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Article

Improving the Sustainability of Farming Practices through the Use of a Symbiotic Approach for Anaerobic Digestion and Digestate Processing

by
Frank Pierie
1,2,*,
Austin Dsouza
1,2,
Christian E. J. Van Someren
1,
René M. J. Benders
2,
Wim J. Th. Van Gemert
1 and
Henri C. Moll
2
1
Centre of Expertise Energy, Hanze University of Applied Science, Zernikeplein 17, 9747 AA Groningen, The Netherlands
2
Centre for Energy and Environmental Sciences, University of Groningen, Nijenborgh 4, 9747 AG Groningen, The Netherlands
*
Author to whom correspondence should be addressed.
Resources 2017, 6(4), 50; https://doi.org/10.3390/resources6040050
Submission received: 22 August 2017 / Revised: 18 September 2017 / Accepted: 19 September 2017 / Published: 26 September 2017
(This article belongs to the Special Issue Sustainability Indicators for Environment Management)

Abstract

:
The dairy sector in the Netherlands aims for a 30% increase in efficiency and 30% carbon dioxide emission reduction compared to the reference year of 1990, and a 20% share of renewable energy, all by the year 2020. Anaerobic Digestion (AD) can play a substantial role in achieving these aims. However, results from this study indicate that the AD system is not fully optimized in combination with farming practices regarding sustainability. Therefore, the Industrial Symbiosis concept, combined with energy and environmental system analysis, Life Cycle Analysis and modeling is used to optimize a farm-scale AD system on four indicators of sustainability (i.e., energy efficiency, carbon footprint, environmental impacts and costs). Implemented in a theoretical case, where a cooperation of farms share biomass feedstocks, a symbiotic AD system can significantly lower external energy consumption by 72 to 92%, carbon footprint by 71 to 91%, environmental impacts by 68 to 89%, and yearly expenditures by 56 to 66% compared to a reference cooperation. The largest reductions and economic gains can be achieved when a surplus of manure is available for upgrading into organic fertilizer to replace fossil fertilizers. Applying the aforementioned symbiotic concept to the Dutch farming sector can help to achieve the stated goals indicated by the Dutch agricultural sector for the year 2020.

1. Introduction

Within the European Union, sustainable agriculture could play an important role in achieving the renewable goals set for 2020 [1], and the renewable vision set for 2050 [2]. Research in the domain of agriculture widely recognizes the importance of sustainable agriculture production systems [3]. However, while modern agriculture is very productive, its negative effects on the environment have become increasingly visible [4]. Current practices aim at reducing per-unit costs of production, which results in increased intensity, more specialised production, and increased emissions of substances (e.g., global warming potential) with negative effects on the surrounding ecosystems and the overall climate [3,4,5] (e.g., environmental impact). Within the context above, and in accordance with the Dutch goals for energy efficiency and renewable energy production [6], the Dutch agricultural sector has formulated goals for sustainable farming. Among others, these goals include: less use of fossil resources and with it lowering anthropogenic emissions; lowering the use of fossil fertilizers; increasing renewability and sustainability of agriculture as a whole; and connecting and integrating agriculture into society [7]. Furthermore, an agreement signed between the dairy sector and the Dutch government aims at 30% increase in efficiency, 30% carbon dioxide emission reductions compared to the reference year of 1990, and 20% share of renewable energy in the year 2020 [6,8].
Among others, Anaerobic Digestion (AD) has been suggested as a potential renewable energy source for use in the farming sector. The AD process has been successfully implemented in the treatment of several biomass feedstocks, AD is already established as a reliable technology in Europe [9], and can extract energy from biomass in the shape of biogas, which is a flexible and storable energy carrier [10]. However, the choice of feedstocks, technologies, and the operational values of AD systems have a substantial influence on environmental impacts of the AD process [11,12,13,14,15,16,17]. The use of intensively cultivated energy crops, long transport distances, and the use of energy intensive processes can negatively affect the environmental impact of AD systems [10,13,17]. Business cases for farm scale AD systems within the Netherlands are often unfeasible due to high investment, feedstock, and operational costs [18,19,20,21] and the lack of stable and consistent subsidy [8]. Also, focus within the agricultural sector is often placed on single-issue regulation and/or single improvement options (e.g., renewable production, emission reduction, or waste reduction). Within a complex system like agriculture there is a good chance that “single factor” manipulation could result in a cumulative negative overall gain [4].
Within the aforementioned context, implementing the Industrial Symbiosis concept focusing on optimizing the AD system could potentially lower the environmental impact and cost of farm scale AD systems. Industrial Symbiosis, a key concept of industrial ecology, studies the physical flows of materials and energy in local industrial systems using a systems approach [22]. Industrial Symbiosis engages separate industries in a collective approach to create a competitive advantage involving the exchange of materials, energy and services [23]. In an ideal symbiotic system, waste material and energy are utilized between/among the actors of the system and the consumption of virgin raw material and energy inputs as well as the generation of wastes and emissions are thereby reduced [23]. The Industrial Symbiosis concept can help avoid the single factor manipulation by making the AD system an integral part of farming activities. In particular, waste resulting from a generic production process can substitute primary inputs in another process [24]. For instance, by creating a circular symbiotic system where bio-waste is used for energy and fertilizer production which can be reused for the production of new biomass [25,26,27,28,29,30], if reuse of waste as fertilizer satisfies the requirements for a negligible concentration of plant harmful elements. Furthermore, the use of local waste products also avoids intensive farming processes [31], long distance transport, and the widespread debate regarding the use of food-quality biomass for energy production [32], while organic fertilizer use avoids the production, import, and use of fossil fertilizers [17]. To achieve the aforementioned, the AD process will need technical adaption and optimization through the use of several improvement options operating symbiotically. This can give the opportunity to gain collective benefits significantly larger than the sum of the individual benefits [23,33].
However, to the authors’ knowledge, no literature discusses the integration and optimization of an AD system within local farming practices using the Industrial Symbiosis concept; which could indicate, among others, that the AD system has not been fully optimized. Therefore, within this article a farm scale AD system, utilizing locally available biomass waste streams, is analyzed and optimized on four indicators of sustainability (i.e., energy efficiency, carbon footprint, environmental impacts, and costs), through the use of the Industrial Symbiosis concept, combined with energy and environmental system analysis, Life Cycle Analysis, and modeling. Exploring the aforementioned, combinations could lead to environmental and economic improvements on current AD systems and lead to the integration of circular symbiotic AD systems within future farming practices to reduce the overall environmental impact and cost of the farming process.

2. Methods

In the following section the methods used during the formation of the results are described.

2.1. The Biogas Simulator

The assessment is performed by modeling the complete AD system. The excel model used [34,35] is based on the industrial metabolism concept. To gain insight into the energy use, carbon footprint, environmental impacts, and costs of the AD system, the model combines Material and Energy Flow Analysis (MEFA) [36], Energy and Environmental System Analysis [10], Attributed Life Cycle Analysis (aLCA), and Net Present Value (NPV) [37]. The model was extensively validated before being used [35]. The overall sustainability is defined within this article as “strong sustainability”, wherein environmental quality precedes social prosperity and then economic prosperity [38,39]. The LCA analysis is undertaken in accordance with European guidance and DIN EN ISO 14040 to 14044: 2006 [40]. The environmental impacts were obtained through the use of the SimaPro v8.0 (2013) utilizing the Eco Invent database v3.0 (2013) as endpoints.

2.2. System Boundary

Dutch regulation states that at least 50% of the feedstock used in an AD system must consist of manure (e.g., cow, pig, chicken manure). The remaining 50% can comprise of other biomass (e.g., harvest remains, catch crops, roadside grass, or maize). The ratio of manure and feedstock and the type of feedstocks used must comply with Dutch regulation in order for the digestate to be used as fertilizer [41]. Energy and material flows and their impacts are taken into account when they are in service of the AD system (e.g., production, processing, and transport), (Figure 1) [31]. The embodied energy (required energy for the production) of the installations is also incorporated. Within this research, mitigation regarding the replacement of current waste treatment chains (e.g., current manure storage and waste crop management) with an AD system, and of fossil fertilizer with organic fertilizers, is taken into account. Regarding the processing of digestate (Figure 1) only the economic cost are incorporated [17]. Emissions from the soil are not included. Internal energy use is included where external sources of energy can be replaced with the energy gained from the AD system (Figure 1). Additional economic costs or revenues saved or lost through the use of improvement options are taken into account as cash flows within the NPV. The current energy and fertilizer use (e.g., manure, fossil fertilizers) of farms are included in a theoretical reference case, for determining the effectiveness of a cooperatively owned circular symbiotic AD system. The costs and revenues of the AD system are based on prices and subsidies within the Netherlands [42].

2.3. Sustainable Impact Indicators (SI Indicators)

The energy efficiency, carbon footprint, and the sustainability of green gas production are expressed in three indicators: First, (Process) Energy Returned on Energy Invested or (P)EROI, defined as the ratio between the energy obtained from a resource to the energy expended in the production and processing of a resource [43]; Second, the carbon footprint, expressed in carbon dioxide equivalents (CO2eq) using the relevant 100-year global warming potential scale or GWP (100), [44]; And finally, the overall impact on the environment, expressed in the ReCiPe 2008 Eco indicator, used by the SimaPro model [45,46]. The specific choice for the above-named indicators and a clear description thereof are discussed in Pierie et al. [47]. The financial feasibility is expressed in Net Present Value (NPV) over 25 years [37]. The NPV method was selected as it is a commonly used indicator for economic feasibility and indicates the overall returns of the investment [37]. The general rule of thumb is if the NPV is positive, “invest”, and if it is negative, “don’t invest”. The NPV rule recognizes that the value of money today is worth more than the value of money tomorrow, because the money can be invested today to start earning interest immediately. NPV depends solely on the forecasted cash flows of the project and the opportunity cost of capital. Since the present values are all measured in today’s value, they can be added [37]. The aforementioned SI indicators will be the measure of sustainability within this article.

3. The Location and Biomass Feedstocks

The AD system is located on a dairy farm in the middle of the biomass collection area, represented as a circle (biomass circle). The distribution of biomass, dairy farms, and agricultural farms, averaged for the Netherlands, are retrieved from Pierie et al. [47]. In addition, catch crops (e.g., flower rich margins or buffer strips) are also used as feedstock for the AD system. During the cultivation of catch crops the use of machinery and fossil fuel is taken into account for seeding and harvesting, no fossil fertilizers are used directly. Average biogas and methane yield values are selected resulting from several combinations of catch crops [48]. The radius of the biomass circle is determined by the feedstock needs of the AD system: Therefore, the mix of feedstocks is determined from the availability of biomass in the biomass circle (Table 1). With the average radius of the biomass circle known, the average transport distances can be determined [31]. Additionally, a tortuosity factor is included, which represents inefficiencies in transport (e.g., winding roads, multiple pickup locations) [31,49] (Table 1). A clear description of the aforementioned can be found in Pierie et al. [47]. For biomass waste flows, only transport cost are included (Table 1), except for manure from external sources where negative prices are used within the Netherlands, due to its over-abundance [50], and for roadside grass where harvesting costs from road embankments are included [51].
All scenarios will use the same AD plant setup as a starting point (normal scenario), (Figure 2). The AD system, with a feedstock throughput of 20,000 Mg/a (Table 1), is stirred and heated to maintain mesophilic temperature. When required, feedstocks are mechanically pre-treated, screened for foreign debris (e.g., plastics, stones), and/or pasteurized. Transport of biomass is conducted by truck, loading and unloading is incorporated (Table 1). Part of the produced biogas is used in a small boiler to produce the needed heat for the digestion process. The remaining biogas is upgraded to green gas through the use of a highly selective membrane upgrader system [52]. The green gas is injected in the national gas grid (Figure 2). A gas pipe of one kilometer is used to transport the green gas from the production site to the injection station. The electricity use for the AD system is imported from the national electricity grid. The digestate is used on site as fertilizer on the pastures (Figure 2). The NPV of the business case, over a technical lifetime of 25 years and an economic write off period of 15 years, is based on economic factors within the Netherlands (e.g., energy prices, CAPEX, OPEX) [20,50,53]. Subsidies for green gas or electricity production are given per kWh of energy injected into the grid [42], (Appendix B).

4. Scenarios

To come to a more sustainable farming concept, first, the effect of the individual improvement components on the SI indicators, applied to the AD system, is analyzed (Appendix A). Second, multiple individual improvements are combined in a symbiotic design with maximum positive impact on all the SI indicators (Figure 3). Finally, the theoretical lessons learned from the symbiotic systems are applied in a theoretical case based on a cooperation of dairy and agricultural farms including average consumption of farming practices, which includes energy, fuel and fertilizer use (Figure 3).

4.1. Circular Symbiotic Scenarios

Within the circular symbiotic scenarios the main biogas production and green gas utilization pathway (Figure 2) is expanded with several improvement options (Appendix A) to research possible improvements on the main SI indicators (Section 2.3). The optimum sub-scenarios (Table 2) are determined through empirical modeling of several combinations of individual improvement scenarios. Additional installation properties, investment, and operational costs of improvement options are included (Appendix B).

Reference Scenarios

The results from the symbiotic scenarios are compared to four reference scenarios (Table 3).

4.2. Cooperative Farming Theoretical Case

The theoretical lessons learned from the individual improvement options and the symbiotic scenarios (Section 4.1) are applied to a theoretical case based on the cooperation of five dairy and seven agricultural farms, which are treated in this article as a single entity called the cooperation. The required amount of farms within the cooperation is determined by the feedstock needs of the AD system (Table 1). The feedstocks acquired within the cooperation (including manure) only include transport costs. Within the theoretical case all manure is retrieved within the cooperation. The cooperation will use biomass from the local government and water board responsible for managing the biomass growth alongside roads, canals, natural areas, and/or parks (Table 4); however, this will include harvesting costs (Table 1). The fields used for roadside grass and natural grasslands do not require fertilization, due to natural inflow of nutrients. Regulation regarding green gas and electricity production using AD within the Netherlands is stable with a guaranteed subsidy for a maximum of 22 years. However, taxes and subsidy schemes for the aforementioned symbiotic systems within the Netherlands are currently undefined, to the authors knowledge; therefore, the effect on the yearly costs is difficult to indicate. For instance, policies and subsidies for green electricity, green gas and green fuel produced and used within the cooperation are currently nonexistent. Within the NPV cost calculation the Dutch low tax rate of 6% is included for the internal energy products produced within the cooperation (e.g., electricity, green gas, green fuel, and organic fertilizers), which is comparable to the current form of subsidy. Additionally, differences in tax rates and their effects on the total cost are discussed in the sensitivity analysis (Section 5.3).
All three theoretical cases (Table 5) are based on the same energy and fertilizer needs of the cooperation (Table 4). Within the cases the SI indicators are calculated over a period of 25 years and are expressed per year. The SI indicators are expressed in absolute numbers, not including mitigation (and return on investment for NPV), as used in the previous Section. The cases (Table 5) are based on the average land occupation and feedstock availability described in Section 3 and the basic AD system described in Section 4.

4.3. National Implementation Case

To indicate the possible effect of the theoretical case aforementioned on a national level, results are extrapolated towards full implementation in the Netherlands. Within this case the assumption is made that all farms will participate in cooperatives and that all the local biomass availability is utilized. Also, the available feedstock in the biomass circle described in Section 3 is assumed to be similar for all cooperations (Table 1). Please note however, that in practice biomass circles can differ. Therefore, when actually implemented at national scale, results can vary. The amount of cooperations is determined by dividing the total land availability for farming in the Netherlands by the land required by the farms within a cooperation (Table 6).
Within the national scope case, the total amount of surplus manure available nationally determines how many AD + M cooperations can be set up. According to the Bureau of Statistics of the Netherlands, in the year 2015 there was a nutrient surplus for both nitrogen and Phosphate of around 25% (Appendix C) [57]. Therefore, within the AD + M national case, 25% of the cooperations are based on an AD + M and the rest are based on AD cooperations (Table 6). The results are compared with the total national carbon footprint and the carbon footprint from the farming sector in the Netherlands, for the year 2015 and the reference year of 1990.

5. Results

Within this section first the results of the symbiotic AD system are discussed, followed by the theoretical case and the national case.

5.1. Symbiotic Circular Systems

When implementing the single improvement options individually, improvement on the SI indicators can already be observed (Appendix A). For instance, a substantial gain in (P)EROI can be achieved through the use of a CHP unit (Figure 4a CHP) by avoiding external electricity and heat requirements. Replacing fossil fertilizer with organic fertilizer has a substantial effect on the carbon footprint and environmental impact as fossil fertilizers require high energy investment during production (Figure 4b,c Fertilizer). Installation of a second digester and additional input of manure directly into the second digester can improve the NPV (Figure 4d Manure). The second digester system requires little additional energy and maintenance but still produces additional biogas. However, the reduction achieved by individual improvement options is often significant for only one or two of the four SI indicators (Appendix A). For instance, organic fertilizers production positively affects carbon footprint and environmental impact but negatively affects the (P)EROI and NPV; this is caused by high energy use in the process, substantial initial investment costs, and additional operational costs for energy and maintenance. Within this context, and given the systemic nature of agricultural systems, focusing on single factors does not necessarily lead to optimal results.
Whereas the impacts of individual improvement options are relatively minor, results from the symbiotic scenarios indicate that a symbiosis of improvement options can substantially improve all SI indicators compared to the reference scenarios, (Figure 4). Internal energy production substantially improve the (P)EROI in all scenarios, with additional improvement in scenario A and C due to the high energy needs of organic fertilizer production (Figure 4a). For both scenarios A and C, the effect of fertilizer replacement is larger than the produced impacts in the biogas pathway, resulting in negative carbon footprint and environmental impacts (Figure 4b,c). In contrast, the actions taken in scenario B reduce the carbon footprint by 69% and environmental impact by 89% (Figure 4b,c), highlighting the effect of fossil fertilizer replacement. Furthermore, scenario C indicates that only operating a CHP unit combined with fertilizer production is sustainable and profitable, suggesting the option for modification of current CHP operated AD systems (Figure 4d). Finally, the NPV for all scenarios are positive, with scenario A being most profitable due to the combination of internal energy production and the production and selling of organic fertilizers (Figure 4d). However, economic success is strongly dependent on possible utilization and added value of digestate: If, for instance, in scenario A, the organic fertilizers cannot be used for replacing fossil fertilizer or sold, the NPV will become negative. Also, if in scenario B more than 65% of the digestate has to be discarded at 10 €/Mg (Average rate in the Netherlands 2010–2016 [19]), the NPV will turn negative.

5.2. The Theoretical Cooperative Farming Cases

Within the theoretical case, focus is placed on combining the circular symbiotic AD system with current farming practices in a cooperative setting. Current farming practices, incorporated in the reference case (REF), include: fossil energy use (e.g., electricity, natural gas) for powering machinery and heating, fossil fuel use (e.g., diesel) for powering machinery, and fossil fertilizer use for nutrient replacement (Figure 5). Results indicate that internal production of energy, transport fuel, and organic fertilizers within a cooperation of farms operating a circular symbiotic AD system can significantly lower energy consumption, environmental impact, and yearly costs (Figure 6).
Energy use in the shape of electricity, diesel, gas and the production of fertilizers can be reduced by 72% in the AD case, and up to 92% in the AD + M case, as compared to the REF case (Figure 6a). The biggest reduction in energy use can be achieved through the replacement of fossil energy sources (e.g., electricity, natural gas, diesel), closely followed by fossil fertilizers that require significant amounts of energy during production (Figure 5a). However, to substitute the fossil energy sources and produce organic fertilizer, around 52% of the produced biogas is used internally within the AD case, and around 49% in the AD + M (Figure 7). The AD + M case produces more biogas due to the added manure in the second digester and, therefore, uses relatively less biogas internally (Figure 7b). Due to internal energy production and fossil energy replacement, external energy demand within both cases is minimal, mostly in the shape of embodied energy (e.g., installations and infrastructure, steel, concrete, etc.), (Figure 7). However, due to insufficient manure availability in the AD case, fossil fertilizers have to be used (Figure 7a).
The carbon footprint can be reduced by 71% in the AD case up to and 91% in the AD + M case, while the environmental impacts can be reduced by 68% and 89% respectively, compared to the REF case, (Figure 6b,c). The biggest emission sources in the REF case are the production of fossil fertilizers (Figure 5b,c). Therefore replacing fossil fertilizers with organic fertilizers has a significant effect on the carbon footprint. Within this context, the availability of excess manure feedstock for processing and upgrading into organic fertilizer used for fossil fertilizer replacement has a substantial effect on energy use, carbon footprint, and environmental impact (Figure 6a,c). Therefore, when looking to reduce energy and impact of farming practices, a spatial distribution of dairy, agricultural, and pig and chicken farms in close proximity working closely together within a cooperation could be suggested. Unfortunately, currently the use of organic fertilizers replacing fossil fertilizers is not allowed by the European Union [55]. There are, however, exceptions made within the Netherlands for some companies [56]. Without the replacement of fossil fertilizers the carbon footprint and environmental impact can only be reduced by a maximum of 31% in the AD case and 27% in the AD + M case, compared to the REF case (Figure 5b,c). Additionally, the remaining green gas is injected into the national grid (Figure 7) replacing natural gas and further reducing carbon footprint and environmental impacts indirectly. This effect is not included within the AD or AD + M case as it does not lower the carbon footprint and environmental impact of farming practices. However, the avoided impacts are still significant and can be included on a national scope (Table 7).
Yearly costs can be reduced by 56% in the AD case and 66% in the AD + M case compared to the REF scenario (Figure 6d). The biggest reductions and economic gains can be achieved when a surplus of manure feedstock is available for processing and upgrading into organic fertilizer used for fossil fertilizer replacement (Figure 7d). However, the effect of additional manure input has less impact on cost reductions than when looking to the other SI indicators, which can be traced back to the higher initial investment needed in the AD + M case and the higher operational and maintenance costs compared to the AD case. Initial investment costs are substantial ranging from 3.1 million € for the AD case up to 3.9 million € for the AD + M case. Another important cost reduction is the selling of green gas. After internal consumption the remaining green gas (around 35% in the AD case and 39% in the AD + M case) is sold and injected into the gas grid lowering the yearly costs (Figure 6).
Additionally, within the local setting of this article, the cooperation can become a local handler of organic waste streams and also a supplier of green fuel, green energy (e.g., electricity, gas, heat), and organic fertilizer. For instance, green gas and/or excess heat could be used locally to balance the electricity grid, heat buildings, and help integrate intermittent energy sources (e.g., solar PV, wind). Within this context, heat losses from the CHP unit (Figure 7) could be used in heating surrounding buildings with district heating. When selling heat to external consumers, energy saving options (e.g., insulation, heat recovery) become viable, where now in the AD and AD + M cases there is excess heat. Unfortunately, regulations on green fuel and fertilizer use and subsidies for circular symbiotic systems are currently unclear. Unstable policies combined with a significant investment and operational costs place substantial risks on the business case. Therefore, to support a stable business case over the economic and technical lifetime of the circular symbiotic AD system, focused and stable policies, improved regulation, and strong cooperation must be initiated to achieve the above results.

5.3. National Scope

When applying the concept described in the theoretical case to the agricultural sector in the Netherlands, the targets set by the Dutch agricultural sector can be achieved for the 25% AD + M case (Table 8). Also, the additional production of green gas could supply the whole agricultural sector with electricity and heat. However, part of the energy and emissions saved within the cases are outside of the agricultural sector: For instance, the production of fertilizers and the mitigation of green gas. Also, within the theoretical case, the energy use and carbon footprint from electricity and fuel production are taken into account, where the carbon footprint from the agricultural sector is often only linked to direct use and emissions. Furthermore, within the total carbon footprint of the agricultural sector, the service sector and other agricultural activities are included (e.g., offices, greenhouses), which are not incorporated in the cooperative case. Overall, by fully utilizing the manure and other biomass waste streams, in a circular symbiotic AD system producing energy, green fuel, and organic fertilizer, the energy efficiency, carbon footprint, and environmental impact can be improved upon. Within this context, the circular symbiotic approach can optimize the AD system and help the agricultural sector to become more sustainable and profitable.

5.4. Sensitivity Analysis

Using organic material in a biological process and uncertainties surrounding business cases inherently creates variations and sensitivities. When comparing scenarios, similar settings will cancel out sensitivities in the used values. This approach has been applied to the symbiosis scenarios (Section 4.1 and Section 5.1). Sensitivities connected to biomass use within the aforementioned scenarios are described in Pierie et al. 2015 [17]. However, in the cooperative scenarios (Section 4.2 and Section 5.2) the results will be more prone to sensitivities as compared with a reference farm in more absolute terms; therefore, focus is placed on these results. The most sensitive values regarding the feedstocks (e.g., biogas potential, methane potential, organic dry matter content, and environmental impacts of the collection and/or cultivation process), are retrieved from Pierie et al. 2015 [17] (Appendix B). The results indicate that within the range of the indicators given, even the worst-case improvement scenario has less impact than the reference scenario (Figure 6a,c). Within the economic variables, biogas production, maintenance, and interest are most dominant. When combined, the sensitivity of all SI indicators varies substantially (Appendix B); in this case scenarios may perform better or worse than the reference scenario (Figure 6d). For instance, in the worst case, projected costs for the cooperation exceed the best case of the reference farms, indicating some risks in the business case. However, for this to happen a combination of circumstances working with or against the process is needed (e.g., bad harvest, high energy use harvest, low methane yields of crop, low market prices, and weak regulations).

6. Discussion

Energy production through AD is a promising method for producing a renewable and flexible energy carrier. However, the reference scenario used in this article only indicates a minor reduction in carbon footprint and environmental impacts and a low efficiency with a negative NPV for farm scale AD installations within the Netherlands. Furthermore, results also indicate that the AD system is not fully optimized in combination with farming practices regarding sustainability. Implementation of the single improvement options individually has a positive impact on the SI indicators (i.e., energy use, carbon footprint, environmental impacts, and costs). However, the reduction achieved by individual improvement options is often substantial for only one or two of the four SI indicators. For instance, organic fertilizer production positively affects the carbon footprint and environmental impact but negatively affects the (P)EROI and NPV; this is caused by high energy use in the process, substantial initial investment costs, and additional operational costs in the shape of energy and maintenance. Given the systemic nature of agricultural systems, focusing on single factors does not necessarily lead to optimal solutions. Using a circular symbiotic system of improvement options, however, can substantially improve all SI indicators, making the system profitable over a lifetime of 25 years. Therefore, when implemented within the theoretical cooperative farming case, the symbiotic AD system can significantly lower external energy consumption by 72 to 92%, carbon footprint by 71 to 91%, environmental impacts by 68 to 89%, and yearly expenditures by 56 to 66% compared to a reference cooperation. Sensitivity analysis indicated stable results regarding efficiency, carbon footprint, and environmental impact, but high variation in the economic results. Therefore, the economic assessment requires more research. Economic success and also the reduction of emissions and environmental impacts within the cooperative case are strongly dependent on the availability of manure and making use of the added value from the digestate. Therefore, a spatial distribution of dairy, agricultural, and pig and chicken farms in close proximity working closely together could be suggested. Unfortunately, existing laws prevent the use of organic fertilizers to replace fossil fertilizers in the Netherlands. However, without fertilizer replacement a circular symbiotic system can still be created which produces positive results for all SI indicators. Within the cooperative case, approximately half of the produced energy is used internally; the remaining green gas, electricity, and/or heat can be sold and used locally to replace fossil energy sources and help integrate other intermittent energy sources in the local energy grids. Applying the aforementioned circular symbiotic AD systems can lower the environmental impact of farming by decreasing dependence on fossil-based energy and fertilizers and lowering the carbon footprint from farming, helping the Dutch agricultural sector in achieving their stated environmental goals. However, to achieve the aforementioned goals, focused and stable policies, improved regulation, and strong cooperation must be initiated, as regulations on green fuel and organic fertilizer use and subsidies for circular symbiotic systems are currently unclear within the Netherlands and the European Union.

Acknowledgments

Research providing this article has been funded by the Hanze University of Applied Sciences, University of Groningen, and the Flexigas project.

Author Contribution

Main research and body of article is written by lead author Frank Pierie and reviewed by second authors on focus and quality. Austin Dsouza helped in shaping the NPV calculations. Christian E. J. van Someren helped in the modeling and scenario phase and with the syntax of the document. René M. J. Benders also helped in the modeling and scenario phase and provided feedback on the research. Wim J. Th. van Gemert as Leading Lector gave guidance on the position of the paper and feedback on the context. Finally, Henri C. Moll provided guidance on both high level position and structure of the paper and in depth feedback on the performed research.

Conflicts of Interest

To the authors knowledge there in no conflict of interest steering the results in any way shape or form towards benefits of stakeholder.

Nomenclature

ADAnaerobic Digestion
CHPCombined Heat and Power
oDMGreen Dry Matter
PJPeta Joule (1015 Joule)
GJGiga Joule (109 Joule)
MJMega Joule (106 Joule)
TgTera gram (106 Mg)
MgMega gram (equivalent to metric ton)
SISustainable Indicator
GHGGreen House Gasses
(P)EROIProcess Energy Returned On Invested
GWP100Global Warming Potential 100 year scale
PtEnvironmental impact in EcoPoint
LCALife Cycle Analysis
aLCAAttributed Life Cycle Analysis
kgCO2eqKilograms of Carbon dioxide equivalent
Nm3Normal cubic meter (Volume at 1bar 0C)
NPVNet Present Value

Appendix A. Individual Improvement Options

The individual improvement options and their location within the AD system indicated in Figure A1 and explained Table A1 using corresponding numbers.
Figure A1. The optimized AD system for use in the sustainable farming concept.
Figure A1. The optimized AD system for use in the sustainable farming concept.
Resources 06 00050 g008
Table A1. Main improvement options.
Table A1. Main improvement options.
Nr.AffiliationDescription of Improvement Option
(1)CHPA Combined Heat and Power unit (CHP) is used to produce electricity and heat [17] to fulfill the energy demand of the complete AD system (e.g., digester, green gas production, digestate upgrading). Cables and pipelines are incorporated for transportation to the AD production processes [17]. Additional heat requirement not supplied by the CHP is produced by the biogas boiler. In the case of overproduction electricity is put on the local electricity grid and heat is discarded.
(2)RecoveryThe main digester operates at a mesophilic temperature of around 35 to 48 degrees Celsius; outgoing digestate will be at the same temperature. Therefore, heat energy in the outgoing digestate can be utilized through a heat exchanger to heat up the ingoing feedstocks at ambient temperature fed into the digester. Infrastructure and energy use for heat recovery is taken into account (Appendix Table A3).
(2)Heat pumpAdditionally, a heat pump can be added to the Heat recovery system aforementioned
(3)InsulationInsulation of the main digester will lower the heat loss from the main digestion tank, which operates at mesophilic temperatures. Therefore, biogas can be saved resulting in more green gas finally produced. Insulation will bring with it additional capital expenditure and embodied energy but will also reduce the heat demand of the process. Heat requirement of the main digester is lowered with 20% to simulate the effect of insulation on the SI indicators.
(4)PreventionGas leakages can be prevented through the use of repair and higher greenhouse gas emissions (e.g., methane) can be reduced using catalytic conversion lowering the carbon footprint. Repair focuses on actual leaks in biogas equipment such as the main and second digester, piping, upgrading installations. Catalytic conversion focuses on outputs from upgrading or combustion, which often contain methane or Nitrogen oxides, which are brought back to CO2 level using catalytic conversion. Within this improvement option, losses and emissions from the main digester and second digester are eliminated and higher greenhouse gas emissions from the green gas utilization pathway and CHP unit are reduced to carbon dioxide level.
(5)Green fuelGreen gas produced by the AD plant is used as fuel for agricultural machinery ranging from tractors, front loaders, and trucks transporting the biomass, replacing the use of fossil fuels (e.g., diesel). To achieve the aforementioned, infrastructure in the shape of a filling station is needed [60] which compresses the green gas and stores it in large enough quantities to fill several tanks (Appendix Table A3).
(6)2nd digesterProcessed digestate still contains some biogas potential [52]. However, it is often not efficient and economical to retain this using the main digester, as it is kept at mesophilic temperature and is stirred continuously. Within this context, a second digester (not heated and often stirred) can be used to store the digestate and collect the residual biogas production. The longer retention time in the second digester (up to 5 to 6 months) gives the AD process additional time to break down the last remaining digestible organic material into biogas. Infrastructure and energy use is taken into account (Appendix Table A4), also including the biogas potential of digestate which is based on an average number, as digestate composition is dependent on the feedstocks use in the digester (Appendix Table A4).
(7)+ManureDue to overabundance and low quality, the available manure is often not fully utilized. Manure can be directly pumped in the second digester to retain the produced biogas to replacing seasonal manure storage during winter or mix it with the digestate for utilization in fertilizer production. This technology can also produce additional environmental benefits, which can be mitigated. A maximum of 10,000 Mg of additional manure is added directly to the second digester. Infrastructure and energy use is taken into account (Appendix Table A4). For determining the biogas production of the additional manure the biogas potential of manure is used (Table 1).
(8)Organic fertilizersWithin this improvement option, a large share of the digestate (80%) is separated into a thick and a thin fraction using a manure separator [61]. The thin fraction is rich in nitrogen and contains most of the water, whereas the thick fraction contains most of the phosphates, potassium and organic materials. The thin fraction is processed using reversed osmosis to decrease the water fraction [56,62]. The processed and upgraded thin and thick fractions are used as organic fertilizers on the farm replacing fossil fertilizers (Table 5). The remaining 20% of the digestate is used for replacing manure fertilization on the pasture; however, this will not replace fossil fertilizers. The needed infrastructure and energy use of the installations is taken into account.
(8)Selling fertilizersOrganic fertilizers can also be sold on the market when own demand is fulfilled, unfortunately for lower prices. Within this improvement option all the organic fertilizer produced is sold on the market (Appendix Table A3).
In the following figures the impact of the individual improvement options on the SI indicators are indicated, the affiliations used to express the results in the figures will use the description in Appendix Table A1. The normal scenario in the graphs describes the basic AD green gas production pathway without any modifications as described in Section 4.1.
Figure A2. (a) The (P)EROI of the improvement scenarios; (b) The carbon footprint of the improvement scenarios; (c) The environmental impact of the improvement scenarios; (d) The NPV of the improvement scenarios.
Figure A2. (a) The (P)EROI of the improvement scenarios; (b) The carbon footprint of the improvement scenarios; (c) The environmental impact of the improvement scenarios; (d) The NPV of the improvement scenarios.
Resources 06 00050 g009

Appendix B. Additional Data Used in Article

Table A2. The main economic values used in the calculation of the NPV.
Table A2. The main economic values used in the calculation of the NPV.
Main Economic ValuesValueUnitSource
Interest on loan and Required rate of return5%[53]
Inflation1.8%[63]
Increase of electricity and gas price per year a2%[64]
Economic write off period15Years
CAPEX Main installationValueUnitSource
AD system53.64€/(Mg/a capacity)[18]
Feedstock pre-treatments systems3.00€/(Mg/a capacity)[65]
Upgrading system4024.88€/(Nm3/hr capacity)[18]
Green gas injection system550.00€/(Nm3/hr capacity)[18]
Scrap value installation after 25 years5%%/CAPEX[66]
OPEXValueUnitSource
Operation and maintenance5% Investment/a[18]
Tax on products6%/costs resource[67]
Income tax 25%/costs resource[68]
Transport by truck0.05€/ton.km[18]
Electricity from grid0.19€/kWh[57]
Natural gas from grid c0.53€/Nm3[57]
Diesel fuel1.40€/L[50]
INCOME GREEN GAS bValueUnitSource
Green gas market price c0.020€/kWh[42]
SDE Subsidization (12 years)0.076€/kWh[42]
SDE extended (additional 12 years)0.067€/kWh[42]
Correction fee SDE Subsidization (12 years)0.022€/kWh[42]
Correction fee SDE extended (12 years)0.022€/kWh[42]
INCOME GREEN ELECTRICITY bValueUnitSource
Green electricity market price0.025€/kWh[42]
SDE Subsidization (12 years)0.114€/kWh[42]
SDE extended (additional 12 years)0.101€/kWh[42]
Correction fee SDE Subsidization (12 years)0.032€/kWh[42]
Correction fee SDE extended(12 years)0.033€/kWh[42]
CAPEX improvementsValueUnitSource
Heat recovery digestate25€/kWth
Heat recovery with heat pump system200€/kWth
Insulation of the AD system4000€/% improvement
Second digester/manure storage90€/m3 (storage capacity)[50]
CHP unit946.16€/kWe[69]
Digestate separation unit1.45€/(m3 digestate/a)[61]
Digestate upgrading system (reversed osmosis)30€/(Mg/a capacity)[56]
Fueling station (approx. 4–8 trucks, tractors per day)75,000€/(20–40 GGE/day)d[70]
a The Increase of electricity and gas price per year is assumed based on [64] as the marked is very volatile and the price dependents on many factors; b The subsidy is determined by the SDE subsidies minus the correction fee; c Based market price gas of 12.5 €/MWh. Groningen natural gas and green gas have an higher energy content of 35 MJ/Nm3 or 9.7 kWh/Nm3; d GGE/day = Gallons of Gasoline Equivalent per day.
Table A3. The main values of the added technologies.
Table A3. The main values of the added technologies.
Added TechnologiesValueUnitSource
Efficiency heat exchanger90%
COP value heat pump 5 [71]
Energy requirement second digester5MJ/Mg FM
Energy requirement separator a4.68MJ/Mg FM[72]
Energy use reversed osmosis35MJ/Mg FM[56]
Energy use filling station b4.68MJ/Nm3[60]
a Based on an electric separator [72]; b INTERMECH BBR/FBR/VIP CNG compressors 55–450 kW/75–600 HP [60].
Table A4. Main values for production of fossil fertilizers replaced by upgraded digestate.
Table A4. Main values for production of fossil fertilizers replaced by upgraded digestate.
Fertilizers ReplacedNitrogen as NPhosphate as P2O5Potassium as K2OUnitsSource
Market price fossil fertilizer1.101.050.65€/kg[50]
Market price organic fertilizer0.600.510.26€/kg[73]
Required energy for production75.9027.912.9MJ/kg[58,59]
Emission during production12.602.222.30kgCO2eq/kg[58,59]
Environmental impact during production1.770.760.24Pt/kg[58,59]
Table A5. Scenarios used within the sensitivity analysis of the more sustainable farming cooperation cases.
Table A5. Scenarios used within the sensitivity analysis of the more sustainable farming cooperation cases.
Variable in Scenario WorstAveBestSource
Percentage%%%
(P)EROI57.18%100.00%149.02%[17]
Emission194.16%100.00%21.74%[17]
Impact207.00%100.00%25.51%[17]
Total investment120.00%100.00%80.00%
Salvage value 0.00%5.00%10.00%[50,66]
Biogas production57.18%100.00%149.02%[17]
Interest6.00%5.00%2.00%
Taxation on internal use21%6%0%[67]
Discarding digestate50.00%0.00%0.00%
Fertilizer price150.00%100.00%50.00%
Maintenances7.00%5.00%3.00%
Table A6. Energy and fertilizer use average Dutch dairy and agricultural farm.
Table A6. Energy and fertilizer use average Dutch dairy and agricultural farm.
Energy or Material FlowDairy FarmAgricultural FarmNatural AreasUnitSource
Total land use the Netherlands 956,000995,756?ha
Diesel use130238-L/ha.a[50]
Electricity use 940 a549-kWh/ha.a[50]
Natural gas use 32 a10-Nm3/ha.a
Water use 80 a10-m3/ha.a[50]
Nitrate cap265170?kg/ha.a[50]
Phosphate cap9565?kg/ha.a[50]
Potassium cap225225?kg/ha.a[50]
a Based on two cows per hectare of land producing 8500 kg of milk per year [50]; b Based on average agricultural farm of 40 ha [57] KWIN table p. 57.

Appendix C. Main Calculation Output National Case

Table A7. Carbon footprint and energy reduction of cooperative cases compared to Dutch carbon footprint and energy use in 2015.
Table A7. Carbon footprint and energy reduction of cooperative cases compared to Dutch carbon footprint and energy use in 2015.
Energy or Material FlowTotal NL aFarming aAD + MADUnit
Carbon footprint193.726.718.120.1Tg
Carbon footprint green gas 23.824.4Tg
Energy 2206.0133.963.475.7PJ
Energy green gas 72.485.3PJ
a Carbon footprint and energy use retrieved from Dutch Central Bureau of Statistics [57].
Table A8. Carbon footprint and energy reduction of cooperative cases compared to Dutch carbon footprint and energy use in 1990.
Table A8. Carbon footprint and energy reduction of cooperative cases compared to Dutch carbon footprint and energy use in 1990.
Energy or Material FlowTotal NL aFarming aAD + MADUnit
Carbon footprint193.726.719.620.1TgCO2eq
Mitigation green gas 23.824.4TgCO2eq
Energy 2206.0133.963.475.7PJ
Mitigation green gas 72.485.3PJ
a Carbon footprint and energy use retrieved from Dutch Central Bureau of Statistics [57].
Table A9. Carbon footprint and energy reduction of cooperative cases compared to Dutch carbon footprint and energy use in 2015.
Table A9. Carbon footprint and energy reduction of cooperative cases compared to Dutch carbon footprint and energy use in 2015.
Energy or Material FlowNitrogenPhosphateSource
Total nutrient production497,500180,100[57]
Possible placement of nutrients a377,000134,300[57]
Nutrient 120,50045,800
Percentage deposit24.22%25.43%
a The possible placement of nutrients within the Netherlands is determined by the available land surface [57].

References

  1. European Parliament. Directive 2009/28/EC of the European Parliament and of the Council of 23 April 2009 on the Promotion of the Use of Energy from Renewable Sources and Amending and Subsequently Repealing Directives 2001/77/EC and 2003/30/EC 2009; European Parliament: Brussels, Belgium, 2009. [Google Scholar]
  2. European Commission. Communication from the Commission to the European Parliament, the Council, the European Economic and Social Committee and the Committee of the Regions; Energy Roadmap 2050; Brussels, 15.12.2011. com(2011) 885 Final; European Commission: Brussels, Belgium, 2011. [Google Scholar]
  3. Pacini, C.; Wossink, A.; Giesen, G.; Vazzana, C.; Huirne, R. Evaluation of sustainability of organic, integrated and conventional farming systems: A farm and field-scale analysis. Agric. Ecosyst. Environ. 2003, 95, 273–288. [Google Scholar] [CrossRef]
  4. Vatn, A.; Bakken, L.; Bleken, M.A.; Baadshaug, O.H.; Fykse, H.; Haugen, L.E.; Lundekvam, H.; Morken, J.; Romstad, E.; Rørstad, P.K.; et al. A methodology for integrated economic and environmental analysis of pollution from agriculture. Agric. Syst. 2006, 88, 270–293. [Google Scholar] [CrossRef]
  5. Meyer-Aurich, A. Economic and environmental analysis of sustainable farming practices—A Bavarian case study. Agric. Syst. 2005, 86, 190–206. [Google Scholar] [CrossRef]
  6. Sociaal-Economiche Raad. Energieakkoord Voor Duurzame Groei 2013; Sociaal-Economiche Raad: Hague, The Netherlands, 2013. (In Dutch) [Google Scholar]
  7. Planbureau Voor Leefomgeving. Duurzame Landbouw in Nederland; Planbureau Voor Leefomgeving: Hague, The Netherlands, 2015. (In Dutch)
  8. Gebrezgabher, S.A.; Meuwissen, M.P.M.; Oude Lansink, A.G.J.M. Energy-neutral dairy chain in the Netherlands: An economic feasibility analysis. Biomass Bioenergy 2012, 36, 60–68. [Google Scholar] [CrossRef]
  9. Li, Y.; Park, S.Y.; Zhu, J. Solid-state anaerobic digestion for methane production from organic waste. Renew. Sustain. Energy Rev. 2011, 15, 821–826. [Google Scholar] [CrossRef]
  10. Berglund, M.; Börjesson, P. Assessment of energy performance in the life-cycle of biogas production. Biomass Bioenergy 2006, 30, 254–266. [Google Scholar] [CrossRef]
  11. Börjesson, P.; Berglund, M. Environmental systems analysis of biogas systems—Part II: The environmental impact of replacing various reference systems. Biomass Bioenergy 2007, 31, 326–344. [Google Scholar] [CrossRef]
  12. Poeschl, M.; Ward, S.; Owende, P. Environmental impacts of biogas deployment—Part II: Life cycle assessment of multiple production and utilization pathways. J. Clean. Prod. 2012, 24, 184–201. [Google Scholar] [CrossRef]
  13. Jury, C.; Benetto, E.; Koster, D.; Schmitt, B.; Welfring, J. Life Cycle Assessment of biogas production by monofermentation of energy crops and injection into the natural gas grid. Biomass Bioenergy 2010, 34, 54–66. [Google Scholar] [CrossRef]
  14. Hamelin, L.; Naroznova, I.; Wenzel, H. Environmental consequences of different carbon alternatives for increased manure-based biogas. Appl. Energy 2014, 114, 774–782. [Google Scholar] [CrossRef]
  15. Hahn, H.; Hartmann, K.; Bühle, L.; Wachendorf, M. Comparative life cycle assessment of biogas plant configurations for a demand oriented biogas supply for flexible power generation. Bioresour. Technol. 2015, 179, 348–358. [Google Scholar] [CrossRef] [PubMed]
  16. Mezzullo, W.G.; McManus, M.C.; Hammond, G.P. Life cycle assessment of a small-scale anaerobic digestion plant from cattle waste. Appl. Energy 2013, 102, 657–664. [Google Scholar] [CrossRef] [Green Version]
  17. Pierie, F.; van Someren, C.E.J.; Benders, R.M.J.; Bekkering, J.; van Gemert, W.J.T.; Moll, H.C. Environmental and energy system analysis of bio-methane production pathways: A comparison between feedstocks and process optimizations. Appl. Energy 2015, 160, 456–466. [Google Scholar] [CrossRef]
  18. Bekkering, J.; Hengeveld, E.J.; van Gemert, W.J.T.; Broekhuis, A.A. Will implementation of green gas into the gas supply be feasible in the future? Appl. Energy 2015, 140, 409–417. [Google Scholar] [CrossRef]
  19. Bekkering, J.; Hengeveld, E.J.; van Gemert, W.J.T.; Broekhuis, A.A. Designing a green gas supply to meet regional seasonal demand—An operations research case study. Appl. Energy 2015, 143, 348–358. [Google Scholar] [CrossRef]
  20. Toekomst Biogas: Van Laagwaardige Input naar Hoogwaardige Output. 2013, pp. 1–12. Available online: https://www.rabobank.nl/images/thema_update_biogas_29519499.pdf (accessed on 25 September 2017). (In Dutch).
  21. Vos, J.; Zwart, K. Mest(co)vergisting en Biogas/Groengas Productie in Overijssel: Ervaringsproblemen, Kansen & Verbeterstrategieën; Biomass Technology Group: Enschede, The Netherlands, 2013. (In Dutch) [Google Scholar]
  22. Sokka, L.; Pakarinen, S.; Melanen, M. Industrial symbiosis contributing to more sustainable energy use—An example from the forest industry in Kymenlaakso, Finland. J. Clean. Prod. 2011, 19, 285–293. [Google Scholar] [CrossRef]
  23. Chertow, M.R. Industrial symbioses: Literature and Taxonomy. Ann. Rev. Energy Environ. 2000, 25, 313–337. [Google Scholar] [CrossRef]
  24. Albino, V.; Fraccascia, L.; Savino, T. Industrial Symbiosis for a Sustainable City: Technical, Economical and Organizational Issues. Procedia Eng. 2015, 118, 950–957. [Google Scholar] [CrossRef]
  25. Bacenetti, J.; Duca, D.; Negri, M.; Fusi, A.; Fiala, M. Mitigation strategies in the agro-food sector: The anaerobic digestion of tomato purée by-products. An Italian case study. Sci. Total Environ. 2015, 526, 88–97. [Google Scholar] [CrossRef] [PubMed]
  26. Barrera, E.L.; Rosa, E.; Spanjers, H.; Romero, O.; De Meester, S.; Dewulf, J. A comparative assessment of anaerobic digestion power plants as alternative to lagoons for vinasse treatment: Life cycle assessment and exergy analysis. J. Clean. Prod. 2016, 113, 459–471. [Google Scholar] [CrossRef]
  27. Jin, Y.; Chen, T.; Chen, X.; Yu, Z. Life-cycle assessment of energy consumption and environmental impact of an integrated food waste-based biogas plant. Appl. Energy 2015, 151, 227–236. [Google Scholar] [CrossRef]
  28. Evangelisti, S.; Lettieri, P.; Borello, D.; Clift, R. Life cycle assessment of energy from waste via anaerobic digestion: A UK case study. Waste Manag. 2014, 34, 226–237. [Google Scholar] [CrossRef] [PubMed]
  29. Stinner, W.; Möller, K.; Leithold, G. Effects of biogas digestion of clover/grass-leys, cover crops and crop residues on nitrogen cycle and crop yield in organic stockless farming systems. Eur. J. Agron. 2008, 29, 125–134. [Google Scholar] [CrossRef]
  30. Holm-Nielsen, J.B.; Al Seadi, T.; Oleskowicz-Popiel, P. The future of anaerobic digestion and biogas utilization. Bioresour. Technol. 2009, 100, 5478–5484. [Google Scholar] [CrossRef] [PubMed]
  31. Pierie, F.; Benders, R.M.J.; Bekkering, J.; van Gemert, W.J.T.; Moll, H.C. Lessons from spatial and environmental assessment of energy potentials for Anaerobic Digestion production systems applied to the Netherlands. Appl. Energy 2016, 176, 233–244. [Google Scholar] [CrossRef]
  32. Dinuccio, E.; Balsari, P.; Gioelli, F.; Menardo, S. Evaluation of the biogas productivity potential of some Italian agro-industrial biomasses. Bioresour. Technol. 2010, 101, 3780–3783. [Google Scholar] [CrossRef] [PubMed]
  33. Kuznetsova, E.; Zio, E.; Farel, R. A methodological framework for Eco-Industrial Park design and optimization. J. Clean. Prod. 2016, 126, 308–324. [Google Scholar] [CrossRef]
  34. Pierie, F.; van Someren, C.E.J.; Liu, W.; Bekkering, J.; Hengeveld, E.J.; Holstein, J.; Benders, R.M.J.; Laugs, G.A.H.; van Gemert, W.; Moll, H.C. An Integrated Approach for the Validation of Energy and Environmental System Analysis Models: Used in the Validation of the Flexigas Excel BioGas Model; Hanzehogeschool Groningen: Groningen, The Netherlands, 2016. [Google Scholar]
  35. Pierie, F.; van Someren, C.E.J.; Bekkering, J.; Benders, R.M.J.; van Gemert, W.J.T.; Moll, H.C. The Development, Validation and Initial Results of an Integrated Model for Determining the Environmental Sustainability of Biogas Production Pathways. Eur. Biomass Conf. Exhib. 2016, 1411, 1411–1421. [Google Scholar]
  36. Haberl, H.; Weisz, H. The Potential use of the Materials and Energy Flow Analysis (MEFA) framework to Evaluate the Environmental Costs of Agricultural Production Systems and Possible Applications to Aquaculture 2007. In Proceedings of the FAO/WFT Expert Workshop (TRUNCATED), Vancouver, BC, Canada, 24–28 April 2006. [Google Scholar]
  37. Brealey, R.A.; Myers, S.C.; Allen, F. Principles of Corporate Finance—Global Edition with Connect Plus; McGraw-Hill Education: New York City, NY, USA, 2013. [Google Scholar]
  38. Elkington, J. Cannibals with forks—The Triple Bottom line of the 21st century Business; Capstone Publishing Ltd.: Oxford, UK, 1999. [Google Scholar]
  39. Mori, K.; Christodoulou, A. Review of sustainability indices and indicators: Towards a new City Sustainability Index (CSI). Environ. Impact Assess. Rev. 2012, 32, 94–106. [Google Scholar] [CrossRef]
  40. Rehl, T.; Lansche, J.; Müller, J. Life cycle assessment of energy generation from biogas—Attributional vs. consequential approach. Renew. Sustain. Energy Rev. 2012, 16, 3766–3775. [Google Scholar] [CrossRef]
  41. Minister van Landbouw, Natuur en Voedselkwaliteit. Uitvoeringsregeling Meststoffenwet: Positieve lijst Vergisting 2016: Artikel 1; Minister van Landbouw, Natuur en Voedselkwaliteit: Hague, The Nederlands, 2016. [Google Scholar]
  42. Rijksdienst voor Ondernemend Nederland (RVO). Biomassa SDE+ 2016; Rijksdienst voor Ondernemend Nederland: Nijkerk, The Netherlands, 2016. (In Dutch)
  43. Hall, A.S.C.; Balogh, S.; Murphy, J.R.D. What is the Minimum EROI that a Sustainable Society Must Have? Energies 2009, 2, 25–47. [Google Scholar] [CrossRef]
  44. Intergovernmental Panel on Climate Change. Climate Change 2007, Working Group I: The Physical Science Basis 2007; Intergovernmental Panel on Climate Change: Geneva, Switzerland, 2012. [Google Scholar]
  45. Goedkoop, M.; de Schryver, A.; Oele, M.; Durksz, S.; de Roest, D. Introduction to LCA with SimaPro 7, version 4.5; PRé Consultants: Amersfoort, The Netherlands, 2010. [Google Scholar]
  46. PRé Consultants, RIVM, CML, Radboud Universiteit Nijmegen. This Site Presents the ReCiPe Methodology for Life Cycle Impact Assessment (LCIA); PRé Consultants, RIVM, CML, Radboud Universiteit Nijmegen: Amersfoort, The Netherlands, 2014; Available online: https://www.pre-sustainability.com/ (accessed on 25 September 2017).
  47. Pierie, F.; Bekkering, J.; Benders, R.M.J.; van Gemert, W.J.T.; Moll, H.C. A new approach for measuring the environmental sustainability of renewable energy production systems: Focused on the modelling of green gas production pathways. Appl. Energy 2016, 162, 131–138. [Google Scholar] [CrossRef]
  48. Amon, T.; Bauer, A.; Ilic, D.; Leonhartsberger, C.; Mair, G. Biogas und Methanpotential von Zwischenfruchten; BOKU: Vienna, Austria, 2010; Available online: http://www.regeneray.com/fileadmin/user_upload/pdf/BOKU-Endbericht-Zwischenfr%C3%BCchte.pdf (accessed on 25 September 2017). (In German)
  49. Overend, R.P. The average haul distance and transportation work factors for biomass delivered to a central plant. Biomass 1982, 2, 75–79. [Google Scholar] [CrossRef]
  50. Wageningen UR Livestock Research. Kwantitatieve Informatie Veehouderij 2013–2014 ed.; Wageningen UR Livestock Research: Wageningen, The Netherlands, 2013. (In Dutch) [Google Scholar]
  51. Brinkmann, A.; Siemer, W. Biogas uit gras een Onderbenut Potentieel; Een Studie naar Kansen Voor Grasvergisting; Pianoo Expertisecentrum Aanbesteden: Hague, The Netherlands, 2014. (In Dutch) [Google Scholar]
  52. Lems, R.; Langerak, J.; Dirkse, E.H.M. “Next Generation Biogas Upgrading Using Highly Selective Gas Seperation Membranes”: Showcasing the Poundbury Project; DMT Environmental Technology: Joure, The Netherlands, 2008. [Google Scholar]
  53. Rabobank. Thema-Update: Benchmark (Co-)Vergisting Boekjaar 2010: Rendement Door Markt in Verdrukking! Available online: https://www.rabobank.nl/images/thema_update_vergisting_1_dec_2011_29302275.pdf (accessed on 25 September 2017). (In Dutch).
  54. Menardo, S.; Gioelli, F.; Balsari, P. The methane yield of digestate: Effect of organic loading rate, hydraulic retention time, and plant feeding. Bioresour. Technol. 2011, 102, 2348–2451. [Google Scholar] [CrossRef] [PubMed]
  55. Dijksma, S.A.M. Beantwoording vragen over het Gebruik Van Mineralenconcentraat als Kunstmestvervanger Binnen de EU; Wageningen University & Research: Wageningen, The Netherlands, 2015; Available online: https://www.rijksoverheid.nl/documenten/kamerstukken/2015/04/16/beantwoording-kamervragen-over-gebruik-mineralenconcentraat-als-kunstmestvervanger-binnen-de-eu (accessed on 25 September 2017). (In Dutch)
  56. Klein, B.; Van Stuijvenberg, M.; Visser, S. Potentiële Mogelijkheden tot Mestverwerking op Bedrijfsniveau; Kennis Coalitie Biobased Economy: Almere, The Netherlands, 2014; Available online: https://www.aereshogeschool.nl/-/media/Aeres-Hogeschool/Dronten/Files/Onderzoek/Publicaties-en-artikelen/Duurzame-energie-en-groene-grondstoffen/Archief/Eindrapportage-Mts--Doppenberg-03-04-2014.ashx?la=nl-NL (accessed on 25 September 2017). (In Dutch)
  57. Bureau of Statistics Netherlands. Statistics Netherlands; Bureau of Statistics Netherlands: Hague, The Nertherlands, 2015. [Google Scholar]
  58. Pre. The Atributed Life Cycle Analysis Model SimaPro 2013; Pre: Amersfoort, The Netherlands, 2013; Available online: https://www.pre-sustainability.com/ (accessed on 25 September 2017).
  59. Ecoinvent. Ecoinvent: Database of Consistent, Transparent, and up-to-Date Life Cycle Inventory (LCI) Data; Ecoinvent: Zurich, Switzerland, 2014; Available online: https://www.pre-sustainability.com/ (accessed on 25 September 2017).
  60. Atlas Copco. Atlas Copco High Pressure CNG Compressors and Refueling Solutions: Intermech BBR/FBR/VIP CNG Compressors 55–450 kW/75–600 HP; Atlas Copco: Nacka, Sweden, 2016. [Google Scholar]
  61. GEA Farm Equipment, Royal De Boer; Operationele kosten XScrew Mestscheider; Royal De Boer: Leeuwarden, The Netherlands, 2015; Available online: http://www.royaldeboer.nl/ (accessed on 25 September 2017). (In Dutch)
  62. Masse, L.; Massé, D.I.; Pellerin, Y. The use of membranes for the treatment of manure: A critical literature review. Biosyst. Eng. 2007, 98, 371–380. [Google Scholar] [CrossRef]
  63. European Central Bank. Inflation Dashboard; European Central Bank: Frankfurt, Germany, 2016. [Google Scholar]
  64. Magyar, A.; Lorubio, G. Analysis of European Power Price Increase Drivers; EURELECTRIC: Bruxelles, Belgium, 2014. [Google Scholar]
  65. Reumerman, P. Biogas Uit Natuurgras Eindrapportage; Eindrapportage: Enschede, The Netherlands, 2013; Available online: http://www.btgworld.com/en/ (accessed on 25 September 2017). (In Dutch)
  66. Kool, A.; Hilhorst, G.J.; van der Vegte, D.Z. Realisatie van Mestvergisting op De Marke; Onderzoek en Demonstratie; CLM-Rapport 608-2005; Wageningen University Research: Wageningen, The Netherlands, 2015; Available online: http://edepot.wur.nl/33208 (accessed on 25 September 2017). (In Dutch)
  67. Belastingdienst. BTW Bedragen in Nederland; Belastingdienst: Hague, The Netherlands, 2016. (In Dutch)
  68. Belastingdienst. Verrekenen van Verliezen: Verrekening Door Carry Back/VERREKENING Door Carry Forward; Belastingdienst: Hague, The Netherlands, 2016. (In Dutch)
  69. Blokhina, Y.N.; Prochnow, A.; Plöchl, M.; Luckhaus, C.; Heiermann, M. Concepts and profitability of biogas production from landscape management grass. Bioresour. Technol. 2011, 102, 2086–2092. [Google Scholar] [CrossRef] [PubMed]
  70. Smith, M.; Gonzales, J. Costs Associated with Compressed Natural Gas Vehicle Fueling Infrastructure. Factors to Consider in the Implementation of Fueling Stations and Equipment 2014; DOE/GO-102014-4471; US Department of Energy: Washington, DC, USA, 2014.
  71. Miara, M.; Gunter, D.; Kramer, T.; Oltersdorf, T.; Wapler, J. Heat Pump Efficiency: Analysis and Evaluation of Heat Pump Efficiency in Real Life Conditions; Fraunhofer Institute for Solar Energy Systems ISE, Division Thermal Systems and Buildings: Freiburg, Germany, 2010. [Google Scholar]
  72. Energie-en Milieu-Informatiesysteem Voor Het Vlaamse Gewest. Mest: Mechanische Scheiding; Energie-en Milieu-Informatiesysteem Voor Het Vlaamse Gewest: Boeretang, Belgium, 2015; Available online: https://emis.vito.be/nl (accessed on 25 September 2017). (In Dutch)
  73. Drosg, B.; Fuchs, W.; Al Seadi, T.; Madsen, M.; Linke, B. Nutrient Recovery by Biogas Digestate Processing; IEA Bioenergy: Berlin, Germany, 2015. [Google Scholar]
Figure 1. System boundaries of biogas production and utilization, included aLCA. Using the circular symbiotic AD system in the theoretical case will replace current energy and fertilizer flows used on the farm.
Figure 1. System boundaries of biogas production and utilization, included aLCA. Using the circular symbiotic AD system in the theoretical case will replace current energy and fertilizer flows used on the farm.
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Figure 2. Main green gas production pathway of the normal scenario.
Figure 2. Main green gas production pathway of the normal scenario.
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Figure 3. The scenarios and cases used in this article.
Figure 3. The scenarios and cases used in this article.
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Figure 4. (a) Efficiency of the symbiotic system; (b) GHG emission of the symbiotic system; (c) The environmental impact of the symbiotic system; (d) Efficiency Net Present Value of the symbiotic system.
Figure 4. (a) Efficiency of the symbiotic system; (b) GHG emission of the symbiotic system; (c) The environmental impact of the symbiotic system; (d) Efficiency Net Present Value of the symbiotic system.
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Figure 5. (a) Shares within total energy use REF case; (b) Shares within total GHG emission REF; (c) Shares within total environmental impact REF case; (d) Shares within total costs REF case.
Figure 5. (a) Shares within total energy use REF case; (b) Shares within total GHG emission REF; (c) Shares within total environmental impact REF case; (d) Shares within total costs REF case.
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Figure 6. (a) Energy use cooperation; (b) GHG Carbon footprint cooperation; (c) Environmental impact cooperation; (d) Yearly costs NPV cooperation.
Figure 6. (a) Energy use cooperation; (b) GHG Carbon footprint cooperation; (c) Environmental impact cooperation; (d) Yearly costs NPV cooperation.
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Figure 7. (a) Sankey diagram of energy flows for AD scenario; (b) Sankey diagram of energy flows for AD + M scenario. a All energy produced by the CHP and green fuel systems is used within the cooperation; b The leakage loss still occurring from the biogas production and CHP and green gas utilization pathway; c Losses during feedstock transport, handling, storage, and leakages of feedstocks; d Energy requirement from outside of the system (e.g., energy, materials).
Figure 7. (a) Sankey diagram of energy flows for AD scenario; (b) Sankey diagram of energy flows for AD + M scenario. a All energy produced by the CHP and green fuel systems is used within the cooperation; b The leakage loss still occurring from the biogas production and CHP and green gas utilization pathway; c Losses during feedstock transport, handling, storage, and leakages of feedstocks; d Energy requirement from outside of the system (e.g., energy, materials).
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Table 1. Feedstocks used including costs and transport retrieved from Pierie et al. [17,31].
Table 1. Feedstocks used including costs and transport retrieved from Pierie et al. [17,31].
Feedstock (Mg/a)Costs (€/Mg)Tortuosity (Factor)Transport (km)Biogas Potential (Nm3/Mg.oDM a)Methane Potential (Nm3/Mg.oDM a)
Manure farm/cooperation1820010.1 d350180
Manure source8000−10 b1.51.5350180
Chicken manure47501.53416212
Natural/roadside grasses600010 c515560297
Tops from sugar beets110001.53550302
Tops from potatoes230001.53550302
Straw from grains50001.53341174
Catch crops110001.53640329
Digestate----47 f19 f
Energy Maize (Reference)10,00035 e150606322
a Biogas and methane production per Mg of organic Dry Matter; b Price of manure from external sources derived from Kwin, 2013 [50]; c Price of retrieving grass from road embankments and natural areas [51]; d Transport by pipeline on farm; e Costs of maize feedstocks derived from Kwin, 2013 [50]; f Biogas and methane potential of the digestate retrieved from [54].
Table 2. The symbiotic scenarios.
Table 2. The symbiotic scenarios.
AffiliationDescription of Symbiotic Scenario
Scenario AScenario A, describes the symbiotic system which combines: a Combined Heat and Power unit (CHP) for internal energy production, a 2nd digester with additional manure input, green fuel production from green gas, prevention of leakages and emission, heat recovery, and organic fertilizer production which is used in the surrounding farms to replace fossil fertilizers (Appendix A). Additional insulation of the AD system is not used as the required heat is already produced internally.
Scenario A’Within this scenario one adaption is made to scenario A, namely: the produced organic fertilizers are sold on the market for lower prices and not used within the surrounding farms to replace fossil fertilizers. This only has an economic effect and, therefore, will only be indicated in the NPV results.
Scenario BWithin scenario B, regulations prevent the use of organic fertilizers for replacing fossil fertilizers in the Netherlands by decree of the European Union [55] (although the Dutch government has made some exceptions [56]). Therefore, organic fertilizer production is not included. The scenario combines: a CHP unit for internal energy production, a 2nd digester with additional manure input, green fuel production from green gas, heat recovery from the digestate, prevention of leakages and emissions, and insulation of the digester (20%) for additional heat savings (Appendix A).
Scenario CCurrently, many farm scale AD systems within the Netherlands utilize CHP instead of green gas production; therefore, scenario C describes the possibilities of a circular symbiotic AD system combined with CHP. The scenario includes: internal energy production based on CHP, a 2nd digester with additional manure input, prevention of leakages and emission, heat recovery, insulating the digester, and organic fertilizer production which is used in the surrounding farms to replace fossil fertilizers (Appendix A). Within the scenario the full utilization of the waste heat is assumed.
Table 3. Reference scenarios used for comparison.
Table 3. Reference scenarios used for comparison.
AffiliationDescription of the Symbiotic Reference Scenario
NormalThe basic AD green gas production pathway without any modifications as described in Section 3.
# CHP # Fertilizer # 2nd DigesterThe best individual improvement options per SI-Indicator are indicated as a reference scenario for comparison with the circular symbiotic scenarios. The best options are: for (P)EROI the CHP unit; for carbon footprint and Environmental impact the organic fertilizer production option; and for NPV the 2nd digester with added manure option. Full description of individual improvement scenarios can be found in Appendix A.
Ref gasThis fossil reference scenario is based on Groningen natural gas and includes: the production, needed infrastructure for transport and distribution, and combustion of the gas when used [31].
Ref maizeWithin the maize reference scenario 50% maize and 50% manure is used as feedstock for green gas production using the same AD system as explained in Section 3, (Table 1). The maize (silage) used as feedstock is specially cultivated for use in the AD system. Therefore, agricultural fieldwork and the use of fossil fertilizers and pesticides during cultivation are incorporated [17]. The maize is transported over a distance of 50 km [10]. Within this scenario, the carbon footprint and environmental impact from normal manure management is also mitigated.
Table 4. Energy and fertilizer requirements cooperation of farms.
Table 4. Energy and fertilizer requirements cooperation of farms.
UnitDairy FarmsAgricultural FarmsNatural AreasTotalSource
Average farms neededfarms5.46.9 12.3
Agricultural land sizeha270 a276 b275 c821[17,50]
Diesel useL/a35,10065,688 100,788[50]
Electricity use kWh/a253,800151,524 405,324[50]
Natural gas use Nm3/a86402898 11,538[50]
Nitrate cap dKg/a71,55046,920 118,470[50]
Phosphate cap dKg/a25,65017,940 43,590[50]
Potassium cap dKg/a60,75062,100 122,850[50]
a Based on average dairy farm with 100 cows and two cows per hectare of land [50]; b Based on production of beat tops, Potato tops, Straw, and Catch crops respectively 40, 20, 41, and 18.5 Mg/ha.a [17]; c Based on the production of roadside and natural grass of 21.8 Mg/ha.a [17]; d Cap means the maximum yearly allowed use of nutrients on a farm.
Table 5. Main cooperative farming cases.
Table 5. Main cooperative farming cases.
AffiliationDescription of the Sustainable Farming Cooperation Cases
REF (Case)The reference cooperation (REF): In this case, based on current average farming activities in the Netherlands, the cooperation will import all of their energy and most of their fossil fertilizers. The dairy farms within the cooperation will use their own manure as fertilizer on their fields, whereas agricultural farms will use fossil fertilizer for all their nutrient demands. Additionally, fuel for the machinery, electricity, and natural gas are imported to supply the energy needs of the cooperation (Table 4). The environmental impacts of fertilizer, fuel, electricity, and natural gas production are included. Inflation and increase of prices for energy and fertilizers are taken into account for the upcoming 25 years (Appendix B).
AD (Case)The AD cooperation (AD): Within this case, the cooperation will operate a circular symbiotic AD system, producing renewable energy and fertilizer from local bio-waste. Dairy farmers within the cooperation use the digestate from the AD system as fertilizer on their fields. Excess digestate is processed into organic fertilizers and used by agricultural farms in the cooperation. Additionally, the fuel for the machinery, electricity, and natural gas is supplied by the AD system (Table 4). The remaining energy or fertilizer requirements are imported. The overall cost of the AD system is based on the NPV calculation (Section 3). Within this case 23% of the total digestate output is upgraded into organic fertilizer to replace fossil fertilizer. The income from selling the remaining green gas is incorporated in the NPV; however, mitigation of carbon footprint and environmental impact by replacing green gas with natural gas is not included, as it does not lower the impacts of farming practices itself.
AD + M (Case)The AD cooperation using surplus manure (AD + M): The AD + M case is similar to the AD case except that within this case a surplus of 10,000 Mg of manure from surrounding dairy, pig, or chicken farms is available for the production of additional energy and green fertilizer. In some parts of the Netherlands there is a surplus of manure available, often linked to farms with no agricultural land (e.g., pig, chicken farms). For the additional manure feedstock mixture the properties of cow manure are assumed (Table 1). Within this scenario around 50% of the total digestate output is available for upgrading to organic fertilizer, which can be used to replace fossil fertilizer. Excess fertilizer is sold on the market for market prices (Appendix B).
Table 6. Possible amount of farming cooperations within The Netherlands.
Table 6. Possible amount of farming cooperations within The Netherlands.
Total Land (ha)Average Farm (ha)Amount of FarmFarms Per CooperationAmount of CooperationsAD CooperationsAD + M CooperationsSource
Dairy farming956,0005019,1205.43541 [57]
Agricultural farming995,7564024,8946.93608 [57]
Average 35742680894
Table 7. Possible mitigation of energy, carbon footprint, and environmental impacts per year through replacement of natural gas with green gas.
Table 7. Possible mitigation of energy, carbon footprint, and environmental impacts per year through replacement of natural gas with green gas.
SI-IndicatorADAD + MUnitSource
Energy a13.617.5TJ/a[58,59]
Carbon footprint a642826MgCO2eq/a[58,59]
Impact a7394kPt/a[58,59]
a Based on Groningen natural gas including production with 40.6 MJ/Nm3, 1.92 kgCO2eq/Nm3, and 0.22 Pt/Nm3 [58,59].
Table 8. National possible saved emission and mitigated fossil energy compared to reference years 2015 and 1990.
Table 8. National possible saved emission and mitigated fossil energy compared to reference years 2015 and 1990.
Reference Year 2015 aReference Year 1990 b
AD25% AD + M cAD25% AD + M c
Total emission savings33.4%37.5%27.1%30.4%
AD cooperative24.8%26.6%20.1%21.6%
Sold green gas8.6%10.9%7.0%8.8%
Total fossil fuel saved79.8%98.6%87.3%104.9%
AD cooperative 43.5%52.7%47.0%55.6%
Sold green gas36.3%45.9%40.3%49.3%
a Carbon footprint and energy use Dutch farming sector 2015, respectively 26.7 Tg and 133.9 PJ [57]; b Carbon footprint and energy use Dutch farming sector 1990, respectively 32.9 Tg and 142.9 PJ [57]; c MAX national scope case exists of 75% AD case and 25% AD + M case, taking into account manure surplus in the Netherlands.

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Pierie, F.; Dsouza, A.; Van Someren, C.E.J.; Benders, R.M.J.; Van Gemert, W.J.T.; Moll, H.C. Improving the Sustainability of Farming Practices through the Use of a Symbiotic Approach for Anaerobic Digestion and Digestate Processing. Resources 2017, 6, 50. https://doi.org/10.3390/resources6040050

AMA Style

Pierie F, Dsouza A, Van Someren CEJ, Benders RMJ, Van Gemert WJT, Moll HC. Improving the Sustainability of Farming Practices through the Use of a Symbiotic Approach for Anaerobic Digestion and Digestate Processing. Resources. 2017; 6(4):50. https://doi.org/10.3390/resources6040050

Chicago/Turabian Style

Pierie, Frank, Austin Dsouza, Christian E. J. Van Someren, René M. J. Benders, Wim J. Th. Van Gemert, and Henri C. Moll. 2017. "Improving the Sustainability of Farming Practices through the Use of a Symbiotic Approach for Anaerobic Digestion and Digestate Processing" Resources 6, no. 4: 50. https://doi.org/10.3390/resources6040050

APA Style

Pierie, F., Dsouza, A., Van Someren, C. E. J., Benders, R. M. J., Van Gemert, W. J. T., & Moll, H. C. (2017). Improving the Sustainability of Farming Practices through the Use of a Symbiotic Approach for Anaerobic Digestion and Digestate Processing. Resources, 6(4), 50. https://doi.org/10.3390/resources6040050

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