Effect of alkaline microwaving pretreatment on anaerobic digestion and biogas production of swine manure.

Microwave assisted with alkaline (MW-A) condition was applied in the pretreatment of swine manure, and the effect of the pretreatment on anaerobic treatment and biogas production was evaluated in this study. The two main microwaving (MW) parameters, microwaving power and reaction time, were optimized for the pretreatment. Response surface methodology (RSM) was used to investigate the effect of alkaline microwaving process for manure pretreatment at various values of pH and energy input. Results showed that the manure disintegration degree was maximized of 63.91% at energy input of 54 J/g and pH of 12.0, and variance analysis indicated that pH value played a more important role in the pretreatment than in energy input. Anaerobic digestion results demonstrated that MW-A pretreatment not only significantly increased cumulative biogas production, but also shortened the duration for a stable biogas production rate. Therefore, the alkaline microwaving pretreatment could become an alternative process for effective treatment of swine manure.

Introduction

an class="Chemical">Animal mclass="Chemical">anure is one of the major wastes in mclass="Chemical">any agricultural countries due to their intensive class="Chemical">animal breeding industry, class="Chemical">and it has become a big challenge that should be appropriately treated[1]. The increased class="Chemical">and concentrated class="Chemical">animal waste generated odour problem class="Chemical">and contained pathogen which will threaten class="Chemical">an class="Species">people’s health if not handled properly. Moreover, it contained nutrients and heavy metals which will impact the quality of surface and ground water if they are discharged directly[2].

Traditionally, animal manure is treated by anaerobic digestion. The results showed pathogens were destroyed and wastes were stabilized through the process. also, it generated biogas that can be used for daily activities[3, 4]. However, the high content of fiber in animal manure was limited the efficiency of anaerobic digestion which cannot be well utilized by anaerobic bacteria[5]. Thus, enhanced biogas production by anaerobic digestion has been paid great attention, and substrate optimization has been focused.

Carlsson et al.[6] mentioned that pretreatment of manure to break down its structures could be effective for the enhancement of anaerobic digestion. Generally, pretreatment can be roughly divided into three groups, physical pretreatment, chemical pretreatment, and biological pretreatment[7]. Among them, thermo-chemical pretreatment is a main method used in current studies[8, 9]. Alkaline is a simpler and easier handling chemical pretreatment method compared with others, especially when combined with thermal effect. Currently, MW pretreatment is a favorable thermal pretreatment method. Compared with traditional heating techniques, MW has the advantages of shorter reaction time and lower energy consumption[10]. Furthermore, microwave pretreatment when combined with other technologies shows better degradation performance[11].

This study was used microwave as pretreatment under alkaline condition (MW-A). By combination of the two different technologies, the performance of pretreatment was significantly improved[12], Currently, MW was successful used in class="Species">activated sludge class="Chemical">and class="Chemical">anaerobic digestion pretreatment[13, 14]. It has great potential to apply in class="Chemical">animal mclass="Chemical">anure. However, few research has been reported on MW pretreatment of class="Chemical">animal mclass="Chemical">anure. This study was to investigate the mechclass="Chemical">anism of MW-A by treating class="Chemical">animal mclass="Chemical">anure class="Chemical">and consider combination effects of microwaving duration, microwave power, class="Chemical">and alkaline dosage. Furthermore, this study deeply researched the effects of combining pretreatment of alkaline class="Chemical">and microwave on class="Chemical">anaerobic digestion at various values of pH class="Chemical">and class="Chemical">an class="Chemical">ammonium nitrogen (AN) concentrations. RSM was involved which is a systematic research strategy for studying the interaction of various parameters effect using statistical methods[14]. The main objective of this study was to evaluate the effect of pH and energy input on swine manure pretreatment and the effects of pH and AN concentration on the consequent anaerobic digestion of swine manure with various pretreatment by RSM.

Results

Optimization for manure pretreatment with RSM

Together with the response values, the complete design matrixes are shown in Table 1. The highest DD reached 63.91% in this study. The corresponding second order polynomial fitting equation was as follows:Whether the model was proper or not was checked by the analysis of variance(an class="Chemical">ANOVA). The model was calculated by F-value class="Chemical">and P-value (Prob > F). When P-value is less thclass="Chemical">an 0.05 which is meclass="Chemical">ans that the model is highly significclass="Chemical">ant. The smaller value shows the greater effect[15]. The class="Chemical">an class="Chemical">ANOVA for the quadratic of model for disintegration degree of manure is listed in Table 2. In the study, the P-value of model was less than 0.05 and the Lack of Fit Test was not significant, which indicated that the model had a favorable fitting degree.

Table 1

Experiment design matrix for combined Alkaline microwaving pretreatment.

Run	Coded variables		Experimental variables		DD (%)
	x1	x2	x1	x2(J/g)
1	0	0	10	54	36.40
2	−2	0	8	54	33.05
3	1	1	11	72	54.98
4	−1	1	9	72	42.34
5	0	−2	10	18	24.13
6	0	0	10	54	33.42
7	2	0	12	54	63.91
8	0	2	10	90	37.14
9	1	−1	11	36	45.32
10	−1	−1	9	36	27.11

Table 2

ANOVA for a quadratic response surface model.

Source	Squares	df	Square	Value	Prob > F
Model	1270.27	5	254.05	11.31	0.0178	significant
A-x1	714.1	1	714.1	31.79	0.0049
B-x2	215.99	1	215.99	9.61	0.0362
x1x2	7.76	1	7.76	0.35	0.5884
x1 2	151.41	1	151.41	6.74	0.0603
x2 2	34.43	1	34.43	1.53	0.2834
Lack of Fit	85.42	3	28.47	6.41	0.2807	not significant
R2 = 0.9339

Figure 1(a) showed the effect of pH and energy on DD. The trend of DD of manure was increase to peak and dropped after. The peak of DD was 63.91% when energy input was 54 J/g and pH was 12.

Figure 1

Analysis of Response surface methodology: interactive effects of pH and E on DD. (a) 3D response surface; (b) Verification result of RSM predicts and determined.

an class="Chemical">Analysis of Response surface methodology: interactive effects of pH class="Chemical">and E on DD. (a) 3D response surface; (b) Verification result of class="Chemical">an class="Chemical">RSM predicts and determined.

In order to investigate model accuracy and practicability, the predicted value and actual value were compared in Fig. 1(b). The maximum experimental DD of manure was 63.91% while the predicted value was 62.75%, and the absolute error was less than 2%. The correctness and validation of the simulation model is demonstrated.

As a conclusion, the optimum conditions for DD was 54 J/g for energy input with stronger alkaline condition (pH 12).

Changes of pH on biodegradation

The two groups of manure samples were pretreated by MW with 300 W power and reaction time of 180 s, which was based on previous conclusion. Figure 2 presented the changes of pH during the anaerobic digestion.

Figure 2

Changes of pH during the anaerobic digestion after different pretreatments.

The results showed that during anaerobic digestion, The MW-A remained weak alkaline environment, while the microwaving pretreatment and control group turn to acidic.

Changes of protein concentration on biodegradation

As shown in Fig. 3, after MW pretreatment, the protein concentration was rapidly reduced at the first four day, and then the rate of the degradation decreased 8 days later. The rates were gradually decreased for MW and MW-A groups. The trend of control group was slightly reduced in the whole process, compared others. The protein concentration of MW-A pretreatment was higher than other two groups.

Figure 3

Changes of soluble organics during the anaerobic digestion after different pretreatments.

The protein concentration after alkaline microwaving pretreatment remained a relative high level during the whole anaerobic digestion.

Changes of ammonium nitrogen (AN) concentration on biodegradation

The an class="Chemical">AN concentration during the class="Chemical">anaerobic digestion by different pretreatments was recorded class="Chemical">and shown in Fig. 4. As it cclass="Chemical">an be seen in Fig. 4, the content of class="Chemical">an class="Chemical">AN were increased for three groups The MW group was the highest amount of AN concentration, and then in control group, the MW-A group was the lowest one. Figure S2 provided a basis for above changes of AN, and it presented that the dissolution rate of ammonia decreased with the increasing of pH. When pH was more than 8, AN density made little change with the increasing of the reaction time. By the stronger alkaline condition, the AN hardly released from manure.

Figure 4

Changes of ammonium nitrogen during the anaerobic digestion after different pretreatments.

Changes of an class="Chemical">ammonium nitrogen during the class="Chemical">anaerobic digestion after different pretreatments.

Biogas accumulation

Figure 5(a) showed the an class="Chemical">methane content by class="Chemical">anaerobic digestion through different pretreatment. The MW-A group reached 75%, class="Chemical">and others lower around 5%.

Figure 5

Methane content and cumulative biogas production of manure after different pretreatments. (a) Methane content; (b) Cumulative biogas production; (c) Daily specific production.

an class="Chemical">Methane content class="Chemical">and cumulative biogas production of mclass="Chemical">anure after different pretreatments. (a) class="Chemical">an class="Chemical">Methane content; (b) Cumulative biogas production; (c) Daily specific production.

The effect of different pretreatments on total biogas production is shown in Fig. 5(b). The cumulative biogas production was the highest in MW-A pretreatment group, and then in MW only group, and it was the lowest in control group. The biogas production rate for MW-A, MW and control groups began to stabilize in 8 days, 14 days and 14 days, respectively. The daily biogas production after different pretreatments is shown in Fig. 5(c), it showed that there was little biogas production after 16 days, 18 days, 18 days, respectively. So the duration for a stable biogas production rate on three groups was 8 days, 4 days, 4 days, respectively.

The results showed MW-A pretreatment was not only effectively increased the total biogas production, but also shortens the time for a stable biogas production rate.

Discussion

Table 1 shows that through the MW-A pretreatment, the DD of manure was increased significantly. This could due to microwave radiation break down the complex structure of the an class="Chemical">polymer substclass="Chemical">ances, class="Chemical">and it cclass="Chemical">an make proteins class="Chemical">and class="Chemical">an class="Chemical">sugars enter into a soluble phase[16], meanwhile alkaline effectively solubilize particulate organic matter and improve the digestibility[17]. There was a positive correlation among the DD of manure, the alkaline degree and the energy input.

According to Table 2, x1 and x2 were significant influence factors, which means that pH and energy could significantly improve the DD of manure. Within the two parameters, pH was more important than energy input which reported by Doğan and Sanin[18]. The 3D response surfaces plot also revealed that the DD of manure increased along with enhancing energy input and alkaline degree (see Fig. 1(a)). The results confirmed that the high pH value was benefit for pretreatment. For example, the energy input remained the same but pH levels increased from 8 to 12, the DD rose from 33.05% to 63.91%. On the contrary, the DD had no significant difference when pH remaining at 10 and energy input enhanced from 54 J/g to 90 J/g, which got 36.42% and 37.14%, respectively. The comparison of predicted value and actual value (Fig. 1(b)) also indicated that the alkaline microwaving pretreatment could promote the disintegration degree of manure.

In general, the appropriate pH is 6.8–7.2 for completely mixed digesters[19]. Therefore, if the initial pH was higher than 10 (class="Chemical">NaOH dose was 0.1 mol/L or 0.2 g/g TS), the class="Chemical">anaerobic digestion process may have been obliterated[20]. In class="Chemical">anaerobic digestion process, class="Chemical">an class="Chemical">organic acids were accumulated when the rate of hydrolysis and acidification stages were over methane-producing stage, and this would cause pH decline. On the contrary, pH would enhance when organic acids could not effectively accumulate with similar rate of two stages[21]. Methanogens showed more sensitive to pH than acid formation bacteria[22], though few acidophilic methanogens had been found[23], most of which could only survive in neutral or weak alkaline environment, the accumulation of organic acids in the process of anaerobic digestion would inhibit the growth of methanogens[24]. In Fig. 2, only the combined pretreatment group remained weak alkaline environment for a long time, which implied that methanogens was always the dominant microflora through alkaline-microwave pretreatment group.

The protein is the main constituent of manure, and the manure proteins converted to soluble proteins and in hydrolysis and acidification process, respectively. The soluble organics were mainly produced by microwave effect, and absorbed by acid formation bacteria rapidly[25]. After burning up initial organics, the hydrolysis of manure began to release soluble organic gradually. The protein content of combined alkaline microwaving pretreatment was relatively higher in Fig. 3, which implied that excess acidity alkali promoted manure’s hydrolysis[26].

The an class="Chemical">AN mainly comes from protein class="Chemical">and other class="Chemical">an class="Chemical">nitrogenous organics’ degradation:

According the results presented in Fig. 4, the pretreatment group’s class="Chemical">AN density of microwave was greater thclass="Chemical">an the control group, the reason may lie in that there was more protein hydrolysis of class="Chemical">an class="Chemical">AN after pretreatment for microwave. Many earlier studies had investigate that pH and AN concentration could affected the methane production[27]. By adjusting pH to 8.0, a stable digestion of a synthetic acetic acid substrate at inhibitory TAN (total AN concentration) levels of 500 mg/l was maintained[27]. The high-solids sludge digester could be operated satisfactorily at pH of 9.0 and AN concentration of 900 mg/l[28]. The methane yields in mesophilic Anaerobic Digester were optimum at pH of 7.9 and 3300 mg TAN/l concentration. However, as TAN went up to 5500 mg/l, 50% reduction in methane production was observed[29]. But few studies showed that the relationship between pH and AN concentration. Figure S2 presented that the dissolution rate of ammonia decreased with the increasing of pH, so although the protein concentration was the highest after combined pretreatment, because of the weak alkaline environment, which resulted in the low activity of enzymes relative, and the degradation of protein and other nitrogenous organics became more difficult. As a results, the AN content was lower in the digester.

The result of Fig. 5(a) shows that there is a linear correlation between solubilisation and biogas yield[30], higher energy increases biogas yield even after reaching the boiling point in pretreatment[31]. The disintegration degree of manure was the highest after combining alkaline microwaving pretreatment, the substrate of methanogens was plenty and the hydrolysis rate grew rapidly in the beginning of the anaerobic digestion[5].

This study showed MW-A group achieved the highest total biogas production than others. The biogas production mainly relies on methanogen. However, the methanogen was inhibited when excess concentration of class="Chemical">AN existed[32]. Even though class="Chemical">an class="Chemical">ammonia is an essential nutrient for bacterial growth, it may inhibit methanogenesis during anaerobic digestion process if it is available at high concentrations[27]. The MW-A pretreatment seemed to improve the recovery speed and stability of an ammonia-inhibited biogas digester fed with cattle manure[33]. The AN concentration was lower and pH presented weak alkalinity during anaerobic digestion process, which was suitable for methanogen growth and consequently improved biogas production. This study demonstrated that the MW-A pretreatment improved performance of anaerobic digestion by increasing biogas amount and accelerating the reaction rate.

Methods

Apparatus

The device of microwave reaction includes the microwave power system, reactor chamber and condenser. The microwave power system whose brand is MY1000S was provided by Huiyan Microwave Corporation (Nanjing, Jiangsu, China). The power of the microwave reaction ranges from 0 to 1000 W. The reaction time was controlled by a timer. The microwave reactor schematic is shown in Fig. S1.

Manure

The an class="Species">swine mclass="Chemical">anure for the experiment was obtained from the rural family class="Chemical">an class="Species">swine farms. Fresh manure was smashed and filtered through a 0.45 mm sizing screen, and then refrigerated at 4 °C before study. The characteristics of the manure were listed in Table 3.

Table 3

Characteristics of swine manure used in this study.

pH	TCOD (mg/g TS)	SCOD (mg/g TS)	TS(%)	VS(%)
7.14 ± 0.26	208.4 ± 16.3	50.39 ± 0.82	6.02 ± 0.12	4.26 ± 0.06

Characteristics of an class="Species">swine mclass="Chemical">anure used in this study.

Microwaving pretreatment

The alkaline microwaving pretreatment for manure disintegration was conducted as follows: The pH value of 100 ml manure was firstly adjusted to 8.0, 9.0, 10.0, 11.0 and 12.0, respectively, by adding 1.0 M class="Chemical">sodium hydroxide (class="Chemical">an class="Chemical">NaOH) or 1.0 M hydrochloric (HCl), and the desired pH values were kept with ±0.1 unit fluctuations. Previous research has shown that the rate of hydrolysis and release rate of protein would arrive at maximum when microwave power reached 300 W, and the earlier study has also reached the same conclusion[26]. So the manure in a quartz reactor was immediately heated in microwave reaction chamber with a microwave power of 300 W. The energy input was set as 18, 36, 54, 72, or 90 J/g by altering the irradiation time. Energy (E) was determined by microwave power (P), microwave time (t), manure solution volume (V), and manure solution volume density (ρ):

Each sample was analyzed in triplicate, and the average values were determined for each set.

Anaerobic digestion experiment

an class="Chemical">Anaerobic digestion experiments were conducted in three glass amber bottles. The effective volume of reaction system is 500 mL each. Every reactor contained a volume of 300 mL mclass="Chemical">anure. The control group was set by adding untreated mclass="Chemical">anure to one reactor class="Chemical">and keeping the pH value at 7.0. The other two experimental groups were added with mclass="Chemical">anure pretreated by microwave power of 300 W class="Chemical">and reaction time of 180 s, which was based on the result of class="Chemical">an class="Chemical">RSM. One experimental group’s pH value was adjusted to 12.0 by 1 M NaOH or 1 M hydrochloric (HCl), the other was kept at 7.0. The reactors were placed in Stirring hot plate (100 rpm, 35 ± 1 °C) for 40 days, and the gas production was recorded once a day. In order to maintain strict anaerobic condition, oxygen was removed by nitrogen gas sparging before fermentation.

Analysis

Soluble chemical an class="Chemical">oxygen demclass="Chemical">and (SCOD), total chemical class="Chemical">an class="Chemical">oxygen demand (TCOD), pH, total solid (TS), and volatile solid (VS) were measured according to the Standard Methods. Soluble protein was determined by the Folin phenol method with bovine serum albumin (BSA) as standard[34]. AN was determined by Nessler reagent spectrophotometry[35]. Biogas production was measured with a wet gas meter. Methane was detected by a gas chromatograph (GC7890A, Agilent Technologies, Inc., USA).

Response surface methodology (RSM)

an class="Chemical">RSM is a sensitivity class="Chemical">analysis method, which cclass="Chemical">an improve the output of the model class="Chemical">and its related input variables. Compared with orthogonal test, class="Chemical">an class="Chemical">RSM can analyze every level of the experiment continuously in the optimization process, while orthogonal test can only study independent data points.

In this study, the experimental design was to combine a central composite design (an class="Disease">CCD) with Design-Expert, a software used for data collection class="Chemical">and class="Chemical">analysis, which was used to research the effect of two independent variables: pH class="Chemical">and energy (E). These two variables’ respective rclass="Chemical">anges were chosen in Table 1.

The target response was the disintegration degree (DD) of manure, which could be calculated by the following formula:where SCOD is the SCOD of the pretreated manure, and SCOD0, an class="Chemical">TCOD0 is the SCOD, class="Chemical">an class="Chemical">TCOD of the untreated manure, respectively.

The experimental data was fitted by a second-degree polynomial equation:Y is the response variable, x1 and x2 are the coded variables. The model prediction is determined by a series of regression coefficient β, including central point β0, linear coefficients β1, β2, interaction coefficient β11 and quadratic coefficients β11, β22.

Ethical statement

This article does not contain any studies with an class="Species">human class="Chemical">an class="Species">participants or animals performed by any of the authors.