Sustainable and efficient sugar production from wheat straw by pretreatment with biogas digestate.

The use of liquid fraction of biogas digestate (LFBD) instead of fresh water (hydrothermal) for the pretreatment of wheat straw was evaluated to improve the yield of released sugars during the following hydrolysis step. The pretreatments were conducted at temperatures of 130, 160, and 190 °C for 30 and 60 min. In most of the cases, pretreatment using LFBD led to higher glucose yields and higher total sugars concentrations, compared to those obtained after applying hydrothermal pretreatments. The increase of temperature resulted in an increase in sugars during the enzymatic hydrolysis. The highest yields of glucose (about 59%) were observed after treatments at 190 °C for 60 min, independently of which type of pretreatment was applied and at 190 °C for 30 min using LFBD. Treatment, with LFBD at 190 °C and for 60 min, resulted in glucose and xylose concentrations of 7.36 g L-1 and 2.41 g L-1, respectively, after the subsequent hydrolysis for 48 h. However, the FTIR analysis indicated that the crystallinity index remained rather constant after treatment. Both FTIR and compositional analysis showed that the removal of hemicelluloses was the main effect of the pretreatment. This journal is © The Royal Society of Chemistry.

Introduction

Wheat is an important food source in many countries all over the world. Wheat crops supply about 21% of the world's food demand. About 200 million hectares of farmland is used for growing this crop. It is predicted that up to 2020, the demand for wheat in developing countries will grow by 1.6% per annum.[1,2] Wheat straw is an abundant agricultural by-product with a very low commercial value. The yield of wheat straw depends on different parameters such as climate and agronomic factors; however an average yield of 1.3–1.4 kg of straw per kg of wheat grain is reported as the most typical one for various areas.[3,4] With global production of 729 Tg wheat per annum and taking in the account of straw/crop ratio of 1.3, a production of over one billion tons of straw can be expected annually.[5] Hence, utilizing this huge amount of wheat residue in appropriate processes is a great concern. Some amount of this is used for animal feed but burning in traditional ways or piling for natural decay are still among the usual methods for managing wheat straw. These methods result in environmental pollution beside wasting valuable resources.[6]

Wheat straw is a lignocellulosic biomass, consisting usually of 33–40% cellulose, 20–25% hemicellulose and 15–20% lignin. Therefore, wheat straw is a rich carbohydrate source containing fermentable pentose and hexose sugars.[7-9] Liberating monomeric sugars via hydrolysis of straw and then converting them into chemicals and biofuels is of economic interest. However, the recalcitrant structure of lignocellulosic biomass limits the degradation of polysaccharides into monomeric sugars. To increase the digestibility of this biomass, the disruption of its complex lignocellulosic network is needed before hydrolysis. Consequently, the application of some kind of pretreatment is a necessary step aiming to break down the structural barriers and enhance the sugar yield in subsequent processes.[10-14] Considerable efforts have been made in this field, including development and investigations of various chemical, physical, and biological pretreatment technologies.[15-18] However, each pretreatment method has its own advantages and disadvantages. Liquid hot water (LHW) pretreatment is one of the most desired pretreatment strategies because of its low cost in comparison with other technologies, i.e., lime, diluted acid, or ammonia fiber explosion pretreatments. Furthermore, as no chemical is added in this process, handling of the downstream residue is also easier.[19] LHW pretreatment has the potential of removing hemicellulose from biomass structure, while minimizing the hydrolysis of cellulose and the sugar degradation. It has been reported that 80% of hemicellulose was removed after LHW pretreatment of sugarcane bagasse[20,21] and corn fiber.[22] Utilization of acids, bases, and other chemicals such as ionic liquids in lignocellulosic feedstock pretreatment was also employed to improve process effectiveness.[23-25] Beside solubilization of hemicellulose, using these chemicals can remove lignin and reduce lignin–cellulose–xylan interactions, leading to higher cellulose digestibility.[26-28] Despite increasing sugar yield in subsequent hydrolysis processes, adding chemicals for the pretreatment are connected to some drawbacks including increasing costs, equipment corrosion, high energy consumption, pH neutralization requirement, and formation of inhibitory by-products.[1,29,30] Therefore, using a waste stream, that consists of effective elements, such as acids and bases, instead for the pretreatment would be more beneficial.

In the biogas process, the digestate is separated into liquid and solid fractions. The solid part can be used for animal feeding or for farmland fertilizer, nevertheless managing the liquid part can be a serious problem.[31,32] This liquid fraction is not rich enough in nutrients to be used as fertilizer, while its nitrogen content is high enough to cause nitrogen pollution. Hence, releasing this liquid fraction to the nature with no further processing would lead to environmental problems. Diluting with water to decrease the concentration of hazardous or toxic compounds is a traditional way, however this method would increase the volume of wastewater produced.[33-35] On the other hand, utilizing this liquid waste stream for suitable pretreatment can be beneficial. The presence of volatile fatty acids, phosphorus, nitrogen, calcium, potassium and sulfur in this waste liquid can increase the efficiency of the pretreatment.[36,37]

In this study, wheat straw, a renewable low-cost lignocellulosic material, was utilized to produce fermentable sugars. LHW pretreatment at different temperatures and times was performed on straw and the results were compared to those obtained by using the liquid fraction of biogas digestate (LFBD) for the pretreatment at same process conditions. The digestibility of untreated and pretreated wheat straw was evaluated via enzymatic hydrolysis. Furthermore, compositional as well as structural changes caused by the pretreatment were also studied using Fourier transform infrared (FTIR) spectroscopy and scanning electron microscopy (SEM).

Materials and methods

Raw materials

The wheat straw used in this study was obtained from a local farm in Shahreza, Isfahan, Iran. The collected straw was milled and then meshed to achieve a particle size between 0.1 and 0.8 mm before pretreatment. The sieved straw was stored at room temperature for further use. The digestate residue was taken from a 3000 m3 large scale anaerobic digester treating the organic fraction of municipal solid waste (Borås Energi och Miljö AB, Borås, Sweden). The digestate contained 4900 mg kg−1 nitrogen, 3600 mg kg−1 ammonium, 0.35 kg per ton phosphorus, 1.1 kg per ton potassium, 0.83 kg per ton calcium, and 0.28 kg per ton sulfur (Robert Kjellstrand, 2017-09-14, personal communication). The concentrations of acids in the digestate were 0.454 g L−1 acetic acid, and 0.051 g L−1 propionic acid. This residue was first centrifuged for 10 min at 4500 rpm and then the supernatant, as the liquid fraction of biogas digestate (LFBD), was used for the pretreatment.

Pretreatment of wheat straw

The pretreatments were conducted in 150 mL tubular stainless steel reactors, tolerating high temperature and pressure. An amount of 6.5 g of dried wheat straw was well mixed with a sufficient amount of water or LFBD to obtain a solid-to-liquid ratio of 1 : 15. The reactors were then closed tightly and put in the oil bath with desired temperatures of 130, 160 or 190 °C used for the treatments and the treatment time was 30 or 60 min. At the end of the time period applied, the reactors were immediately immersed in cooling water to reduce the pressure and temperature. The pretreated wheat straw was then separated from the pretreatment liquor by filtration and manual squeezing. The solid residue was dried at room temperature to a constant weight. The dried solid residue was weighted and the solid recovery at different pretreatment conditions was calculated. The pretreated wheat straw samples were then maintained in plastic bags in the cold room (4 °C) until further investigations.

Enzymatic hydrolysis

The enzymatic hydrolysis was conducted in 118 mL glass bottles using 50 mM sodium acetate buffer at pH 4.8. The bottle containing 0.25 g of treated or untreated straw was autoclaved at 121 °C for 20 min to avoid any contamination. The samples were then cooled to room temperature. Then 10 mL of buffer was added to achieve a substrate concentration of 25 g L−1 and each sample was then well mixed. The cellulase enzyme, Cellic CTec2, was provided by Novozyme, Denmark and used for the enzymatic hydrolysis process. The enzyme load was 20 FPU per g substrate. The enzymatic hydrolysis was performed in a shaker at 50 °C, and 120 rpm for 48 h. To determine the amount of released sugars, liquid samples were taken after 24 and 48 h of hydrolysis time. The concentration of glucose and xylose was then determined by high performance liquid chromatography (HPLC, Waters 2695, Waters Corporation, Milford, USA). A hydrogen ion-based ion-exchange column (Aminex HPX-87H, Bio-Rad, USA) at 60 °C together with a Micro-Guard cation-H guard column (Bio-Rad, USA) was used for the measurements. The eluent was H2SO4 with concentration of 5 mM and at a flow rate of 0.6 mL min−1.

Analytical methods

Total solids (TS) of the treated and untreated samples were measured by keeping the samples in an oven at 105 °C until constant weight, and then the dried samples was further heated in a furnace at 575 °C, to determine the volatile solids (VS) content, as it is described in details by Sluiter et al.[38] The activity of cellulase enzyme was determined to 90 FPU mL−1 following the standard method recommended by Adney and Baker.[39]

The composition of the straw samples was determined according to the method published by the National Renewable Energy Laboratory (NREL, USA),[40] and the main steps are summarized as follows: 0.3 g of samples were treated with 3 mL H2SO4 (72% w/w) for 1 h at 30 °C. The mixture was then diluted with 84 mL deionized water to 4% H2SO4 (w/w) and then autoclaved for 1 h at 121 °C. After filtration, the liquid fraction was analyzed by high-performance liquid chromatography (HPLC, Waters 2695, Waters Corporation, Milford, USA) to determine the concentration of monomeric sugars. The HPLC was equipped with an Aminex HPX-87P column (Bio-Rad, USA) and RI detector (Jasco International Co., Tokyo, Japan). The column temperature was 85 °C and deionized water with flow rate of 0.6 mL min−1 was applied as mobile phase. The acid soluble lignin (ASL) was determined by measuring the absorbance of the liquid at 240 nm. The solid fraction was dried at 105 °C overnight in an oven and then placed in the furnace at 575 °C until constant weight. The weight of the ash was measured and used to calculate the content of acid insoluble lignin (AIL).

To investigate the effect of pretreatment on chemical structure and crystallinity of wheat straw, FTIR spectroscopy was used. The spectrometer (Bruker Tensor 27 FT-IR, USA) was equipped with an universal ATR (attenuated total reflectance) accessory and deuterated triglycine sulfate (DTGS) detector. Initially, the samples were well mixed with KBr at a weight ratio of 1 : 100 and then pressed into discs. The spectra were recorded from 600 to 4000 cm−1, with an average of 60 scans and 4 cm−1 resolution.

Scanning electron microscopy (SEM) images of treated and untreated wheat straw samples were obtained to study the effect of pretreatment on surface morphology. All samples were freeze-dried for 24 h and then coated with gold (Emitech Sputter Coater SC7640, Quorum Technologies, UK). Images at magnifications of 250, 500, and 700 were taken by SEM (Zeiss, Germany) at 13 kV.

Statistical analysis

Statistical validation of achieved results was performed by Analysis of variance (ANOVA) test. SAS software and Newman–Keuls or Student–Newman–Keuls (SNK) method with 95% confidence were used for comparing and estimating the significant difference between the means.

Results and discussion

Chemical composition of wheat straw before and after pretreatment

Total solids (TS), volatile solids (VS) for untreated and pretreated wheat straw and the solid recovery at different treatment conditions were measured and are reported in Table 1. No serious changes were detected in the TS and VS contents of the samples after pretreatment, however the solid recovery has decreased by increasing pretreatment temperature. Consequently, more solid was released during pretreatment at more severe conditions as it was expected. The minimum solid recovery was around 50% for straw treated at 190 °C for 60 min both with LFBD and with hot water (Table 1).

Total solid, volatile solid, and solid recovery of untreated and pretreated wheat straw at different conditions

Pretreatment conditions			Total solids (%)	Volatile solids (%)	Solid recovery (%)
Pretreatment liquid	Time (min)	Temperature (°C)
Hot water	30	130	91.16 ± 0.08	82.43 ± 0.41	76.9
	60	130	91.71 ± 0.33	81.51 ± 0.56	77.2
	30	160	91.00 ± 0.58	86.05 ± 0.52	73.8
	60	160	92.46 ± 0.75	83.53 ± 0.59	67.5
	30	190	93.37 ± 0.25	82.89 ± 0.99	52.9
	60	190	92.98 ± 0.74	82.33 ± 0.95	48.9
Liquid fraction of biogas digestate	30	130	91.66 ± 0.97	82.31 ± 1.01	77.1
	60	130	91.78 ± 0.12	81.69 ± 0.84	77.2
	30	160	92.13 ± 0.63	81.94 ± 0.36	77.2
	60	160	91.64 ± 0.71	83.01 ± 0.89	67.1
	30	190	92.67 ± 0.22	81.93 ± 0.37	63.7
	60	190	93.06 ± 0.75	81.42 ± 0.77	50.5
Untreated			92.59 ± 0.18	79.57 ± 0.10	—

The compositions of original and treated wheat straw are presented in Table 2. As in other lignocellulosic materials, the carbohydrate fraction is the main constituent, with 30.4% glucan and 17% xylan, for dried untreated wheat straw. This high content of carbohydrates makes this biomass an attractive feedstock for biofuel production utilizing the sugars. After treatment at 130 and 160 °C for 30 and 60 min there was only a slight increase in the glucan content, however, when treating at more severe conditions, i.e., at 190 °C a larger increment in the glucan content was observed compared to that in the untreated straw. The highest glucan content, of 48.8%, was achieved for straw treated with hot water at 190 °C for 60 min (Table 2). This is the result of the destruction and solubilization of hemicelluloses at these conditions. In line with these findings, the xylan content of straw treated at 190 °C for 60 min with hot water or with LFBD decreased to 2.53 or to 11.34%, respectively. Furthermore, a complete omission of the arabinan fraction was achieved after treatment at these conditions (Table 2).

Compositional analysis of untreated and pretreated wheat straw (All data are calculated based on the oven dried weight of the samples.)

Pretreatment conditions			Glucan (%)	Xylan (%)	Arabinan (%)	AIL (%)	ASL (%)
Pretreatment medium	Time (min)	Temperature (°C)
Hot water	30	130	34.24 ± 0.81	19.74 ± 0.56	2.23 ± 0.31	15.81 ± 0.20	3.79 ± 0.32
	60	130	35.46 ± 0.68	18.34 ± 0.07	1.84 ± 0.12	16.25 ± 0.36	3.47 ± 0.16
	30	160	35.39 ± 0.40	19.23 ± 0.40	1.53 ± 0.10	16.83 ± 0.75	3.44 ± 0.06
	60	160	37.46 ± 0.06	18.47 ± 0.30	1.05 ± 0.00	17.74 ± 0.41	3.24 ± 0.06
	30	190	48.40 ± 0.21	9.39 ± 0.04	0.00 ± 0.00	19.85 ± 0.87	3.05 ± 0.76
	60	190	48.80 ± 0.58	2.53 ± 0.19	0.00 ± 0.00	23.09 ± 0.25	3.71 ± 0.00
Liquid fraction of biogas digestate	30	130	35.42 ± 0.28	19.78 ± 0.21	2.13 ± 0.00	15.91 ± 0.38	3.30 ± 0.02
	60	130	35.71 ± 0.15	19.23 ± 0.19	2.09 ± 0.02	15.34 ± 0.28	3.33 ± 0.01
	30	160	35.11 ± 0.34	19.20 ± 0.23	2.06 ± 0.02	16.59 ± 0.56	3.71 ± 0.00
	60	160	37.94 ± 0.36	19.30 ± 0.46	1.88 ± 0.10	16.11 ± 0.10	3.35 ± 0.02
	30	190	40.73 ± 0.21	15.26 ± 0.17	0.00 ± 0.00	16.96 ± 0.48	3.79 ± 0.01
	60	190	45.32 ± 1.00	11.34 ± 0.25	0.00 ± 0.00	17.28 ± 0.13	3.66 ± 0.01
Untreated			30.38 ± 0.40	16.97 ± 0.00	1.92 ± 0.04	14.44 ± 0.92	4.45 ± 0.05

The acid insoluble lignin (AIL) and the acid soluble lignin (ASL) content accounted for 14.4% and 4.5%, respectively, in the dried untreated straw. According to the results obtained, delignification of straw did not occur during the pretreatments with hot water or LFBD under the investigated conditions. In conclusion, treatments with hot water or LFBD had similar effects regarding compositional changes in the wheat straw (Table 2). Both liquids caused partial removal of hemicelluloses resulting in an increment in the glucan content. The amounts of xylan decreased more due to the treatment with hot water compared to that with LFBD regarding treatments at same conditions (Table 2).

Previously, Petersen et al.[41] reported that at least 90% of the lignin content is recovered in the solid residue after hydrothermal treatment under all of the conditions (185–205 °C and 6–12 min) investigated. Furthermore, they indicated that the hemicellulose recovery in the solid fraction had decreased by increasing the severity factor, i.e., where R0 = severity factor, t = time (min), T = temperature (°C). Perez et al.[42] also showed that only 6% of the xylan present in the raw wheat straw remains in its solid structure after hot water pretreatment at 200 °C for 40 min. They concluded that an increase in the treatment temperature and time will lead to a higher degree of hemicellulose solubilization. These results are similar to those reported in the literature regarding similar treatment procedures for other kinds of lignocellulosic feedstocks as well.[43-46]

FTIR and SEM analyses

Fig. 1 and Table 3 present the results of FTIR analyses for some treated samples compared to those for untreated wheat straw; the wavelength attributed to different functional groups and their appearance in the lignocellulosic structure can also be found in the table. The peak at 1510 cm−1 represents the aromatic ring stretch vibration in lignin, which was applied as an internal reference band for normalizing to compare the spectra quantitatively.[47] The peak around 3400 cm−1 is attributed to the OH stretching, and a reduction in this peak intensity after the treatments indicates a disruption of hydrogen bonds in cellulose.[48] The peak at 2900 cm−1 is indicative for C–H stretching, which was reduced after hot water pretreatment, demonstrating a rupture of the methyl and methylene parts of cellulose.[49-51] For all treated samples, the peak intensity at 1730 cm−1 had a notable reduction. This band position is assigned to the uronic ester and hemicellulose acetyl groups or ester linkage of carboxylic group of the p-coumaric and ferulic acids of lignin/hemicelluloses.[52] In line with the results of the compositional analyses (Table 2), the pretreatment with hot water and LFBD caused the destruction/solubilization of hemicelluloses. The removal of hemicelluloses causes considerable changes in the structure of lignocellulosic materials, leading to easier accessibility for enzymes and microorganisms to the cellulose.[48] The adsorption peak of the band at 1250 cm−1 was detectable in raw wheat straw, representing the acetyl groups in the structure. However, this band could not be found for the pretreated samples due to the hemicellulose removal as discussed above.[49]

Fig. 1

FTIR spectra of untreated vs. pretreated samples at 190 °C (W = hot water; LFBD = liquid fraction of biogas digestate).

Characteristics of bands in FTIR spectra for untreated and pretreated wheat straw (W = hot water; LFBD = liquid fraction of biogas digestate.)

Wavenumber (cm−1)	Functional group	Band assignment	Untreated straw	W (190 °C, 30 min)	LFBD (190 °C, 30 min)	W (190 °C, 60 min)	LFBD (190 °C, 60 min)
3400	–OH stretching intramolecular hydrogen bonds	Cellulose II	1.45	1.24	1.4	1.24	1.38
2900	C–H stretching cellulose	Cellulose	0.96	0.82	1.02	0.93	0.97
1730	C <svg xmlns="http://www.w3.org/2000/svg" version="1.0" width="13.200000pt" height="16.000000pt" viewBox="0 0 13.200000 16.000000" preserveAspectRatio="xMidYMid meet"><metadata> Created by potrace 1.16, written by Peter Selinger 2001-2019 </metadata><g transform="translate(1.000000,15.000000) scale(0.017500,-0.017500)" fill="currentColor" stroke="none"><path d="M0 440 l0 -40 320 0 320 0 0 40 0 40 -320 0 -320 0 0 -40z M0 280 l0 -40 320 0 320 0 0 40 0 40 -320 0 -320 0 0 -40z"/></g></svg> O stretching of acetyl or carboxylic acid	Hemicellulose & lignin	0.97	No peak	No peak	No peak	No peak
1627	CC stretching of the aromatic ring	Lignin	1.11	0.91	1.06	1	1
1465	Asymmetric bending in C–H3	Lignin	1.12	1.16	1.12	1.12	1.16
1430	C–H2 bending	Cellulose	1.16	1.18	1.15	1.14	1.18
1375	C–H bending	Cellulose	1.17	1.12	1.14	1.11	1.14
1315	C–H2 wagging	Cellulose	1.12	1.05	1.12	1.08	1.12
1250	C–O adsorption	Cellulose	1.24	No peak	No peak	No peak	No peak
1158	C–O–C asymmetric stretching	Cellulose	1.34	1.18	1.33	1.12	1.18
1098	C–O stretch	Cellulose I	1.46	1.25	1.41	1.25	1.4
896	Asym., out of phase ring stretching (cellulose)	Cellulose II	0.94	0.79	0.93	0.81	0.9
CI 1098/896			1.55	1.58	1.51	1.54	1.55

Furthermore, another important result of the pretreatment that can occur is the change in the ratio between crystalline and amorphous cellulose presented in the biomass structure. The absorbance band at 1098 cm−1 is assigned to cellulose I, or high crystalline cellulose, which is a highly resistant structure to hydrolysis, whereas the absorbance band at 896 cm−1 denotes cellulose II, or amorphous cellulose, with greater ability to be hydrolyzed. Hence, the crystallinity index was defined as the absorbance ratio of A1098/A896,[49,53] which is shown for each of the samples treated at 190 °C in Table 3. However, no notable changes occurred in the crystallinity index after treatments at these conditions. Though the peak intensity referred to cellulose I has decreased after the pretreatment, but as a consequence of the treatment the peak for cellulose II has also declined and the crystallinity index remained constant. In another study, it was also found that hydrothermal pretreatment of wheat straw had no significant effect on the crystallinity of the samples.[54]

To investigate changes in the microscopic structure of straw after pretreatment SEM images were captured and these are shown in Fig. 2. The presence of organized and crystalline cellulose fibers is one of the most important obstacles regarding the digestibility of lignocellulosic materials. This organized structure can be seen for untreated straw (1(a–c)) and also for treated straw at low temperatures (2 and 3(a–c)) on the SEM images presented in Fig. 2. By increasing the severity of the pretreatment conditions (4 and 5(a–c)), a significant morphological modification can be observed. Packed structure of straw was converted to a more porous structure, which is expected to be more accessible for the enzymes during the following degradation process. These observations were previously reported in the literature and also supported with further analyses.[55]

Fig. 2

SEM images of untreated (1) and four pretreated samples of wheat straw treated at the following conditions: hot water (W) at 130 °C for 60 min (2); liquid fraction of biogas digestate (LFBD) at 130 °C for 60 min (3); W at 190 °C for 60 min (4); LFBD at 190 °C for 60 min (5). The images representing magnifications of 250 (a), 500 (b), and 750 (c).

The performance of the enzymatic hydrolysis was followed up by measuring the concentrations of glucose and xylose released from the samples due to the enzymatic treatment. Fig. 3 shows the amount of released sugars obtained after 24 and 48 h of hydrolysis times for untreated compared to those for treated samples. It was found that the digestibility of straw could significantly be increased after pretreatments at high temperature with either hot water or with LFBD. The possible reason behind this improvement might be the removal of hemicelluloses (Table 2) together with changes observed in the cellulose structure (Fig. 1 and 2). The highest glucose release of 8.0 g L−1, was obtained from the sample treated with hot water at 190 °C for 60 min (Fig. 3). According to the compositional analysis, this sample also showed the highest xylose removal after pretreatment (Table 2). During the enzymatic hydrolysis of straw treated with LFBD at the same conditions almost as high amount of glucose, i.e. 7.4 g L−1, was released, indicating the suitability of this waste liquid fraction to be used for the pretreatment. Moreover, when straw was treated with LFBD at severe conditions, a higher xylose concentration was obtained after the hydrolysis compared to that when the straw was treated with hot water at same conditions. The highest xylose concentration of 2.6 g L−1 was achieved after 48 h enzymatic hydrolysis of wheat straw samples pre-treated with LFBD at 190 °C for 30 min and at 160 °C for 60 min. Furthermore, these results also show, that there were no inhibitory compounds presented affecting the enzyme activity in this waste liquid, since high concentrations of sugars were liberated during the hydrolysis. In comparison, only 2.68 and 1.18 g L−1, glucose and xylose, respectively was released from untreated wheat straw after 48 h enzymatic digestion. Moreover, solid residues pretreated at low temperature gave similar amount of glucose concentrations during the hydrolysis as untreated wheat straw (Fig. 3).

Fig. 3

Enzymatic digestibility of untreated and pretreated wheat straw (W = hot water; LFBD = liquid fraction of biogas digestate). The columns are representing the total amount of released sugars, showing the sum of glucose (blue) and xylose (red). The reported data are the mean of the results obtained from three repeated tests performed at same conditions. There are no significant differences at a 5% probability level (P < 0.05) among the means marked with the same letter.

The glucose yield for treated and untreated samples was calculated according to eqn (1)[56] and is reported in Table 4.where F is the glucan fraction in the substrate and the constant 1.11 stands for hydrolysis of glucan to glucose. The highest yields were around 59%, and these were obtained after treatments at 190 °C and for 60 min, independently if the treatment was carried out with hot water or with LFBD. Moreover, similar yield of glucose could be reached even when the treatment with LFBD was held for only 30 min, while the yield after treatment with hot water at similar conditions was significantly, i.e. about 10%, lower (Table 4). In summary, except for the most severe pretreatment conditions (190 °C and 60 min), the glucose yield was higher for the samples treated with LFBD compared to those treated with hot water at the same conditions. The presence of effective elements such as nitrogen, ammonium, phosphorus, and acids may be the main reason for the better performance of LFBD. Although each element concentration is low, the effect of all elements together might be considerable.[57]

Glucose yield during enzymatic hydrolysis of untreated and pretreated wheat straw obtained after 24 and 48 h of hydrolysis time (The reported data correspond to the mean of results obtained from three repeated tests performed at same conditions. There are no significant differences at a 5% probability level (P < 0.05) among the data belonging to a group marked with the same letter.)

Pretreatment condition			Glucose yield (%)
Pretreatment liquid	Time (min)	Temperature (°C)	24 h	48 h
Hot water	30	130	26.94 ± 0.52 (G)	28.96 ± 1.15 (H)
	60	130	26.82 ± 0.21 (G)	28.57 ± 0.81 (H)
	30	160	31.04 ± 0.46 (F)	34.02 ± 0.81 (F)
	60	160	37.64 ± 0.31 (D)	41.67 ± 0.61 (D)
	30	190	44.10 ± 0.95 (C)	48.39 ± 1.12 (C)
	60	190	52.78 ± 0.30 (B)	59.37 ± 0.97 (A)
Liquid fraction of biogas digestate	30	130	28.52 ± 0.51 (G)	30.92 ± 0.61 (GH)
	60	130	30.39 ± 1.11 (F)	32.64 ± 1.40 (FG)
	30	160	35.44 ± 0.65 (E)	37.90 ± 0.65 (E)
	60	160	45.75 ± 0.63 (C)	52.04 ± 0.71 (B)
	30	190	52.35 ± 1.36 (B)	58.32 ± 1.23 (A)
	60	190	54.57 ± 0.74 (A)	58.46 ± 0.37 (A)
Untreated			27.78 ± 0.33 (G)	31.71 ± 0.50 (FG)

Although the glucose yield was increased considerably after treatment at severe conditions, the solid recoveries are low at these conditions. Therefore, the actual sugar yields achieved per gram of straw entering the pretreatment process are lower than those reported in Table 4. However, according to the compositional analysis (Table 2), the main target component of the straw for the hydrolysis, i.e., the content of glucose, was increased after the treatment, indicating that the components dissolved due to the pretreatment step are mostly the useless parts. Consequently, by the elimination of these useless components through the pretreatment, the reactor volume can be decreased and also the amount of enzymes required for the hydrolysis will be reduced.[58]

These results are comparable with those reported from previous investigations. The glucose yield after enzymatic hydrolysis of wheat straw treated with ionic liquid, 1-ethyl-3-methyl imidazolium diethyl, at 130 °C for 30 min was 54.8%.[59] In another work, the effect of dilute acid pretreatment for wheat straw was investigated. Pretreatment with 0.75 (v/v) H2SO4 at 121 °C for 1 h, resulted in a yield of 74% regarding the total sugars content.[4] In another study, the effects of alkaline wet oxidation on wheat straw was investigated using conditions of 10 bar of oxygen pressure at different temperatures and pretreatment times. The highest sugar yield was 85%, obtained from the straw treated at 170 °C for 10 min.[60]

Overall mass balance

An overall mass balance throughout the process steps of the treatment of wheat straw using LFBD at 190 °C and for 30 min followed by enzymatic hydrolysis is depicted in Fig. 4. As it was presented and discussed previously, the highest glucose yields were achieved after LFBD and hot water treatment at 190 °C for 60 min and after LFBD treatment at 190 °C for 30 min (Table 4). Since there was a higher solid recovery, i.e. 63.7% (Table 1) after treatment with LFBD for 30 min, this treatment could be more promising for large scale processing due to the shorter duration time required. Therefore, the overall mass balance calculation was performed for this pretreatment condition. The glucan content of untreated straw was 30.38%, which was increased to 40.73% after treatment at this condition (Table 2). After pretreatment, the straw was dried at room temperature and subjected to enzymatic hydrolysis using an initial substrate concentration of 25 g L−1. Finally, 6.6 g L−1 (17 g) glucose and 2.6 g L−1 (6.6 g) xylose was produced during enzymatic hydrolysis for 48 h (Fig. 3).

Fig. 4

Overall mass balance over the process steps of wheat straw pretreated with liquid fraction of biogas digestate (LFBD) at 190 °C with for 30 min followed by enzymatic hydrolysis.

Conclusions

Wheat straw is one of the most abundant agricultural wastes all over the world. Hence, this lignocellulosic biomass is an attractive feedstock for biofuel production. The present study focused on investigating the effects of different pretreatment conditions using either hot water or the liquid fraction of biogas digestate. The results were evaluated both regarding changes in chemical composition and in the structure as well as in enzymatic digestibility. During this study it was proved that treatment using a waste liquid stream from biogas production, i.e. LFBD, can be applied as an economically feasible and environmentally friendly method with no need of addition of chemicals, aiming to increase the possibility for the utilization of released sugars. Both the compositional as well as the FTIR analysis showed solubilization of the hemicellulose, leading to enhanced yield of released sugars during the following enzymatic hydrolysis.

Conflicts of interest

There are no conflicts of interest to declare.