Printer Friendly

Evaluation of temperature and moisture response surface on the lipase from pumpkin seeds fermentation using Aspergillus niger/Avaliacao entre temperatura e umidade por superficie de resposta sobre lipase da fermentacao de sementes de abobora utilizando Aspergillus niger.

Introduction

Among the enzymes of interest stand out industrial lipases, which are hydrolases acting on ester bonds of triacylglycerols, having the lipid compounds as natural substrate, and can be produced by plants, animals, bacteria and fungi (POLAINA; MAC CABE, 2007). Lipases can be used in a wide range of industrial processes, such as: reduced fermentation time in the brewing industry, softening bread, improves crumb structure and controls the non-enzymatic browning, enhancing the aroma and hydrolysis of fat milk in the dairy industry, synthesis of short chain fatty acids esters and alcohols (HASSAN et al., 2006).

The enzymes produced by fungi are those that currently have received greater attention due to ease of production by fermentation processes, the production speed, ease of recovery from the culture medium and the fact that, mostly are not harmful to human health. Among the genera of fungi used for lipase production stand out: Aspergillus, Rhizopus, Mucor, Penicillium, Geotrichum and Rhizomucor (BURKERT et al., 2004; CARVALHO et al., 2005; DELLA et al., 2006; GUTARRA et al., 2009; MENONCIN et al., 2009; MHETRAS et al., 2009; MOHAMED et al., 2010; PASTORE et al., 2003; RAJENDRAN; THANGAVELU, 2009; RODRIGUEZ et al., 2006).

The agro-industrial residues have shown great potential for use as substrate in solid state fermentation, due to the low cost, the possibility of manufacturing high added value products, and because they present in their composition organic matter liable to be consumed by microorganisms (PELIZER et al., 2007). Several agro-industrial residues have shown potential for the production of lipases such as sugarcane bagasse (ELLAIAH et al., 2004; PELIZER et al., 2007), soybean meal (MENONCIN et al., 2009), wheat bran (MARTINS et al., 2002; SILVA et al., 2005), apple pomace (PAGANINI et al., 2005) and castor bean cake (GODOY et al., 2009). The success of solidstate fermentation depends on several factors such as temperature, pH, substrate moisture, aeration, inoculum concentration, type of substrate and microorganism species. The study on the influence of these parameters is very important to maximize the production of compounds of biotechnological interest (BELLON-MAUREL et al., 2003).

Among the filamentous fungi that can be used in solid state fermentation, Aspergillus niger has been highlighted in relation to others in the production of microbial lipase, in addition, there are several reports in the literature about the use of this microorganism to obtain lipase by fermentation in solid state (DUTRA et al., 2008; EDWINOLIVER et al., 2010; KAMINI et al., 1998; MAHADIK et al., 2002; MENEZES et al., 2006). In this context, the objective of this study was to evaluate, by means of response surface methodology, the influence of temperature and moisture of the substrate on the obtaining a lipase from the solid-state fermentation of pumpkin seed flour, using the microorganism Aspergillus niger.

Material and methods

The survey was conducted at the Laboratory of Food Microbiology from the Department of Food Technology, Federal University of Sergipe and in the Food Research Laboratory from the Institute of Technology and Research (ITP, Aracaju, Sergipe State).

Materials

Pumpkin seeds of Curcubita moschata were purchased at street markets of the city of Aracaju, State of Sergipe. The microorganism Aspergillus niger IOC 3677 was purchased from the collection of cultures from the Oswaldo Cruz Institute (Rio de Janeiro State, Brazil) preserved in tubes with slanted nutrient agar and stored at 4[degrees]C. All reagents used were of analytical grade.

Preparation of the pumpkin seed meal

Pumpkins seeds were subjected to drying (Pardal- EP 100) at 60[degrees]C for 8h and then crushed until getting an average diameter of 1.06 mm, sterilized by autoclaving at 121[degrees]C for 15 min. and stored in sterile glass vials until use. The flour was analyzed for lipid content through hot extraction in a Soxhlet extraction apparatus (Nova Etica, Brazil) using ethyl ether as solvent (IAL, 2005), obtaining 43% lipids.

Microbial lipase production from pumpkin seed waste

The fermentations were conducted in Petri dishes containing 10 g of pumpkin seed flour and a spore suspension of Aspergillus niger ([10.sup.6] cells [mL.sup.-1]). The kinetics of lipase production was monitored throughout the fermentation by removing a Petri dish from the oven to perform the analysis every 24h. The enzyme extraction was performed by adding to the fermented, sodium phosphate buffer 0.1 M, pH 7.0, in the proportion 1:5 (mass: volume), keeping in stirring at 30[degrees]C for 15 min. Then the material was centrifuged (Eppendorf Centrifuge 5804R) at 120 x g for 10 min., yielding the crude enzyme extract. The influence of fermentation temperature (30-40[degrees]C) and initial moisture content of the flour (30-60%) on the lipase production was evaluated by the response surface methodology, using the central composite rotational design (CCRD) [2.sup.2] with four replicates at the central point and four axial points (RODRIGUES; IEMMA, 2009). The statistical analyses were performed using the program STATISTIC 6.0.

Determination of hydrolytic activity

The enzyme activity of crude enzyme extract was determined by the titration method, modified from Soares et al. (2006). The substrate was prepared using 25 mL of olive oil and 25 mL of gum arabic at 7% in distilled water. In Erlenmeyer flasks were added 5 mL of the substrate, 2 mL of sodium phosphate buffer at 0.1 M, pH 7.0, and 1 mL of crude enzyme extract; the mixture was incubated at 37[degrees]C for 5 min. The reaction was stopped with acetone and ethanol (1:1, v:v). The fatty acids released were titrated using a solution of 0.04 M KOH, using phenolphthalein as indicator. One activity unit was defined in terms of amount of enzyme to release 1gmol of fatty acid per min. of reaction, under the experimental conditions.

Determination of microbial growth

Indirect quantification of cell growth was performed by measuring glucosamine, using methods described by Aidoo et al. (1981). The procedure consisted of adding 0.5 g of fermented to 5 mL of 6 M hydrochloric acid, keeping the mixture in a boiling water bath for 2h. Then the sample was cooled and filtered under vacuum. It was added a drop of alcoholic solution of phenolphthalein (0.5% w [v.sup.-1]) to the supernatant (1 mL), neutralizing the solution with 3 N sodium hydroxide (until getting pink color). Then, it was performed the reverse titration by adding a solution of 1% KHS[O.sub.4] until the pink color disappears, completing the volume with distilled water. After the extraction, it was mixed 1 mL of the solution to 1 mL of acetyl acetone in 0.5 N [Na.sub.2]C[O.sub.3], keeping in boiling water bath for 20 min. After cooling the samples, were added 6 mL of ethanol and 1 mL of Ehrlich's reagent (2.67 g p-dimethylaminobenzaldehyde in 30 mL of ethanol/hydrochloric acid 1:1). The tubes were then incubated at 65[degrees]C for 10 min. and the absorbance was read in a spectrophotometer at 530 nm. To determine the glucosamine concentration it was used a standard curve ranging from 0 to 0.2 g [mL.sup.-1].

Results and discussion

Kinetics of lipase production

The kinetics of lipase production was monitored throughout the fermentation process (Figures 1 and 2) in order to determine, for each experiment, at which time was obtained the maximum hydrolytic activity. The results are presented in Table 1.

It was observed in all fermentations that the lipase production increased over the fermentation time, reaching a maximum value followed by a stability or drop (Figures 1 and 2). In experiments 1; 2; 3; 4; 5; 6; 7; 8; 9; 10; 11 and 12, it was obtained maximum hydrolytic activity of 71.88, 26.07, 53.39, 54.37, 46.00, 29.00, 25.54, 58.67, 70.56, 60.00, 56.27, 57.25 and 64.64 U [g.sup.-1] dry, at 120, 24, 264, 216, 96, 96, 240, 264, 96, 120, 144 and 96h of fermentation, respectively.

[FIGURE 1 OMITTED]

[FIGURE 2 OMITTED]

The maximum hydrolytic activity (71.88 U [g.sup.-1] dry) was obtained in experiment 1, when using waste containing 30% moisture and 30[degrees]C in 120h of fermentation (repeated in triplicate). The results of this study were higher than those found by Kamini et al. (1998), which fermented peanut cake, rice bran and sugarcane bagasse with the fungus Aspergillus niger ([10.sup.8] spores [mL.sup.-1]) and has obtained in 120 fermentation hours, hydrolytic activities of 10; 35 and 5 U [g.sup.-1] dry, respectively, and Colla et al. (2010) which fermented a mixture of soybean meal and rice husk with Aspergillus sp. (106 spores [g.sup.-1]) and achieved a maximum hydrolytic activity of 25 U [g.sup.-1] dry in 96 fermentation hours.

However, some researchers have obtained higher hydrolytic activities in solid state fermentation of waste, such as Edwinoliver et al. (2010), Mahadik et al. (2002), Martins et al. (2008) and Kamini et al. (1998), which obtained maximum hydrolytic activity of 521.6, 340, 120, 169.0 and 198.3 U [g.sup.-1] dry after the fermentation of a mixture of soybean meal, cake of coconut and wheat, wheat bran, rice husk meal, cake of sesame and wheat bran with Aspergillus niger, respectively.

Kinetics of microbial growth

The kinetics of microbial growth was determined (in triplicate) during fermentation, in which it was used 30% of initial moisture of the substrate, and temperature of 30[degrees]C (which had the highest production of lipase). The results are shown in Figure 3.

[FIGURE 3 OMITTED]

Microbial growth increased with fermentation time reaching its maximum value (123.46 mg [g.sup.-1] dry) in 288h of fermentation. The increase in microbial growth was not proportional to the increase in hydrolytic activity, since the maximum value of lipase production was achieved in 120h of fermentation. One hypothesis for this is that the high microbial growth promoted an higher production of proteases than lipases, resulting in a decrease of hydrolytic activity, pattern also observed by Dutra et al. (2008).

The values obtained in this study were higher than those found by Chiou and Wu (2004), Menezes et al. (2006), Edwinoliver et al. (2010), Kamini et al. (1998), Dutra et al. (2008) and Hamidi-Esfahani et al. (2004), which obtained maximum growth of 21.6 mg [g.sup.-1] dry of Aspergillus oryzae in Koji prepared with extruded rice; 21.54 mg [g.sup.-1] dry of Aspergillus niger in fermented waste of passion fruit and wheat bran; 20 mg [g.sup.-1] dry of Aspergillus niger in a mixture of soybean meal, cake of coconut and wheat; 5.9 mg [g.sup.-1] dry of Aspergillus niger in sesame cake; 15 mg [g.sup.-1] dry of Aspergillus niger in wheat bran; and 50 mg [g.sup.-1] of dry Aspergillus niger in wheat bran, respectively. This result demonstrated the potential of pumpkin seed meal as a natural substrate for the growth of Aspergillus niger, regarding that no nutrient was added to the flour.

Influence of parameters on lipase production by solid state fermentation--assessment of response surface

It was evaluated the influence of temperature and initial moisture of substrate on the lipase production through the fermentation of pumpkin seeds. The Table 2 shows the estimative of the effects and which parameters were statistically significant in the production of lipase.

The linear and quadratic moisture was not statistically significant for the determination of the hydrolytic activity at 95% level (p < 0.05), i.e., it had no effect on the lipase production. The significant parameters were the temperature (linear and quadratic) and the interaction between temperature and moisture. The Pareto chart (Figure 4) shows that the effect on the hydrolytic activity will be more significant the more it is to the right of the red line. The length of each bar is proportional to the variable effect. According to the graph, the temperature (quadratic) was the variable that most interfered with the hydrolytic activity (lipase production), but negatively (negative coefficient), i.e., the higher the temperature the lower the hydrolytic activity. The interaction between moisture and temperature had a positive effect on the hydrolytic activity. The moisture was the parameter that least affected the hydrolytic activity.

In Equation 1 is presented the second order encoded model for the lipase production as a function of the fermentation temperature and substrate moisture, where T is the temperature and U is the moisture.

Hydrolytic activity (U [g.sup.-1] dry) = 59.49 - 9.27 T - 11.50 [T.sup.2] + 11.70 T U (1)

The empirical model obtained was validated by the analysis of variance (ANOVA) presented in Table 3. The correlation coefficient [R.sup.2] = 0.96745 and the calculated F (about 8 times higher than the tabulated F = 4.39) have validated statistically the model and allowed obtaining the response surface.

According to the response surface (Figure 5), the best conditions for the lipase production through solid state fermentation of pumpkin seed flour are: fermentation temperature between 28 and 34.5[degrees]C, and initial moisture of the flour from 25 to 32.5%; and fermentation temperature between 32 and 40[degrees]C and initial moisture of the flour from 58 to 65%.

[FIGURE 5 OMITTED]

Conclusion

The interaction between temperature and moisture positively influences the lipase production through the fermentation of pumpkin seed meal, with maximum values between 28.0 and 34.5[degrees]C, and between 25 and 32.5%, or between 32 and 40[degrees]C, and between 58 and 65%, respectively. Given these findings, pumpkin seeds, commonly discarded in household waste, demonstrated to be a potential source of natural substrates (without adding nutrients) in solid state fermentation processes, aiming to obtain fungal lipase from Aspergillus niger.

Doi: 10.4025/actascitechnol.v34i3.12497

Acknowledgements

The authors thank the Foundation for Research and Technological Innovation of the Sergipe State (FAPITEC/SE), the graduate scholarship granted, and the Graduate Program in Science and Food Technology, Federal University of Sergipe, for financial support.

References

AIDOO, K. E.; HENDRY, R.; WOOD, B. J. B. Estimation of fungal growth in a solid state fermentation system. Applied Microbiology and Biotechnology, v. 12, n. 1, p. 6-9, 1981.

BELLON-MAUREL, V.; ORLIAC, O.; CHRISTEN, P. Sensors and measurements in solid state fermentation: a review. Process Biochemistry, v. 38, n. 6, p. 881-896, 2003.

BURKERT, J. F. M.; MAUGERI, F.; RODRIGUES, M. I. Optimization of extracellular lipase production by Geotrichum sp. Using factorial design. Bioresource Technology, v. 91, n. 1, p. 77-84, 2004.

CARVALHO, P. O.; CALAFATTI, S. A. P.; MARASSI, M.; SILVA, D. M.; CONTESINI, F. J.; BIZACO, R.; MACEDO, G. A. Potencial de biocatalise enantiosseletiva de lipases microbianas. Quimica Nova, v. 28, n. 4, p. 614-621, 2005.

CHIOU, S.-H.; WU, W.-T. Immobilization of Candida rugosa lipase on chitosan with activation of the hydroxyl groups. Biomaterials, v. 25, n. 2, p. 197-204, 2004.

COLLA, L. M.; RIZZARDI, J.; PINTO, M. H.; REINEHR, C. O.; BERTOLIN, T. E.; COSTA, J. A. V. Simultaneous production of lipases and biosurfactants by submerged and solid substrate process. Bioresource Technology, v. 101, n. 21, p. 8308-8314, 2010.

DELLA, V. P.; HOTZA, D.; JUNKES, J. A.; OLIVEIRRA, A. P. N. Estudo comparativo entre silica obtida por lixivia acida da casca de arroz e silica obtida por tratamento termico da cinza de casca de arroz. Quimica Nova, v. 29, n. 6, p. 1175-1179, 2006.

DUTRA, J. C. V.; TERZI, S. C.; BEVILAQUIA, J. V.; DAMASO, M. C. T.; COURI, S.; LANGONE, M. A. P.; SENNA, L. F. Lipase production in solid-sate fermentation monitoring biomass growth of Aspergillus niger using digital image processing. Applied Biochemistry and Biotechnology, v. 147, n. 1-3, p. 63-75, 2008.

EDWINOLIVER, N. G.; THIRUNAVUKARASU, K.; NAIDU, R. B.; GOWTHAMAN, M. K.; KAMBE, T. N.; KAMINI, N. R. Scale-up of a novel of a tri-substrate fermentation for enhanced production of Aspergillus niger lipase for tallow hydrolysis. Bioresource Technology, v. 101, n. 17, p. 6791-6796, 2010.

ELLAIAH, P.; PRABHAKAR, T.; RAMAKRISHNA, B.; TALEB, A. T.; ADINARAYANA, K. Production of lipase by immobilized cells of Aspergillus niger. Process Biochemistry, v. 39, n. 5, p. 525-528, 2004.

GODOY, M. G.; GUTARRA, M. L. E.; MACIEL, F. M.; FELIX, S. P.; BEVILAQUA, J. V.; MACHADO, O. L. T.; FREIRE, D. M. G. Use of a low-cost methodology for biodetoxification of castor bean waste and lipase production. Enzyme and Microbial Technology, v. 44, n. 5, p. 317-322, 2009.

GUTARRA, M. L. E.; GODOY, M. G.; MAUGERI, F.; RODRIGUES, M. I.; FREIRE, D. M. G.; CASTILHO, L. R. Production of an acidic and thermostable lipase of the mesophilic fungus Penicillium simplicissimum by solidstate fermentation. Bioresource Technology, v. 100, n. 21, p. 5249-5254, 2009.

HAMIDI-ESFAHANI, Z.; SHOJAOSADATI, S. A.; RINZEMA, A. Modelling of simultaneous effect of moisture and temperature on A. niger growth in solid-state fermentation. Biochemical Engineering Journal, v. 21, n. 3, p. 265-272, 2004.

HASSAN, F.; SHAH, A. A.; HAMEED, A. Industrial applications of microbial lipases. Enzyme and Microbial Technology, v. 39, n. 2, p. 235-251, 2006.

IAL-Instituto Adolfo Lutz. Normas Analiticas do Instituto Adolfo Lutz. 4. ed. Sao Paulo: IAL, 2005.

KAMINI, N. R.; MALA, J. G. S.; PUVANAKRISHNAN, R. Lipase production from Aspergillus niger by solid-state fermentation using gingelly oil cake. Process Biochemistry, v. 33, n. 5, p. 505-511, 1998.

MAHADIK, N. D.; PUNTAMBEKAR, U. S.; BASTAWDE, K. B.; KHIRE, J. M.; GOKHALE, D. V. Production of acidic lipase by Aspergillus niger in solid state fermentation. Process Biochemistry, v. 38, n. 5, p. 715-721, 2002.

MARTINS, V. G.; KALIL, S. J.; COSTA, J. A. V. Coproducao de lipase e biossurfactante em estado solido para utilizacao em biorremediacao de oleos vegetais e hidrocarbonetos. Quimica Nova, v. 31, n. 8, p. 1942-1947, 2008.

MARTINS, E. S.; SILVA, D.; SILVA, R.; GOMES, E. Solid state production of thermostable pectinases from thermophilic Thermoascus aurantiacus. Process Biochemistry, v. 37, n. 9, p. 949-954, 2002.

MENEZES, G. D. G.; OLIVEIRA, A. C. P.; DAMASO, M. C. T.; OLIVEIRA, M. A. C. L.; COURI, S. Producao de poligalacturonase pela linhagem Aspergillus niger mutante 3T5B8 em fermentacao semi-solida utilizando como substrato residuo de maracuja e farelo de trigo. Revista da Universidade Rural, v. 25, n. 1, p. 15-27, 2006.

MENONCIN, S.; DOMINGUES, N. M.; FREIRE, D. M. G.; OLIVEIRA, J. V.; DI LUCCIO, M.; TREICHEL, H.; OLIVEIRA, D. Imobilizacao de lipases produzidas por fermentacao em estado solido utilizando Penicillium verrucosum em suportes hidrofobicos. Ciencia e Tecnologia de Alimentos, v. 29, n. 2, p. 440-443, 2009.

MHETRAS, N. C.; BASTAWDE, K. B.; GOKHALE, D. V. Purification and characterization of acidic lipase from Aspergillus niger NCIM 1207. Bioresource Technology, v. 100, n. 3, p. 1486-1490, 2009.

MOHAMED, S. A.; ABDEL-MAGEED, H. M.; TAYEL, S. A. ; EL-NABRAWI, M. A.; FAHMY, A. S. Characterization of Mucor racemosus with potential application for the treatment of cellulite. Process Biochemistry, v. 46, n. 3, p. 642-648, 2010.

PAGANINI, C.; NOGUEIRA, A.; SILVA, N. C.; WOSIACKI, G. Aproveitamento de bagaco de maca para a producao de alcool e obtencao de fibras alimentares. Ciencia e Agrotecnologia, v. 29, n. 6, p. 1231-1238, 2005.

PASTORE, G. M.; COSTA, V. S. R.; KOBLITZ, M. G. B. Purificacao parcial e caracterizacao bioquimica de lipase extracelular produzida por nova linhagem de Rhizopus sp. Ciencia e Tecnologia de Alimentos, v. 23, n. 2, p. 135-140, 2003.

PELIZER, L. H.; PONTIERI, M. H.; MORAES, I. O. Utilizacao de residuos agro-industriais em processos biotecnologicos como perspectiva de reducao do impacto ambiental. Journal of Technology Management and Innovation, v. 2, n. 1, p. 118-127, 2007.

POLAINA, J.; MACCABE, A. P. Industrial enzymes: structure, function and applications. The Netherlands: Springer, 2007.

RAJENDRAN, A.; THANGAVELU, V. Statistical experimental design for evaluation of medium components for lipase production by Rhizopus arrhizus MTCC 2233. Food Science and Technology, v. 42, n. 5, p. 985-992, 2009.

RODRIGUES, M. I.; IEMMA, A. F. Planejamento de experimentos e otimizacao de processos: uma estrategia sequencial de planejamentos. 2. ed. Campinas: Editora Casa do Espirito Santo, Amigo Fraternidade, Fe e Amor, 2009.

RODRIGUEZ, J. A.; MATEOS, J. C.; NUNGARAY, J.; GONZALEZ, V.; BHAGNAGAR, T.; ROUSSOS, S.; CORDOVA, J.; BARATTI, J. Improving lipase production by nutrient source modification using Rhizopus homothallicus cultured in solid state fermentation. Process Biochemistry, v. 41, n. 11, p. 2264-2269, 2006.

SILVA, D.; TOKUIOSHI, K.; MARTINS, E. S.; SILVA, R.; GOMES, E. Production of pectinase by solid-state fermentation with Penicillium viridicatum RFC3. Process Biochemistry, v. 40, n. 8, p. 2885-2889, 2005.

SOARES, C. M. F.; SANTOS, O. A.; CASTRO, H. F.; MORAES, F. F.; ZANIN, G. M. Characterization of solgel encapsulated lipase using tetraethoxysilane as precursor. Journal of Molecular Catalysis B: Enzymatic, v. 39, n. 1-4, p. 69-76, 2006.

Received on February 14, 2011.

Accepted on May 3, 2011.

Rafaela Cristiane Andrade Santos (1), Kyzzes Barreto Araujo (1), Cleide Mara Faria Soares (2) and Luciana Cristina Lins de Aquino (1) *

(1) Programa de Pos-graduacao em Ciencia e Tecnologia de Alimentos, Departamento de Tecnologia de Alimentos, Universidade Federal de Sergipe, Av. Marechal Rondon, s/n, 49100-000, Sao Cristovao, Sergipe, Brazil. (2) Universidade Tiradentes, Farolandia, Aracaju, Sergipe, Brazil. * Author for correspondence. E-mail: aquinoluciana@hotmail.com
Table 1. Coded levels and real values of the independent
variables of the factorial design and maximum hydrolytic
activity obtained in each fermentation.

Exp    [X.sub.1]    [X.sub.2]    T ([degrees]C)    U (%)

1          -1           -1             30            30
2          +1           -1             40            30
3          -1           +1             30            60
4          +1           +1             40            60
5        -1.41          0              28            45
6        +1.41          0              42            45
7          0          -1.41            35            24
8          0          +1.41            35            66
9          0            0              35            45
10         0            0              35            45
11         0            0              35            45
12         0            0              35            45

Exp    Hydrolytic Activity (U [g.sup.-1])

1              71.88 [+ or -] 0.0
2              26.07 [+ or -] 2.82
3              53.39 [+ or -] 5.44
4              54.37 [+ or -] 0.0
5              46.29 [+ or -] 4.22
6              25.54 [+ or -] 0.0
7              58.67 [+ or -] 4.83
8              70.56 [+ or -] 6.11
9              60.00 [+ or -] 0.0
10             56.27 [+ or -] 0.0
11             57.25 [+ or -] 3.40
12             64.44 [+ or -] 3.85

[X.sub.1]: Coded values for temperature (T). [X.sub.2]: Coded values
for moisture (U).

Table 2. Estimative of the effects for the hydrolytic activity and
statistical analysis of the fermentation process.

Parameters     Effect     Standard-       t           p
                            error

Principal      59.4900      1.829      32.524    0.000064 *
U(L)           6.6562       2.587       2.573     0.082266
U(Q)           5.7062       2.892       1.973     0.143023
T(L)          -18.5437      2.587      -7.169     0.005592*
T(Q)          -22.9938      2.892      -7.950     0.004150*
U(L) x T(L)    23.3950      3.658       6.395     0.007744*

Parameters     Confidence     Confidence
              limit - 95%    limit + 95%

Principal        53.669         65.311
U(L)             -1.576         14.888
U(Q)             -3.498         14.910
T(L)            -26.776        -10.311
T(Q)            -32.198        -13.781
U(L) x T(L)      11.753         35.037

* Significant factors (p < 0.05).

Table 3. Analysis of variance (ANOVA) for the hydrolytic
activity of lipase produced by FES.

Source of         Sum      Degree of      Mean     Calculated
variation       Squared     freedom     squared         F

Regression     2346.605        5        469.321       35.66
Residue         78.959         6         13.16         --
Lack of fit     38.810         3           --          --
Pure error      40.149         3           --          --
Total          2425.564        11          --          --

Correlation coeficient [R.sup.2] = 0.96745; [F.sub.0.95;5;6] = 4.39.

Figure 4. Pareto chart for the lipase production through the
fermentation of pumpkin seed flour.

Standardized Effect Estimate (Absolute Value)

Temperature ([degrees]C)(Q)            -7,95051
(2)Temperature ([degrees]C)(L)         -7,16865
1Lby2L                                 6,395117
(1)Moisture (%)(L)                     2,573179
Moisture (%)(Q)                        1,973041

Note: Table made from bar graph.
COPYRIGHT 2012 Universidade Estadual de Maringa
No portion of this article can be reproduced without the express written permission from the copyright holder.
Copyright 2012 Gale, Cengage Learning. All rights reserved.

Article Details
Printer friendly Cite/link Email Feedback
Author:Santos, Rafaela Cristiane Andrade; Araujo, Kyzzes Barreto; Soares, Cleide Mara Faria; de Aquino, Luc
Publication:Acta Scientiarum. Technology (UEM)
Date:Jul 1, 2012
Words:3966
Previous Article:Kraft pulping and ECF bleaching of Eucalyptus globulus pretreated by the white-rot fungus Ceriporiopsis subvermispora/Polpacao kraft e branqueamento...
Next Article:Masonry concrete block strength compound with sawdust according to residue treatment/ Resistencia de blocos de concreto para alvenaria compostos com...
Topics:

Terms of use | Privacy policy | Copyright © 2019 Farlex, Inc. | Feedback | For webmasters