Open Access Article
This Open Access Article is licensed under a Creative Commons Attribution-Non Commercial 3.0 Unported Licence

Enhanced biohydrogen production from nutrient-free anaerobic fermentation medium with edible fungal pretreated rice straw

Tao Shengab, Lei Zhao*ad, Lingfang Gaoc, Wenzong Liu*c, Guofeng Wue, Jieting Wuf and Aijie Wangac
aState Key Laboratory of Urban Water Resources and Environment, Harbin Institute of Technology, Harbin 150090, China. E-mail: lzhao@hit.edu.cn; Fax: +86 451 86282110
bCollege of Environmental and Chemical Engineering, Heilongjiang Institute of Science and Technology, Harbin, China
cCAS Key Laboratory of Environmental Biotechnology, Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing, China
dAdvanced Water Management Centre, Faculty of Engineering, Architecture and Information Technology, The University of Queensland, Brisbane, Queensland 4072, Australia
eCollege of Life Sciences, Heilongjiang University, Harbin, China
fSchool of Environmental Science, Liaoning University, Shenyang, China

Received 19th April 2018 , Accepted 19th June 2018

First published on 22nd June 2018


Abstract

An edible fungal pretreatment of rice straw was proposed for enhanced hydrogen production while reducing the chemical cost for traditional biological hydrogen production from lignocellulose. In this research, rice straw was pretreated by edible fungus Gymnopus contrarius J2 at room temperature under static conditions for 15 d at first. The highest hydrogen yield of 5.71 mmol g−1-pretreated rice straw was obtained, 74% higher than the counterpart without pretreatment. Chemical composition analysis demonstrated that lignin removal was up to 22.4% with a little cellulose and hemicellulose loss of 13.3% and 17.1%, respectively, which is in favor of hydrogen production. Additionally, microscopic structure observation combined with FT-IR and XRD analysis illustrated the structural disruption of pretreated rice straw, and the crystalline index of rice straw can be decreased by 46.2% after pretreatment, which might account for the hydrogen production enhancement. The results also indicated that the hydrogen yield from pretreated rice straw was not affected without the addition of yeast extract and vitamins to the culture medium, which is substantial evidence that edible fungal pretreated rice straw could provide prerequisite nutrients for hydrogen-producing bacteria. Overall, edible fungal pretreatment has great potential under the mild conditions for high hydrogen yields and thus leads to a new direction to realize a highly efficient and economically competitive biological hydrogen production process from lignocellulosic biomass.


1. Introduction

With the dwindling of finite reserves of fossil fuels and rise of global energy consumption, renewable energy has become a fundamental and growing part of the world's ongoing energy transformation. Hydrogen gas (H2) plays an essential role in the all new energy options developed, because it can be supplemented to any energy stream and applied to any load, as a significant amount of H2 can be easily stored in a number of different ways.1 What's more, as a carbon-free fuel, H2 has high efficiency and low polluting characteristics that can be used for transportation, heating, and power generation where electricity is difficult to use.2 Till now, among the H2 production methods, biological hydrogen (bio-H2) production from lignocellulosic biomass has been widely regarded as one of the most promising approaches due to its environmentally friendly and sustainable process. In China, agricultural wastes make-up the majority of lignocellulosic biomass. Take rice straw as an example, the annual yield is over 230 million tons,3 however, most of which is used for combustion directly, leading to severe environmental pollution and enormous resource waste. If rice straw can be used for H2 production reasonably, additional value would be gained for both environmental and economic benefits.4

Given the crystallinity and heterogeneity of lignocellulose, direct bioconversion of rice straw to H2 has significantly been hindered.5 Hence, selecting an appropriate pretreatment method to disrupt the crystalline structure of rice straw, and increase the accessibility of cellulose and hemicellulose embedded in lignin matrix for H2 producing bacteria is essential.6 Conventional lignocellulose pretreatment mainly includes physical, chemical, and combined physicochemical methods (e.g., grinding, ultrasonic, microwave, alkali, acid, stream explosion, organosolv, and ionic liquid).7 However, most of these approaches are cost-intensive due to high energy and/or chemical requirements,8 the severe pretreatment conditions induced by acid, alkaline, and high temperature also produce various inhibitory byproducts such as furfural and hydroxymethyl furfural (HMF) that would repress the subsequent fermentation process.9 Thus, downstream detoxification is needed, which will unquestionable increase the complexity and cost of the whole fermentation process. In addition, the dumped excessive chemical liquids will lead to severe negative environmental consequences.

Biological pretreatment has been emerging as the most promising methods in recent years,10 it offers advantages such as low investment cost, little energy and chemicals requirement, and mild pretreatment condition when compared with physicochemical pretreatment methods. What's more, no inhibitors that are affecting the following hydrolysis and fermentation processes will be generated,11 thus the procedure related to detoxification can be avoided. The main drawback to the development of biological methods is the low fermentation rate obtained compared to other technologies. To move forward to a more competitive biological lignocellulose pretreatment process, and improve H2 yields, there is a need to keep on studying more fungi for their ability to delignify lignocellulose efficiently. Recent research results showed that during vegetative growth period, the lignin degradation ratio of edible fungi was higher than the cellulose and hemicellulose,12 thus suggesting a great potential to apply on pretreatment of lignocellulose. In addition to the common advantages of inedible fungal pretreatment, edible fungal pretreatment owns some unique features. Firstly, edible fungi processed feedstock can be used for biofuel production directly.13 Besides, edible fungi contained lysine, arginine, and threonine in high concentration, which is an obvious indicator that edible fungi may not only pretreat lignocellulose on purpose, but also owns the potential to provide nutrients for bioenergy producers.13,14 Although some studies showed the mushroom (common edible fungi) waste could be used as the feedstock of bio-H2,15,16 till now, no research is available on H2 production from edible fungal pretreated lignocellulose.

Therefore, this study was carried out to investigate if edible fungal pretreatment could improve H2 yield from rice straw without nutrient addition. The biodelignification characteristics of edible fungus Gymnopus contrarius J2 pretreated rice straw were described first. After that the pretreated rice straw was subjected to H2 production by Thermoanaerobacterium thermosaccharolyticum DD32 (ref. 17) directly to evaluate the enhancement efficiency of edible fungal pretreatment. At last, the nitrogen source and vitamin were removed from the H2 producing culture medium to confirm if edible fungal pretreated rice straw could provide sufficient nutrient to support bacterial growth and H2 production. This is the first study to employ edible fungal pretreatment of rice straw for enhanced H2 production from nutrient-free anaerobic fermentation medium.

2. Materials and methods

2.1 Preparation of raw feedstock

The rice straw used in this research was collected from Shuangyashan farm, Heilongjiang Province, China. The air-dried feedstock was milled to pass through 40-mesh screen at first, then dried under 40 °C until constant weight was obtained.

2.2 Edible fungal pretreatment of rice straw

The edible fungus Gymnopus contrarius J2 was provided by College of Life Science (Heilongjiang University, Heilongjiang Province, China) and maintained on potato dextrose agar (PDA) plates at 4 °C. Sterilized 250 mL Erlenmeyer flask containing 100 mL basic medium were prepared to activate the fungus as described by Swatzell et al. (1996).18 Five pieces of agar medium (about 0.9 cm in diameter) with fungus mycelium was inoculated into each Erlenmeyer flask, and then cultured in an incubator at 28 °C under static conditions for 7 days. Then the edible fungal pretreatment was carried out with grown liquid culture as inoculum. 3 g preserved rice straw samples were added to 250 mL Erlenmeyer flasks, distilled water containing 4 mg L−1 NaNO3, 10 mg L−1 KCl, 14 mg L−1 MgSO4·7H2O, 0.14 mg L−1 FeSO4·7H2O, and 40 mg L−1 KH2PO4 was adjusted to obtain a moisture content of 65%.19,20 After the autoclaved Erlenmeyer flasks containing wet rice straw were cooled to room temperature, each flask was inoculated with 2 mL of homogeneous liquid culture prepared before. After that, the flasks were sealed with a sterile sealing membrane to allow air exchange. Edible fungal pretreatment was conducted at room temperature (25 °C) under static condition for 21 days. Erlenmeyer flasks without fungus inoculation were conducted as control. Samples were taken every third day for further analysis. All tests were performed in triplicate. Solid fractions after pretreatment were dried at 40 °C for 24 h and then kept at 4 °C for further chemical analysis and H2 production.

2.3 Bio-H2 potential tests

Raw and pretreated rice straw samples were fermented by strain T. thermosaccharolyticum DD32, isolated by Sheng et al., (2015)17 that could use lignocellulose for H2 production under anaerobic condition directly. Fermentations were conducted in 100 mL serum bottles with 50 mL culture medium containing: 3.0 g L−1 K2HPO4; 1.5 g L−1 KH2PO4; 1.0 g L−1 NaCl; 0.2 g L−1 KCl; 0.2 g L−1 MgCl2; 1.0 g L−1 NH4Cl; 1.5 g L−1 yeast extract; 0.5 g L−1 cysteine–HCl; 1.0 mL L−1 vitamin solution; 1.0 mL L−1 trace element solution; and 5.0 g L−1 rice straw with or without pretreatment unless otherwise stated as carbon source, vitamin solution and trace element solution were prepared as described by Wolin et al. (1963).21 All fermentation tests were carried out at 55 °C with an initial pH of 7.5, in an orbital incubator shaker with a rotation speed of 150 rpm for 96 hours. Samples were taken every 6 h to determine gas production, biomass concentration, substrate degradation, and liquid end products. All bio-H2 production tests were performed in triplicate.

2.4 Analytical methods

Automatic cellulose analyzer (ANKOM A200i, USA) was used to detect the rice straw composition before and after edible fungal pretreatment in accordance with the manufacturer's instructions.17 To observe the microstructural changes of rice straw caused by edible fungal pretreatment, the rice straw samples were rinsed with water at first, then the dried samples were prepared by mounting on stubs and sputter-coated with gold for scanning electron microscopic (SEM, JEOL JSM-840 SEM 1–5 kV) analysis. Fourier transform infrared spectroscopy (FT-IR) spectra of rice straw samples were analyzed on a Magna-IR 750 (Nicolet Instrument Co., USA) FT-IR Microscope. Each spectrum was recorded in the range between 4000 and 400 cm−1, with the background pure potassium bromide spectrum subtracted from the sample. The crystallinity index (CrI) of rice straw was determined by X-ray diffraction (XRD) using the deconvolution method.22 The gas composition and volatile fatty acids concentration during H2 fermentation was determined by GC (4800, Agilent Technologies, USA), with detected conditions as established by Wang et al. (2011).23 High-performance liquid chromatography (HPLC, LC-10A, Shimadzu Corporation, Kyoto, Japan) equipped with an Aminex HPX-87 P column (Bio-Rad, Hercules, CA) at 80 °C, using 0.02 mol H2SO4 as eluent at a flow rate of 0.4 mL min−1 was employed to measure the potential reducing sugars exist in the supernatant of culture broth.24 Biomass concentration of T. thermosaccharolyticum DD32 was estimated using the Bradford method25 that has been described by Wiegel et al. (2008).26 Activities of cellulase and hemicellulase secreted by H2-producing bacteria T. thermosaccharolyticum DD32 were measured by the method established by Wood and Bhat (1988).27

Analysis of variance (ANOVA) and a Tukey's post hoc test was conducted to compute significant differences among H2 production from different pretreatment time. A P value of less than 0.05 was considered statistically significant.

3. Results and discussion

3.1 Edible fungal pretreatment of rice straw

3.1.1 Chemical composition of raw and pretreated rice straw. To evaluate the lignocellulose degradation efficiency of fungus Gymnopus contrarius J2, chemical composition of rice straw as a function of pretreatment time was analyzed at first and the results were shown in Fig. 1. The raw rice straw used in this study contained 50.4% cellulose, 28.7% hemicellulose, and 19.9% lignin. Shortly after inoculating G. contrarius J2 to the pretreatment medium, rice straw began to be degraded. It can be obtained from Fig. 1 that the cellulose and hemicellulose degradation efficiency was faster than lignin at the beginning. However, 9 days later, an interesting phenomenon was observed that lignin degradation rate began to increase, and the value was even higher than cellulose and hemicellulose. When the processing time extended from 15 d to 18 d, lignin degradation ratio was apparently increased (22.4% to 31.7%), at the same time, the cellulose and the hemicellulose degradation ratio were slightly increased 1.8% (13.3% to 15.1%) and 1.1% (17.1% to 18.2%) respectively. After 21 d pretreatment, 41.9% lignin was removed, accompanied with 22.9% cellulose and 22.7% hemicellulose loss. To prevent further cellulose and hemicellulose loss, and taking into account the whole pretreatment efficiency, the edible fungal pretreatment was carried out for 21 d in the following experiments. During conventional physico-chemical pretreatment processes, abundant cellulose and hemicellulose loss is inevitable.28 Although biological pretreatment is a good method for cellulose and hemicellulose preservation, biological degradation characteristics of lignocellulose varies with different fungi adopted.29–31 For example, Phanerochaete chrysosporium could degrade more cellulose (55.67%) than lignin (18.89%) within 20 days' wheat straw pretreatment,32 Song et al. (2004) employed Pleurotus cetrinopileatus to pretreat corn straw, the same amount of holocellulose (5.4%) and lignin (5.6%) was removed. When using Pholiota nameko for straw pretreatment, cellulose removal ratio (17.3%) was in advance of lignin (14.1%).33 Actually, a higher level of cellulose and hemicellulose content would be favourable for microorganism that could ferment lignocellulosic biomass for bioenergy production. Compared with the reports regarding biological pretreatment by far, the lignin removal and cellulose and hemicellulose reservation yield obtained in this research is the highest. This result primarily indicates that edible fungus G. contrarius J2 owns high potential for application on lignocellulose pretreatment.
image file: c8ra03361g-f1.tif
Fig. 1 Rice straw degradation profile after edible fungal pretreatment.
3.1.2 Biochemical and structural features of raw and pretreated rice straw. SEM was employed to give an insight into the structural modifications of rice straw with different pretreatment time. As shown in Fig. 2, in accordance with the chemical composition of raw and pretreated rice straw, the untreated rice straw showed compact and smooth flat surface, and little corrosion was found on rice straw pretreated with 9 d (Fig. 2A and B).
image file: c8ra03361g-f2.tif
Fig. 2 Scanning electron micrographs (SEMs) of rice straw under different pretreatment duration. (A) 0 d, (B) 9 d, (C) 12 d, (D) 15 d, (E) 18 d, (F) 21 d.

However, after 12 d pretreatment, the surface structure of the pretreated rice straw became rugged and less compact, even some minor erosion was generated (Fig. 2C). When further extend the pretreatment time to 15 d, the initial connected structure became loose, and more erosion troughs and cracks can be observed on the surface of pretreated rice straw (Fig. 2D). The high lignin, cellulose and hemicellulose ratio from 15 days to 18 days leads to the depolymerization of rice straw structure. After 21 d pretreatment, the structure of the rice straw was severely destructed, and plenty of cracks and large holes can be found (Fig. 2F). The SEM analysis could further demonstrate from the point of surface morphology that the edible fungal pretreatment could give rise to the serious structural destruction of rice straw that is suitable for further fermentation. FT-IR was also applied as an analytical tool to determine the chemical structural changes of rice straw under different pretreatment time. The FT-IR spectra of samples were shown in Fig. 3, the functional groups change of pretreated rice straw were particularly reflected between the absorbance spectra 400 cm−1 and 1800 cm−1. The band at 1728 cm−1 (related to the uronic acid ester bonds formed between the carboxylic acid group in hemicellulose and the phenolic hydroxyl group in lignin34), 1603 cm−1 and 1512 cm−1 (assigned to aromatic skeletal vibrations in lignin35), 1464 cm−1 (associated with C–H deformations in lignin), 1416 cm−1 (possibly associated with nonesterified uronic acid or phenolic rings36), 1244 cm−1 (assigned to β-ether bonds in lignin and between lignin and carbohydrates35), and 835 cm−1 (possibly belonging to a C–H out of plane vibration in lignin)37 all diminished in the FT-IR spectrum of Gymnopus contrarius J2 pretreated rice straw. Such results further confirm the chemical components and SEM microstructural analysis.


image file: c8ra03361g-f3.tif
Fig. 3 FT-IR spectra of raw and pretreated rice straw samples.
3.1.3 The crystallinity of raw and pretreated rice straw. The main purpose of pretreatment is not only to remove lignin, but also to break the inter- and intra-chain hydrogen bonding of cellulose fibrils and destruct the cellulose crystalline structure in rice straw,38 thus making the feedstock more accessible to a broad range of microorganisms. In order to investigate the crystallinity changes of rice straw under different pretreatment time, X-ray diffraction (XRD) was performed and the XRD patterns of the raw and pretreated rice straw were shown in Fig. 4. It can be obtained from the results that the crystalline index of raw rice straw was 0.39. After pretreated by G. contrarius J2 for 9 d, the crystalline index was slightly declined to 0.36, which coincide with the chemical composition changes of rice straw. After 15 d pretreatment, the crystalline index of rice straw dramatically declined to 0.21, 46.2%crystallinity reduction of rice straw was achieved. When further increase the operational time, the crystalline index of pretreated rice straw was stepwise decreased from 0.20 to 0.17, which indicated that a maximum of 56.4% crystallinity reduction of rice straw could be achieved after 21 d pretreatment. Crystalline index is an important indicator to evaluate the efficiency of the pretreatments, and the XRD method has been adopted by many researchers. Ma et al. (2015)39 pretreated corncob with alkaline potassium permanganate, the reduction of crystalline index after pretreatment was only 2.53%. When microwave-assisted calcium chloride was adopted for corn stover pretreatment by Li et al., (2013),40 the crystalline index was decreased by only 13.91%.40 From these research results, it can be obtained that G. contrarius J2 pretreatment is a promising method to remove lignin, preserve holocellulose, and decrease the crystalline of rice straw. The pretreatment efficiency can even compare to physicochemical pretreatment, thus suggesting a promising application prospect.
image file: c8ra03361g-f4.tif
Fig. 4 X-ray diffraction spectra of raw and pretreated rice straw samples.

3.2 Edible fungal pretreatment for enhanced H2 production

3.2.1 H2 production profile from edible fungal pretreated rice straw. H2 production profile from rice straw pretreated by edible fungus G. contrarius J2 was shown in Fig. 5. It can be obviously found that H2 production yield was promoted by increasing the pretreatment time within 15 d, the maximum H2 yield of 5.71 mmol g−1 was obtained from 15 d pretreated rice straw, 74% higher than that without pretreatment. When rice straw with longer pretreatment time was used as substrate, the H2 production yield kept constant (5.65 mmol g−1 and 5.71 mmol g−1 for 18 d and 21 d respectively). In theory, the more time spend on pretreatment, the more H2 yields. However, in this research, as the pretreatment time longer than 15 d, lignin removal was accompanied with less cellulose and hemicellulose preservation. Since the substrate available for H2 producing bacteria is limited, the H2 production yield from rice straw would not be increased anymore after 15 d pretreatment, similar results have also been verified by Zhao et al. (2014).5
image file: c8ra03361g-f5.tif
Fig. 5 Profile of H2 production from edible fungal pretreated rice straw.
3.2.2 Comparison of H2 production from edible fungal pretreated rice straw with and without nutrient addition. As mentioned at the beginning of this paper, edible fungi could not only depose the structure of lignocellulosic feedstock, but also improve the nutritive value of lignocellulose.41 The edible fungi themselves were good resources of digestible proteins, β-glucans, and B-vitamins42 that were necessary for microorganism growth. Therefore, if edible fungal pretreated rice straw was subjected to H2 fermentation directly, it is feasible to reduce the addition of essential nutrient elements to H2 producing medium, and thus further reduce the H2 production cost. In this research, H2 production potential tests were carried out from 15 d pretreated rice straw, the organic nitrogen source yeast extract (YE), vitamin solution, and a combination of both were omitted from the H2 fermentation hemicellulose preservation, H2 yield, and additional nutrients provided, edible fungal pretreatment would be suggested as a promising pretreatment method for enhancing direct H2 production from lignocellulose. The results presented here demonstrate a new biological conversion of lignocellulosic culture separately. Rice straw without pretreatment was used as control. As shown in Fig. 6a, when raw rice straw was used as substrate, the maximum H2 yield of 3.72 mmol g−1 was obtained from the culture contained both YE and vitamin. This value was much higher than the medium without YE (2.51 mmol g−1) and vitamin (3.24 mmol g−1) separately, and a mixture of both (2.24 mmol g−1). When the pretreated rice straw was used as substrate, the H2 yield obtained from the medium without addition of YE and vitamin was 5.21 mmol g−1 (Fig. 6b), this value was not significant different (P-value > 0.05) from the medium contained both YE and vitamin (5.63 mmol g−1). What's more, the maximum H2 production yield obtained in this research was comparable to relevant studies through physicochemical pretreatments and even higher than the biological pretreatments (as shown in Table 1). The cellulose and hemicellulose degradation ratios of rice straw were further investigate to give an insight into the phenomenon. As shown in Fig. 6c and d. In accordance with H2 production profile, when pretreated rice straw was used as substrate, the cellulose and hemicellulose degradation ratios were similar to each other. However, the value differed when raw rice straw was used as substrate, as YE, vitamin, or a mixture of both was removed from culture medium, the holocellulose degradation ratio declined obviously. The activities of cellulase (endo-glucanase and exo-glucanase) and hemicellulase (xylanase and β-xylosidase) were also measured and the results listed in Table 2 showed that although YE, vitamin, and a mixture of both were removed from the medium respectively, the cellulase and hemicellulase activities were almost not affected. While the cellulase and hemicellulase activities with raw rice straw as substrate presented a different performance. When YE, vitamin, or a mixture of both was removed from the medium respectively, the maximum activities of β-D-glucanohydrolase, endo-glucanase, exo-glucanase, xylanase, and β-xylosidase were 2.0–4.5 times lower than that contained both YE and vitamin. Although T. thermosaccharolyticum DD32 could be able to use ammonia as nitrogen source, the cellulase and hemicellulase activities can be only promoted by the organic nitrogen source.43 The results obtained above demonstrated that edible fungal pretreatment is an efficient pretreatment method for enhanced H2 production, and could provide sufficient nitrogen source and vitamins to support efficient lignocellulose hydrolysis by cellulase and hemicellulase. Overall, from the aspects of lignin removal, crystalline reduction, cellulose and biomass to H2 process which is more economically feasible and energy efficient.
image file: c8ra03361g-f6.tif
Fig. 6 H2 production from edible fungal pretreated rice straw with nutrient deletion. (a) H2 production from raw rice straw with nutrient deletion; (b) H2 production from edible fungal pretreated rice straw with nutrient deletion; (c) Substrate degradation of raw rice straw with nutrient deletion; (d) substrate degradation of edible fungal pretreated rice straw with nutrient deletion.
Table 1 Comparison of H2 yields with other relevant works
Microorganism Temperature (°C) Substrate Pretreatment method H2 yield (mL g−1) Ref.
Cow manure and a sediment 35 Wheat straw Ozone pretreatment for 45 min 174.7 44
C. perfringens 40 Wheat straw White-rot fungal-pretreatment 78.5 45
Sewage sludge from a local winery 55 Mixed cornstalk (treated/raw = 1/5) Fungal-pretreatment, 48.7 46
T. thermosaccharolyticum 60 Cornstalk Fungal-pretreatment, 80.3 8
Rotted wood crumb 60 Wheat straw 1[thin space (1/6-em)]:[thin space (1/6-em)]1 (w/w) biomass/ammonia 78.2 47
Anaerobic digester 35 Laminaria japonica Heat-pretreatment 121 °C, 30 min 83.45 48
T. thermosaccharolyticum DD32 55 Rice straw Fungal-pretreatment 126.1 This study
T. thermosaccharolyticum DD32 55 Rice straw Unpretreated 68.09 This study


Table 2 The cellulase/hemicellulase activities during H2 production from rice straw with and without nutrient addition
Cellulase/hemicellulase activity (IU mL−1) Pretreated Rice straw Untreated Rice straw
YE + vitamin YE Vitamin Control YE + vitamin YE Vitamin Control
β-D-glucan glucanohydrolase 0.36 ± 0.05 0.35 ± 0.03 0.36 ± 0.01 0.36 ± 0.02 0.21 ± 0.05 0.16 ± 0.05 0.12 ± 0.05 0.10 ± 0.05
Endo-glucanase 0.27 ± 0.04 0.24 ± 0.02 0.25 ± 0.03 0.22 ± 0.01 0.20 ± 0.02 0.14 ± 0.03 0.11 ± 0.03 0.06 ± 0.02
Exo-glucanase 0.13 ± 0.01 0.12 ± 0.02 0.13 ± 0.02 0.14 ± 0.02 0.08 ± 0.02 0.08 ± 0.01 0.04 ± 0.01 0.02 ± 0.01
Xylanase 0.07 ± 0.01 0.07 ± 0.03 0.05 ± 0.02 0.06 ± 0.01 0.04 ± 0.01 0.03 ± 0.01 0.03 ± 0.02 0.02 ± 0.01
β-Xylosidase 0.20 ± 0.04 0.19 ± 0.02 0.18 ± 0.01 0.18 ± 0.02 0.09 ± 0.03 0.08 ± 0.04 0.04 ± 0.01 0.02 ± 0.01


4. Conclusion

This study demonstrated H2 production from rice straw can be greatly improved by employing edible fungal pretreatment. Rice straw pretreated with G. contrarius J2 for 15 d showed 22.4% lignin removal and 46.2% crystalline reduction with less cellulose and hemicellulose loss. Afterwards, the pretreated rice straw was subjected to H2 production by T. thermosaccharolyticum DD32 directly, high H2 yield of 5.21 mmol g−1 was obtained under the condition with or without nutrient addition. Overall, edible fungal pretreatment could be an economically and technically feasible approach for enhancing biological lignocellulosic biomass conversion to H2.

Conflicts of interest

There are no conflicts to declare.

Acknowledgements

This research was supported by the National Science Foundation for Distinguished Young Scholars (Grant No. 51225802). Lei Zhao acknowledges the Open Project of State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology (No. ES201810-01), the Fundamental Research Funds for the Central Universities (Grant No. HIT. NSRIF. 201859), China, and the UQ Fellowship (2016000091), UQ Early Career Research Grant (2017003152) from the University of Queensland, Australia.

References

  1. M. Calusinska, C. Hamilton, P. Monsieurs, G. Mathy, N. Leys, F. Franck, B. Joris, P. Thonart, S. Hiligsmann and A. Wilmotte, Biotechnol. Biofuels, 2015, 8, 27 CrossRef PubMed.
  2. B. F. Liu, G. J. Xie, R. Q. Wang, D. F. Xing, J. Ding, X. Zhou, H. Y. Ren, C. Ma and N. Q. Ren, Biotechnol. Biofuels, 2015, 8, 8 CrossRef PubMed.
  3. Y. He, Y. Pang, Y. Liu, X. Li and K. Wang, Energy Fuels, 2008, 22, 2775–2781 CrossRef.
  4. M. Kim, Y. Yang, M. S. Morikawa-Sakura, Q. Wang, M. V. Lee, D. Y. Lee, C. Feng, Y. Zhou and Z. Zhang, Int. J. Hydrogen Energy, 2012, 37, 3142–3149 CrossRef.
  5. L. Zhao, G. L. Cao, A. J. Wang, H. Y. Ren, K. Zhang and N. Q. Ren, Biotechnol. Biofuels, 2014, 7, 178 CrossRef PubMed.
  6. W. Seunggon, C. Eunjin, L. Daeseok, L. Soojung, L. Youngju and B. Hyeunjong, Biotechnol. Biofuels, 2015, 8, 228 CrossRef PubMed.
  7. T. Sheng, L. Zhao, W. Z. Liu, L. Gao and A. J. Wang, RSC Adv., 2017, 7, 32076–32086 RSC.
  8. L. Zhao, G.-L. Cao, A.-J. Wang, H.-Y. Ren, D. Dong, Z.-N. Liu, X.-Y. Guan, C.-J. Xu and N.-Q. Ren, Bioresour. Technol., 2012, 114, 365–369 CrossRef PubMed.
  9. E. Palmqvist and B. Hahn-Hägerdal, Bioresour. Technol., 2000, 74, 17–24 CrossRef.
  10. Z. Jian, Z. Zhu, X. Wang, W. Nan, W. Wei and B. Jie, Biotechnol. Biofuels, 2010, 3, 26 CrossRef PubMed.
  11. Z. Gao, T. Mori and R. Kondo, Biotechnol. Biofuels, 2012, 5, 28 CrossRef PubMed.
  12. V. Pandey and M. Singh, Cell. Mol. Biol., 2014, 60, 29–34 Search PubMed.
  13. R. Bisaria, M. Madan and S. N. Mukhopadhyay, Biotechnol. Lett., 1983, 5, 811–812 CrossRef.
  14. E. Jwanny, M. Rashad and H. M. Abdu, Appl. Biochem. Biotechnol., 1995, 50, 71–78 CrossRef PubMed.
  15. Y.-C. Li, S.-Y. Wu, C.-Y. Chu and H.-C. Huang, Int. J. Hydrogen Energy, 2011, 36, 14245–14251 CrossRef.
  16. C. H. Lay, I. Y. Sung, G. Kumar, C. Y. Chu, C. C. Chen and C. Y. Lin, Int. J. Hydrogen Energy, 2012, 37, 16473–16478 CrossRef.
  17. T. Sheng, L. Gao, L. Zhao, W. Liu and A. Wang, RSC Adv., 2015, 5, 99781–99788 RSC.
  18. L. J. Swatzell, M. J. Powell and J. Z. Kiss, Int. J. Plant Sci., 1996, 157, 53–62 CrossRef PubMed.
  19. J. Lalak, A. Kasprzycka, D. Martyniak and J. Tys, Bioresour. Technol., 2016, 200, 194–200 CrossRef PubMed.
  20. A. M. Mustafa, T. G. Poulsen and K. Sheng, Appl. Energy, 2016, 180, 661–671 CrossRef.
  21. E. Wolin, M. J. Wolin and R. Wolfe, J. Biol. Chem., 1963, 238, 2882–2886 Search PubMed.
  22. R. Teeäär, R. Serimaa and T. Paakkarl, Polym. Bull., 1987, 17, 231–237 CrossRef.
  23. a. Wang, L. Gao, R. Nanqi, X. Jifei, L. Chong, C. Guangli, Y. Hao, L. Wenzong, C. L. Hemme and H. Zhili, Appl. Environ. Microbiol., 2011, 77, 517–523 CrossRef PubMed.
  24. A. Wang, N. Ren, Y. Shi and D.-J. Lee, Int. J. Hydrogen Energy, 2008, 33, 912–917 CrossRef.
  25. M. M. Bradford, Anal. Biochem., 1976, 72, 248–254 CrossRef PubMed.
  26. J. Wiegel, L. G. Ljungdahl and A. L. Demain, Crit. Rev. Biotechnol., 2008, 3, 39–108 CrossRef.
  27. T. M. Wood and K. M. Bhat, Methods Enzymol., 1988, 87–112 Search PubMed.
  28. C. Wan and Y. Li, Biotechnol. Adv., 2012, 30, 1447 CrossRef PubMed.
  29. E. Rouches, S. Zhou, J. P. Steyer and H. Carrere, Process Biochem., 2016, 51, 1784–1792 CrossRef.
  30. R. Wang, T. You, G. Yang and F. Xu, ACS Sustainable Chem. Eng., 2017, 5(11), 10849–10857 CrossRef.
  31. F. Ma, X. Huang, M. Ke, Q. Shi, Q. Chen, C. Shi, J. Zhang, X. Zhang and H. Yu, ACS Sustainable Chem. Eng., 2017, 5(10), 8884–8894 CrossRef.
  32. S. Kuhar, L. M. Nair and R. C. Kuhad, Can. J. Microbiol., 2008, 54, 305 CrossRef PubMed.
  33. R. Q. Song and X. Deng, J. For. Res., 2004, 15, 223–226 CrossRef.
  34. N. C. Carpita and D. M. Gibeaut, Plant J., 1993, 3, 1–30 CrossRef PubMed.
  35. L. Liu, J. S. Sun, M. Li, S. H. Wang, H. S. Pei and J. S. Zhang, Bioresour. Technol., 2009, 100, 5853–5858 CrossRef PubMed.
  36. A. Alonso-Simón, P. García-Angulo, H. Mélida and A. Encina, Plant Signaling Behav., 2011, 6, 1104–1110 CrossRef PubMed.
  37. M. D. Harrison, Z. Zhang, K. Shand, I. M. O'Hara, W. O. S. Doherty and J. L. Dale, Bioresour. Technol., 2013, 148, 105–113 CrossRef PubMed.
  38. A. D. Moreno and L. Olsson, Pretreatment of Lignocellulosic Feedstocks, Springer International Publishing, 2017 Search PubMed.
  39. L. Ma, Y. Cui, R. Cai, X. Liu, C. Zhang and D. Xiao, Bioresour. Technol., 2015, 180, 1 CrossRef PubMed.
  40. H. Li and J. Xu, Bioresour. Technol., 2013, 127, 112–118 CrossRef PubMed.
  41. M. Yamakawa, H. Abe and M. Okamoto, Nihon Chikusan Gakkaiho, 1992, 63, 129–133 CrossRef.
  42. M. Sadler, Nutr. Bull., 2003, 28, 305–308 CrossRef.
  43. J. Steiner, C. Socha and J. Eyzaguirre, World J. Microbiol. Biotechnol., 1994, 10, 280–284 CrossRef PubMed.
  44. T. A. D. Nguyen, S. J. Han, J. P. Kim, S. K. Mi, K. O. You and J. S. Sang, Int. J. Hydrogen Energy, 2008, 33, 5161–5168 CrossRef.
  45. Z. Zhi and W. Hui, Bioprocess Biosyst. Eng., 2014, 37, 1–12 CrossRef.
  46. X. Y. Cheng and C. Z. Liu, Appl. Energy, 2012, 91, 1–6 CrossRef.
  47. G. L. Cao, X. F. Xia, L. Zhao, Z. Y. Wang, X. Li and Q. Yang, Int. J. Hydrogen Energy, 2013, 38, 15653–15659 CrossRef.
  48. H. Liu and G. Wang, Int. J. Hydrogen Energy, 2014, 39, 9012–9017 CrossRef.

This journal is © The Royal Society of Chemistry 2018