Elsevier

Process Biochemistry

Volume 37, Issue 5, 20 December 2001, Pages 549-554
Process Biochemistry

Design of a new rotating drum bioreactor for ligninolytic enzyme production by Phanerochaete chrysosporium grown on an inert support

https://doi.org/10.1016/S0032-9592(01)00233-3Get rights and content

Abstract

The production of ligninolytic enzymes by the white-rot fungus Phanerochaete chrysosporium BKM-F-1767 was studied in a new bioreactor configuration based on a standard rotating drum bioreactor. P. chrysosporium was grown on cubes of nylon sponge, and cultivation was carried out in batch. Two aeration levels: 0.5 and 1 vvm were tested. The latter led to activities about 3-fold higher than the former, achieving maximum manganese-dependent peroxidase (MnP) and lignin peroxidase (LiP) activities of 1350 and 364 U/l, respectively. Moreover, laccase activity was also detected, showing a highest activity of 56 U/l. In addition, the in vitro decolorisation of a model dye (Poly R-478) by the extracellular liquid obtained in the bioreactor was monitored in order to assess its ligninolytic ability. A percentage of Poly R-478 decolorisation of about 19% was achieved, after 15 min of dye incubation.

Introduction

The white-rot fungus Phanerochaete chrysosporium secretes, during its secondary metabolism, several lignin-degrading enzymes including lignin peroxidase (LiP), manganese-dependent peroxidase (MnP) and laccase. The secondary metabolism in this fungus is triggered by nitrogen [1], carbon or sulphur [2] deprivation. In addition to lignin, the above-mentioned enzymes are also able to degrade a wide range of hazardous environmental pollutants [3], [4]. Their application to industrial processes (biobleaching, biopulping, decolorisation, etc.) on a large scale requires the production of high amount of enzyme at low cost. Thus, the design of a system permitting the continuous production of ligninolytic enzymes efficiently is required.

Solid-state fermentation (SSF) involves the growth of microorganisms on moist solid substrates in the absence or near absence of free liquid [5]. The physical nature of the medium is quite different from that in submerged fermentation. For example, a solid bed is more difficult to mix effectively than a liquid broth, and as a consequence, O2 supply and heat removal can be restricted in SSF processes [6]. The kind of solid materials that can be employed in this type of cultivation are classified in two main categories: inert support and non-inert support. The former acts as an attachment place (e.g. plastic foams) whereas the latter also functions as a source of nutrients (e.g. crop wastes).

SSF has gained importance in recent years due to several advantages over submerged fermentation such as superior productivity, simpler techniques, reduced energy requirements, low wastewater output, and improved product recovery [7], [8], [9]. Nevertheless, bioreactor design aspects have not been received enough attention by researchers of SSF and the present state of the art does not indicate an ideal type of bioreactor for solid state processes.

In earlier reports, a high production of extracellular ligninolytic enzymes in semi-solid-state cultures has been achieved and the utility of such cultures has been demonstrated [10], [11], [12].

Among the diverse types of support tested for semi-solid-state processes in previous papers [11], [12], [13], nylon sponge was preferred in the present work, mainly due to its inert nature, which allowed study the efficiency of the bioreactor without interactions of a series of variables related to the composition of a non-inert support. Moreover, its physical features (high roughness, hydrophobic nature and high porosity), permit good attachment of the fungus to the carrier as well as efficient oxygen and nutrients diffusion into the reactor bed.

In previous work [14], [15], different bioreactor configurations were assayed to produce ligninolytic enzymes in semi-solid-state conditions. Those results showed that the choice of an adequate reactor configuration is essential operating in such conditions. Most of these configurations are a modification of conventional bioreactors. Hence, this paper focuses on the development of a new bioreactor configuration, which produces high ligninolytic activities, functioning in semi-solid-state conditions, for a long time period without operational problems.

The bioreactor configuration employed in the present work is very appropriate to operate with immobilised biomass. In order to apply this bioreactor to semi-solid-state processes the volume of the culture medium in contact with the microorganism has been reduced to conditions near to semi-solid-state.

Section snippets

Microorganism and growth medium

P. chrysosporium BKM-F-1767 (ATCC 24725) was grown on a medium prepared according to Tien and Kirk [16] with 10 g glucose/l as carbon source, and replacement of dimethylsuccinate with 20 mM acetate buffer (pH 4.5) [17]. The fungus was grown in 90 ml of this medium at 37 °C in complete darkness for 48 h. After this, the whole culture was homogenised in a blender for 1 min. This homogenate suspension was used to inoculate (10% v/v) the production medium for the preinoculum.

Carrier

The bioreactor was

Results and discussion

Several bioreactor configurations have been employed to obtain ligninolytic enzymes not only in submerged but also in immobilised conditions [25], [26], [27], [28]. In contrast there are few studies on the production of such enzymes in bioreactors operating in semi-solid-state conditions [6], [29]. In the present report, a new bioreactor design, based on conventional rotating drum bioreactors, was tested for the production of ligninolytic enzymes in semi-solid-state conditions.

Conclusions

In view of the results attained, it can be concluded that the bioreactor configuration developed in the present paper is appropriate for the production of ligninolytic enzymes in semi-solid-state conditions. Moreover, it allowed the continuous production of LiP at high activity levels for long times without operational problems.

Acknowledgements

This research was financed by Xunta (PGIDT00PXI30118PR).

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