versão impressa ISSN 1516-8913
Braz. arch. biol. technol. v.47 n.6 Curitiba nov. 2004
ENGINEERING AND TECHNOLOGY
Marcia Regina PanseraI, *; Gelson Antonio IobI; Ana Cristina Atti-SantosI, II; Marcelo RossatoI, III; Luciana Atti-SerafiniI, II; Eduardo CasselIV
IInstituto de Biotecnologia; Universidade de Caxias do Sul; Rua Francisco Getúlio Vargas, 1130; 95001-970; Caxias do Sul - RS - Brazil
IIDepartamento de Física e Química; Universidade de Caxias do Sul; Rua Francisco Getúlio Vargas, 1130; 95001-970; Caxias do Sul - RS - Brazil
IIIDepartamento de Ciências Exatas e da Natureza; Universidade de Caxias do Sul; Rua Francisco Getúlio Vargas, 1130; 95001-970; Caxias do Sul - RS - Brazil
IVFaculdade de Química e Faculdade de Engenharia; Pontifícia Universidade Católica do Rio Grande do Sul; Av. Ipiranga, 6681; 90619-900; Porto Alegre - RS - Brazil
Studies were carried out on solvent and supercritical extraction to obtain natural tannins. The results showed that the best co-solvent to extract tannin with CO2 supercritical was water with a concentration of 5.0% and the best trap rinse solvent was methanol.
Key words: Co-solvents, tannin, CO2 supercritical
Neste trabalho foram utilizados dois processos de extração de tanino vegetal: extração a quente em aparelho Soxhlet e extração com CO2 supercítico. Os resultados mostraram que o melhor co-solvente para extração de taninos com CO2 supercrítico foi a água na concentração de 5% e o melhor solvente para lavagem do trap foi o metanol.
Tannins are polyphenolic compounds present in plants, foods and beverages (Makkar and Becker, 1998) which are soluble in water and polar organic solvents (Haslam, 1996). Tannin of Acacia mearnsii finds application in the natural tannage of leather, as alternative procedure instead of leather chromium tannage. The traditional tannage process, with chromium, is highly polluent. Brazil produces about 40,000 ton/year of the tannins which represents 90% of the world extracted from Acacia mearnsii (Deixheimer, 1998). The process used to extract tannins is the hydrosolubilization. Because this process operates with temperatures around 100°C, the extraction process motives a hydro cracking of sugar and others organic compounds with a darkening of the final product.
We studied the supercritical extraction process as alternative procedure to obtain the natural raw material to leather tannage (Readel, 2001). In which supercritical carbon dioxide and polar or non-polar co-solvents were used as solvents. The advantages of supercritical extraction process with regard to hydrosolubilization and solvent extraction are low extraction temperature, short extraction time and absence organic solvent concentration in the extract. Another objective was to compare the different extraction technology (Taylor, 1996).
MATERIAL AND METHODS
The raw material, black acacia bark, was provided by EXTRATOS BRASIL. A part of bark was milled with cutting mill (TECNAL - Willye TE 650) with 2.0 mm average particle diameter. In the solvent extraction with Soxhlet apparatus, dry natural material was employed. The dryer used was a BIOMATIC Equipment. The tannin was dried for 10 days at 36°C.
Solvent Extraction Process
Samples (50 g of dark acacia bark) were extracted with 500 mL of solvent for 24 h. The extracted solution was concentrated on a SAVANT Lyofilizator.
Supercritical Extraction Process
A Hewlett Packard 7680 extraction module was used to perform all the experiments. This system consisted of a nozzle/trap assembly that acted as a controllable variable restrictor, allowing an instantaneous depressurization of the supercritical fluid as well as the decoupling of flow and pressure. The material to be extracted was loaded into a self-sealing extraction cell of 7.0 mL thick-walled stainless steel thimble. Supercritical fluid extracts were deposited in an internal trap rinsed off into a vial with 1 mL of hexane and methanol. Samples (0.4 g of bark) were extracted with supercritical carbon dioxide according to the described procedure, where different experiments to optimize the extraction conditions were done. The operation temperature and pressure ranges tested were 40 to 80ºC and 150 to 200 bar, respectively. All other variables were kept constant: CO2 flow, 2.0 mL/min; and extraction time, 30 minutes. The pressure and temperature conditions tested in experiments are shown in Table 1.
The identification of tannins was made by thin layer chromatography (TLC). The analyses were run with standard compounds, catequin and tannic acid, using aluminum cromatofoils. Plates were developed using ethyl acetate:acetic acid (20:4) as the mobile phase. After drying, tannic acid was viewing using FeCl3 (Sharma et al., 1998).
The quantification of tannins was made by spectrophotometry (BECKMANN Model Life Science). Standard solutions were formulated by Folin Denis reagent and the calibration curve was developed at 725 nm (Seigler et al., 1986).
RESULTS AND DISCUSSION
Solvent Extraction Process
Three organic solvents were tested to obtain the tannin with Soxhlet Apparatus: ethanol, dimethyl ether, and n-hexane. The experimental results, using TLC showed that n-hexane and dimethyl ether solubilizated only non-polar organic compounds presented in acacia bark, while the ethanol extracted the tannin compounds. The results for ethanol extract can be seen in Fig. 1.
With regard to quantification of tannins by ethanol, using spectrophotometry analysis, the results are written in Table 2. Sample 1 presented higher tannins concentration, but a milled and dry bark was not feasible in the industrial process.
Supercritical Extraction Process
The supercritical carbon dioxide extraction did not present good results. As alternative on selectivity and quantity augment of extracts obtained was co-solvents addition (Taylor, 1996). Four solvents as co-solvents were tried in the process: acetone, methanol, ethanol and water. The co-solvents concentration employed in the experiments to select the best tannins extraction was 5.0 % with regard to carbon dioxide quantity. Fig. 2 showed the concentration of the tannins, percent tannins in acacia bark (p/p), obtained with co-solvents extractions.
To define the best temperature and pressure condition, after selecting water as the best co-solvent, the extraction experiments were carried with 2.0 mL/min during 30 min. Ten experiments were realized changing temperature and pressure conditions, respectively (40 to 60° C; and 150 to 200 bar). The results are presented in Table 3.
Results showed T = 60°C and P = 200 bar as the best conditions to extract tannins. Figure 3 showed the presence of tannic acid in the supercritical extract.
Results indicated the possibility of changing the traditional process (hydrosolubilization) that resulted approximated 20 % of tannins from Acacia mearnsii (Graebin, 2000).
The solvent laboratory experiments with Soxhlet Apparatus were important in this study to demonstrate the poor tannin extraction with non-polar solvents. The complexity of natural tannins molecules demand experiment test to choose the solvent, therefore it was tried solvents with different polarity.
Research supported by Universidade of Caxias do Sul, Fundação de Amparo à Pesquisa do Estado do Rio Grande do Sul - FAPERGS, Secretaria de Estado da Ciência e Tecnologia and CNPq.
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Received: March 17, 2003;
Revised: January 27, 2004;
Accepted: July 02, 2004.
* Author for correspondence