terms of various models of mixtures. For this purpose models based on the Flory and Huggins non-athermal mixture theory, such as Acree and Rytting (AR), and the authors (TT) model, are tested. Both models predict qualitatively size and shape of the beta-carotene solubility curves, including the maximum solubility and asymmetry, in contrary to UNIFAC model. The analysis of the TT and AR models indicate an important role of value and asymmetry of the excess Gibbs energy of the mixtures of solvents as a source-increased solubility. The difference between the solubility of beta-carotene in pure solvents and value of the excess Gibbs energy are responsible for the appearance, position and shift of the maximum solubility .
3. Acetic Acid Extraction Followed by Hexane Separation
3.1. Principle of the Process Betacarotenes Extraction with Acetic Acid Followed by Hexane Separation
The principle and steps of this second process are the same than the first process as far as step3 "Fig. 7" - "Fig. 9". The difference is on step4, to break the hydrogen bonds links between betacarotenes molecules and acetic acid molecules, we use hexane solvent. Betacarotenes are soluble in hexane "Fig. 9". We have transvased the solution in the funnel. Let it rest for thirty minutes. There were two phases, the underneath solution was acetic acids and on top there were betacarotenes molecules soluble in hexane (dhexane=0.655 g.cm-3) "Fig. 9". To separate these two phases we use decantation for thirty minutes and take off the acetic acid "Fig. 9". Then, to get back the betacarotenes, we have done first distillation of the hexane on rotavapor (TebHexane=68.73°C) "Fig. 9". The evaporator consists of a heating bath with a rotating flask, in which the liquid is distributed as a thin film over the hot wall surfaces and can evaporate easily .
3.2. Flow-Sheet of the Process Betacarotenes Extraction with Acetic Acid Followed by Hexane Separation
4. Comparisons Between the Two Processes
The weight of betacarotenes extracted change proportionally with the weight of unrefined oil used for extraction "Fig. 10 – Table 1". In this way we can assert that with both processes we have extracted pure betacarotenes molecules "Fig. 8". The extraction yield is between 27% and 38%. In other words, the betacarotenes content in 5[g] of the unrefined palm oil for example is 1.365[g], either 27.3%. It increase proportionally with the weight of unrefined palm oil used for extraction.
|Unrefined palm oil quantity used for extracting [g]||Betacarotenes quantity extracted by the first process using acetic acid followed by water neutralization [g]||Betacarotenes quantity extracted by the second process using acetic acid followed by hexane separation [g]|
As we see in figure 11 the extractions yield of the first process and second process are equally good. However, the second process seems all the same good when the unrefined oil quantity used for extraction increases. In any case using the first process is energetically profitable. It doesn’t use any energy source during the process. However, the second process uses energies during the last stage of distillation which makes it possible to separate the pure molecules of betacarotenes from the solvent hexane .
Special Thanks to everyone who have supported and helped us to carry out this paper. As well, we express our sincere thanks to Director of E.S.P.A Polytechnics of the Antananarivo University and Chemical Engineering Laboratory staff. Special thanks to the company Savonnerie Tropically for giving us unrefined palm oil used during the experiences.