Open access peer-reviewed chapter

Digestate: The Coproduct of Biofuel Production in a Circular Economy, and New Results for Cassava Peeling Residue Digestate

Written By

Sammy N. Aso

Submitted: 12 September 2019 Reviewed: 23 January 2020 Published: 11 May 2020

DOI: 10.5772/intechopen.91340

From the Edited Volume

Renewable Energy - Technologies and Applications

Edited by Tolga Taner, Archana Tiwari and Taha Selim Ustun

Chapter metrics overview

1,431 Chapter Downloads

View Full Metrics

Abstract

Circular economic paradigm applies residue from one process as input material for another, fostering sustainable benefits for humanity. Anaerobic digestion (AD) is an attractive technology for biogas production in a circular economy. Digestate is the residual organic matter generated as coproduct of biogas. Because digestate is nutrient rich and largely stabilized, it has varied management options. Digestate is suitable for direct use as bio-fertilizer and is a good amendment material to improve soil physical properties. However, the quality, safety, and utility of digestate are dependent upon the characteristics of feedstock, digester process, pre- and post- digestion treatments. Digestates emanating from AD of animal manure, energy crops, food processing residues, and other feedstocks have been reported in published literature. On the other hand, there is dearth of reports on digestate emanating from AD process that utilized cassava peeling residue (CPR) as sole feedstock. This chapter presents relevant information on digestates including production, feedstock, quality and safety requirements, processing and treatment technologies, regulatory aspects, applications management options, cost implications, as well as challenges and opportunities. In addition, new results of nitrogen (N), phosphorus (P), and potassium (K) compositions of liquid fraction of CPR digestate are reported.

Keywords

  • anaerobic digestion
  • biofuel
  • biogas
  • cassava
  • cassava peeling residue
  • CPR
  • circular economy
  • digestate
  • management options
  • renewability
  • sustainability

1. Introduction

Linear economic model has been constructed on the premise of production, use, and disposal of used resources as wastes. However, there are serious limitations associated with the linear paradigm. These include nonrenewability, unsustainability, and environmental perturbations characterized by negative impacts on air, eco-diversity, soil, and water quality and safety. On the other hand, circular economic model maximizes the 3 (three)Rs of reduce, reuse, and recycle resources. In particular, circular economy applies residue from one process as input material for another process. This approach delivers sustainable benefits for humanity in terms of air, ecology, energy, environment, food, forest, housing, sanitation, soil and water quality, safety and security; as well as improvements in animal and human health, economic, social, and industrial developments.

On the predicate of biorefinery platform, biotechnological upgrading of biomass via biological, chemical, physical or some combinations of these would create bio-based energy, chemicals, and other beneficial metabolites and products within the domain of circular economic model. In this context, anaerobic digestion (AD) is an attractive technology as it would utilize organic resources in waste streams to generate biogas and digestate. However, the quality of digestate is dependent upon variables such as characteristics of feedstock, digester process, and treatment options. Digestates emanating from AD of animal manure, energy crops, agricultural residues, organic fraction of municipal solid wastes (OFMSW), and other feedstocks have been reported in published literature [1, 2, 3]. On the other hand, there is dearth of reports on nutrient properties of digestate generated from AD processes that utilized cassava peeling residue (CPR) as sole feedstock. This chapter presents relevant information on digestates in general, and new results of a technical experiment conducted to secure overview assessment of nitrogen (N), phosphorus (P) and potassium (K) compositions of liquid fraction of CPR digestate.

Advertisement

2. Anaerobic digestion (AD)

AD is a biochemical process that decomposes organic matter to generate flammable biogas and residual digestate. The process is achieved with the assistance of a suite of microorganisms in a near oxygen free environment. Biogas is basically composed of methane and carbon dioxide in the respective range of 40–75% and 25–40%. Other constituents are hydrogen, nitrogen, oxygen, hydrogen sulfide and other trace components ranging from 0.1 to 3% [4]. Successful AD operations are carried out within digester or reactor systems designed to supply nutrients required for metabolic activities of the microbes, as well as prevent conditions or elements that may become stressors or present inhibitory effects. AD digester operations and systems may be classified according to the following [5, 6, 7]:

  • Optimal temperature regimen: psychrophilic (<20°C), mesophilic (30–38°C), and thermophilic (48–57°C);

  • Total solid (TS) content: wet digestion (TS < 12%), semi-dry digestion (TS 12–20%), and dry digestion (TS ˃ 20%);

  • Feeding mode: batch, fed-batch, semi-continuous, and continuous;

  • Process stage or step: single-stage (where all AD processes—hydrolysis, fermentation, acetogenesis, and methanogenesis are executed in one reactor), and multi-stage (where the processes are separated into two or more reactors);

  • Fluid-dynamic mode: plug flow, completely stirred or mixed, and hybrid; as well as

  • Digester design: anaerobic baffled reactor (ABR), anaerobic filter (AF), anaerobic dynamic membrane reactor (AnDMBR), anaerobic mixed biofilm reactor (AMBR), completely or continuous stirred-tank reactor (CSTR), covered lagoon, expanded granular sludge bed (EGSB), fixed dome, flexible balloon or tube, floating cover or drum, sequential batch anaerobic composting (SEBAC), stirred anaerobic sequencing batch reactor (SASBR), up-flow anaerobic sludge bed (UASB) or up-flow multistage anaerobic reactor (UMAR).

Today there are millions of anaerobic digesters (domestic, medium, and large-scale versions) operating in the world and generating tremendous amount of biogas. In 2016 for instance, about 60.8 billion m3 of biogas (1.31 EJ) was generated worldwide; most of it, 84%; in Europe (54%) and Asia (30%) [8]. The technical status of AD plants varies widely. Advanced state-of-the-art systems are prevalent in Europe and more low-tech installations in Africa, Asia and South America. However, irrespective of the level of sophistication, the two fundamental products of AD are biogas and digestate.

Advertisement

3. Digestate

Digestate is the residual organic matter generated as coproduct of biogas production. Digestate is suitable for direct use as bio-fertilizer, as raw material for production of bio-fertilizers, and as amendment material to improve soil physical properties such as bulk density, hydraulic conductivity, and moisture retention capacity. Digestate is also attributed with improved sustainability and veterinary safety; reductions in odors, weed seeds, plant pathogens, food chain contamination risks and greenhouse gas emissions. The three basic types of digestate are: whole digestate, liquor (liquid fraction) digestate, and fiber (solid fraction) digestate. Whole digestate is the digestate as obtained leaving the digester at the end of AD process. It contains less than 15% dry matter. This whole digestate could be separated into liquid and solid fractions using appropriate technology and method. The liquid fraction constitutes up to 90% of the digestate by volume, contains 2–6% dry matter, particles <1.2 mm in size, and most of the soluble nitrogen and potassium, while the solid fraction retains most of the digestate phosphorus, and contains dry matter content ˃ 15% [9, 10].

However, the quality, safety, and utility of digestate are dependent upon variables such as feedstock characteristics (pH, chemical composition, carbon-nitrogen ratio (C/N), particle size), digester process (temperature, inoculum, microbial community, hydraulic retention time (HRT)), as well as pre- and post-digestion treatments. Feedstock should possess balanced nutrients, including optimal C/N to satisfy physiological needs of the microorganisms. High or low C/N would disrupt biogasification and lead to reduced biogas output due to low buffer capacity (high C/N) or ammonia inhibition (low C/N). Generally, for biogas production, C/N of 20–30 is considered optimal. For food wastes, C/N of around 15 could be appropriate. Digestates within C/N range of 15–20 are regarded as safe for application to agricultural land without further treatment [11]. When sole feedstock lacks sufficient nutrients for adequate C/N, feedstocks with complimentary nutrients profile are co-digested to offset the limitations. Table 1 highlights some feedstocks that have been used in AD operations and digestate studies.

S/NFeedstockS/NFeedstock
1Agro-industrial residues61Miscanthus sacchariflorus (Maxim.) Hack silage
2Animal manure62Miscanthus sinesis giganteus Silage
3Barley straw63Molasses
4Biodegradable plastics64Mozzarella Cheese Whey
5Biodiesel wastewaters65Municipal solid waste
6Biowastes66Municipal waste water
7Blood industry residues67Oat silage
8Buffalo farming wastewater68Olive oil mill wastewater
9Buffalo manure69Olive Pomace, olive waste
10Cacao70Orange peel waste
11Cardboard71Organic fraction of municipal solid waste
12Cattle/cow: manure/slurry72Paper
13Cattle (beef) urine73Paper sludge
14Cereal bran74Peach-juice pulp
15Cereal-WPS75Peeled Cassava wash water
16Cereals76Pharmaceutical industry sludge
17Cheese Whey77Phleum pratense L. silage
18Chicken manure78Pig urine
19Chroococcus sp. (algal biomass)79Piggery wastewater
20Coconut chips80Pig/swine effluent; manure; slurry
21Coffee grounds81Plum stones
22Corn82Potato chips production residues
23Corn cob mix83Potato waste
24Cornmeal84Potatoes
25Corn residue85Poultry litter/manure/waste
26Cover crops86Primary sludge
27Crushed cassava juice87Pumpkin waste
28Dairy manure88Rabbit manure
29Distiller’s waste89Rape residue
30Dried blood of slaughterhouse waste90Restaurant food waste
31Duck slaughterhouse sludge91Rice residues
32Edible oil92Rye
33Energetic crops93Sewage sludge
34Energy maize94Sida Hermaphrodita Rusby silage
35Fennel waste95Slaughterhouse waste
36Fish by-product96Sludge from Slaughterhouse wastewater treatment plant
37Food industry residues97Solid farmyard manure
38Food waste98Sorghum silage
39Fruits and distillery by-products99Source-separated organic household waste
40Fruit Marc100Source-separated municipal solid waste
41Garden wastes101Starch processing wastewater
42Glycerin102Straws (cereal, pea)
43Grape seeds103Sugar beet pulp
44Grass (clover, Sudan); grass silage104Sugar sorghum (S. saccharatum L. Moench.) silage
45Green waste105Sunflower residue, sunflower silage
46Hemp106Tea leaves
47Household kitchen waste107Tetraselmis sp. (algal biomass)
48Household waste108Thin stillage (bioethanol by-product)
49Human excreta109Triticale
50Human urine110Triticale silage
51Industrial and commercial wastes111Turkey manure
52Jute Caddis112Vegetable waste
53Kitchen waste113Vinasse
54Landscape waste114Waste-activated sludge
55Ley silage115Waste potato starch
56Livestock waste116Wastewater
57Maize stover117Wastewater sludge
58Medicago sativa L. silage118Wheat
59Milk (serum, whey)119Yeast production wastewater
60Millet120Zea mays L. (corn, maize) silage

Table 1.

Feedstocks used in digestate production and studies.

Source: Assembled from scientific literatures in the public domain, most of them cited in this present work.

Advertisement

4. Regulations, quality, and safety requirements

Perhaps the most important variable affecting the quality and safety of digestate is feedstock. Starting with a high-quality feedstock would virtually guarantee a safe and quality digestate. Source separation can be used to achieve high purity feedstock. The biological, chemical, and physical properties of digestate may be governed by regulations and quality assurance systems. The European Union (EU) and many European national governments have hygienic, quality and safety standards for digestate certification that consider feedstock source and other aspects such as digester process, treatment options, handling and storage requirements. The essential quality and safety requirements for digestate destined as biofertilizer must be achieved regardless of the initial raw material. Essential quality and safety parameters include nutrients content, dry matter and organic dry matter contents, homogeneity, pH, purity (free of inorganic impurities such as glass, metal, plastic, and stones), sanitized and safe for soil organisms and the environment with regards to biological status (pathogenic organisms) and chemical status (organic and inorganic contaminants/pollutants). Furthermore, the digestate should be free of odor, phytotoxicity and weed seeds; and be satisfactorily stabilized.

Quality assurance systems for digestate certification may comprise monitoring to ensure control; standardization to ensure repeatable performance; characterization label to identify product fitness; declaration to describe product constituents; application guidelines to ensure safe and proper use; and documentation to prove that the product received required treatments following approved protocols. Table 2 presents established criteria and characteristics for the production and use of quality and safe digestates. In the EU, conformity with these criteria is enough to ensure that digestate complies with European “End of Waste” criteria; and can be used without further waste management controls.

CriteriaProcess/parameterRequirements
HygienePasteurization at 70°C1 h
Sterilization at 133°C20 min
Weed seeds and sprouting plant parts≤2/L
OdorFree of annoying odors
PathogensE. coli≤1000 CFU/g fresh matter
Salmonella spp.Absent in 25 g fresh matter
Heavy metalsCadmium (Cd)0.8–20 mg/kg DM
Chromium (Cr)75–1000 mg/kg DM
Copper (Cu)75–1000 mg/kg DM
Lead (Pb)80–900 mg/kg DM
Mercury (Hg)0.6–16 mg/kg DM
Nickel (Ni)30–300 mg/kg DM
Zinc (Zn)300–4000 mg/kg DM
Organic pollutantsPolycyclic aromatic hydrocarbons3–6 mg/kg DM
Dioxins and furans20 ng TE/kg
Chlorinated pesticides0.5 mg/kg Product
Polychlorinated biphenyls0.2 mg/kg DM
Absorbable organic halogens500 mg/kg DM
Linear alkylbenzene sulphonates1300 mg/kg DM
Nonylphenol and nonylphenolethoxylates10 mg/kg DM
DEPH: Di (2-ethylhexyl) phthalate50 mg/kg DM
Inorganic pollutantsNon-stone impurities >2 mm (glass, metal, plastic, etc.)0.5% m/m dry matter
Stones > 5 mm8% m/m dry matter
StabilityVolatile fatty acids0.43 g COD/g VS
Residual biogas potential0.25 l/g VS
Respiration rate16 mg CO2 g VS−1 day−1
DeclarationsName of producer, type of product (whole, liquid, solid), mass of product, total nitrogen, ammonium nitrogen, total phosphorus, total potassium, soluble chloride, soluble sodium, dry matter, volatile solids, pH, bulk density, etc.Relevant units where applicable (e.g., kg; kg/m3; mg/(kg DM); mg/L; %;)
Additives and chemicalsLime, iron chloride, iron oxide, bentonite, diatomaceous earth
Feedstock sourcesAgriculture (e.g., manure, harvesting by-products, silage, energy crops); animal by-products (e.g., manure, stomach intestine, raw milk); food industry (residues from food industry that contain food grade additives); food related shops (e.g., potatoes, dairy waste, bread, meat remnants, flowers, plants); forrest (e.g., bark, wood chips, sludge from the cellulosic industry); parks, gardens (e.g., leaves, grass); greenhouses (e.g., tops, peat products); households, kitchens, restaurants (e.g., fruit and vegetables residues, food, coffee and tea remainders, egg shells); etc.

Table 2.

Quality and safety validation criteria for digestates.

Source: [9, 12, 13, 14, 15, 16].

Advertisement

5. Treatment technology options

In the context of AD and digestate, we may distinguish between pre- and post-treatment processes. A pretreatment process refers to a processing operation applied upstream, before the digestate emerges from the digester. This could range from size reduction or thermochemical treatment of feedstock substrate; to process management (such as pH, temperature, and retention time control). On the other hand, a posttreatment process is that processing operation applied downstream of digestate harvest. This may also involve size reduction, other unit operations; composting, and end-product requirements that ensure the digestate sanitation. Post treatment may generate nutrient concentrates, liquid and solid fraction digestates conditioned to standardized biofertilizers, and final liquid effluent that could be discharged into a stream or sewage system. Benefits of posttreatment include enhanced marketability, reductions in handling, storage and transportation costs/requirements, and compliance with environmental regulations.

Depending on the starting feedstock and desired end product form of the digestate, similar technologies could be used for pre and post treatment processing. Applied technologies and methods may be classified as biological, chemical, or physical. The methods could also be used in combination. Biological treatment could be accomplished with the use of microorganisms and catalysts; chemical treatment with acids, alkalis and oxidants; and physical treatment by mechanical and thermal means. Physicochemical treatment combines physical and chemical techniques. Ammonia fiber explosion (AFEX), and supercritical CO2 explosion are examples. The major classifications of treatment options and associated technologies are presented in Table 3.

Category/methodTechnology optionExample means/aids
BiologicalBacteriaClostridium sp. strains LDC-8-c12, 5-8, CO6-72; Rhodobacter sphaeroides KD131; Thermosaccharolyticum strain M18
CompostingGreen waste, vine shoot pruning, wood chips
EnzymeCarbohydrase, laccase, lignin peroxidase
FungiCeriporia lacerata, Ceriporiopsis subvermispora (ATCC 96608), Pleurotus ostreatus
ChemicalAcids, organosolvsInorganic acids (hydrochloric, nitric, phosphoric, sulfuric); organic acids (fumaric, maleic). May be used in percolation, plug flow, shrinking-bed, batch, and countercurrent modes
AlkalisAmmonia, lime
Ammonia recoveryIon exchange; scrubbing, stripping, precipitation (struvite)
Ionic liquids1-Butyl-3-methylimidazolium hydrogen sulfate [bmim]HSO4], 1-ethyl-3-methylimidazolium acetate (EMIM-OAc), 1-ethyl-3-methylimidazolium diethyl phosphate, 3-allyl-1-methyl-1H-imidazol3-ium chloride [Amim][Cl]
OxidantsHydrogen peroxide, ozone
PhysicalMechanical
Dewatering:Centrifuges, gravity tables, presses (belt, filter, rotary, screw)
Disintegration/maceration (chipping, grinding, milling, shredding):Ball mill, colloid mill, hammer mill, two-roll mill
Extrusion:Band, single screw, twin screw
Homogenization:High pressure homogenizers
Lysis:Lysis-centrifuges
Membrane separation:Electrodialysis, microfiltration, nanofiltration, pervaporation, reverse osmosis, ultrafiltration
Sonication:Ultrasound/sonoreactors (bath, flat plate, probe, tube)
IrradiationElectron beam, gamma ray
ThermalDrying/torrefaction, electric heating, evaporation, hot oil, hot water, hydrothermal, microwave, steam
PhysicochemicalExpansion/explosionAmmonia fiber expansion/explosion (AFEX), steam explosion, supercritical carbon dioxide (SC-CO2) explosion

Table 3.

Major categories of treatment and technology options for AD and digestate processing.

Source: [10, 15, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34, 35, 36].

Advertisement

6. Applications management options for digestate

In the service of circular economy, there are many applications management options for digestate. These may include algae cultivation, energy production, bio-adsorbent production, building materials production, nutrients recovery/production, soil creation and other value-added commodities. Perhaps the two most widely recognized utilities of digestate are as land application for soil amendment and as biofertilizer.

6.1 Biofertilizer and soil amendment

Technological aids used in modern agriculture such as inorganic fertilizers and antibiotics have negative impacts on soil, water, and air quality and safety, and therefore pose health risks to humans and the ecosystem. Inorganic fertilizers for instance have caused environmental and soil quality degradation, eutrophication and heavy metals pollution. Similarly, field-spreading agricultural land with raw/untreated manures derived from medicated livestock contributes to dissemination of veterinary antibiotic residues and antibiotic-resistant pathogens. Lincomycin, monensin, and sulfamethazine antibiotics were reported to affect soil microbial community composition and respiration, denitrification and nitrogen transformations [37]. Applications of digestate for biofertilizer and soil amendment purposes could ameliorate some of these adverse effects.

Amendment propensity relates to capability to maintain soil fertility and humus balance. Dairy slurry digestate was found richer in humic substances than raw dairy slurry [38]. Researchers concluded that digestate enhanced soil biological stability, microbial biomass and enzymatic activities [39].

On the other hand, fertilizer properties relate to provision of nutrients necessary for good crop performance. Leaves of alfalfa plant fertilized with digestate had higher contents of N, P, and K in comparison to alfalfa fertilized with mineral fertilizers [40]. Digestate also produced higher yields of dent corn than the application of chemical fertilizers [38]; higher yield of potato (Solanum tuberosum) over the application of compost [41]; and 30% increase in yield over farm yard manure [42].

6.2 Nutrients recovery

Digestate is applied in recovery of nutrients, production of fertilizers and volatile fatty acids (VFAs). Livestock manure contains about 49 g N/kg TS and 6 g P/kg TS; energy crops, 17 g N/kg TS and 2.5 g P/kg TS; and agro-wastes, 27 g N/kg TS and 3 g P/kg TS [43]. Much of these nutrients remain in digestate after AD operation. For example, total N, P, and K values for digestates obtained from wet AD of agricultural wastes were reported respectively in the ranges 44–120, 8–42, and 28–95 g/kg DM [44]. These nutrients could be recovered/harvested with the technologies outlined in Table 3.

VFAs are important input organic acids used extensively in the bioenergy, food, chemical, cosmetic, pharmaceutical, textile, and other industries. Acetic acid (E 260), propionic acid (E 280) and butyric acid are examples; and are GRAS (generally regarded as safe) rated by the FDA. Acetic acid is used to defend against Campylobacter, Escherichia coli, Listeria, Salmonella, and other pathogens in beef, chicken, pork, turkey, carcasses, skin and hides [45]. Butyric acid is used in the textile industry to enhance heat and sunlight resistance of fibers. In the food industry, it is used as additive for flavor formulation and modification [46]. Similarly, propionic acid (E 280) is used as antibacterial and antifungal agent to decontaminate packaging films and coatings, and to protect meat and meat products such as sausages, bologna and ham. VFAs have been harvested from digestates generated from short-term dry AD of swine manure, generated from AD of food waste, and used in recovery of biological nitrogen and phosphorus from sewage sludge [47, 48, 49].

6.3 Energy production

Digestate can be deployed for energy generation. Recirculating digestate into the digester maximizes biogas production, at the same time minimizing methane emissions during digestate storage, transport, and use. Digestate was pyrolyzed (via the use of Pyroformer, quartz rotary kiln reactor, and thermo-catalytic reforming reactor) to produce biofuels: pyrolysis oil (biooil) and pyrolysis gas (syngas). The biooil generated by thermo-catalytic reforming process at 750°C had a higher heating value of 33.9 MJ/kg, and a total acid number of 4.9 mgKOH/g [50].

Algae have widespread applications and potentials in: biofuels, cosmetics, biofertilizer, infant formulas, nutritional supplements, livestock feeds, chemical and allied industries, and biodegradable packaging. Perhaps more importantly, digestate could be used for the cultivation and production of microalgae. In the context of biorefinery platform and circular economy, various compounds produced by microalgae and their applications have been reported [51, 52].

6.4 Other applications

Digestates have other utilities and management options. These include applications in aquaculture, gardening and horticulture, and the production of building materials and biochar.

6.4.1 Biochar

Biochar (charcoal) is the byproduct of thermal pyrolysis of carbonaceous biomass; and has carbon sink properties. Dairy waste and whole sugar beet digestate biochar were effective in eliminating heavy metals (Pb2+, Cu2+, Ni2+, and Cd2+) from aqueous solutions [53].

6.4.2 Gardening and horticulture

Due to its organic origin and physicochemical characteristics, digestate is useful in gardening and horticulture. It could be applied in soil creation or remediation, and has found applications in green houses, plant nurseries, and home gardening [54].

6.4.3 Building materials

A 50% substitution of wood with cattle manure digestate produced particleboard panels that met ANSI performance requirements [55]. USDA reported that medium-density fiberboard and wood/plastic composite engineered materials could be created using digestate solids without compromising mechanical or aesthetic values [56].

6.4.4 Aquaculture

Digestate is better than raw manure in fertilizing fish ponds. Firstly, digestate is hygienic because most of the bacteria, parasites and their eggs are destroyed in the AD process. Thus, pond sanitation is improved; minimizing fish diseases and the cost of veterinary services. Secondly, the digestate is largely stabilized and therefore does not consume and compete with fish for dissolved oxygen. Tilapia, Silver carp, Bighead carp, Silver barb and Mrigal fish species raised in pond fertilized with digestate matured faster and achieved higher net weight gain than counterparts raised in pond fertilized with chemical fertilizer or raw manure. By comparison, while chemical fertilizer increased net yield over raw manure by 27%, digestate increased net yield by 55% [57].

6.4.5 Bio-adsorbents and bedding

Digestates have been applied as bio-adsorbents to scavenge heavy metals from contaminated soils and water [58], and as chicken litter [54], and other livestock bedding [56, 59].

Advertisement

7. Cost implications

The big picture cost elements relevant to AD systems include land acquisition, site preparation/development, plant and machinery (including digester/reactor, pre and post treatment technologies), personnel, feedstock, environmental impact, other operating costs (electricity, logistics, regulations), and revenue from products (biogas and digestate). In the case of digestate, feedstock, treatment processes, and the logistics of storage, transport, handling and field application bear crucial concerns. Cost-effective digestate production process is presaged by efficient feedstock collection and sorting operations. A cost benefit analysis of municipal solid waste management system in Yangon, Myanmar, identified weak organizational structure and ineffective collection methods in the existing system that operated with just 32% waste collection efficiency. An alternative system with increased waste collection efficiency was then proposed. The new system required labor and vehicular productivity; using vehicles with container-hoist handling mechanism. The new system reduced operating and other costs associated with the old system by up to 42% [60]. It is noteworthy that consumer and public environmental behavior and cooperation on waste management could be modified by pecuniary and nonpecuniary information. In Surabaya city, Indonesia, researchers found that in the reference case in which the no information treatment was applied, mean WTP (willingness to pay) for marginal improvements in a waste collection and disposal program was estimated to be US$ 14.65. The researchers reported that pecuniary information increased WTP by 20.5%, whereas non-pecuniary information had a negative but statistically insignificant effect on WTP [61].

A situation where 50% of whole unprocessed digestate was applied on agricultural land near the generating biogas plant and the other 50% transported to a location 20 km away was studied. Cost for digestate utilization near the biogas plant was € 3.34 (US$ 3.73)/t, and that at a location 20 km away was € 5.47 (US$ 6.10)/t [62]. This study highlights the impact that location or site of digestate utilization could have on cost. Such distance related cost also applies to feedstock substrate. Generally, the farther the distance, the higher the cost.

Researchers performed specific cost analysis for six scenarios that involved direct land application of digestate as reference, and various treatment technology options that included screw press and decanter centrifuge separation, belt drying, evaporation concentration, purification by ultrafiltration and reverse osmosis, and nutrients recovery by ammonia stripping and precipitation. Result indicated that net specific costs ranged from € 1.94 (US$ 2.16)/m3 of digestate for the reference scenario, to € 5.45 (US$ 6.08)/m3 for stripping, to € 6.80 (US$ 7.58)/m3 for belt dryer [62]. Similarly, the costs of AD were found to vary up to € 109 (US$ 122)/t of digestate from € 35 (US$ 39)/t for basic storage of digestate for aerobic conditioning, to € 70 (US$ 78)/t for digestate ready for direct land application, to € 79 (US$ 88)/t for on farm co-digestion [63].

Case studies were conducted for separation systems in three regions (Aachen, Borken, and Siegen) of Germany. The researchers determined that investment and variable costs were respectively € 23,000 (US$ 25,536) and € 0.47 (US$ 0.52)/m3 for screw press; € 27,000 (US$ 29,977) and € 0.48 (US$ 0.53)/m3 for screening drum press; and € 163,000 (US$ 180,970) and € 1.46 (US$ 1.62)/m3 for decanter centrifuge. Further analysis revealed the unit cost of digestate disposal for screening drum press varied from € 4.1 (US$ 4.6)/m3 in Aachen to € 4.8 (US$ 5.3)/m3 in Borken, and Siegen [64].

The following were reported about AD in the UK. Least cost post treatment technology for digestate derived from a 10% solids content food waste was biological oxidation at £13.18 (US$ 16.97)/t of feedstock. At 20% solids content, least cost option was direct application of whole digestate to agricultural land at £8.76 (US$ 11.28)/t. The cost of treating 4000 t of slurry with a mechanical screen separator was £0.44 (US$ 0.57)/t per year, and treatment with decanting centrifuge cost £2.21 (US$ 2.85)/t per year. Furthermore, about £3.5M (US$ 4.5 M) would be required to construct a 1 (one) MWe AD plant utilizing farm wastes as feedstock [65, 66, 67].

In the continent of Africa, cost of establishing a 4 m3 anaerobic digester was found to range from US$ 555 in Uganda to US$ 698 in Cameroun to US$ 979 in Rwanda [68]; while that of founding a family size floating drum plant was estimated at US$ 1667 [69].

Techno-economic analyses were performed for post treatment technologies used to recover nutrients from the digestates of five full scale farm AD systems. Results showed membrane technology had specific cost of € 6.97 (US$ 7.72)/m3 of treated digestate. Drying was estimated at € 5.81 (US$ 6.44)/m3, while stripping operated at € 5.44 (US$ 6.03)/m3 [70]. In addition, the process economics of membrane-based nutrients extraction and fractionation from dairy manure digestate indicated cost of solid-liquid separation unit to be US$ 11,000; the microfiltration extraction unit cost US$ 30,000; the nanofiltration fractionation unit was priced at US$ 60,000; and the daily cost of operation (chemicals, energy and water) was approximately US$ 24 [71].

Finally, digestates are used as quilt for cattle bedding and poultry litter due to significant cost offsets to livestock farms. The cost of solid digestate as animal bedding (US$ 55 per dry ton) is cheaper than the cost of alternative wood-based replacement materials such as wood chips at US$ 65 per dry ton or sawdust and shavings at US$ 124 to US$ 248 per tonne [55, 59].

Advertisement

8. Challenges and opportunities

Digestates have good fertilizer qualities: nutrients, safety and other properties required for soil amendment and plants production. However, relative to mineral fertilizers, digestates are not well known in many countries. Therefore, their potential as mineral fertilizer alternative/substitute is limited. Perhaps, standardized quality assurance and control protocols, regulations, certifications, legal and other institutional management systems organized internationally could help demonstrate digestates’ benefits, quality and safety, and thereby engender confidence in their utilization as sustainable fertilizer and soil amendment products. Reconciling and bringing such issues and their benefits to existence present challenges and opportunities. Presented in Table 4 are some of these challenges and opportunities of the waste, AD and digestate system.

IssuesChallenges and opportunities
8.1. Concept of wasteChallenge: the conventional or customary status of looking at waste as a problem presents significant challenge.
Opportunity: seeing waste as potential resource would help change perception and attitude, possibly stimulating salient management options. Opportunities may emerge in the areas of prevention, recovery, collection, sorting, reducing, reusing, and recycling. For developing countries these have implications for environmental hygiene and sanitation.
8.2. BiowasteChallenge: because biodegradable waste could be a source of heavy metals and polluting organic compounds, it presents challenges to life generally, and to the environment.
Opportunity: these challenges create opportunities to develop management options (e.g., biological treatments) to protect life, environment, and to benefit agriculture and ecosystem. Biowaste is reported to have potential to tackle climate change in the areas of nitrous oxide (NO2) emissions mitigation, and sequestration capacity of agricultural soils [72].
8.3. E-wasteChallenge: problems and dangers of e-waste, heavy industry products and components; including electrical and electronic equipment, waste batteries, engine blocks, paint, etc.
Opportunity: guidance/support for the informal (non or loosely regulated) establishments, to call attention to dangers and health risks that may be associated with used or discarded electronic devices/items (acids, other chemicals, radioactive materials, etc.).
8.4. Mineral wasteChallenge: mining of solid minerals do present health and environmental challenges.
Opportunity: chances to implement safeguards for hazardous minerals and to divert safe wastes to beneficial applications. Examples are uses as substitute for backfill material in open pit mining, landfill, or as grit in construction materials. Production of concrete and brick for structural work (bridges, dams, launch pads, highways) are possibilities.
8.5. Source of feedstockChallenge: the source of digestate feedstock and its treatment could present barriers. PAS 110 in the UK does not approve certification for digestate generated from mechanically biologically treated waste. Such digestates require proof of biodegradability test to be considered suitable for recycling; like land spreading. There is also the issue of digestate originating from co-digestion of industrial waste and household waste. In the Netherlands, the desire in AD electricity regime to maximize biogas production by mixing manure with other organic material conflicts with AD biofertilizer rules for spreading digestate from co-digested manure on farm land.
Opportunity: some of these challenges are consumer-induced barriers and lack quantitative elements. Opportunities might lie in the sociocultural realm, such as modifying social and cultural attitudes and behaviors towards waste and its inherent heterogeneity.
8.6. Unrecovered organic matterChallenge: AD is more adapted to easily putrescible carbohydrates (starch, sugar). Recalcitrant lignocellulosic components (lignin, etc.) remain undigested. Efficiency of organic matter conversion was quite low as ˃97% of lignin in maize stover was found undigested [73]. AD could thus lead to unrecovered organic matter still present in digestate
Opportunity: prospects for advanced and innovative pretreatment technologies to fractionate, recover, purify and convert lignin or other recalcitrant organics to more digestible biopolymers. Alkaline treatment, gamma irradiation, membrane technologies, organosolv, steam explosion, wet oxidation, etc. may come to the rescue (Table 3).
8.7. Informal and low statusChallenge: AD and digestate are perceived to be in domain of informal waste management system and service; and therefore, relegated as only appropriate for the rural populace.
Opportunity: integration of formal and informal systems. Training to abate misconceptions, lack of awareness, and raise public profile of digestate. These may purge image of biogas and digestate as products that are derived from wastes, and hence belong to poor/rural settings.
8.8. Legal barriersChallenge: lack of binding global (and for developing countries, own country) coherent rules, laws, directives, regulations and policy frameworks.
Opportunity: the formulation of these guidelines and laws on waste governance system. Implementing appropriate technologies and business models for waste management.
8.9. Data and waste reporting systemChallenge: lack of reliable data on waste management systems, design features, standard operating procedures (SOPs), etc. could limit exchange of ideas and retard progress.
Opportunity: waste management value chain information is vital. Quantity, type, economic sector, source, and composition data could guide prioritization of strategies and enable trends forecast that deliver better outcomes. Global exchange of briefs would catalyze spread of best practices.
8.10. StandardizationChallenge: although digestate products have similar characteristics as commercial chemical fertilizers, they are not classified in any way, are poorly developed in most countries, and there is no overall guidance [20, 62, 70]. These barriers restrict utilization and trade.
Opportunity: these challenges create opportunities to establish frameworks that enable digestate utilization through standardization, fair comparison, commerce development, and international trade.
8.11. MarketingChallenge: regional nutrient availability, agricultural structure, season, feedstock and degree of upgrading have been reported to challenge and impact digestate prices and marketing [54].
Opportunity: upgraded products offer increased marketability due to their denser nutrients. Marketing to nutrient deficient regions, non-agricultural sectors and purposes represent prospects. Manufacturers of organic soils, particle- and fiber- boards, landscapers, and private customers all represent credible market outlets.
8.12. Cost barrierChallenge: initial investment fund is a major issue. Cost of establishing a 4 m3 AD digester in the continent of Africa ranges from US$ 555 to US$ 979 [68]; and the price for a family size floating drum reactor was reported at US$ 1667 [69]. In Sri Lanka, a family unit digester generating 6–10 m3 of biogas per day cost Rs. 17,000 (US$ 5459); and described as difficult proposition for low-income families [74]. In the UK, a 1 MWe AD plant utilizing farm wastes as feedstock cost about £3.5M (US$ 4.5 M) to construct [67]. Also, costs associated with animal breeding and maintenance (veterinary care, feed, water, etc.) escalate operating costs, and constrain availability of manure for feedstock.
Opportunity: easing cost barriers would require support with appropriate and necessary interventions (policies, credit facilities, subsidy schemes, preventive maintenance that promote solutions, prolong facilities productive lifespan, and minimize operating costs). Furthermore, transparency on proposals and bidding for new plants and projects could build confidence in the process.
8.13. Urban and rural dichotomyChallenge: differences between metropolitan, urban, sub-urban, and rural areas can compromise AD projects. Segregation by infrastructure and income for example could affect waste collection and limit access to feedstock.
Opportunity: prospects for rural development with public utilities, services, and infrastructure (roads, power, water, etc.) These would facilitate logistics for waste collection, AD processes, and digestate handling/evacuation.
8.14. Contamination of agricultural landChallenge: most of the digestate produced in AD is used for soil amendment and as biofertilizer. There are risks of spreading animal pathogens, heavy metals, and other pollutants on soils due to the presence of these hazards in animal by-products used in AD. Sulfadiazine and oxytetracycline are antibiotics found in manure of medicated animals that affect soil quality. Twenty five percent of 70 digestate and compost samples assessed in Switzerland contained polycyclic aromatic hydrocarbons (PAHs) concentrations beyond the regulated threshold value of 4000 μg/kgdw [75].
Opportunity: digestate is a sustainable fertilizer and soil improver; thus, necessary to assure its safety. The potential to contaminate soils with pollutants from digestate application beacons vigilance and chances to develop technical and monitoring strategies that sequester and purge the digestates of polluting hazards before their use.
8.15. Air pollutionChallenge: digestate has potential to emit substances and gasses that contaminate the air and influence global warming [11]. Challenges also exist due to lack of practical tools to monitor primary air pollutants [76].
Opportunity: advanced methods of digestate management and reutilization to minimize emissions of air pollutants (ammonia: NH3, nitrous oxide: NO2) and greenhouse gases (methane: CH4, nitrogen dioxide: N2O). Strategies may include processing (composting, curing, dewatering); alternative applications (in construction, aquaculture, regeneration activities); and storage. Development of software tools that enable quantitative monitoring of emissions from digestate soil applications on a routine basis is another prospect area.
8.16. Bad odorsChallenge: compared to raw manure slurry, digestate has fewer bad odors. However, this may not be true when compared to chemical fertilizer. There have been complaints of nuisance odors associated with land-spreading of digestate [77], and at landfills and composting plants [78].
Opportunity: this problem could be due to spreading practice and/or the spreading of unstable digestates. Application of good timing and spreading techniques (trailing-shoes, injection), and use of stabilized digestates (sufficient HRT, aerobic composting) would minimize odor issues.
8.17. Bad legaciesChallenge: there are challenges associated with bad reputation of AD systems and biogas plants around the world. A study in 2006 found that 60% of 600–700 domestic biogas plants in Ethiopia was not functioning [79]. During the 7 years period from 2009, more than 3600 biogas plants were installed in the Tigray region of Ethiopia; and a 2017 study reported that 58.1% of the installations was not operational [80]. The 21 biogas plants installed by Pakistan council for appropriate technology (PCAT) in the 1970s were reported to have failed to perform [81]. In 1986, a survey of the status of 25 biogas plants in Kenya found 36% to be alive, functional and maintained. Another 36% was described as dead, not functional, and not maintained. Unfinished projects accounted for 8%; while remaining plants were reported in disrepair, with varied patterns of being alive, dead, not functional, and not maintained [82]. The regional bioenergy program of the Latin American energy organization (OLADE), catalogs biogas technology projects in Latin American countries. Experience began in 1953 and by 1986 at least 22 countries including Bolivia, Colombia, Costa Rica, Dominican Republic, Ecuador, Grenada, Guatemala, Guyana, Haiti, Honduras, Nicaragua, Jamaica, and Peru had projects at varying levels of implementation. Out of the 3950 biodigesters inventoried, 60% was found operable and 40% was either shut down or functioning irregularly or completely abandoned [83]. Though China rebounded and emerged as a major reference on household digesters, about 50% of biogas tanks installed from 1958 into the 1970s were abandoned in the 1980s. By 1988 the seven million rural digesters existing in 1980 dropped to 4.7 million [84]. In 1986, a survey of biogas plants in Sri Lanka indicated that 61% was functional. By 1996 only 28.5% of completely surveyed 365 biogas systems was reported functional. At this point 16 units had been abandoned and the success rate for biogas systems implementation was reported as 32.9% [74]. In the Netherlands, for a period of over 30 years beginning in the 1970s, many AD projects using biomass were considerably delayed, suspended, abandoned and out rightly never realized. [85, 86]. These failures and circumstances taken together portrayed negative images and bad legacies for biogas plants.
Opportunity: reasons adduced for failures included economic, social, technical, and policy components such as high investment and maintenance costs, urbanization and socio-cultural constraints, poor dissemination strategy, complicated permit regulations, shortage of feedstocks, lack of or inadequate training, poor digester design, etc. These reasons provide opportunities to create circumstances, provisions and tools that would promote and sustain biogas systems. Some examples are mobilization of local and external funds, more business-friendly policies and rules, appropriate and sustainable technologies, technical training, warranties for plant performance. Also, public dissemination of information and follow-up on successful programs could help.
8.18. Low diffusion rateChallenge: in Latin America, the number of rural biogas plants installed yearly from mid-1985 to 1992 was less than 15% of that installed from 1982 to mid-1985. Challenges included technology adoption, technical manpower and materials of construction. However, non-technical reasons for biogas adoption failures accounted for up to 69%, 50% and 25%, respectively, in Cote d’Ivoire (Ivory Coast), Costa Rica and Tanzania [84]. Unstable institutional environment, lack of network and lobby activities, lack of initiatives between academia, research institutes, private sector entrepreneurs and stakeholders were cited nontechnical reasons. For the Netherlands, apart from technological problems; limited economic feasibility, fragmented support from the government, decreases in energy prices, and lack of financial support which made return on investment uncertain contributed to inadequate AD diffusion.
Opportunity: cooperation between academia, government, industry and other stakeholders (farmers, energy sector, municipalities). Cooperative efforts that landed mutually beneficial outcomes should be highlighted, applauded and replicated. Well planned long-term, clear and supportive arrangements would facilitate continuity. Government policy that guide search for solutions, market formation and resources mobilization. Ease of technology adoption would also require reliable and sustainable infrastructure (technical assistance, manpower, cohesive farming approach with biogas and digestate, integration and dissemination of societal and cultural values and norms).
8.19. Inhibition of microalgaeChallenge: it has been shown that the green alga (Raphidocelis subcapitata) is sensitive to digestate, with ecotoxicity index; EC50 of 0.77% [87]. Similarly, Scenedesmus bijuga; and oil-rich Chlorella sp., including C. minutissima and C. sorokiniana were found sensitive to digestate. Also, the dark color of liquid digestate of algal biomass inhibited the growth of Chroococcus sp. Therefore, cultivation of algae for value added products recovery could be minimized in the presence of digestate.
Opportunity: because algae are exploited for biofuels, and various other useful biotechnological metabolites production by valorization of digestate, the inhibitory effect of digestate on algae cultivation is of practical interest. Therefore, digestate pretreatment or at least its dilution before use [88], would aid good algal productivity.
8.20. Nomadic and free-range cultureChallenge: many developing nations have nomadic animal husbandry architecture and free-range culture. These make the gathering of animal manure as feedstock for digesters a major challenge. In Pakistan, for example, livestock farmers from time to time relocate to weather conditions more benign to their livestock. However, current digester designs used by rural populations such as the fixed dome and floating drum are sedentary and cannot be readily moved by the farmers with their livestock.
Opportunity: perhaps this challenge creates opportunity for a mobile biogas system such as the portable biogas plant reported in the year 2016 [81].
8.21. Disparity between developed and developing countriesChallenge: the economic, political and technological mismatches and divides between industrialized and industrially developing countries are challenging local, regional and international waste management systems. Environmental and health dangers do not know or respect boundaries (local, regional, or international) by land, sea, air or space. Planet earth is perhaps at the cusp of the axiomatic global village and economy. Sooner than later, pollution and instability at one corner of the earth would reverberate and affect other parts (Plastics in the oceans? Heavy metals in food, aquatic and terrestrial biota? Ebola in America? Flood events in Zimbabwe, Mozambique, Puerto Rico and U.S. Virgin Islands? Wildfires in Australia, Brazil, Portugal and USA? Coronavirus (COVID–19) in Japan, Singapore, and USA?).
Opportunity: cooperation and support are needed to enable developing nations to leapfrog and shorten the learning curve and development timescales. Developing nations need guidance and assistance to cope with technological demands and challenges, and eschew reinventing the wheel. Waste management offers an opportunity for cooperation among nations for the betterment of humanity and planet earth.

Table 4.

Challenges and opportunities of the waste, AD and digestate system.

Advertisement

9. Cassava peeling residue (CPR) digestate

N, P, and K are critical macro nutrients for crops production. N is considered the limiting nutrient in growth and yield [89]. P is required for energy transfer, signal transduction, photosynthesis, and macromolecular respiration [90]. K is responsible for metabolism of cell division, enzymatic reactions of amide formation, and amino acid activation during proteins biosynthesis and substrate phosphorylation [91]. To be a credible mineral fertilizer substitute, digestate must have the capacity to deliver the necessities and requirements of N, P, and K.

Table 1 presented a broad gamut of materials used in biogas and digestate creation. The table covered energy crops, agricultural byproducts, food processing residues, livestock effluents, organic fraction of municipal solid wastes, and pharmaceutical industry sludge. However, cassava peeling residue (CPR) was not represented in the table. There is a published report on ammonium, potassium, total nitrogen, and total phosphorus contents of digestate generated from co-digestion of human urine, cow dung, and cassava effluent (a mixture of peeled cassava wash water and crushed cassava juice) [92]. CPR is a solid substrate abundantly generated during production of cassava root-based food systems such as gari and starch [93]. The present author is not aware of any report on nutrients value of digestate generated from the AD of CPR as sole feedstock. Therefore, a technical experiment was conducted to secure an overview assessment of N, P, and K compositions of liquid fraction of CPR digestate.

Some results of the research work on CPR as sole substrate for AD were reported earlier. These included proximate properties (e.g., moisture content, total solids, volatile solids), digester performance characteristics (methane content of biogas, pH, discharge effluent COD), feedstock materials, sampling procedures, analyses [94]. Presented in Table 5 are results of nutrient values of liquid fraction of CPR digestate. Table 5 results appear to be within the range of some published nutrients values for liquid digestates derived from other feedstocks such as algal biomass (Chroococcus sp.) [88], starch processing wastewater [95], source separated household waste [96], as well as liquid and solid manure slurries [97].

S/NNutrientValue [mg/L]
1Ammonia nitrogen561
2Ortho-phosphorus20
3Potassium1066
4Total Kjeldahl nitrogen573
5Total phosphorus31

Table 5.

Nutrients values of liquid fraction of cassava peeling residue (CPR) digestate.

Advertisement

10. Conclusions

Cassava (Manihot esculenta Crantz) is perhaps third largest source of food energy for humans. Cassava supports the nutrition and subsistence of up to one billion persons in over 100 countries. Also, cassava is gluten free and could thus assuage medical complications for individuals with celiac disease. Cassava root processing byproduct such as CPR has organic matter content with applications in biogas and digestate production. This is a welcome development in views of biorefinery platform and the emergent circular economy. CPR digestate may be applied directly for agronomic uses or treated to generate products with varied applications and utilities. Treatment technologies may be biological, chemical, physical, or some combinations. Global benefits would include carbon sequestration, energy recovery, resource sustainability and recycling, waste reduction, profitability of AD process, biogas facilities, and agricultural systems in general. End effects of climate change mitigation, enhanced energy and food security, environmental and ecological protection, and sustainable development are good news for humanity and planet earth. These outcomes should motivate and provide consumers, farmers, regulators, managers, and other stakeholders in the emergent circular economy with insights to integrate and apply quality, safety, marketing, handling, storage, transportation, compliance with environmental regulations, and cost considerations and requirements strategies for digestate; into a renewable and sustainable energy production and waste management system.

Acknowledgments

All currency conversions to US$ were based on exchange rate taken at different times and days, during the period of last quarter of the year 2019, from the Foreign Exchange Converter Site: https://www1.oanda.com/currency/converter/

Conflict of interest

There is no conflict of interest (private or public) associated with this work.

References

  1. 1. Gómez X, Cuetos MJ, García AI, Morán A. An evaluation of stability by thermogravimetric analysis of digestate obtained from different biowastes. Journal of Hazardous Materials. 2007;149(1):97-105. DOI: 10.1016/j.jhazmat.2007.03.049
  2. 2. Tambone F, Orzi V, D’Imporzano G, Adani F. Solid and liquid fractionation of digestate: Mass balance, chemical characterization, and agronomic and environmental value. Bioresource Technology. 2017;243:1251-1256. DOI: 10.1016/j.biortech.2017.07.130
  3. 3. Antoniou N, Monlau F, Sambusiti C, Ficara E, Barakat A, Zabaniotou A. Contribution to circular economy options of mixed agricultural wastes management: Coupling anaerobic digestion with gasification for enhanced energy and material recovery. Journal of Cleaner Production. 2019;209:505-514. DOI: 10.1016/j.jclepro.2018.10.055
  4. 4. Salomon KR, Lora ES. Estimate of the electric energy generating potential for different sources of biogas in Brazil. Biomass and Bioenergy. 2009;3(9):1101-1107. DOI: 10.1016/j.biombioe.2009.03.001
  5. 5. Kusch S, Schäfer W, Kranert M. Dry digestion of organic residues. In: Kumar S, editor. Integrated Waste Management. Vol. 1. Croatia: IntechOpen; 2011. pp. 115-134. ISBN: 978-953-307-469-6. Available from: http://cdn.intechopen.com/pdfs/17433/InTech-Dry_digestion_of_organic_residues.pdf
  6. 6. Aso SN, Teixeira AA, Achinewhu SC. Cassava residues could provide sustainable bioenergy for cassava producing nations. Chapter 13. In: Waisundara VY, editor. Cassava. Rijeka, Croatia: IntechOpen; 2018. pp. 219-240. DOI: 10.5772/intechopen.72166
  7. 7. Liu H, Wang L, Zhang X, Fu B, Liu H, Li Y, et al. A viable approach for commercial VFAs production from sludge: Liquid fermentation in anaerobic dynamic membrane reactor. Journal of Hazardous Materials. 2019;365:912-920. DOI: 10.1016/j.jhazmat.2018.11.082
  8. 8. WBA: World Bioenergy Association. WBA Global Bioenergy Statistics 2018. Stockholm, Sweden: World Bioenergy Association; 2018. Available from: https://worldbioenergy.org/uploads/181203%20WBA%20GBS%202018_hq.pdf
  9. 9. BSI: British Standards Institution. Specification for whole digestate, separated liquor and separated fibre derived from the anaerobic digestion of source-segregated biodegradable materials. PAS 110:2010. British Standards Institution, London, UK. 2010. pp. 60. Available from: http://www.wrap.org.uk/sites/files/wrap/PAS110_vis_10.pdf
  10. 10. Tampio E, Marttinen S, Rintala J. Liquid fertilizer products from anaerobic digestion of food waste: Mass, nutrient and energy balance of four digestate liquid treatment systems. Journal of Cleaner Production. 2016;125:22-32. DOI: 10.1016/j.jclepro.2016.03.127
  11. 11. Zeshan S, Visvanathan C. Evaluation of anaerobic digestate for greenhouse gas emissions at various stages of its management. International Biodeterioration & Biodegradation. 2014;95(Part A):167-175. DOI: 10.1016/j.ibiod.2014.06.020
  12. 12. EC: European Commission. Regulation (EC) No. 208/2006 of 7 February 2006 amending Annexes VI and VIII to regulation (EC) No. 1774/2002 of the European parliament and of the council as regards processing standards for biogas and composting plants and requirements for manure. Official Journal of European Community. 2006;L36:25-31. Available from: https://publications.europa.eu/en/publication-detail/-/publication/eb5ea96c-1ee9-4654-931a-37a1f581b32e/language-en
  13. 13. Petersson A. English summary of SPCR 120—Certification rules for digestate from biowaste by the quality assurance system of Swedish Waste Management. Swedish Gas Centre; 2008. Available from: http://www.fao.org/fileadmin/user_upload/nr/sustainability_pathways/docs/Certification%20rules%20for%20digestate%20from%20biowaste.pdf
  14. 14. Siebert S. Quality requirements and quality assurance of digestion residuals in Germany. In: ECN/ORBIT Workshop: The future for Anaerobic Digestion of Organic Waste in Europe. Nüremberg, Germany. 2008. Available from: http://www.kompost.de/uploads/media/Quality_Requirements_of_digestion_residuals_in_Germany_text_01.pdf
  15. 15. Al Seadi T, Lukehurst C. Quality management of digestate from biogas plants used as fertiliser. IEA Bioenergy. 2012:4-36. Available from: https://www.researchgate.net/profile/Teodorita_Seadi/publication/265227188_Quality_Management_of_Digestate_from_Biogas_Plants_Used_as_Fertiliser/links/54b62dec0cf26833efd35c9d.pdf
  16. 16. Saveyn H, Eder P. End-of-waste criteria for biodegradable waste subjected to biological treatment (compost & digestate): Technical proposals. In: European Commission, Joint Research Centre, Institute for Prospective Technological Studies (IPTS). Seville: Spain; 2014. Available from: http://ftp.jrc.es/EURdoc/JRC87124.pdf
  17. 17. Mottet A, Steyer JP, Déléris S, Vedrenne F, Chauzy J, Carrère H. Kinetics of thermophilic batch anaerobic digestion of thermal hydrolysed waste activated sludge. Biochemical Engineering Journal. 2009;46(2):169-175. DOI: 10.1016/j.bej.2009.05.003
  18. 18. Alvira P, Tomás-Pejó E, Ballesteros M, Negro MJ. Pretreatment technologies for an efficient bioethanol production process based on enzymatic hydrolysis: A review. Bioresource Technology. 2010;101(13):4851-4861. DOI: 10.1016/j.biortech.2009.11.093
  19. 19. Hjorth M, Christensen KV, Christensen ML, Sommer SG. Solid-liquid separation of animal slurry in theory and practice. A review. Agronomy and Sustainable Development. 2010;30:153-180. DOI: 10.1051/agro/2009010
  20. 20. Mouat A, Barclay A, Mistry P, Webb J. Digestate market development in Scotland. Vol. OPR080-801. Stirling, UK: Zero Waste Scotland; 2010. Available from: http://www.wrap.org.uk/sites/files/wrap/Zero_Waste_Scotland_Digestate_Market_Development.pdf
  21. 21. Moon HC, Song IS. Enzymatic hydrolysis of foodwaste and methane production using UASB bioreactor. International Journal of Green Energy. 2011;8(3):361-371. DOI: 10.1080/15435075.2011.557845
  22. 22. Pilli S, Bhunia P, Yan S, LeBlanc RJ, Tyagi RD, Surampalli RY. Ultrasonic pretreatment of sludge: A review. Ultrasonics Sonochemistry. 2011;18:1-18. DOI: 10.1016/j.ultsonch.2010.02.014
  23. 23. van der Stelt MJC, Gerhauser H, Kiel JHA, Ptasinski KJ. Biomass upgrading by torrefaction for the production of biofuels: A review. Biomass and Bioenergy. 2011;35:3748-3762. DOI: 10.1016/j.biombioe.2011.06.023
  24. 24. Zhang Q, He J, Tian M, Mao Z, Tang L, Zhang J, et al. Enhancement of methane production from cassava residues by biological pretreatment using a constructed microbial consortium. Bioresource Technology. 2011;102(19):8899-8906. DOI: 10.1016/j.biortech.2011.06.061
  25. 25. Bustamante M, Alburquerque J, Restrepo A, de la Fuente C, Paredes C, Moral R, et al. Co-composting of the solid fraction of anaerobic digestates, to obtain added-value materials for use in agriculture. Biomass and Bioenergy. 2012;43:26-35. DOI: 10.1016/j.biombioe.2012.04.010
  26. 26. Elliott A, Mahmood T. Comparison of mechanical pretreatment methods for the enhancement of anaerobic digestion of pulp and paper waste activated sludge. Water Science & Technology. 2012;84(6):497-505. DOI: 10.2175/106143012X13347678384602
  27. 27. Liu X, Wang W, Gao X, Zhou Y, Shen R. Effect of thermal pretreatment on the physical and chemical properties of municipal biomass waste. Waste Management. 2012;32(2):249-255. DOI: 10.1016/j.wasman.2011.09.027
  28. 28. WRAP: Waste and Resources Action Programme. Enhancement and Treatment of Digestates from Anaerobic Digestion. Banbury, Oxon, United Kingdom: WRAP; 2012. Available from: http://www.wrap.org.uk/sites/files/wrap/Digestates%20from%20Anaerobic%20Digestion%20A%20review%20of%20enhancement%20techniques%20and%20novel%20digestate%20products_0.pdf
  29. 29. Zhao P, Shen Y, Ge S, Chen Z, Yoshikawa K. Clean solid biofuel production from high moisture content waste biomass employing hydrothermal treatment. Applied Energy. 2014;131:345-367. DOI: 10.1016/j.apenergy.2014.06.038
  30. 30. Peleteiro S, Rivas S, Alonso JL, Santos V, Parajo JC. Utilization of ionic liquids in lignocellulose biorefineries as agents for separation, derivatization, fractionation, or pretreatment. Journal of Agricultural and Food Chemistry. 2015;63(37):8093-8102. DOI: 10.1021/acs.jafc.5b03461
  31. 31. Carrere H, Antonopoulou G, Affes R, Passos F, Battimelli A, Lyberatos G, et al. Review of feedstock pretreatment strategies for improved anaerobic digestion: From lab-scale research to full-scale application. Bioresource Technology. 2016;199:386-397. DOI: 10.1016/j.biortech.2015.09.007
  32. 32. Liguori R, Faraco V. Biological processes for advancing lignocellulosic waste biorefinery by advocating circular economy. Bioresource Technology. 2016;215:13-20. DOI: 10.1016/j.biortech.2016.04.054
  33. 33. Zeng Y, Guardia AD, Dabert P. Improving composting as a post-treatment of anaerobic digestate. Bioresource Technology. 2016;201:293-303. DOI: 10.1016/j.biortech.2015.11.013
  34. 34. Bhutto AW, Qureshi K, Harijan K, Abro R, Abbas T, Bazmi AA, et al. Insight into progress in pre-treatment of lignocellulosic biomass. Energy. 2017;122:724-745. DOI: 10.1016/j.energy.2017.01.005
  35. 35. Duque A, Manzanares P, Ballesteros M. Extrusion as a pretreatment for lignocellulosic biomass: Fundamentals and applications. Renewable Energy. 2017;114:1427-1441. DOI: 10.1016/j.renene.2017.06.050
  36. 36. Shi L, Xie S, Hu Z, Wu G, Morrison L, Croot P, et al. Nutrient recovery from pig manure digestate using electrodialysis reversal: Membrane fouling and feasibility of long-term operation. Journal of Membrane Science. 2019;573:560-569. DOI: 10.1016/j.memsci.2018.12.037
  37. 37. D’Alessio M, Durso LM, Miller DN, Woodbury B, Ray C, Snow DD. Environmental fate and microbial effects of monensin, lincomycin, and sulfamethazine residues in soil. Environmental Pollution. 2019;246:60-68. DOI: 10.1016/j.envpol.2018.11.093
  38. 38. Tani M, Sakamoto N, Kishimoto T, Umetsu K. Utilization of anaerobically digested dairy slurry combined with other wastes following application to agricultural land. International Congress Series. 2006;1293:331-334. DOI: 10.1016/j.ics.2006.03.013
  39. 39. Alburquerque JA, Fuente C, Campoy M, Carrasco L, Nájera I, Baixauli C, et al. Agricultural use of digestate for horticultural crop production and improvement of soil properties. European Journal of Agronomy. 2012;43:119-128. DOI: 10.1016/j.eja.2012.06.001
  40. 40. Koszel M, Lorencowicz E. Agricultural use of biogas digestate as a replacement fertilizers. Agriculture and Agricultural Science Procedia. 2015;7:119-124. DOI: 10.1016/j.aaspro.2015.12.004
  41. 41. Garfí M, Ferrer-Martí L, Velo E, Ferrer I. Evaluating benefits of low-cost household digesters for rural Andean communities. Renewable and Sustainable Energy Reviews. 2012;16(1):575-581. DOI: 10.1016/j.rser.2011.08.023
  42. 42. Marchaim U. Biogas process for sustainable development. FAO Corporate Document Repository. M-09. 1992. ISBN: 92-5-103126-6. Available from: https://www.build-a-biogas-plant.com/PDF/BiogasSustainableDevolpment.pdf
  43. 43. Giuliano A, Bolzonella D, Pavan P, Cavinato C, Cecchi F. Co-digestion of livestock effluents, energy crops and agro-waste: Feeding and process optimization in mesophilic and thermophilic conditions. Bioresource Technology. 2013;128:612-618. DOI: 10.1016/j.biortech.2012.11.002
  44. 44. Monlau F, Sambusiti C, Ficara E, Aboulkas A, Barakat A, Carrère H. New opportunities for agricultural digestate valorization: Current situation and perspectives. Energy and Environmental Science. 2015;8(9):2600. DOI: 10.1039/c5ee01633a
  45. 45. Carpenter CE, Smith JV, Broadbent JR. Efficacy of washing meat surfaces with 2% levulinic, acetic, or lactic acid for pathogen decontamination and residual growth inhibition. Meat Science. 2011;88(2):256-260. DOI: 10.1016/j.meatsci.2010.12.032
  46. 46. Li C, Wang Y, Xie G, Peng B, Zhang B, Chen W, et al. Complete genome sequence of Clostridium butyricum JKY6D1 isolated from the pit mud of a Chinese flavor liquor-making factory. Journal of Biotechnology. 2016;220:23-24. DOI: 10.1016/j.jbiotec.2016.01.003
  47. 47. Huang WW, Huang WL, Yuan T, Zhao ZW, Cai W, Zhang ZY, et al. Volatile fatty acids (VFAs) production from swine manure through short-term dry anaerobic digestion and its separation from nitrogen and phosphorus resources in the digestate. Water Research. 2016;90:344-353. DOI: 10.1016/j.watres.2015.12.044
  48. 48. Wang K, Yin J, Shen D, Na L. Anaerobic digestion of food waste for volatile fatty acids (VFAs) production with different types of inoculum: Effect of pH. Bioresource Technology. 2014;161(6):395-401. DOI: 10.1016/j.biortech.2014.03.088
  49. 49. Liu H, Han P, Liu H, Zhou G, Fu B, Zheng Z. Full-scale production of VFAs from sewage sludge by anaerobic alkaline fermentation to improve biological nutrients removal in domestic wastewater. Bioresource Technology. 2018;260:105-114. DOI: 10.1016/j.biortech.2018.03.105
  50. 50. Neumann J, Binder S, Apfelbacher A, Gasson JR, Ramírez García P, Hornung A. Production and characterization of a new quality pyrolysis oil, char and syngas from digestate–Introducing the thermo-catalytic reforming process. Journal of Analytical and Applied Pyrolysis. 2015;113:137-142. DOI: 10.1016/j.jaap.2014.11.022
  51. 51. Singh R, Parihar P, Singh M, Bajguz A, Kumar J, Singh S, et al. Uncovering potential applications of cyanobacteria and algal metabolites in biology, agriculture and medicine: Current status and future prospects. Frontiers in Microbiology. 2017;8:515. DOI: 10.3389/fmicb.2017.00515
  52. 52. Koutra E, Economou CN, Tsafrakidou P, Kornaros M. Bio-based products from microalgae cultivated in digestates. Trends in Biotechnology. 2018;36(8):819-833. DOI: 10.1016/j.tibtech.2018.02.015
  53. 53. Inyang M, Gao B, Yao Y, Xue Y, Zimmerman AR, Pullammanappallil P, et al. Removal of heavy metals from aqueous solution by biochars derived from anaerobically digested biomass. Bioresource Technology. 2012;110:50-56. DOI: 10.1016/j.biortech.2012.01.072
  54. 54. Dahlin J, Herbes C, Nelles M. Biogas digestate marketing: Qualitative insights into the supply side. Resources, Conservation and Recycling. 2015;104:152-161. DOI: 10.1016/j.resconrec.2015.08.013
  55. 55. Spelter H, Winandy J, Zauche T. Anaerobically digested bovine biofiber as a source of fiber for particleboard manufacturing: An economic analysis. BioResources. 2008;3(4):1256-1266. Available from: https://ojs.cnr.ncsu.edu/index.php/BioRes/article/viewFile/BioRes_03_4_1256_Spelter_WZ_ADBF_Particleboard/278
  56. 56. USDA. Uses of solids and by-products of anaerobic digestion. Farm Energy. 2019;3:2019. Available from: https://farm-energy.extension.org/uses-of-solids-and-by-products-of-anaerobic-digestion/#Livestock_bedding
  57. 57. Sophin P, Preston TR. Effect of processing pig manure in a biodigester as fertilizer input for ponds growing fish in polyculture. Livestock Research for Rural Development. 2001;13:60. Available from: https://www.lrrd.cipav.org.co/lrrd13/6/pich136.htm
  58. 58. Garcia-Sánchez M, Garcia-Romera I, Cajthaml T, Tlustoš P, Száková J. Changes in soil microbial community functionality and structure in a metal-polluted site: The effect of digestate and fly ash applications. Journal of Environmental Management. 2015;162:63-73. DOI: 10.1016/j.jenvman.2015.07.042
  59. 59. Alexander R. Digestate utilization in the U.S. Biocycle. 2012;53(1):56. Available from: https://www.biocycle.net/2012/01/12/digestate-utilization-in-the-u-s/
  60. 60. Tin AM, Wise DL, Su WH, Reutergardh L, Lee SK. Cost-benefit analysis of the municipal solid waste collection system in Yangon, Myanmar. Resources, Conservation and Recycling. 1995;14(2):103-131. DOI: 10.1016/S0921-3449(95)80004-2
  61. 61. Setiawan RP, Kaneko S, Kawata K. Impacts of pecuniary and non-pecuniary information on pro-environmental behavior: A household waste collection and disposal program in Surabaya city. Waste Management. 2019;89:322-335. DOI: 10.1016/j.wasman.2019.04.015
  62. 62. Drosg B, Fuchs W, Al Seadi T, Madsen M, Linke B. Nutrient recovery by biogas digestate processing. IEA Bioenergy. 2015. Available from: https://www.iea-biogas.net/files/daten-redaktion/download/Technical%20Brochures/NUTRIENT_RECOVERY_RZ_web2.pdf
  63. 63. Hogg D. Eunomia Research & Consulting. Costs for municipal waste management in the EU. Final Report to Directorate General Environment, European Commission. 2002. Available from: http://ec.europa.eu/environment/waste/studies/pdf/eucostwaste.pdf
  64. 64. Delzeit R, Kellner U. The impact of plant size and location on profitability of biogas plants in Germany under consideration of processing digestates. Biomass and Bioenergy. 2013;52:43-53. DOI: 10.1016/j.biombioe.2013.02.029
  65. 65. Baddeley A, Ballinger A, Cessford I, Smith EM, Enviro A. Assessing the costs and benefits for production and beneficial application of anaerobic digestate to agricultural land in Wales. In: Project OMK007-203. WRAP: Waste and Resources Action Programme. Cardiff, UK; 2014. Available from: http://www.wrapcymru.org.uk/sites/files/wrap/Assessing%20the%20Costs%20and%20Benefits%20for%20Production%20and%20Beneficial%20Application%20of%20Anaerobic%20Digestate%20to%20Agricultural%20Land%20in%20Wales%202014.pdf
  66. 66. Møller HB, Lund I, Sommer SG. Solid–liquid separation of livestock slurry: Efficiency and cost. Bioresource Technology. 2000;74(3):223-229. DOI: 10.1016/S0960-8524(00)00016-X
  67. 67. Stiles WAV, Styles D, Chapman SP, Esteves S, Bywater A, Melville L, et al. Using microalgae in the circular economy to valorise anaerobic digestate: Challenges and opportunities. Bioresource Technology. 2018;267:732-742. DOI: 10.1016/j.biortech.2018.07.100
  68. 68. Mulinda C, Hu Q, Pan K. Dissemination and problems of African biogas technology. Energy and Power Engineering. 2013;5(08):506. Available from: http://www.build-a-biogas-plant.com/PDF/ProblemsAfricanBiogas2013.pdf
  69. 69. Amigun B, Von Blottnitz H. Capacity-cost and location-cost analyses for biogas plants in Africa. Resources, Conservation and Recycling. 2010;55(1):63-73. DOI: 10.1016/j.resconrec.2010.07.004
  70. 70. Bolzonella D, Fatone F, Gottardo M, Frison N. Nutrients recovery from anaerobic digestate of agro-waste: Techno-economic assessment of full scale applications. Journal of Environmental Management. 2018;216:111-119. DOI: 10.1016/j.jenvman.2017.08.026
  71. 71. Gerardo ML, Aljohani NHM, Oatley-Radcliffe DL, Lovitt RW. Moving towards sustainable resources: Recovery and fractionation of nutrients from dairy manure digestate using membranes. Water Research. 2015;80:80-89. DOI: 10.1016/j.watres.2015.05.016
  72. 72. Favoino E, Hogg D. Effects of composted organic waste on ecosystems—A specific angle: The potential contribution of biowaste to tackle Climate Change and references to the soil policy. Proceedings of the International Congress CODIS. 2008;2008:145-156. Available from: https://orgprints.org/13135/1/fuchs-etal-proceedings-codis-2008.pdf#page=151
  73. 73. Hu Y, Shen F, Yuan H, Zou D, Pang Y, Liu Y, et al. Influence of recirculation of liquid fraction of the digestate (LFD) on maize stover anaerobic digestion. Biosystems Engineering. 2014;127:189-196. DOI: 10.1016/j.biosystemseng.2014.09.006
  74. 74. de Alwis A. Biogas—A review of Sri Lanka’s performance with a renewable energy technology. Energy for Sustainable Development. 2002;6(1):30-37. DOI: 10.1016/S0973-0826(08)60296-3
  75. 75. Brändli RC, Bucheli TD, Kupper T, Furrer R, Stahel WA, Stadelmann FX, et al. Organic pollutants in compost and digestate. Part 1. Polychlorinated biphenyls, polycyclic aromatic hydrocarbons and molecular markers. Journal of Environment Monitoring. 2007;9(5):456-464. DOI: 10.1039/B617101J
  76. 76. Tiwary A, Williams ID, Pant DC, Kishore VVN. Assessment and mitigation of the environmental burdens to air from land applied food-based digestate. Environmental Pollution. 2015;203:262-270. DOI: 10.1016/j.envpol.2015.02.001
  77. 77. Wallace P, Harris G, Frederickson J, Howell G, Tompkins D. Biofertiliser management: Best practice for agronomic benefit & odour control. In: Tompkins D, editor. Project OAV036-210. Cardiff: The Waste and Resources Action Program (WRAP); 2011. Available from: http://www.wrapcymru.org.uk/sites/files/wrap/Digestate%20odour%20management%20-%20Cymru.pdf
  78. 78. Cheng Z, Sun Z, Zhu S, Lou Z, Zhu N, Feng L. The identification and health risk assessment of odor emissions from waste landfilling and composting. Science of The Total Environment. 2019;649:1038-1044. DOI: 10.1016/j.scitotenv.2018.08.230
  79. 79. Eshete G, Sonder K, ter Heegde F. Report on the Feasibility Study of a National Programme for Domestic Biogas in Ethiopia. SNV Netherlands Development Organization: Addis Ababa, Ethiopia; 2006. Available from: http://www.bibalex.org/Search4Dev/files/338849/172350.pdf
  80. 80. Berhe TG, Tesfahuney RG, Desta GA, Mekonnen LS. Biogas plant distribution for rural household sustainable energy supply in Africa. Energy and Policy Research. 2017;4(1):10-20. DOI: 10.1080/23815639.2017.1280432
  81. 81. Mushtaq K, Zaidi AA, Askari SJ. Design and performance analysis of floating dome type portable biogas plant for domestic use in Pakistan. Sustainable Energy Technologies and Assessments. 2016;14:21-25. DOI: 10.1016/j.seta.2016.01.001
  82. 82. Day DL, Chen TH, Anderson JC, Steinberg MP. Biogas plants for small farms in Kenya. Biomass. 1990;21(2):83-99. DOI: 10.1016/0144-4565(90)90051-K
  83. 83. Caceres R, Chiliquinga B. Experiences with Rural Biodigesters in Latin America. Dordrecht: Springer; 1986. pp. 150-165. DOI: 10.1007/978-94-009-4313-1_21
  84. 84. Ni J-Q, Nyns E-J. New concept for the evaluation of rural biogas management in developing countries. Energy Conversion and Management. 1996;37(10):1525-1534. DOI: 10.1016/0196-8904(95)00354-1
  85. 85. Raven RPJM. Implementation of manure digestion and co-combustion in the Dutch electricity regime: A multi-level analysis of market implementation in the Netherlands. Energy Policy. 2004;32(1):29-39. DOI: 10.1016/S0301-4215(02)00248-3
  86. 86. Negro SO, Hekkert MP, Smits RE. Explaining the failure of the Dutch innovation system for biomass digestion—A functional analysis. Energy Policy. 2007;35(2):925-938. DOI: 10.1016/j.enpol.2006.01.027
  87. 87. Tigini V, Franchino M, Bona F, Varese GC. Is digestate safe? A study on its ecotoxicity and environmental risk on a pig manure. Science of the Total Environment. 2016;551-552:127-132. DOI: 10.1016/j.scitotenv.2016.02.004
  88. 88. Prajapati SK, Kumar P, Malik A, Vijay VK. Bioconversion of algae to methane and subsequent utilization of digestate for algae cultivation: A closed loop bioenergy generation process. Bioresource Technology. 2014;158:174-180. DOI: 10.1016/j.biortech.2014.02.023
  89. 89. Möller K, Habermeyer J, Zinkernagel V, Reents H-J. The impact and the interaction of nitrogen and Phytophthora infestans as yield-limiting and yield-reducing factors in organic potato (Solanum tuberosum L.) crops. Potato Research. 2006;49(4):281-301. DOI: 10.1007/s11540-007-9024-7
  90. 90. Shenoy VV, Kalagudi GM. Enhancing plant phosphorus use efficiency for sustainable cropping. Biotechnology Advances. 2005;23(7-8):501-513. DOI: 10.1016/j.biotechadv.2005.01.004
  91. 91. Sobachkin AA. The physiological role of potassium in increasing the productivity of farm crops. In: Potassium Research and Agricultural Production. Proceedings of the 10th Congress of the International Potash Institute held in June 1974 in Budapest, Hungary. International Potash Institute. 1974. pp. 147-152. Available from: https://www.ipipotash.org/uploads/udocs/potassium_research_and_agricultural_production.pdf
  92. 92. Edith KKN, Francis KY, Martin KK, Felix KK. Characterization of digestates from anaerobic co-digestion of manioc effluent, human urine and cow dung. Journal of Water Resource and Protection. 2019;11(06):777-788. DOI: 10.4236/jwarp.2019.116047
  93. 93. Aso SN. Food engineering stratagem to protect the environment and improve the income opportunities of gari processors. Journal of Nigerian Environmental Society (JNES). 2004;2(1):31-36
  94. 94. Aso SN, Pullammanappallil PC, Teixeira AA, Welt BA. Biogasification of cassava residue for on-site biofuel generation for food production with potential cost minimization, health and environmental safety dividends. Environmental Progress & Sustainable Energy. 2019. DOI: 10.1002/ep.13138
  95. 95. Tan X, Chu H, Zhang Y, Yang L, Zhao F, Zhou X. Chlorella pyrenoidosa cultivation using anaerobic digested starch processing wastewater in an airlift circulation photobioreactor. Bioresource Technology. 2014;170:538-548. DOI: 10.1016/j.biortech.2014.07.086
  96. 96. Haraldsen TK, Andersen U, Krogstad T, Sørheim R. Liquid digestate from anaerobic treatment of source-separated household waste as fertiliser to barley. Waste Management & Research. 2017;29:1271-1276. DOI: 10.1177/0734242X11411975
  97. 97. Pirelli T, Rossi A, Miller C. Sustainability of biogas and cassava-based ethanol value chains in Viet Nam: Results and recommendations from the implementation of the Global Bioenergy Partnership indicators. In: FAO Environment and Natural Resources Management Working Paper 69. Rome: FAO; 2018. Available from: http://www.fao.org/3/i9181en/I9181EN.pdf

Written By

Sammy N. Aso

Submitted: 12 September 2019 Reviewed: 23 January 2020 Published: 11 May 2020