Scholarly article on topic 'Comparison of Seven Chemical Pretreatments of Corn Straw for Improving Methane Yield by Anaerobic Digestion'

Comparison of Seven Chemical Pretreatments of Corn Straw for Improving Methane Yield by Anaerobic Digestion Academic research paper on "Chemical engineering"

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Academic research paper on topic "Comparison of Seven Chemical Pretreatments of Corn Straw for Improving Methane Yield by Anaerobic Digestion"

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Comparison of Seven Chemical Pretreatments of Corn Straw for Improving Methane Yield by Anaerobic Digestion

Zilin Song1, GaiheYang2, Xiaofeng Liu1*, Zhiying Yan2*, Yuexiang Yuan1, Yinzhang Liao1

1 Chengdu Institute of Biology, Chinese Academy of Science, Chengdu, Sichuan, PR China, 2 Research Center of Recycle Agricultural Engineering Technology of Shaanxi Province, Northwest A&F University, Yangling, Shaanxi, PR China


Agriculture straw is considered a renewable resource that has the potential to contribute greatly to bioenergy supplies. Chemical pretreatment prior to anaerobic digestion can increase the anaerobic digestibility of agriculture straw. The present study investigated the effects of seven chemical pretreatments on the composition and methane yield of corn straw to assess their effectiveness of digestibility. Four acid reagents (H2SO4, HCl, H2O2, and CH3COOH) at concentrations of 1%, 2%, 3%, and 4% (w/w) and three alkaline reagents (NaOH, Ca(OH)2, and NH3?H2O) at concentrations of 4%, 6%, 8%, and 10% (w/ w) were used for the pretreatments. All pretreatments were effective in the biodegradation of the lignocellulosic straw structure. The straw, pretreated with 3% H2O2 and 8% Ca(OH)2, acquired the highest methane yield of 216.7 and 206.6 mL CH4 g VS " in the acid and alkaline pretreatments, which are 115.4% and 105.3% greater than the untreated straw. H2O2 and Ca(OH)2 can be considered as the most favorable pretreatment methods for improving the methane yield of straw because of their effectiveness and low cost.

Citation: Song Z, GaiheYang, Liu X, Yan Z, Yuan Y, et al. (2014) Comparison of Seven Chemical Pretreatments of Corn Straw for Improving Methane Yield by Anaerobic Digestion. PLoS ONE 9(4): e93801. doi:10.1371/journal.pone.0093801

Editor: Dwayne Elias, Oak Ridge National Laboratory, United States of America

Received December 4, 2013; Accepted March 5, 2014; Published April 2, 2014

Copyright: © 2014 Song et al. This is an open-access article distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.

Funding: This study was supported by the National 973 of China (No. 2013CB733502), Applied Basic Research Program of Sichuan Province, China (No. 2013JY0050) and Deployment Project of Chinese Academy of Sciences (No. KGZD-EW-304-1). The funders had no role in study design, data collection and analysis, decision to publish, or preparation of the manuscript.

Competing Interests: The authors have declared that no competing interests exist. * E-mail: (XL); (ZY)


Biomass is considered as a valuable alternative energy source to fossil fuels worldwide because it can be converted into various available forms of energy, such as heat, electricity, steam, biogas, hydrogen, and liquid transportation biofuels [1,2]. As the largest agricultural country in the world, China has an abundance of biomass resources. Approximately 800 million tons of various crop residues are produced in China per year, of which corn and wheat straw account for 216 and 135 million tons, respectively [3]. Crop straws have not been widely used for bioenergy production because of the undeveloped conversion technology. Instead, many crop straws are burnt or directly dumped into the fields, causing serious environmental pollution and degraded soil conditions [4]. Therefore, the development of inexpensive and effective technologies for corn straw utilization is necessary.

Anaerobic digestion (AD) of agricultural straw for bioenergy production is widely used as a promising and alternative energy source to fossil fuels [5]. This technology has been considered as the main commercially viable option for the both treatment and recycling of biomass wastes, and thus is of great interest from an environmental and bioenergy source perspective [6]. However, the efficiency of this technology in treating agricultural straws is limited because the components of straw (lignin, cellulose, and hemicellulose) are difficult to degrade; thus, soluble compounds with low molecular weights are less available for anaerobic microorganisms [7]. Straw pretreatments prior to AD is a simple

and effective method of improving the biodegradability of lignocellulosic materials because it can decompose cellulose and hemicellulose into relatively readily biodegradable components while breaking down the linkage between polysaccharide and lignin to make cellulose and hemicellulose more accessible to bacteria [8,9].

Pretreatment methods mainly include physical methods [2,10], chemical methods [11-14], biological methods [1,15], and a combination of the abovementioned methods [16,17]. Compared with physical and biological treatment methods, chemical pretreatment methods are predominantly used because they are inexpensive and are effective for enhancing the biodegradation of complex materials [18]. In chemical pretreatment methods, sulphuric acid (H2SO4), hydrochloric acid (HCl), hydrogen peroxide (H2O2), acetic acid (CH3COOH), sodium hydroxide (NaOH), lime (Ca(OH)2), and aqueous ammonia (NH3.H2O) are the common chemicals to improve AD performance of agricultural residues [19-26]. For instance, Fernandez-Cegri et al. [2] reported that the methane yield of sunflower oil cake with Ca(OH)2 is 130 CH4 g"1 COD, which is 25% higher that of the untreated sample. Zhu et al. [12] found that NaOH-pretreated corn stover yields 37.0% to 72.9% higher biogas productions than the untreated sample. Kang et al. [23] showed that the optimal conditions for the ethanol production of rapeseed straw is through immersion in aqueous ammonia containing 19.8% ammonia water at 69.0°C for 14.2 h. In addition, H2SO4, HCl, and

Table 1. Effect of acid pretreatment on the chemical composition of corn straw.

Pretreatment Concentration Cellulose % Hemicellulose % Lignin % TC % C/N

H2SO4 1% 47.1 ±2.5 a 26.961.2 a 7.560.5 a 37.3 62.0 b 45.562.0 b

2% 41.361.8 b 22.561.8 b 7.360.4 a 30.661.9 c 38.761.6 c

3% 38.061.6 bc 16.261.2 c 7.360.4 a 30.3 62.1 c 37.961.1 c

4% 36.1 ±1.6 c 13.060.9 d 6.760.5 a 25.3 61.5 d 30.963.2 d

Untreated 49.361.8 a 28.861.4 a 7.560.4 a 42.3 62.8 a 51.463.6 a

HCl 1% 46.7 ±2.2 a 26.261.9 a 7.960.5 a 37.1 62.0 b 44.261.8 b

2% 40.462.0 b 22.262.0 b 7.260.7 a 32.462.0 c 39.560.9 c

3% 38.261.6 b 17.361.0 c 6.460.6 a 29.2 61.9 c 38.462.1 c

4% 35.460.8 c 14.561.3 d 6.961.0 a 26.1 61.2 d 32.660.7 d

Untreated 49.361.8 a 28.861.4 a 7.560.4 a 42.362.8 a 51.463.6 a

CH3COOH 1% 43.861.9 b 26.862.6 a 7.1 60.9 a 38.662.9 a 47.761.6 ab

2% 37.462.4 c 21.761.1 b 6.760.5 a 34.860.9 b 46.461.9 b

3% 34.260.9 d 18.1 61.4 c 6.860.5 a 29.5 60.9 c 36.962.6 c

4% 30.461.5 e 15.1 60.5 d 6.760.7 a 26.461.6 d 32.260.7 d

Untreated 49.361.8 a 28.861.4 a 7.560.4 a 42.3 62.8 a 51.463.6 a

H2O2 1% 40.561.5 b 25.061.4 b 7.060.2 a 34.462.6 b 44.762.3 b

2% 34.662.1 c 20.862.3 c 6.560.3 b 28.760.8 c 37.361.1 c

3% 30.860.8 d 14.361.2 d 5.760.4 c 25.1 61.2 d 30.662.4 d

4% 22.560.6 e 9.560.7 e 5.1 60.2 d 20.461.3 e 25.262.1 e

Untreated 49.361.8 a 28.861.4 a 7.560.4 a 42.3 62.8 a 51.463.6 a

Data are expressed as mean ± deviation of triplicate measurements. TC: Total carbon.

The ANOVA test was conducted to determine the differences between each pretreatment. Values with the same letters in each pretreatment indicate no significant

difference at P<0.05.


CH3COOH pretreatments have been used to improve the AD of lignocellulosic materials [24,25]. However, the most economically and effectively favorable treatments, among these, have yet to be identified. Additionally, the optimal concentration for the favorable pretreatment has been scarcely reported. Such information is important for the reasonable and efficient utilization of agricultural residues. The present study compared the effects of four acid and three alkaline pretreatments on the lignocellulosic compositions and methane yield of corn straws by AD. Our objective was to determine the most cost-effective pretreatment methods for enhancing the methane yield of straws.

Materials and Methods

Raw Material

Corn straw was obtained from a local villager near the Northwest A&F University (Yangling, Shaanxi, China). Prior to use, the straws were air dried, cut into lengths of 20 mm to 30 mm using a grinder, and then individually homogenized for further use. The full composition and main features of the corn straw were as follows (mean values of three determinations ± standard deviations): total solids (TS), 93.6% ±2.8%; volatile solids (VS), 86.7% ±1.9%; total carbon (TC), 42.3% ±2.8%; total nitrogen (TN), 0.82%±0.05%; hemicellulose, 28.8%±1.4%; cellulose, 49.3%±1.8%; and lignin, 7.5%±0.4%.

Pretreatment Process

Seven pretreatment methods were used in this study, including four acid treatments (H2SO4, HCl, CH3COOH, and H2O2) and three alkaline treatments (NaOH, Ca(OH)2, and NH3?H2O). The

reagents were purchased from Sinophram Chemical Reagent Co. Ltd, Beijing, China. The chosen pretreatment conditions were based on previous studies [9,20] and carried out using different concentrations of reagents. Acid reagents (H2SO4, HCl, H2O2, and CH3COOH) at concentrations of 1%, 2%, 3%, and 4% (w/ w) and alkaline reagents (NaOH, Ca(OH)2, and NH3?H2O) at concentrations of 4%, 6%, 8%, and 10% (w/w) were used for the pretreatments. The corn straw not pretreated with any chemicals was used as the control. Each pretreatment was conducted in triplicate.

Dried corn straw (500 g) was soaked in the prepared 1.5 L solutions contained in beakers, yielding straw samples with 75% moisture. All prepared beakers were covered with plastic films, secured with a plastic ring, and then stored in a chamber at an ambient temperature of 25±2°C for 7 days. After the pretreat-ment, the straws were removed from the beakers, dried in an electronic oven (HengFeng SFG-02.600, Huangshi, China) at 80°C for 48 h, and then kept in a refrigerator for composition determination and AD experiments to investigate the effect of different chemical treatments on methane yield.

Anaerobic Digestion

The digestion experiment was conducted according to methods described by Song et al. [22] using laboratory-scale simulated anaerobic digesters in 1 L Erlenmeyer flasks. The batch reactors were used to determine the digestion levels of the straws with different pretreatments. Each pretreated straw was used as the digestion material, with the untreated straw as the control. The digestion inoculum was collected from an anaerobic digester in a model village powered by household biogas (Yangling, Shaanxi,

Pretreatment Concentration Cellulose % Hemicellulose % Lignin % TC % C/N

NaOH 4% 48.063.9 a 23.861.4 b 6.760.5 a 39.360.8 a 49.161.0 a

6% 46.163.0 a 20.660.9 c 5.560.5 b 35.462.3 b 46.060.8 b

8% 46.762.2 a 16.260.9 d 4.660.3 c 33.761.6 b 42.162.1 c

10% 47.462.6 a 11.361.2 e 4.060.2 d 28.161.2 c 34.761.3 d

Untreated 49.361.8 a 28.861.4 a 7.560.4 a 42.362.8 a 51.463.6 a

Ca(OH)2 4% 47.561.8 a 24.662.2 b 6.860.2 a 37.861.5 a 45.061.8 b

6% 46.162.4 a 21.261.4 c 6.060.3 b 32.863.1 b 40.062.0 c

8% 46.361.9 a 16.461.1 d 5.460.2 c 29.462.0 b 38.760.7 c

10% 48.061.1 a 12.361.2 e 4.660.3 d 22.661.8 c 28.361.9 d

Untreated 49.361.8 a 28.861.4 a 7.560.4 a 42.362.8 a 51.463.6 a

NH3-H2O 4% 48.161.2 a 25.761.9 a 7.060.6 ab 39.261.9 a 48.462.1 a

6% 45.463.3 a 22.460.8 b 6.660.3 b 36.662.5 b 48.860.4 a

8% 45.963.0 a 18.661.8 c 6.260.2 c 33.260.9 b 41.561.8 b

10% 45.162.9 a 17.861.1 c 5.560.2 d 30.761.6 c 37.461.8 b

Untreated 49.361.8 a 28.861.4 a 7.560.4 a 42.362.8 a 51.463.6 a

Hemicellulose %

Lignin %

Untreated Ca(OH)2

Untreated NH3.H,O


6% 8% 10%

6% 8% 10%

47.462.6 a 49.361.8 a

47.561.8 a 46.162.4 a

46.361.9 a

48.061.1 a

49.361.8 a

48.161.2 a

45.463.3 a 45.963.0 a

45.162.9 a 49.361.8 a

11.361.2 e 28.861.4 a 24.66 2.2 b 21.26 1.4 c 16.46 1.1 d 12.361.2 e 28.861.4 a 25.761.9 a 22.46 0.8 b

18.66 1.8 c 17.86 1.1 c 28.861.4 a

6.760.5 a

5.560.5 b

4.660.3 c 4.060.2 d

7.560.4 a

6.860.2 a

6.060.3 b

5.460.2 c

4.660.3 d

7.560.4 a

7.060.6 ab

6.660.3 b 6.260.2 c 5.560.2 d

7.560.4 a

39.360.8 a 35.462.3 b 33.761.6 b 28.161.2 c 42.362.8 a 37.861.5 a 32.863.1 b 29.462.0 b 22.661.8 c

42.362.8 a

39.261.9 a

36.662.5 b 33.260.9 b

30.761.6 c 42.362.8 a

49.161.0 a 46.060.8 b

42.162.1 c

34.761.3 d

51.463.6 a

45.061.8 b

40.062.0 c

38.760.7 c

28.361.9 d 51.463.6 a

48.462.1 a

48.860.4 a

41.561.8 b 37.461.8 b 51.463.6 a

Data are expressed as mean 6 deviation of triplicate measurements. TC: Total carbon.

The ANOVA test was conducted to determine the differences between each pretreatment. Values with the same letters in each pretreatment indicate no significant

difference at P<0.05.


China). This particular inoculum was selected because of its high methanogenic activity. The characteristics and features of the anaerobic inoculum used were as follows: pH, 7.660.1; TS, 86.6%; and VS, 47.5%. The digestion material (500 g) and inoculums (200 g) were added to each digester, followed by deionized water to obtain an 8% TS content. They were stirred and placed in a thermostatic water bath at the mesophilic condition of 376 1°C for 35 d of AD. All reactors were tightly sealed with rubber septa and screw caps. All reactors were gently mixed manually at approximately 1 min d21 prior to biogas

volume measurement to ensure mixing of the reactor contents. Moreover, 200 g of the inoculums was digested to serve as the blank in determining the normalized methane yield of the inoculum by itself. The digestion of each pretreatment was performed in triplicate.

Analysis and Calculations

The volume of biogas was measured by water displacement. The methane content in the produced biogas was analyzed with a fast methane analyzer (Model DLGA-1000, Infrared Analyzer,


Acid pretreatment Alkaline pretreatment

Figure 1. Effect of pretreatments on the methane yield of corn straw. (a) Acid pretreatment; (b) Alkaline pretreatment. Data was expressed at mean ± deviation of triplicate measurements. The ANOVA test was conducted to determine the differences between each pretreatment. Values with the same letters in each pretreatment indicate no significant difference at P<0.05. doi:10.1371/journal.pone.0093801.g001

Figure 2. Effect of pretreatments on the VS consumption of corn straw. (a) Acid pretreatment; (b) Alkaline pretreatment. Data was expressed at mean 6 deviation of triplicate measurements. The ANOVA test was conducted to determine the differences between each pretreatment. Values with the same letters in each pretreatment indicate no significant difference at P<0.05. doi:10.1371/journal.pone.0093801.g002

Dafang, Beijing, China). The TS, VS, TN, and pH of the materials were measured according to the Standard Methods for the Examination of Water and Wastewater of the American Public Health Association [27]. The pH was tested once every 5 d. TC content was analyzed using the method described by Cuetos et al. [28]. The C/N ratio was determined by dividing the total organic carbon content to the TN content. The volatile fatty acid (VFA) was analyzed using a colorimetric method [29], and the result was expressed in terms of acetic acid content. The cellulose, hemicellulose, and lignin contents were analyzed based on the methods previously described by Wang and Xu [30].

Data Analysis

Data is expressed as mean ± standard deviation (SD) of the triplicate measurements. Differences between mean values were examined by ANOVA. Comparisons among means were made using the Duncan multiple range test, and significance was set at P<0.05. All statistical analyses were performed using the software program SPSS 15.0. (SPSS Inc., Chicago, USA).

Figure 3. Change in the pH of pretreated corn straw during digestion. (a) Acid pretreatment; (b) Alkaline pretreatment. Data was expressed

at mean 6 deviation of triplicate measurements.


Figure 4. Change in the VFA of pretreated corn straw during digestion. (a) Acid pretreatment; (b) Alkaline pretreatment. Data was expressed

at mean 6 deviation of triplicate measurements.


Chemicals Concentration Price a(CNY) Cost b(CNY) Methane yield (mL CH4 gVS1)

Acid H2SO4 2% 21 2.57 175.6

HCl 2% 15 4.92 163.4

CH3COOH 4% 12.5 9.34 145.1

H2O2 3% 6 3.6 216.7

Alkaline NaOH 8% 9 4.2 163.5

Ca(OH)2 8% 9.5 4.58 206.6

NH3-H2O 10% 9 19.28 168.3

Corn Straw

The aim of the pretreatments was to change the raw material properties, remove or dissolve lignin and hemicellulose, and reduce the crystallinity of cellulose [31]. In the present study, both acid and alkaline pretreatments changed the lignocellulosic composition of corn straw (Tables 1 and 2). Compared with the untreated straw, the hemicellulose and cellulose contents of the acid-treated straw significantly decreased by 6.6% to 66.0%, and 4.4% to 54.3% (P<0.05), and the hemicellulose and lignin contents of alkaline-treated corn straw decreased by 10.7% to 46.7%, and 10.8% to 60.7%. These results indicated that pretreatments are more effective in breaking down the lignocel-lulose matrix and in changing the chemical components of straw. Considerable amounts of lignocellulose appeared to be decomposed and converted into other soluble components that are available to anaerobic microorganisms [32].

Guo et al. [20] reported that corn stalk mainly lost its hemicellulose and cellulose fractions after the acid treatment and

lost its lignin fraction after the alkaline treatment. Fernandez-Cegri et al. [2] observed that H2SO4 cannot dissolve the lignin of sunflower oil cake, maintaining the same proportion as that of the untreated case. They also found that alkali pretreatments give higher removal levels of lignin compared with other reagents regardless of the temperature effect. The present study revealed a similar phenomenon that acid and alkaline pretreatments had different effects on the lignocellulose composition. In the case of acid reagents, hemicellulose and cellulose contents significantly decreased while the lignin content remained constant in the treated and untreated samples, except when the H2O2 was used that the lignin content decreased by 6.7% to 32.0%. The alkaline treatment was mainly effective in removing the lignin fraction. The effectiveness of degrading the lignocellulosic structure usually depends on the type of pretreatment method used, because of the attack on the different parts of the substrate by different chemicals. Acid pretreatment results in disruption of covalent bonds, hydrogen bonds, and Van der Waals forces that hold together the biomass components, which consequently causes the solubilization of hemicellulose and the reduction of cellulose [33]. In contrast, alkali treatment breaks the links between lignin

Table 3. Economic performance of the different pretreatments.



Price a(CNY)

Cost b(CNY)

Methane yield (mL CH4 gVS1)




2% 2% 4% 3% 8% 8% 10%

21 15 12.5 6 9

2.57 4.92 9.34 3.6 4.2

4.58 19.28

163.4 145.1

206.6 168.3

aThe price was collected from the Sinophram Chemical Reagent Co. Ltd, Beijing China, and the unit of H2SO4, HCl, CH3COOH, H2O2, and NH3.H2O price was per 500 mL, NaOH and Ca(OH)2 was per 500 g. CNY is the abbreviation for Chinese Yuan, and a dollar is equivalent to 6.12 CNY on Oct 1, 2012; Bank of China. b The cost was calculated based on the pretreatment of 1 kg corn straw. doi:10.1371/iournal.pone.0093801.t003

monomers or between lignin and polysaccharides that makes the lignocelluloses swell through saponification reactions [34]. Among the pretreatments, H2O2 and NaOH showed the highest solubilization of hemicellulose cellulose, and lignin contents. This trend can be attributed to the strong oxidation ability of H2O2 [35] and the high alkalinity of NaOH that allow them to break down the lignocellulose matrix to change the chemical components of the straw. The increased degradation of lignocellulosic materials by H2O2 and NaOH suggests that these two chemicals are the most effective in degrading the lignocellulosic structure of corn straw.

The C/N ratio of anaerobic feedstock is significant for AD performance [36]. Analysis of the C/N ratio showed that the percentage of C in the pretreated straw significantly decreased with increasing chemical concentration (P<0.05, Tables 1 and 2). The decrease in TC content also affirmed this result. Although the C/N ratio in the pretreated straw was lower than that of the untreated sample, it was still higher than the optimum C/N ratio of feedstock materials (between 20 and 30) [36]. Therefore, the pretreated straw still represents a good co-digestion biomass because it provides a higher carbon fraction for digestion.

Effects of Pretreatments on the Methane Yield of Corn Straw

The methane yield, defined as CH4 production per unit volatile solids (in mL CH4 g VS '), was determined to compare the energy conversion efficiency and the improvement in biodegradability (Fig. 1). As shown in Fig. 1, the straws pretreated by acid and alkaline had significantly increased methane yields (P<0.05), i.e., an approximate 10.3% to 115.4% higher yield than for the untreated samples. These results are consistent with previous studies [11,17] which verified the effectiveness of chemical pretreatment in improving biodegradability and enhancing bioenergy production. This phenomenon can be explained by the fact that alkaline and acid pretreatments promote organic solubilization and increase the surface area available for enzymatic action [31]. Chemical pretreatments have different effects on the anaerobic digestibility of corn straw. The methane yield was not improved as the chemical concentration increased. The highest methane yield was achieved at different concentrations for the seven pretreatments. For instance, the highest methane yield was achieved by H2SO4 and HCl at 2% concentration, CH3COOOH at 4%, H2O2 at 3%, Ca(OH)2 and NaOH at 8%, and NH3?H2O at 10%. The reason may due to the fact that successful biogasification is not only affected by the sufficient soluble component available but also by anaerobic bacteria. More soluble components from the biodegradation of the lignocellulosic composition need more bacterial to assimilate them. In the present study, the same amount of inoculums (200g) was applied in each digestion experiment, thus, the relative shortage of inoculums could be responsible for the lower methane yield of the chemical pretreatment with high concentration. Among the acid and alkaline treatments, H2O2 and Ca(OH)2 respectively produced the highest methane yield in the straw. This result suggests that H2O2 and Ca(OH)2 are best for improving the methane yield of corn straws compared with the other pretreatments. The methane yield was significantly heightened as the H2O2 concentration increased from 1% to 3% and 4%. However, the methane yield did not increase with further dose increases, showing no significant difference between 3% and 4%. The same trend was also observed for the Ca(OH)2 pretreatment at concentrations between 8% and 10%. The presence of excessive H+ in 4% H2O2 and OH" in the 10% Ca(OH)2 pretreatment can cause toxicity to the methanogens thereby inhibiting their activity and interfering with their

metabolism [37]. Therefore, 3% and 8% are the most suitable concentrations for the H2O2 and Ca(OH)2 pretreatments of corn straw, respectively.

Effects of Pretreatments on VS Reduction of Corn Straw

Methane is generated from the conversion of substrates; thus, the methane yield can be determined by reductions in the amount of dry matter of the substrate, as represented by VS. The VS reductions in the straw are shown in Fig. 2. Consistent with previous studies [22], the chemically-treated corn straw obtained higher VS reductions than untreated samples and exhibited reduction of 57.3% to 70.0% for the acid pretreatment and 57.5% to 70.8% for the alkaline pretreatment. 3% H2O2 and 8% Ca(OH)2 yielded the greatest reduction in the amount of dry matter of the substrate. The pretreatment triggers the conversion of VS into soluble compounds, including sugar, starch, pectin, tannin, cyclitol, and some inorganics, which become available to anaerobic microorganisms. Generally, this treatment contributes to a substantial improvement in the biodegradability of corn straw. High methane production requires more substrates for digestion; thus, increased VS reductions could explain why the methane yield of the treated straw was highly improved.

Effects of Pretreatments on pH during AD

To investigate the effect of pretreatment on the VFA and pH during the AD of corn straw, the optimal concentration of each pretreatment for methane production was selected as follows: 2% H2SO4, 2% HCl, 4% CH3COOH, 3% H2O2, 8% NaOH, 8% Ca(OH)2, and 10% NH3H2O.

Fermentative microorganisms can function in a wider pH range of between 4.0 and 8.5 [38]. In the present study over the first 10 d, the pH of the fermentation broth of the acid-pretreated corn straws was below 7.0 (Fig. 3), whereas that of the three alkaline-pretreated corn straws was over 7.0. The pH curves of all pretreatments were similar, showing a decreasing trend in the initial 10 d and an increasing trend thereafter, slight fluctuations between days 10 to 20. At the end of the fermentation, all pretreatments maintained a pH of approximately 7.0. This trend can be attributed to the variation in VFA concentration because the production of VFA during AD decreases pH. The highly concentrated substrate at the initial phase ofAD supplies sufficient organic acid from the degradation of hemicellulose, cellulose, lignin, and VS for the methanogens [20], which decreases pH and accelerates methanogen growth. As digestion proceeded, the content of organic acid gradually decreased with the consumption by the methanogens, which increased the pH. The shortage in organic acid limited the activities of the methanogens but stimulated the acidogens, which increased the amount of organic acids and the dropped the pH. The activity of the methanogens increased again when the organic acid accumulated to an extent, which increased the pH. However, compared with the dramatic fluctuation in the initial phase of AD, the change in the pH in the middle-late phase was slightly heightened because the concentration of the organic acid in the substrate was not as high as the initial concentration. The lack of significant differences in the pH for all pretreatments at the end of AD indicates that these pretreatments can recover the pH. As shown in Fig. 3, the pH of the fermentation broth of the pretreated corn straw markedly declined compared with that of the untreated corn straw. This result can be ascribed to the various acids in the soluble substance of the pretreated straw being significantly higher than that of the untreated straw.

Effects of Pretreatments on VFA during AD

The VFA concentration of each pretreatment initially increased (Fig. 4) and then decreased, which is contrary to the trend of the pH curve. The VFA content of the fermentation broth from the pretreated straw increased more sharply than that of the untreated corn straw. This result can be attributed to the significantly higher soluble substance content of the pretreated corn straw compared with the untreated samples. Among the seven pretreatments, the average VFA concentrations (mg acetic L21) of the pretreatments during the AD were as follows: 7629 (H2SO4), 7879 (HCl), 4821 (CH3COOH), 9321 (H2O2), 5810(NaOH), 6818 (Ca(OH)2), and 4964 (NH3?H2O). The highest VFA values were observed for H2O2 in the acid treatment, whereas the lowest was observed for CH3COOH. This result is consistent with the results of the hemicellulose, cellulose, and lignin decomposition and methane yield (Table 1), which further confirmed the effectiveness of H2O2 in biodegrading the lignocellulosic structure of straws. Large amounts of hemicellulose and cellulose are converted into simple sugars, lipids (fats) into fatty acids, amino acids, and short-chain organic acids (butyric acid, propionic acid, acetate, and acetic acid), all of which are utilized by methanogens for methane production [15]. In the alkaline pretreatments, the highest VFA content was observed after using Ca(OH)2. This result was consistent with the observations from the methane yield experiments, but contradicted the lignocellulosic composition results where degradation of the lignin fraction was highest after NaOH pretreatments. This disparity can be explained by the fact that successful biogasification is not only affected by the sufficient soluble component available for the anaerobic bacteria but also by the balance between methanogens and acidogens [39]. The excessively high concentration of OH2 in NaOH likely inhibited acetogenesis and disturbed this balance. However, this hypothesis warrants further investigation.

Economic Performance of the Pretreatment Methods

The effectiveness of a pretreatment is not only based on the effectiveness ofAD but also on the economic performance. Table 3 compares the economic performance of the pretreatments at the optimal concentrations for methane yield. H2O2 and H2SO4 showed the lowest costs among the acid pretreatments. However, H2O2 was more favorable because it produced higher methane yields than H2SO4. In the alkaline pretreatments, although no great difference in the expenses was observed between the Ca(OH) 2 and NaOH pretreatments, Ca(OH)2 produced is slightly advantageous over NaOH as it generates a higher methane yield. Therefore, with respect to economic performance and effectiveness, H2O2 and Ca(OH)2 can be considered as the most suitable pretreatments for corn straw.

Recently, some researchers combined chemical and physical treatments to improve the biodegradability of lignocellulose composition. High temperature (120-250°C) is often used in combination with dilute acids or base in a pressure cell for much shorter durations. For instance, Saha et al. [40] found the 74% higher saccharification yield wheat straw was subjected to 0.75%


1. Zhong WZ, Zhang ZZ, Luo YJ, Sun SS, Qiao W, et al. (2011) Effect of biological pretreatments in enhancing corn straw biogas production. Bioresour Technol 102: 11177-11182.

2. Fernandez-Cegri F, Raposo F, de la Rubia MA, Borja R (2013) Effects of chemical and thermochemical pretreatments on sunflower oil cake in biochemical methane potential assays. J Chem Technol Biotechnol 88: 924-929.

3. National Burean of Statistics of China (2010) China Statistical Yearbook of 2009. China Statistics Press, Beijing, China.

v/v of H2SO4 at 121°C for 1 h. Cara et al. [41] shown that olive tree biomass pretreated with 1.4% H2SO4 at 210°C resulted in 76.5% of hydrolysis yields. Rocha et al. [42] reported that ethanol yield as high as 0.47 g/g glucose was achieved in fermentation tests with cashew apple bagasse pretreated with diluted H2SO4 at 121 °C for 15 min. These studies showed the advantage of combination treatment on solubilizing the lignocellulosic composition and shortening the pretreatment time. Nevertheless, depending on the process temperature, some sugar degradation compounds such as furfural and aromatic lignin degradation compounds are detected, and affect the microorganism metabolism in the fermentation step [40]. Furthermore, the pretreatment of high temperature combined with chemicals consumes a substantial amount of energy, and need high facility investment and high treatment cost.

In the present study, although pretreatment time (7 day) was longer than that of chemical treatment with the addition of heat and pressure, the contents of hemicelluloses, cellulose, and lignin fractions of corn straw was greatly reduced, which was contribute to the enhancement of methane production. Furthermore, using single chemicals have no excessive energy consumption and less operation cost. Since cost reduction and low energy consumption are required for an effective pretreatment, chemical pretreatment without the addition of heat and pressure would be desirable to optimize the effectiveness on the process. As for the longer incubation time of the chemical pretreatment, more efforts should be made to investigate the combination of chemicals and low temperature (Below 100°C) pretreatment to shorten the incubation time and improve the anaerobic digestion efficiency.


Four acid pretreatments (H2SO4, HCl, CH3COOH, and H2O2) and three alkaline pretreatments (NaOH, Ca(OH)2, and NH3?H2O) for improving the methane yield of corn straw were compared. All pretreatments were effective in the biodegradation of the lignocellulosic structure. Straw pretreated with 3% H2O2 and 8% Ca(OH)2 elicited the highest methane yields of 216.7 and 206.6 mL CH4 g VS"1, which are 115.4% and 105.3% higher than that of the untreated straw, respectively. H2O2 and Ca(OH)2 are economically and effectively superior to the other pretreat-ments. Therefore, H2O2 and Ca(OH)2 are both recommended as the pretreatments for improving the methane yield of straw.


We thank Dr. Chao Zhang for assistance of improving the paper and advice on statistical treatments.

Author Contributions

Conceived and designed the experiments: ZLS GHY XFL. Performed the experiments: ZLS XFL. Analyzed the data: ZLS ZYY. Contributed reagents/materials/analysis tools: YXY YZL. Wrote the paper: ZLS.

4. Pang YZ, Liu YP, Li XJ (2008) Improving biodegradability and biogas production of corn stover through sodium hydroxide solid state pretreatment. Energ Fuel 22: 2761-2766.

5. Murphy JD, Power NM (2009) An argument for using biomethane generated from grass as a biofuel in Ireland. Biomass Bioenerg 33: 504-512.

6. Amon T, Amon B, Kryvoruchko V, Machmuller A, Hopfner SK, et al. (2007) Methane production through anaerobic digestion of various energy crops grown in sustainable crop rotations. Bioresour Technol 98: 3204-3212.

7. Taherzadeh MJ, Karimi K (2008) Pretreatment of lignocellulosic waster to improve ethanol and biogas production: a review. IntJ Mol Sci 9: 1621—1651.

8. Teghammar A, Yngvesson J, Lundin M, Taherzadeh MJ, Horvath IS (2010) Pretreatment of paper tube residuals for improved biogas production. Bioresour Technol 101: 1206-1212.

9. Ferreira LC, Donoso-Bravo A, Nilsen PJ, Fdz-Polanco F, Perez-Elvira SI (2013) Influence of thermal pretreatment on the biochemical methane potential of wheat straw. Bioresour Technol 143: 251-257.

10. Sapci Z (2013) The effect of microwave pretreatment on biogas production from agricultural straws. Bioresour Technol 128: 487^94.

11. Zheng MX, Li XJ, Li LQ, Yang XJ, He YF (2009) Enhancing anaerobic biogasification of corn stover through wet state NaOH pretreatment. Bioresour Technol 100: 5140-5145.

12. Zhu J, Wan C, Li Y (2010) Enhanced solid-state anaerobic digestion of corn stover by alkaline pretreatment. Bioresour Technol 101: 7523-752.

13. Cao WX, Sun C, Liu RH, Yin RZ, Wu XW (2012) Comparison of the effects of five pretreatment methods on enhancing the enzymatic digestibility and ethanol production from sweet sorghum bagasse. Bioresour Technol 111: 215-221.

14. Michalska K, Miazek K, Krzystek L, Ledakowicz S (2012) Influence of pretreatment with Fenton's reagent on biogas production and methane yield from lignocellulosic biomass. Bioresour Technol 119: 72-78.

15. Gomez-Tovar F, Celis LB, Razo-Flores E, Alatriste-Mondragon F (2012) Chemical and enzymatic sequential pretreatment of oat straw for methane production. Bioresour Technol 116: 372-378.

16. Zhang QH, Tang L, Zhang JH, Mao ZG, Jiang L (2011) Optimization of thermal-dilute sulfuric acid pretreatment for enhancement of methane production from cassava residues. Bioresour Technol 102: 3958-3965.

17. Chandra R, Takeuchi H, Hasegawa T, Kumar R (2012) Improving biodegradability and biogas production of wheat straw substrates using sodium hydroxide and hydrothermal pretreatments. Energy 43: 273-282.

18. Zhou SX, Zhang YL, Dong YP (2012) Pretreatment for biogas production by anaerobic fermentation of mixed corn stover and cow dung. Energy 46: 644648.

19. Gonzalez G, Urrutia H, Roeckel M, Aspe E (2005) Protein hydrolysis under anaerobic, saline conditions in presence of acetic acid. J Chem Technol Biotechnol 80: 151-157.

20. Guo P, Mochidzuki K, Cheng W, Zhou M, Gao H, et al. (2011) Effects of different pretreatment strategies on corn stalk acidogenic fermentation using a microbial consortium. Bioresour Technol 102: 7526-7531.

21. Li Q, Gao Y, Wang HS, Li B, Liu C, et al. (2012) Comparison of different alkali-based pretreatments of corn stover for improving enzymatic saccharification. Bioresour Technol 125: 193-199.

22. Song ZL, Yang GH, Guo Y, Ren GX, Feng YZ (2012) Comparison of two chemical pretreatments of rice straw for biogas production by anaerobic digestion. BioResources 7: 3223-3236.

23. Kang KE,Jeong GT, Swoo CS, Park DH (2012) Pretreatment of rapeseed straw by soaking in aqueous ammonia. Bioprocess Biosyst Eng 35: 77-84.

24. Pakarinen OM, Kaparaju PLN, Rintala JA (2011) Hydrogen and methane yields of untreated, water-extracted and acid (HCl) treated maize in one-and two-stage batch assays. Int J Hydrogen Energy 36: 14401-14407.

25. Monlau F, Latrille E, Da Costa AC, Steyer JP, Carrère H (2013) Enhancement of methane production from sunflower oil cakes by dilute acid pretreatment. Appl Energ 102: 1105-1113.

26. Us E, Perendeci NA (2012) Improvement of methane production from greenhouse residues: optimization of thermal and H2SO4 pretreatment process by experimental design. Chem. EngJ 182: 120-131.

27. APHA (1998) Standard methods for the examination of water and wastewater, 20th ed, American Public Health Association, Washington, DC, USA.

28. Cuetos MJ, Fernandez C, Gomez X, Moran A (2011) Anaerobic co-digestion of swine manure with energy crop residues. Biotechnol Bioprocess Eng 16: 10441052.

29. Chengdu Institute of Biology, Chinese Academy of Sciences (1984) Routine Analysis of Biogas Fermentation, Science Technology Press, Beijing, China.

30. Wang YW, Xu WY (1987) The method for measurement the content of cellulose, hemicellulose and lignin in solid materials, Microbiology China 2: 8185.

31. Silverstein RA, Chen Y, Sharma-Shivapp RR, Boyette MD, Osborne J (2007) A comparison of chemical pretreatment methods for improving saccharification of cotton stalks. Bioresour Technol 98: 3000-3011.

32. Lin YQ, Wang DH, Wu SQ, Wang CM (2009) Alkali pretreatment enhances biogas production in the anaerobic digestion of pulp and paper sludge. J Hazard Mater 170: 366-373.

33. Li C, Knierim B, Manisseri C, Arora R, Scheller HV, et al. (2010) Comparison of dilute acid and ionic liquid pretreatment of switchgrass: biomass recalcitrance, delignification and enzymatic saccharification. Bioresource Technol 101: 49004906.

34. Xiao B, Sun XF, Sun R (2001) Chemical, structural, and thermal characterizations of alkali-soluble lignins and hemicelluloses, and cellulose from maize stems, rye straw, and rice straw. Polymer Degrad Stability 74: 307-319.

35. Li ZL, Chen CH, Hegg EL, Hodge DB (2013) Rapid and effective oxidative pretreatment of woody biomass at mild reaction conditions and low oxidant loadings. Biotechnol Biofuels 6: 119. doi:10.1186/1754-6834-6-119.

36. Estevez MM, Linjordet R, Morken J (2012) Effects of steam explosion and codigestion in the methane production from Salix by mesophilic batch assays. Bioresour Technol 104: 749-756.

37. Chen Y, Cheng JJ, Creamer KS (2008). Inhibition of anaerobic digestion process: A review. Bioresour Technol 99: 4044-4064.

38. Hwang MH, Jang NJ, Hyum SH, Kim IS (2004) Anaerobic bio-hydrogen production from ethanol fermentation: the role of pH. J Biotechnol 111: 297309.

39. Zhang T, Liu L, Song Z, Ren G, Feng Y (2013) Biogas production by co-digestion of goat manure with three crop residues. PLoS ONE 8(6): e66845.

40. Saha BC, Iten LB, Cotta MA, Wu YV (2005) Dilute acid pretreatment, enzymatic accharification and fermentation of wheat straw to ethanol. Process Biochem 40: 3693-3700.

41. Rocha MV, Rodrigues TH, de Macedo GR, Goncalves LR (2009) Enzymatic hydrolysis and fermentation of pretreated cashew apple bagasse with alkali and diluted sulfuric acid for bioethanol production. Appl Biochem Biotechnol 155: 407-417.

42. Cara C, Ruiz E, Oliva JM, Saez F, Castro E (2008) Conversion of olive tree biomass into fermentable sugars by dilute acid pretreatment and enzymatic saccharification. Bioresour Technol 99: 1869-1876.