Production of inulinase from Kluyveromyces marxianus using Dahlia tuber extract

INDUSTRIAL MICROBIOLOGY

Production of inulinase from Kluyveromyces marxianus using Dahlia tuber extract

Sumat Chand Jain; P.C. Jain; Naveen Kango^*

Department of Applied Microbiology and Biotechnology, Dr. Hari Singh Gour University, Sagar, M.P. 470003, India

ABSTRACT

Various carbon sources were evaluated for production of inulinase by yeast, Kluyveromyces marxianus MTCC 3995. Highest inulinase activity was observed with Dahlia extract (25.3 nkat mL^-1) as carbon source. The enzyme activity was 1.4 folds higher than that observed in media containing pure chicory inulin (17.8 nkat mL^-1). The yeast showed good growth on a simple medium containing dahlia extract (20% w/v) and yeast extract (2%w/v) as carbon and nitrogen source respectively, in 96 h. at 28°C and 120 rpm. Lowest inulinase yield (4.8 nkat mL^-1) was seen in the medium containing glucose as C-source. Although varied inulinase levels were noticed on different C- sources, Inulinase: Sucrase (I/S) ratios were noticed to be similar. Among various protein sources tested, yeast extract was found to be the best source followed by beef extract (17.9 nkat mL^-1) and peptone (13.8 nkat mL^-1). The enzyme was optimally active at pH (4.0) and 50°C. TLC analysis of end product revealed that inulinase hydrolyzed inulin exclusively into fructose. Results suggest that the dahlia extract induced exoinulinase synthesis in Kluyveromyces marxianus and can be utilized as a potential substrate for inulinase production.

Key words: Inulinase, dahlia, fructose, Kluyveromyces marxianus

INTRODUCTION

Microbial inulinases are important industrial enzymes, which are usually inducible and extracellular. A number of yeasts, filamentous fungi and some bacteria are reported to produce inulinases (7, 13). Inulinases are receiving increasing attention due to availability of relatively inexpensive and abundant renewable substrate (inulin) for the production of high fructose syrup. The production of fructose syrup from inulin or inulin rich materials is a major area of applications of inulinases. Fructose is emerging as a healthy and safe alternative sweetener than sucrose, which causes problems, related to corpulence, cariogenicity, atherosclerosis and diabetes (22). Conventional fructose production from starch needs at least three enzymatic steps involving α-amylase, glucoamylase and glucose isomerase and yields only 45% fructose. In contrast, the complete hydrolysis of inulin by a single step using inulinase gives a yield of about 90-95% fructose (24). Apart from being a low calorie sweetener, fructose is also used in the production of ethanol, acetone and butanol, gluconic acid, sorbitol and fructo-oligosaccharides etc. (12, 19).

Industrial applications of this enzyme, however, would only be feasible if it were available in large quantities at a competitive price. Production of inulinase is affected by medium components and type of the organism used for fermentation. Various carbon sources like fructose, sucrose, purified inulin have been examined for production of this enzyme (22). To compensate the high cost of inulin various plant materials like Jerusalem artichoke, dahlia (Dahlia pinnata), chicory, kuth roots, etc. have also been used for the production of inulinases (7, 19). Influence of sucrose concentration and culture conditions (pH and aeration rate) were studied on inulinase production by K. marxianus var. bulgaricus ATCC 16045 to obtain maximum yield of 15.29 U mL^-1 (2). More recently, optimization of agro-industrial medium comprised of sugarcane bagasse, molasses and Corn steep liqour has been attempted to maximize the production of inulinase upto 436 U/gds (9). Ethanol precipitation of K. marxianus inulinase extracted from SSF was optimized using central composite design. An enhanced activity yield percentage (168%) suggested removal of enzyme inhibitors after precipitation (5). The stability and kinetic behavior of immobilized K. marxianus inulinase in aqueous-organic solvent, butyl acetate was studied. Immobilized enzyme was more stable towards pH change while its affinity was found to decrease with the increase in organic solvent (16).

Dahlia is a flowering plant of family asteraceae commonly grown for ornamental purpose. The tubers of dahlia contain about 12.5% of inulin as a storage polysaccharide (3). Among the microbial strains used for inulinase production, those of K. marxianus and A. niger are the most commonly used ones (6, 7,12). In the present study, production and properties of inulinase by K. marxianus MTCC 3995 were examined on various carbon sources including crude dahlia extract.

MATERIALS AND METHODS

Microorganism

The yeast Kluyveromyces marxianus MTCC 3995 was obtained from Microbial Type Culture Collection (MTCC), Chandigarh, India. The culture was grown on wort agar at 28°C and maintained at 4°C on the slants of the same media.

Substrates and chemicals

Inulin (from chicory), fructose, 3,5-dinitrosalicycilc acid and corn steep liquor were obtained from Sigma chemical co., U.S.A. Precoated silica gel plates UV₂₅₄ were obtained from Merck, Germany. Wort agar and other chemicals were of analytical grade (Hi-media, India). Mature dahlia tubers were obtained from a local nursery.

Preparation of dahlia extract

100 g of the tubercles were washed in running water and crushed in a blender with 500 mL of distilled water. The slurry obtained was allowed to stand for sedimentation of particulate matter. Afterwards, it was filtered through muslin cloth and the filtrate was used in media formulation.

Enzyme production

50 mL of dahlia extract was supplemented with 2% (w/v) yeast extract as nitrogen source and was used for inulinase production. Production media with pure inulin (chicory root, Sigma), sucrose, fructose and glucose as carbon sources were prepared using the following composition: yeast extract: 14.0 g, (NH₄)₂SO₄: 2.1 g, MgSO₄.7H₂O: 0.3 g, CaCl₂.2H₂O: 0.3 g, FeSO₄.7H₂O: 0.5 g, KH₂PO₄: 10.0 g and carbon source: 20.0g per liter (pH 5.0). Erlenmeyer flasks (150 mL) containing 50 mL aliquots of medium were autoclaved (20 min, 121°C) and incubated with two loops from 48 h old culture of K. marxianus. Flasks were incubated at 28°C on a rotary shaker (120 rpm). Flasks were withdrawn at regular interval of 24 h and clear culture filtrate was obtained by filtering the broth through Whatman filter paper no. 1. All the experiments were carried out in triplicate and mean values ± SD are reported as results.

Effect of nitrogen sources

Effect of different nitrogen sources including peptone, beef extract, yeast extract, and corn steep liquor (organic N-sources) and NaNO₃, KNO₃, (NH₄)₂SO₄ and (NH₄)H₂PO₄ (inorganic N-sources) was studied by incorporating 2% (w/v) of each N- source in dahlia extract medium.

Enzyme assay

0.2 mL of appropriately diluted enzyme (culture filtrate) was added to 1.8 mL of inulin (1% w/v dissolved in 200 mM sodium acetate buffer, pH 5.0) and incubated at 50°C for 30 min. After incubation, total reducing sugars liberated from inulin were measured by adding 3 mL DNS reagent and boiling in a water bath for 5 min (10). Samples were allowed to cool and their absorbance was read at 540 nm. Invertase activity was measured using sucrose solution (1% w/v dissolved in 200 mM sodium acetate buffer, pH 5.0). One nanokatal (nkat) of inulinase/invertase activity was defined as the amount of enzyme which produced 1nano mol of fructose/glucose per second under the assay conditions as described above.

Effect of temperature and pH on inulinase activity

Effect of temperature was determined by incubating 0.2 mL of suitably diluted enzyme and 1.8 mL of inulin (1% w/v in 200 mM sodium acetate buffer, pH 5.0) for 30 min at different temperatures. The effect of pH on inulinase activity was determined by incubating 0.1 mL of undiluted enzyme sample in 0.4 mL of appropriate buffers (0.2 M sodium acetate buffer: pH 4.0 and 5.0; 0.1 M phosphate buffer: pH 6.0, 7.0 and 8.0; 0.1 M Tris–HCl buffer: pH 9.0). To this, 0.5 mL of inulin (1% w/v in distilled water) was added and the reaction mixture was incubated at 50°C for 30 min (6).

Thin layer chromatography

The end products of enzyme reaction were visualized using thin layer chromatography as described earlier (6). 200 μL of undiluted enzyme (culture filtrate) was added to 200 μL of inulin (5% w/v in 200 mM NaAc buffer, pH 5.0) and was incubated at 50°C. Aliquots of 1 μL were withdrawn after 30 min and spotted on TLC plate. Plates were developed with the solvent system containing isopropyl alcohol: ethyl acetate: water (2:2:1 by volume). Sugar spots were developed with reagent containing 0.5% α-naphthol and 5% conc. sulfuric acid in absolute ethanol and by heating the plate at 100°C for 10 min. Fructose and Raffinose were used as sugars standards.

RESULTS AND DISCUSSION

Among various substrates employed as carbon source for inulinase production, inulin-containing plant materials offer advantage in comparison to purified substrates in terms of lower cost and high productivity. Complex substrates from agro-industrial wastes have been of wider interest for production of microbial enzymes (9, 14). Root extract of a perennial herb, dandelion (Taraxacum officinale), has been reported as a competitive substrate for inulinase production by Aspergillus niger (6). Tubercles of yacon (Polymnia sanchifolia), also a member of Asteraceae, have been reported as an inexpensive substrate for inulinase production from Kluyveromyces marxianus (1) and garlic bulbs (Allium sativum) have been used for inulinase production from Streptomyces sp. (18). In the present study K. marxianus MTCC 3995 was able to utilize all the test C-sources for its growth. Growth on dahlia extract was maximum and a sharp decrease in turbidity of the medium was also noticed. Infusion prepared from tubers of dahlia was found to support maximal inulinase production (25.3 nkat mL^-1) as compared to pure inulin and other substrates (Figure 1). Dahlia extract has been reported to contain inulin (3, 21) and possibly this fructan component induced higher titres of inulinase. In the present study, compared to pure inulin as a carbon source, about 1.4-fold higher activity was obtained with dahlia. Cruz et al. (3) have also compared various carbon sources for inulinase production and obtained 1.26- fold higher activity with dahlia extract (3.68 U mL^-1) as compared to pure inulin (2.92 U mL^-1). Dahlia is an interesting alternative, since, it is a relatively cheap and easily available substrate, that can serve as a feedstock for large-scale fermentation, whereas pure inulin is only available in limited quantities and at very high cost. Singh et al. (21) have extracted raw inulin from dahlia tubers by processing at 15 Kg cm^-2 for 10 min. and used an optimized medium in a bioreactor to obtain 55.4 IU mL^-1 in 60 h by an indigenous strain K. marxianus YS-1. Recently, Singh and Bhermi (20) have evaluated root tubers of Asparagus officinalis for production of exoinulinase by the same strain and have observed that enzyme yield (8.42 IU mL-1) was three folds higher as compared to pure inulin (2.7 IU mL^-1). Some of the recent reports of inulinase production and properties have used 2% (w/v) sucrose as substrate for the assay of inulinase activity (5, 9, 17). In comparison to these reports, we have also obtained higher activity towards sucrose 56 U mL^-1 (945 nkat mL^-1) and 52 U mL^-1 (880 nkat mL^-1).

Many microbial preparations of inulinase possess remarkable invertase activity accompanying the inulinase activity. Their catalytic activity is described in terms of I/S ratio which represents ratio of the activity of enzyme preparation on inulin and sucrose (22). Almost similar I/S ratios (0.02) were observed on all the carbon sources. This indicated a direct corresponding relationship between sucrase (invertase) and inulinase activity (Table 1). Large variation in I/S ratios has been noticed in case of A. niger grown on various C-sources (6). The ratios in the range of 0.02-7.9 have been reported in literature (11).

Furthermore, with all the substrates, maximum inulinase activity was obtained on the fourth day of cultivation and dahlia extract with a pH shift from 6.3 to 8.2, on dahlia -yeast extract medium (Figure 2). The optimum pH for inulinase activity was found to be 4.0 (Figure 3). Optimal pH 4.0 has also been reported for inulinase activity from Kluyveromyces marxianus var. bulgaricus (1). Inulinase of Kluyveromyces sp. Y-85 had optimum pH 4.5 (25). Pessoa and Vitolo (15) have found for K. marxianus inulinase optimum pH between 3.2 and 5.0 for inulinase. Kushi et al. (8) found optimum pH 4.7 for K. marxianus var. bulgaricus. K. marxianus inulinase showed optimal activity at 50°C (Figure 4). Temperature optima of 50°C have also been reported for K. marxainus (4, 25).

Yeast extract was found to be the best nitrogen source to be used in conjunction with dahlia extract for inulinase production followed by beef extract (Figure 5). Complex nitrogen sources were better than inorganic nitrogen sources. Kango (6) also found yeast extract to be the best N-source in media containing dandelion roots. While meat extract (21) and corn steep liquor (23) have also been reported to be better N-source.

Thin layer chromatography was used for qualitative analysis of the products of inulinase action. Inulinases obtained from various medium showed liberation of fructose from chicory inulin indicating only exoinulinase activity (Figure 6). In the present study we have found that crude Dahlia extract can be used as a low-value substrate for production of exoinulinase using K. marxianus MTCC 3995. Inulinase thus produced is optimally active at pH 4.0 and 50°C and liberates fructose from inulin. There seems to be a direct relationship between inulinase and invertase activities as similar I/S ratios were observed on different C-sources.

ACKNOWLEDGEMENTS

Authors are thankful to University Grants Commission, New Delhi and MPCST, Bhopal for financial assistance. SCJ is thankful to MPCST, Bhopal for project fellowship.

Submitted: December 24, 2009; Approved: January 16, 2012.

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Publication Dates

• Publication in this collection
  02 May 2012
• Date of issue
  Mar 2012

History

• Received
  24 Dec 2009
• Accepted
  16 Jan 2012