Open Access

Utilization of corncob xylan as a sole carbon source for the biosynthesis of endo-1,4-β xylanase from Aspergillus niger KIBGE-IB36

Bioresources and Bioprocessing20174:19

DOI: 10.1186/s40643-017-0149-5

Received: 1 January 2017

Accepted: 11 April 2017

Published: 21 April 2017

Abstract

Background

Xylan is a hemicellulose polysaccharide which is composed of β-1,4-linked d-xylosyl residues. Endo-1,4-β xylanase has the ability to cleave xylan back bone chains to release xylose residues. They are produced by a number of prokaryotic and eukaryotic organisms. Among them, filamentous fungi are attracting great attention due to high secretion of xylanolytic enzymes. Endo-1,4-β xylanase has wide industrial applications such as in animal feed, bread making, food and beverages, textile, bleaching of wood pulp, and biofuel production.

Results

In this study, different Aspergillus species were screened for the production of endo-1,4-β xylanase, and Aspergillus niger KIBGE-IB36 was selected for optimum production of enzyme in submerged fermentation technique. Influence of various fermentation conditions was investigated to produce high titer of endo-1,4-β xylanase. The results indicated that A. niger KIBGE-IB36 showed optimum production of endo-1,4-β xylanase at 30 °C, pH 8 after 6 days of incubation. Different macro- and micronutrients were also amalgamated in the fermentation medium to increase the enzyme production. The parametric optimization of endo-1,4-β xylanase resulted in tenfold increase after hydrolysis of 20 g L−1 corncob xylan.

Conclusions

The use of low-cost substrate approach for high production of endo-1,4-β xylanase has been developed successfully that can be consumed in different industrial applications especially in paper and pulp industry.

Keywords

Aspergillus species Corncob Fermentation Hemicellulose Endo-1,4-β xylanase

Background

Substantial consideration has been given for the use of microorganisms in industrial processes particularly for the production of enzymes. Amid different microorganisms, fungi, bacteria, and actinomycetes are the abundant producers of endo-1,4-β xylanase (Lu et al. 2008). Filamentous fungi such as Aspergillus and Trichoderma species have immense significance over bacteria due to their efficient ability to degrade plant cell wall (Kaushik and Malik 2009). Aspergillus niger is a filamentous fungus that has been used extensively in different biotechnological applications. According to Food and Drug Administration (FDA), A. niger can be “generally regarded as safe” (GRAS) under good manufacturing* practices for industrial products and they can be isolated easily from soil, compost, and plant-decaying materials (Klich 2002; Schuster et al. 2002). Aspergillus niger has the ability to produce high yield of broad range of enzymes under both submerged and solid-state fermentation conditions, and approximately 80–90% endo-1,4-β xylanases are produced using submerged fermentation technique (Polizeli et al. 2005; Pel et al. 2007).

Among different industrially important enzymes, xylanolytic enzymes have been used extensively in food and pharmaceutical industries. This complex enzyme includes endo-1,4-β- xylanase [EC 3.2.1.8], β-xylosidase [EC 3.2.1.37], α-arabinofuranosidase [EC 3.2.1.55], and acetyl xylan esterase [EC 3.1.1.72] (Biely 1993). Xylan is the second most abundant resource after cellulose and is the main constituent of hemicellulose which consists of long chain of 1,4-β-d-xylose monomers (Izidoro and Knob 2014). Endo-1,4-β xylanase is an enzyme which has the ability to hydrolyze β-1,4 glycosidic bonds in xylan into small series of xylooligosaccharides (Chanwicha et al. 2015). In the presence of β-xylosidase, these oligosaccharides are further hydrolyzed into xylose molecules. Alone exo-xylanase will not be able to hydrolyze the complex xylan structure. After this synergistic effect, more xylose is produced as a by-product which confirms the presence of endo-1,4-β xylanase. Being an industrially important enzyme, endo-1,4-β xylanase has several applications: in baking and in food industries, it is utilized as a taste and texture enhancer; in poultry, it is used as a food additive; and in beverages, it acts as a juice clarifying agent. Commonly, it is also used in pre-bleaching process of kraft and pulp to diminish the use of harmful chemicals (Arulanandham and Palaniswamy 2014).

To achieve entire enzymatic degradation of xylan into its monosaccharide components, a group of synergistic xylanolytic enzymes is required due to the presence of differences in xylan structure from different sources (Latif et al. 2006). Previously, corncob is reported as one of the valuable by-products of food industry which can be utilized as growth-inducing substrate for bacteria and fungi. In addition, it is also used to synthesize xylose, alcohol, xylitol, and xylooligosaccharides (Chapla et al. 2012). In this study, commercial corncob xylan was used for the synthesis of endo-1,4-β xylanase by A. niger KIBGE-IB36 under submerged fermentation conditions. Different physiological and chemical factors were also optimized to enhance the production of endo-1,4-β xylanase.

Results and discussion

Screening of fungal species for endo-1,4-β xylanase production

To screen the production of endo-1,4-β xylanase, four different species of Aspergillus were used. It was observed that A. niger KIBGE-IB36 is a hyper producer endo-1,4-β xylanase (837 U mg−1) as compared to other species (Fig. 1a). In addition, it was also confirmed by Congo red dye method in which A. niger KIBGE-IB36 expressed a clear xylanolytic zone around the growing colony on medium containing corncob xylan as a sole carbon source (Fig. 1b). Further experimental studies were carried out using A. niger KIBGE-IB36 for the production of endo-1,4-β xylanase.
Fig. 1

a Production of endo-1,4-β xylanase by different fungal species; b qualitative screening of endo-1,4-β xylanase by Congo red dye method showing hydrolyzing zone around colony. Error bars represent the standard deviation (n = 3)

Selection of fermentation medium

To produce high titers of endo-1,4-β xylanase, five different reported media were analyzed. Among these media, maximum endo-1,4-β xylanase was synthesized in Czapek medium (1239 U mg−1) as compared to other media (Fig. 2).
Fig. 2

Production of endo-1,4-β xylanase by different reported medium. Error bars represent the standard deviation (n = 3)

Selection of fermentation temperature

The fermentation temperature not only influences the growth curve of an organism but it also has an impact on the production of endo-1,4-β xylanase (Senthilkumar et al. 2005). Most of the filamentous fungi grow in between 25 and 35 °C, while some thermophilic fungal species can also grow at high temperature with maximum at or above 50 °C (Suresh and Chandrasekaran 1999; Maheshwari et al. 2000). Mostly Aspergillus niger is reported to show growth pattern in between 25 and 30 °C (Adinarayana et al. 2003). In current study, optimum temperature for the production of enzyme was recorded at 30 °C with 1485 U mg−1 of endo-1,4-β xylanase. A gradual decline in enzyme titer was noted at 50 °C (50 U mg−1) and this decline is due to the lower growth rate of this fungi at high temperature (Fig. 3a). The high- and low incubation temperatures cause the inhibition of fungal growth that ultimately leads to the decline in enzyme synthesis (Lenartovicz et al. 2003). This investigation synchronizes with those of the previously reported data where activity of endo-1,4-β xylanase was optimum at 30 °C (Subbulakshmi and Iyer 2014; Kanimozhi and Nagalakshmi 2014).
Fig. 3

a Effect of incubation temperatures on endo-1,4-β xylanase production from Aspergillus niger KIBGE-IB36. b Effect of Initial pH on endo-1,4-β xylanase production from Aspergillus niger KIBGE-IB36. Error bars represent the standard deviation (n = 3)

Selection of fermentation pH

The pH of the medium plays a significant role in enzyme production. It can either lower the enzyme production by effecting the growth of microorganism or by creating unsuitable toxic environment that leads to the denaturation or inactivation of enzyme produced (Bajaj and Abbass 2011). In the present study, the optimum pH for the production of endo-1,4-β xylanase was achieved at pH 8.0 with specific activity of 1523 U mg−1, whereas minimum activity was observed at pH 4.0 (249 U mg−1) (Fig. 3b). Most of the researchers reported maximum endo-1,4-β xylanase production by filamentous fungi in acidic pH ranging from 5.0 to 6.5 and also near pH 8.0 (Murthy and Naidu 2012; Bajaj and Abbass 2011). Some other investigators reported enzyme production at pH 9.0 and 10.0 (Kapilan and Arasaratnam 2012; Nair et al. 2008). In the present study, A. niger KIBGE-IB36 showed effective tolerance and potential to grow and produce endo-1,4-β xylanase at both acidic and alkaline pH values (pH 6.0–10.0).

Selection of fermentation time period

In this experiment, the production of endo-1,4-β xylanase by A. niger KIBGE-IB36 was determined during different intervals of time (01–10 days) along with fungal biomass estimation. The exponential phase was observed from days 01 to 06, entering the stationary phase up to day 08, and afterwards unstable decline was observed at day 10. The enzyme synthesis increased in the exponential phase (days 03 to 06) and after reaching its maxima both the enzyme activity and fungal biomass then started to decline gradually (Fig. 4a). It has been suggested that prolonged incubation period stimulates the secretion of non-specific proteases that degrade the synthesized enzyme in the medium. Therefore, it is suggested to control the end point of fermentation period (Pal and Khanum 2010). It has been proposed previously that the optimum fermentation period relies on the nature of substrate, organism, macro- and micronutrients and many other fermentation events (Dekker 1983). This obtained result coincides with the previous studies in which maximum endo-1,4-β xylanase was achieved in 6 days of fermentation period (Sharma et al. 2015; Pal and Khanum 2010).
Fig. 4

a Optimization of fermentation period for the production of endo-1,4-β xylanase from Aspergillus niger KIBGE-IB36. b Effect of different concentrations of corncob xylan on endo-1,4-β xylanase production from Aspergillus niger KIBGE-IB36. Effect of different concentrations of salts on endo-1,4-β xylanase production from Aspergillus niger KIBGE-IB36, c MgSO4, d K2HPO4. Error bars represent the standard deviation (n = 3)

Effect of substrate concentration

Specific substrate plays an important role for any enzyme production. In this study, endo-1,4-β xylanase was synthesized using different concentrations (5–20 g L−1) of corncob xylan which was studied in many past studies (Ahmad et al. 2012). In present study, the efficiency of corncob xylan in the maximum induction of endo-1,4-β xylanase production was established in 20 g L−1 of concentration, while 25g L−1 of corncob xylan created inhibitory effect on the production of endo-1,4-β xylanase (Fig. 4b). It might be due to the increased viscosity of the medium that ultimately leads to feedback inhibition of enzyme (Karim et al. 2014). Our results are in line with other research in which they used 20 g L−1 of xylan for the induction of endo-1,4-β xylanase (Shah and Madamwar 2005).

Effect of different nitrogen sources

In the present study, different nitrogen sources (organic/in organic) were studied (Table 1). The result showed that organic nitrogen sources have a profound effect on the production of endo-1,4-β xylanase as compared to inorganic nitrogen sources. Among different organic sources, peptone proved was the inducer for maximum endo-1,4-β xylanase production (3069 U mg−1). Previously, it is also reported that endo-1,4-β xylanase yield was enhanced by the supplementation of peptone (Qinnghe et al. 2004). Other organic nitrogen sources such as tryptone, meat extract, and yeast extract also showed endo-1,4-β xylanase production but to a lower extent as compared to peptone. When different nitrogen sources were combined, a very unique expression was observed to the production of xylanase suggesting that A. niger requires different types of nitrogen sources for its growth and enzyme production. Among five different combinations, meat extract and peptone produce high titers of endo-1,4-β xylanase (4219 U mg−1) which was 1.37 times higher when compared with the medium incorporated solely with peptone. Various researchers have also reported the augmentation of nitrogen source into the fermentation media (Gomes et al. 1994; Bansod et al. 1993).
Table 1

Effect of different nitrogen sources on endo-1,4-β xylanase production from Aspergillus niger KIBGE-IB36

Types of nitrogen source

Nitrogen source (5 g L−1)

Specific activity (U mg−1)

Organic nitrogen sources

Yeast extract

1713 ± 9.24

Meat extract

2166 ± 11.4

Tryptone

2028 ± 7.75

Peptone

3069 ± 18.49

Inorganic nitrogen sources

Urea

1090 ± 8.22

NH4Cl

642 ± 8.86

KNO3

492 ± 10.43

NH4NO3

360 ± 20.85

Combination of organic nitrogen sources

Yeast extract + tryptone

3116 ± 13.54

Yeast extract + peptone

2539 ± 18.90

yeast extract + meat extract

1215 ± 24.37

Meat extract + peptone

4219 ± 8.65

Meat extract + tryptone

3056 ± 9.46

All the experiments were performed in triplicate and the results expressed are the mean values of all experimental setup

Effect of K2HPO4 and MgSO4 concentrations

Microbial metabolism and regulation of enzyme production are reciprocal to the supplementation of salts in the medium (Maciel et al. 2008). In this study, the medium was optimized using different concentrations of K2HPO4 and MgSO4·7H2O. Magnesium ions have a significant effect on the equalization of the ribosomes and cellular membrane (Cui and Zhao 2012). In this study, with the increase of MgSO4·7H2O, a gradual increase was noticed in endo-1,4-β xylanase production up to 0.75 g L−1 (3987 U mg−1), while at 1 g L−1 of magnesium salt the production of endo-1,4-β xylanase was declined (850 U mg−1) (Fig. 4c). In contrast, Naveen and Siddalingeshwara (2015) reported 0.1 g L−1 of MgSO4·7H2O as a finest inducer of endo-1,4-β xylanase.

On the other hand, the presence of K2HPO4 in the growth medium also showed a positive effect on the yield of endo-1,4-β xylanase. At 0.5 g L−1 of K2HPO4, maximum endo-1,4-β xylanase production was observed (6214 U mg−1) but as the concentration of salt increased, it leads towards a decline in endo-1,4-β xylanase production (729 U mg−1) (Fig. 4d). According to the previous investigation, 0.3 g L−1 of K2HPO4 was found to be appropriate for the production of endo-1,4-β xylanase (Salihu et al. 2015). It is reported that K2HPO4 has the potential to maintain the ideal osmotic pressure for high endo-1,4-β xylanase production (Berk 2000). Hence, after optimizing all the medium formulation and physical parameters, a tenfold increase in endo-1,4-β xylanase synthesis was observed (Fig. 5).
Fig. 5

Endo-1,4-β xylanase production before and after optimization of medium from Aspergillus niger KIBGE-IB36. Error bars represent the standard deviation (n = 3)

The result obtained in the present study indicates that among different Aspergillus species, A. niger KIBGE-IB36 has more potential to saccharify corncob xylan efficiently into ample amount of endo-1,4-β xylanase through submerged fermentation. The production at low temperature (30 °C) indicates the mesophilic nature of A. niger KIBGE-IB36 and the production of endo-1,4-β xylanase at alkaline pH makes this enzyme a promising candidate for bio-bleaching processes and other industrial applications. Hence, the current investigation provides direct comparison of enhanced production of endo-1,4-β xylanase up to tenfold after optimization of different physico-chemical parameters of fermentation medium such as pH, temperature, fermentation period, substrate concentration, suitable nitrogen source, and salt concentration.

Methods

Microorganisms

The initial screening was carried out using four strains of Aspergillus species namely Aspergillus fumigatus KIBGE-IB33 [GenBank: KF905648], Aspergillus flavus KIBGE-IB34 [GenBank: KF905649], Aspergillus terreus KIBGE-IB35 [GenBank: KF905649], and A. niger KIBGE-IB36 [GenBank: KF905650] which were isolated previously (Pervez et al. 2015).

Screening of endo-1,4-β xylanase production

All fungal isolates were grown on xylan-containing medium containing; g L−1: (corncob xylan (Carbosynth, UK) 5.0; Nutrient broth 13.0; K2HPO4 2.5; KH2PO4 0.5; CaCl2 0.1; and NH2SO4 0.5). After incubation at 30 °C for 05 days, culture broth was centrifuged at 4000 rpm at 4 °C for 30 min and filtered through Whatman filter paper No. 1. The supernatant was used for the estimation of endo-1,4-β xylanase production. For qualitative confirmation of endo-1,4-β xylanase production, the selected strain was grown on corncob xylan agar medium for 03 days maintaining the condition same as used for the fermentation. The clear hydrolytic zone around the fungal colony was observed after flooding with Congo red (Teather and Wood 1982).

Endo-1,4-β xylanase assay

The enzyme activity of endo-1,4-β xylanase was estimated by evaluation of reducing sugars released from 10 g L−1 of xylan in 10 mM citrate phosphate buffer (pH 5.0) by 3,5,dinitrosalicylic acid method using xylose as a standard (Miller 1959). One unit of enzyme of enzyme activity is defined as the amount of enzyme required to release 1 µmol of xylose per minute of reaction under standard assay conditions. Specific activities were expressed as unit of enzyme per milligram of protein.

Total protein estimation

The total protein was determined in the supernatant by Lowry’s method (1951) using BSA (bovine serum albumin) as a standard.

Selection of fermentation medium

Five different reported media were initially used for the production of endo-1,4-β xylanase and these reported media were designated as media 1 (Kulkarni and Gupta 2013), media 2 (Adhyaru et al. 2014), media 3 (Kocabas and Ozben 2014), media 4 (Yuan et al. 2005), and media 5 (Bibi et al. 2014).

After selection of suitable medium, fermentation conditions were optimized by varying different physico-chemical parameters using A. niger KIBGE-IB36 for the production of maximum endo-1,4-β xylanase.

Optimization of fermentation temperature, pH, and time

For the selection of appropriate temperature for the production of endo-1,4-β xylanase, different temperatures were tested ranging from 20 to 50 °C.

In the next step, the culture was also grown in a different pH medium ranging from 4.0 to 10.0.

The time course and fungal biomass for the production of endo-1,4-β xylanase were also estimated by incubating A. niger KIBGE-IB36 for different time intervals ranging from 03 to 10 days.

Optimization of macro- and micronutrients

In the present study, corncob xylan was used as a substrate for endo-1,4-β xylanase production with different concentrations of xylan ranging from 5 to 30 g L−1.

To determine the effect of nitrogen source, different organic and inorganic nitrogen sources were assimilated in the production medium. Furthermore, the effect of different nitrogen sources in combination was also investigated.

To analyze the influence of MgSO4 and K2HPO4 on endo-1,4-β xylanase production, different concentrations of salts were incorporated in the production medium ranging from 0.1–1 to 0.1 to 10 g L−1, respectively.

Declarations

Authors’ contributions

All authors discussed the results and proofread the manuscript. All authors read and approved the final manuscript.

Acknowledgements

This research was funded by The Karachi Institute of Biotechnology and Genetic Engineering (KIBGE), University of Karachi, Pakistan.

Competing interests

The authors declare that they have no competing interests.

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Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.

Authors’ Affiliations

(1)
The Karachi Institute of Biotechnology and Genetic Engineering, University of Karachi
(2)
Department of Biochemistry, University of Karachi

References

  1. Adhyaru DN, Bhatt NS, Modi HA (2014) Enhanced production of cellulase-free, thermo-alkali-solvent-stable xylanase from Bacillus altitudinis DHN8, its characterization and application in sorghum straw saccharification. Biocatal Agric Biotechnol 3:182–190. doi:10.1016/j.bcab.2013.10.003 Google Scholar
  2. Adinarayana K, Prabhakar T, Srinivasulu V, Rao MA, Lakshmi PJ, Ellaiah P (2003) Optimization of process parameters for cephalosporin C production under solid state fermentation from Acremonium chrysogenum. Process Biochem 39:171–177. doi:10.1016/S0032-9592(03)00049-9 View ArticleGoogle Scholar
  3. Ahmad Z, Butt MS, Anjum FM, Awan MS, Rathore HA, Nadeem MT, Ahmad A, Khaliq A (2012) Effect of corn cobs concentration on xylanase biosynthesis by Aspergillus niger. Afr J Biotechnol 11:1674–1682. doi:10.5897/ajb11.1769 Google Scholar
  4. Arulanandham TV, Palaniswamy M (2014) Production of xylanase by Aspergillus nidulans isolated from litter soil using rice bran as substrate by solid state fermentation. World J Pharm Sci 3: 1805–13. http://www.wjpps.com
  5. Bajaj BK, Abbass M (2011) Studies on an alkali-thermostable xylanase from Aspergillus fumigatus MA28. 3 Biotech 1:161–171. doi:10.1007/s13205-011-0020-x View ArticleGoogle Scholar
  6. Bansod SM, Dutta-Choudhary M, Srinivasan MC, Rele MV (1993) Xylanase active at high pH from an alkalotolerant Cephalosporium species. Biotechnol Lett 15:965–970. doi:10.1007/BF00131765 View ArticleGoogle Scholar
  7. Beily P (1993) Biochemical aspects of the production of microbial hemicellulase. In: Coughlan MP, Hazlewood GP (eds) Hemicellulose and hemicellulases. Portland Press, London, pp 29–51Google Scholar
  8. Berk A (2000) Molecular cell biology, vol 4. WH Freeman, New YorkGoogle Scholar
  9. Bibi Z, Ansari A, Zohra RR, Aman A, Qader SA (2014) Production of xylan degrading endo-1,4-β-xylanase from thermophilic Geobacillus stearothermophilus KIBGE-IB29. J Radiat Res Appl Sci 7:478–485. doi:10.1016/j.jrras.2014.08.001 View ArticleGoogle Scholar
  10. Chanwicha N, Katekaew S, Aimi T, Boonlue S (2015) Purification and characterization of alkaline xylanase from Thermoascus aurantiacus var. levisporus KKU-PN-I2-1 cultivated by solid-state fermentation. Mycoscience 56:309–318. doi:10.1016/j.myc.2014.09.003 View ArticleGoogle Scholar
  11. Chapla D, Pandit P, Shah A (2012) Production of xylooligosaccharides from corncob xylan by fungal xylanase and their utilization by probiotics. Bioresour Technol 115:215–221. doi:10.1016/j.biortech.2011.10.083 View ArticleGoogle Scholar
  12. Cui F, Zhao L (2012) Optimization of xylanase production from Penicillium sp. WX-Z1 by a two-step statistical strategy: Plackett–Burman and Box–Behnken experimental design. Int J Mol Sci 13:10630–10646. doi:10.3390/ijms130810630 View ArticleGoogle Scholar
  13. Dekker RF (1983) Bioconversion of hemicellulose: aspects of hemicellulase production by Trichoderma reesei QM 9414 and enzymic saccharification of hemicellulose. Biotechnol Bioeng 25:1127–1146. doi:10.1002/bit.260250419 View ArticleGoogle Scholar
  14. Gomes DJ, Gomes J, Steiner W (1994) Factors influencing the induction of endo-xylanase by Thermoascus aurantiacus. J Biotechnol 33:87–94. doi:10.1016/01681656(94)90101-5 View ArticleGoogle Scholar
  15. Izidoro SC, Knob A (2014) Production of xylanases by an Aspergillus niger strain in wastes grain. Acta Sci Biol Sci 36:313–319. doi:10.4025/actascibiolsci.v36i3.20567 View ArticleGoogle Scholar
  16. Kanimozhi K, Nagalakshmi PK (2014) Xylanase production from Aspergillus niger by solid state fermentation using agricultural waste as substrate. Int J Curr Microbiol App Sci 3: 437–446. http://www.ijcmas.com
  17. Kapilan R, Arasaratnam V (2012) Comparison of the kinetic properties of crude and purified xylanase from Bacillus pumilus with commercial xylanase from Aspergillus niger. Vingnanam J Sci 10:1–7. doi:10.4038/vingnanam.v10i1.4072 View ArticleGoogle Scholar
  18. Karim A, Nawaz MA, Aman A, Ul Qader SA (2014) Hyper production of cellulose degrading endo (1,4) β-d-glucanase from Bacillus licheniformis KIBGE-IB2. J Radiat Res Appl Sci 8:160–165. doi:10.1016/j.jrras.2014.06.004 View ArticleGoogle Scholar
  19. Kaushik P, Malik A (2009) Fungal dye decolourization: recent advances and future potential. Environ Int 35:127–141. doi:10.1016/j.envint.2008.05.010 View ArticleGoogle Scholar
  20. Klich MA (2002) Biogeography of Aspergillus species in soil and litter. Mycologia 94: 21–27. http://www.mycologia.org/content/94/1/21.short
  21. Kocabas DS, Ozben N (2014) Co-production of xylanase and xylooligosaccharides from lignocellulosic agricultural wastes. RSC Adv 4:26129–26139. doi:10.1039/C4RA02508C View ArticleGoogle Scholar
  22. Kulkarni P, Gupta N (2013) Screening and evaluation of soil fungal isolates for xylanase production. Recent Res Sci Technol 5. http://recent-science.com/
  23. Latif F, Asgher M, Saleem R, Akrem A, Legge RL (2006) Purification and characterization of a xylanase produced by Chaetomium thermophile NIBGE. World J Microbiol Biotechnol 22:45–50. doi:10.1007/s11274-005-5745-4 View ArticleGoogle Scholar
  24. Lenartovicz V, Marques De Souza CG, Guillen Moreira F, Peralta RM (2003) Temperature and carbon source affect the production and secretion of a thermostable β-xylosidase by Aspergillus fumigatus. Process Biochem 38:1775–1780View ArticleGoogle Scholar
  25. Lowry OH, Rosebrough NJ, Farr AL, Randall RJ (1951) Protein measurement with the Folin phenol reagent. J Biol Chem 193: 265–275. http://www.jbc.org/content/193/1/265.citation.full.html#ref-list-1
  26. Lu F, Lu M, Lu Z, Bie X, Zhao H, Wang Y (2008) Purification and characterization of xylanase from Aspergillus ficuum AF-98. Bioresour Technol 99:5938–5941. doi:10.1016/j.biortech.2007.10.051 View ArticleGoogle Scholar
  27. Maciel GM, de Souza Vandenberghe LP, Haminiuk CW, Fendrich RC, Della Bianca BE, da Silva Brandalize TQ, Pandey A, Soccol CR (2008) Xylanase production by Aspergillus niger LPB 326 in solid-state fermentation using statistical experimental designs. Food Technol Biotechnol 46:183–189. http://www.ftb.com.hr/index.php/component/content/article/69-volume-46-issue-no-2/281-xylanase-production-by-aspergillus-niger-lpb-326-in-solid-state-fermentation-using-statistical-experimental-designs
  28. Maheshwari R, Bharadwaj G, Bhat MK (2000) Thermophilic fungi: their physiology and enzymes. Microbiol Mol Biol Rev 64:461–488View ArticleGoogle Scholar
  29. Miller GL (1959) Use of dinitrosalicylic acid reagent for determination of reducing sugar. Anal Chem 31:426–428. doi:10.1021/ac60147a030 View ArticleGoogle Scholar
  30. Murthy PS, Naidu MM (2012) Production and application of xylanase from Penicillium sp. utilizing coffee by-products. Food Bioprocess Technol 5:657–664. doi:10.1007/s11947-010-0331-7 View ArticleGoogle Scholar
  31. Nair SG, Sindhu R, Shashidhar S (2008) Purification and biochemical characterization of two xylanases from Aspergillus sydowii SBS 45. Appl Biochem Biotechnol 149:229–243. doi:10.1007/s12010-007-8108-9 View ArticleGoogle Scholar
  32. Naveen M, Siddalingeshwara KG (2015) Influence of metal source for the production of xylanase from Penicillium citrinum. Int J Curr Microbiol App Sci 4: 815–819. http://www.ijcmas.com
  33. Pal A, Khanum F (2010) Production and extraction optimization of xylanase from Aspergillus niger DFR-5 through solid-state-fermentation. Bioresour Technol 101:7563–7569. doi:10.1016/j.biortech.2010.04.033 View ArticleGoogle Scholar
  34. Pel HJ, de Winde JH, Archer DB, Dyer PS, Hofmann G, Schaap PJ, Turner G, de Vries RP, Albang R, Albermann K, Andersen MR (2007) Genome sequencing and analysis of the versatile cell factory Aspergillus niger CBS 513.88. Nat Biotechnol 25:221–231. doi:10.1038/nbt1282 View ArticleGoogle Scholar
  35. Pervez S, Siddiqui NN, Ansari A, Aman A, Qader SAU (2015) Phenotypic and molecular characterization of Aspergillus species for the production of starch-saccharifying amyloglucosidase. Ann Microbiol 65:2287–2291. doi:10.1007/s13213 View ArticleGoogle Scholar
  36. Polizeli ML, Rizzatti AC, Monti R, Terenzi HF, Jorge JA, Amorim DS (2005) Xylanases from fungi: properties and industrial applications. Appl Microbiol Biotechnol 67:577–591. doi:10.1007/s00253-005-1904-7 View ArticleGoogle Scholar
  37. Qinnghe C, Xiaoyu Y, Tiangui N, Cheng J, Qiugang M (2004) The screening of culture condition and properties of xylanase by white-rot fungus Pleurotus ostreatus. Process Biochem 39:1561–1566. doi:10.1016/S0032-9592(03)00290-5 View ArticleGoogle Scholar
  38. Salihu A, Bala SM, Olagunju A (2015) A statistical design approach for xylanase production by Aspergillus niger using soybean hulls: optimization and determining the synergistic effects of medium components on the enzyme production. Jordan J Biol Sci 8:319–323. doi:10.1016/S0032-9592(03)00290-5 View ArticleGoogle Scholar
  39. Schuster E, Dunn-Coleman N, Frisvad JC, Van Dijck P (2002) On the safety of Aspergillus niger—a review. Appl Microbiol Biotechnol 59:426–435. doi:10.1007/s00253-002-1032-6 View ArticleGoogle Scholar
  40. Senthilkumar SR, Ashokkumar B, Raj KC, Gunasekaran P (2005) Optimization of medium composition for alkali-stable xylanase production by Aspergillus fischeri Fxn 1 in solid-state fermentation using central composite rotary design. Bioresour Technol 96:1380–1386. doi:10.1016/j.biortech.2004.11.005 View ArticleGoogle Scholar
  41. Shah AR, Madamwar D (2005) Xylanase production by a newly isolated Aspergillus foetidus strain and its characterization. Process Biochem 40:1763–1771. doi:10.1016/j.procbio.2004.06.041 View ArticleGoogle Scholar
  42. Sharma S, Vaid S, Bajaj BJ (2015) Screening of thermo-alkali stable fungal xylanases for potential industrial applications. Curr Res Microbiol Biotechnol 3:536–541. doi:10.1016/j.procbio.2004.06.041 Google Scholar
  43. Subbulakshmi S, Iyer PR (2014) Production and purification of enzyme xylanase by Aspergillus niger. Int J Curr Microbiol App Sci 3: 664–668. http://www.ijcmas.com
  44. Suresh PV, Chandrasekaran M (1999) Impact of process parameters on chitinase production by an alkalophilic marine Beauveria bassiana in solid state fermentation. Process Biochem 34:257–267. doi:10.1016/S0032-9592(98)00092-2 View ArticleGoogle Scholar
  45. Teather RM, Wood PJ (1982) Use of Congo red-polysaccharide interactions in enumeration and characterization of cellulolytic bacteria from the bovine rumen. Appl Environ Microbiol 43:777–780Google Scholar
  46. Yuan QP, Wang JD, Zhang H, Qian ZM (2005) Effect of temperature shift on production of xylanase by Aspergillus niger. Process Biochem 40:3255–3257. doi:10.1016/j.procbio.2005.03.020 View ArticleGoogle Scholar

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