versão impressa ISSN 0103-5053
J. Braz. Chem. Soc. vol.23 no.4 São Paulo abr. 2012
A. M. Girelli*,I; L. SalvagniII; and A. M. TarolaII
IDepartment of Chemistry
IIDepartment of Management, Sapienza University of Rome, Piazza le Aldo Moro 5, 00185 Rome, Italy
The present study reports (i) the covalent immobilization of lipase on different cellulose supports (cotton buds, make-up remover pads, cellulose powder, cotton and tissues) using sodium periodate as activating agent and (ii) its application on the aged linseed oil removal from canvas. The optimization of experimental conditions such as pH, temperature and reaction time was performed for both, immobilization procedure and the biocatalyst application. Thus optimal conditions of immobilization were pH 7.0, 20 ºC, 0.3 mg lipase loading per mg support and 200 min reaction time, while those for treating canvas surface, having stratified aged linseed oil were pH 6, 40 ºC and 45 min reaction time. The ability of the immobilized lipase to remove aged oil films was confirmed by UV-Vis spectroscopy, high performance liquid chromatography (HPLC) and scanning electron microscopic (SEM) analysis.
Keywords: cleaning aged oil layers, lipase immobilized, cellulose support
O presente estudo relata (i) a imobilização covalente da lipase de Candida rugosa sobre diferentes suportes de celulose (cotonetes, algodão para remoção de maquiagem, pó de celulose, algodão e lenços), usando periodato de sódio como agente ativo, e (ii) suas aplicações na remoção de óleo de linhaça envelhecido, de telas. A otimização das condições experimentais como pH, temperatura e tempo de reação foi realizada para o procedimento de imobilização e para a aplicação do biocatalisador. Assim, as condições ótimas de imobilização foram pH 7,0, 20 ºC, 0,3 mg de lipase por mg do suporte e tempo de reação de 200 min, enquanto as condições necessárias para o tratamento da superfície de telas contendo óleo de linhaça envelhecido, foram pH 6, 40 ºC e tempo de reação de 45 min. A habilidade da lipase imobilizada em remover filmes de óleo envelhecido foi confirmada por análises de espectroscopia UV-Vis, cromatografia líquida de alta eficiência (HPLC) e microscopia eletrônica de varredura (SEM).
Enzymes are organic macromolecules present in all living organisms, which increase the rate of a substratum conversion. They have a high selectivity degree in the acceleration of specific chemical reactions. This happens without the formation of by-products, acting in aqueous solutions diluted in mild temperature and pH conditions.
Generally, hydrolases are used like amylases for polysaccharide degradation,1-3 proteases for proteic material degradation1,4 and lipases for fat material degradation in the restoration.2,4,5
In particular lipases are able to degrade lipids, organic molecules made of triacylglycerols.
The real problem of cleaning doesn't deal with the removal of unwanted material from the surface of paintings, but by doing it without removing, disturbing or otherwise altering the original design layer. This can be extremely difficult, especially if the solubility of the overlying layer is similar to the paint binder's one. Recently,6-10 biotechnological technique is considered a useful alternative to the mechanical methods supported by solvents, spirits, alkalis, acids and soaps. Indeed it can reduce the damage to artwork since they combine an aqueous medium, which is safer than conventional highly polar organic solvents or alkaline mixtures for the user. Moreover this technique is more specific and less aggressive action because mild conditions are required.11-14 Nowadays the use of enzymes is in free solution or in gel, but this use emphasizes many drawbacks like mould, opaque, craquelure and raising, due to water penetration in painting layers for the repetitive washings required to remove the enzyme which generally is not completely cleared.1,15
The aim of this paper is to immobilize the lipase covalently on appropriate supporting materials, in order to overcome the above cited inconvenients of the free enzyme and to allow repetitive uses. In addition, covalent immobilization offers greatest advantages such as increasing the stability of the enzyme and preventing it from leaking into the solution. Among the numerous supports available for lipase immobilization, cellulosic materials are chosen for their availability in different economic forms, such as powder, cotton buds, make-up remover pads and tissues. In addition they can be easily activated even if they do not have reactive groups for direct coupling of enzyme. In this paper the optimum experimental conditions of immobilization (pH, temperature, enzyme loading, reaction time, supports) of lipase from Candida rugosa and those concerning the removal of aged stratified linseed oil on the surface of canvas (temperature, pH, time) are presented. The study of fat compounds removed from layers treated enzymatically is made by UV-Vis spectrophotometric and HPLC analysis.
Lipase from Candida rugosa type VII (4780 U per mg protein), glutaraldehyde 25% (v/v), tributyrrin, NaH2PO4, Na2HPO4, NaIO4, CuSO4, phenophtalein, potassium acid phthalate and all the fatty acids are purchased from Sigma-Aldrich (Milan, Italy). The solvents acetonitrile and methanol HPLC-grade, n-heptane and potassium sodium tartrate are from Carlo Erba Reagents (Milan, Italy). The standard solution of KOH 0.1 mol L-1 is from Merck, while triethylamine and p-bromophenacil bromide from Fluka (Milan, Italy). Linseed fresh oil is from Kremer Pigments (Aichstetten, Germany). The supports employed are: cellulose powder (Fluka Ag. Buchs, Suisse), cotton buds (Sisma s.p.a., Fortex, Europe), disc make-up remover pads (supermarket PAM s.p.a.) and cotton and linen tissues.
Purified water from Milli-Q Ultra-pure water purification system (Millipore, Bedford, Mass., USA) is used to prepare both solutions and eluents.
Chromatographic analyses are performed with a Kontron system (Milan, Italy), consisting of a model 422 pump and a UV-Visible 432 detector, complete with a Rheodyne 7125 injector with a 20 μL sample loop (Rheodyne, Berkeley, CA, USA). The absorbance values of the effluent monitored are registered by an integrator system constituting a PC equipped with an Intel processor, Pentium III 800 MHz CPU, and Agilent ChemStation software for LC version A.08.03 (847) running under MS Windows NT 4.00.31 OS.
Spectrophotometric determinations are performed using a UV-Vis Uvikon 942 spectrophotometer (Kontron instruments, Milan, Italy) and cuvettes of 1 cm length.
Scanning electron microscope (SEM) model LEO 145VP is used to study the morphological properties of canvas before and after the enzymatic application.
The lipase immobilization procedure consists of two steps: cellulose oxidation and enzyme coupling to dialdehyde cellulose (DAC) supports.
Cellulose oxidationIn order to determine the best conditions, an oxidation of cellulose (ca. 70 mg) is carried out with 5 mL of 0.5 mol L-1 NaIO4 solution for 1-24 h at room temperature and darkness. After that, activated celluloses are filtered and washed several times with water. The formation of dialdehydic groups is confirmed by Fehling test and their amount can be determined spectrophotometrically by the absorbance decrease at 670 nm of the copper(II)-tartrate complex. The assay is based on the following steps: (i) reaction of activated cellulose (ca. 70 mg) at 100 °C with 3 mL of Fehling reactive obtained by mixing equal volumes of Fehling I (69.27g hydrated copper (II) sulphate dissolved in 1 L of distilled water) and Fehling II (362 g of potassium sodium tartrate and 100 g of sodium hydroxide in 1 L) for 10 min; (ii) 1:8.5 dilution of 0.4 mL solution with deionized water; (iii) determination of % copper(II) reacted, expressed as
where Ao and A are the absorbance at 670 nm of the Fehling reactive alone and with the DAC samples, respectively.
The amount of aldehydic groups in cellulose supports are finally determined by interpolation with a calibration curve obtained in the same experimental conditions (time, temperature) and employing as standard reference a dialdehyde, which reacts with Fehling test more similar to DACs. A good linear trend in the range 8-70% of Cu(II) reacted (equation y = 79.124x, r2 0.9889) is obtained plotting different glutaraldehyde amount in the range 0.05-1.2 mmol.
Lipase coupling to dialdehyde cellulose supports
DACs are then incubated with 4 mL of native lipase solution (50 mg crude lipase in 10 mL phosphate buffer pH 6, activity 8.7 mmoL min-1) at 20 °C for 200 min under low shaking. After binding, any unbound enzyme is removed by filtration and by washing the supports with at least 100 mL of water, afterwards with 100 mL 0.1 mol L-1 sodium phosphate buffer pH 6 and stored in this buffer at 4 °C until use. The effects of time, temperature, pH and enzyme loading on immobilized and removed activity ratio are investigated.
Lipase activity assay
The lipase activity in the initial and filtrate solutions as well as the immobilized lipase activity is estimated employing tributyrin as substrate. The reaction mixture of free lipase activity is constituted by 0.188 mL of tributyrin, 1.0 mL of phosphate buffer and 0.25 mL of lipase (final volume 1.138 mL), while that of immobilized lipase activity, by 2.5 mL of phosphate buffer, 70 mg of biocatalyst (dry wt.) and 0.38 mL of substrate (final volume 2.88 mL). Both the reaction mixtures are agitated and incubated for 15 min in the water bath at 30 °C. Then the enzymatic hydrolysis is stopped by adding 10 mL of methanol to the total volume of the first reaction mixture and to an aliquot of 1.5 mL of the second one. The fatty acids formed are quantified by titration with 0.05 mol L-1 hydroxide potassium. Activities are expressed as international units (IU), where 1 IU is defined as the amount of enzyme required to produce 1 µmol of free fatty acids per minute under the assay conditions (30 °C, pH 7) and so were determined by
where VKOH and Vo are, respectively, the KOH volume needed to titrate the samples and the respective blank, 1.92 is the factor which takes in account the aliquot (1.5 mL) prelevated from 2.88 mL of reaction mixture.
Removed activity ratio
This parameter, defined by Villanova et al.,16 represented the activity removed from the enzyme solution as a consequence of the enzyme immobilization as well as the inactivation which could be produced on the non-coupled enzyme due to its interaction with the support and the coupling conditions. The removed activity ratio is calculated by:
where A10 and A1200 are free lipase activity in the solution before and after the immobilization process, respectively.
Activity immobilization yield
The efficiency of immobilization is evaluated in terms of activity coupling yields. The activity coupling yield, hact (%) is calculated as follows:
where A2 is the immobilized lipase activity and A1 the free lipase activity.
Removal of linseed oil stratified on raw canvas by biocatalyst
An amount of fresh linseed oil is applied on small areas of raw canvas with a cotton swab and left for 2 weeks until to obtain a solid and transparent film. Successively the biocatalyst wetted in 0.1 mol L-1 phosphate buffer pH 7, is applied to the area and pressed by a weight, so that the contact lipase-oil is well done. In order to optimise the experimental conditions the system is left undisturbed for 15-60 min range at different temperature (25‑50 °C) in a thermostat. In the end, the lipase-cellulose support is removed and put in a glass tube in which 2.88 mL of extraction solvent (phosphate buffer, acetonitrile or n-heptane) is added. The products extraction is facilitated by sonication for 5 min. Their identifications are made by HPLC and by UV spectroscopy (210-350 nm range, 1 cm cell length and the respective solvent extraction as blank). The fatty acids presence in extracts obtained by the enzymatic treatment on canvas area with linseed oil stratified respect those obtained without any enzymatic treatment an adjacent area confirmed the hydrolytic action of lipase.
The HPLC analyses are carried out in two different chromatographic systems so that the short and long chains fatty acids could be discriminated.
In the first system, 20 µL of the extract in phosphate buffer or in acetonitrile are injected directly on a RP‑18 (25 cm × 4.6 mm ID) employing a mobile phase of H2O:CH3CN, 45:55 (v/v) containing 30 µL of formic acid (flow rate 0.8 mL min-1, λ = 220 nm and room temperature).
In the second system, 20 µL of phenacyl bromide esters of the fatty acids extracted in n-heptane are injected on a RP-18 (15 cm × 4.6 mm ID) employing a mobile phase of H2O:CH3CN, 17:83 (v/v) (flow rate 1.2 mL min‑1, λ = 242 nm and 45 °C). The derivatization process is made in accordance to literature.17 Briefly, to 250 µL of lipid extract, dried under stream of N2, are added 50 µL of a-bromoacetophenone solution (20 mg mL-1 acetone) and 50 µL of triethylamine (25 mg mL-1 acetone), than the solution is heated at 100 °C for 15 min and cooled until room temperature. Successively, 75 µL of acetic acid (10 mg mL-1 acetone) are added and reheated for an additional 5 min at 100 °C. Finally the products are dried under stream of N2 and dissolved in mobile phase.
As control, analysis of the extracted from cellulose native and oxidized (DAC) supports (without enzyme) applied on linseed oil stratified on canvas (blanks) are also made.
Results and Discussion
Oxidation degree of different cellulose supports
The periodate oxidation of all cellulose supports, made at 20 °C and in darkness, causes the specific cleavage of the C2-C3 bond of glucopyranoside ring, resulting in the formation of dialdehyde cellulose (DAC).18 This compound is spectrophotometrically determined by quantitative estimation of Fehling reaction. Figure 1 shows the spectra just of Fehling reactive (a) and after its reaction with glutaraldehyde (b) and DAC support (c). Both mixture reactions show a same spectral behaviour: a decrease in absorbance at 670 nm and a formation of maximum at 410 nm. These confirm the presence of dialdehydic groups in activated cellulose supports.
Afterwards, the oxidation degrees of all DACs are determined after 6 h from the beginning of the reaction (Table 1). It shows that the number of formed aldehyde groups depends on the kind of fibres (cotton or linen) and on morphological characteristics of support materials (disc or tissue). Similar amount is shown for the cellulose powder and for the make-up remover pads. However pads disc can be used in restoration in an easier way. In fact its removal is facilitated thanks to more homogeneous and compact structures respect to powder ones. In this way the enzyme removal is easier and safer respect that of free enzyme which generally is mixed into an aqueous gel base. In addition, it can reduce the water washing and the risk of paintings damage too.
Optimization of lipase immobilization
The covalent immobilization of lipase to the DAC pad disc is studied estimating the effect of time, temperature, ratio lipase/support and pH on the immobilized and/or the residue free lipase activity. In the first case data are expressed as fatty acid produced per unit time per unit mass of support (mmol min-1g-1), while in the second case they are expressed as mmol min-1. Experiments are always made employing the same DAC disc and similar portion mass (ca. 70 mg) so that the same number of aldehyde groups is present.
Since immobilization time favors the enzyme-support reaction, time's course for different lipase/DAC support ratios is followed by monitoring the residue lipase activity in the solution. From results shown in Figure 2, it appears an optimal value of 200 min, independently from the lipase/support ratios.
Afterwards, considering the high temperature influence on the activity, the stability and the immobilization process, two series of triplicate measurements are made at 20 and 30 °C. Results, obtained at 200 min, are reported in Table 2. The highest immobilized activity and immobilization yield obtained at 20 °C make this value optimal. Moreover the highest removed activity from aqueous solution, evidences a probable instability of the enzyme at 30 °C for a reaction time too prolonged.
The lipase/support ratio is also investigated to achieve binding of high levels of enzyme with a high retention of hydrolytic activity. In each experiment, ca. 70 mg of oxidized support are immersed in a certain volume of enzyme solution. Results, reported in Figure 3, show that both immobilized lipase activity and immobilization yield increase while the removed activity decreases, with the increase of the lipase/support ratio to 0.3 value. Above this value, all parameters decline roughly, evidencing the achievement of support saturation.
The effect of pH is also examined by the comparison of pH-profiles in function of lipase immobilized and removed activities. Data, reported in Figure 4, show an optimal activity value at pH 7 and a probable inactivation of the enzyme at pH > 7 for its interaction with the support as evidenced from the different behaviour of immobilized and free removed activities.
The immobilization stability of the lipase is investigated considering the number of possible reuse of biocatalyst and by lipase/support interactions which are correlated with pH. These tests are carried out for 6 reuses of the biocatalysts obtained by different immobilization pH. Figure 5 shows results, at pH 6, 7, 8, and 9, expressed as the ratio % of the immobilized activity obtained before and after reuses. It appears that, at pH 7, 8 and 9, the biocatalyst loses just at the first reuse 60, 40 and 45%, respectively, while at pH 6 a value of 57% is reached after 5 reuses. This is probably due to nucleophilic addition of amine groups of lipase to DAC aldehyde groups, which is highly influenced by pH. This regulates aminoacid dissociation and oxygen carbonilic protonation. Therefore, at pH 6, lipase is more highly coupled to the supports, probably, because at this value the chemical interaction is predominant with respect to the physical absorption.
In order to confirm the action of immobilized lipase to remove aged drying oils, a study on the compounds formed by the reaction between lipase and oil stratified layer is performed. The approach is based firstly on the extraction of compounds, adsorbed on the lipase-cellulose pad disc, by different solvents (phosphate buffer, acetonitrile and n-heptane) and successively on their analysis by UV-Vis spectrophotometry and HPLC. The extraction is facilitated by the use of ultrasound radiations.
The absorption spectra of extracts in phosphate buffer, acetonitrile and n-heptane, obtained after the application of the DAC support without (blank) and with immobilized enzyme (samples) on the oil stratified, show spectral behavior significantly different (Figure 6). In particular it appears a broad band around 230 nm in sample extracts. A shoulder at 270 nm is also evident in n-heptane. These results are in accordance to the spectra of dienes ( λmax = 234 nm) and trienes ( λmax = 270 nm).19 So, it is possible to hypothesize the formation of coniugated fatty acids only when the lipase-cellulose pad disc is applied on the canvas with sicative oil stratified.
The chromatographic profiles of extracts in acetonitrile and in phosphate buffer are similar. As example, only the extracts of a sample in acetonitrile and of blank are reported with a standard mixture of some fatty monocarboxilic (esanoic and caprylic acids) and dicarboxilic (suberic, azelaic and sebacic acids) acids (Figure 7). So it is possible to firstly evidence the absence of fatty acids in the blank and then the presence of azelaic acid in the sample. This is consistent with the lipase oxidative process, based on hydroperoxide intermediates breaking and formation of degradation products with low molecular weight. In fact taking into account that the hydroperoxy group is generally in the middle of the C18 fatty acid chain, the formation of azelaic acid is highly probable.20
Analysis of fatty acids released by enzymatic treatment and extracted in n-heptane is carried out after their derivatization with bromophenacyl bromide.21
In Figure 8 chromatograms of extracts in n-heptane obtained by lipase-cellulose pads disc application (sample) and by DAC disc (blank) on the oiled canvas are shown. The presence of fatty acids like miristic (11.7 min), palmitic (20.4 min), oleic (21.3 min) and linoleic (13.8 min) acids is evidenced only in the sample. The absence of linolenic acid (9.6 min), probably is due to its triply unsaturation, which causes the highest reactivity in the oxidative processes.
All these features further confirm that the hydrolysis reaction of oil is activated by the lipase-cellulose treatment.
Similar conclusions are obtained by scanning electron microscope (SEM) analysis (Figure 9). In fact, it is evident by the comparison of the surfaces of the native canvas (a), with a layer of linseed oil (b) and after the lipase-cellulose treatment (c), that the homogenous and compact fog of the fibers present in Figure 9b is reduced by the enzymatic treatment (Figure 9c).
Optimization of lipase-cellulose treatment
Temperature and application time are the experimental conditions investigated for the optimization of the lipase treatment. The effect of temperature, in the range 25-50 °C, on the lipase-cellulose application is investigated by the determination of absorbance values at 235 nm of the extract solution. The increase of the absorbance values evidences that T until 40 °C favors the enzymatic reaction, and above this value a rapid decreasing is due to a probable enzyme inactivation (Figure 10).
Time of the enzymatic treatment is varied between 15‑60 min maintaining T at 40 °C. Results reported in Figure 11 evidence that, above 45 min, the reaction declines for a probable inactivation of lipase caused by a thermic treatment too prolonged. In conclusion, 40 °C and 45 min are chosen as the optimal values.
Although further research is needed to confirm these experimental findings, this newly developed method seems to be of practical importance. Indeed lipase immobilized on cellulose make-up remover supports works well to clean aged linseed oil layers, even if the reaction system is composed of solid-solid phases. This unusual approach could be a better alternative for aged siccative oil removal than the conventional one because it is safer both for the conservator's health and the integrity of the artwork. In addition, it does not require the cleaning of the painting with water since the enzyme, being chemically attached to the support, can be easily removed and even reused.
The authors are grateful to the support from University Sapienza of Rome, Italy.
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Submitted: September 22, 2011
Published online: February 2, 2012