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Review

Household Biogas Digesters—A Review

by
Karthik Rajendran
*,
Solmaz Aslanzadeh
and
Mohammad J. Taherzadeh
School of Engineering, University of Borås, Borås 50190, Sweden
*
Author to whom correspondence should be addressed.
Energies 2012, 5(8), 2911-2942; https://doi.org/10.3390/en5082911
Submission received: 11 May 2012 / Revised: 27 July 2012 / Accepted: 30 July 2012 / Published: 8 August 2012

Abstract

:
This review is a summary of different aspects of the design and operation of small-scale, household, biogas digesters. It covers different digester designs and materials used for construction, important operating parameters such as pH, temperature, substrate, and loading rate, applications of the biogas, the government policies concerning the use of household digesters, and the social and environmental effects of the digesters. Biogas is a value-added product of anaerobic digestion of organic compounds. Biogas production depends on different factors including: pH, temperature, substrate, loading rate, hydraulic retention time (HRT), C/N ratio, and mixing. Household digesters are cheap, easy to handle, and reduce the amount of organic household waste. The size of these digesters varies between 1 and 150 m3. The common designs include fixed dome, floating drum, and plug flow type. Biogas and fertilizer obtained at the end of anaerobic digestion could be used for cooking, lighting, and electricity.

1. Introduction

Due to the increasing prices of fossil fuels and taxes on energy sources, finding alternative, clean and economical sources of energy has nowadays become a major concern for households’ and nations’ economies. In addition, economic prosperity and quality of life, which are linked in most countries to per-capita energy consumption, is a great determinant and indicator of economical development [1,2,3,4]. Energy demand is a critical reason for extensive climate change, resource exploitation, and also restricts the living standards of humans [5,6].
By the time fuel and fertilizer reaches rural areas, the end price is relatively expensive due to high transport costs, leaving people to find alternative resources other than oil [7]. Starke [8] reported wood as the traditional source of fuel to produce energy for domestic purposes for 2.5 billion people in Asia. Many of the rural communities in developing countries are forced to rely on the traditional energy sources such as firewood, dung, crop residues, and paraffin. These traditional methods are often expensive and/or time-consuming [9,10,11]. Cooking accounts for 90% of energy consumption in the households of developing countries [12]. Furthermore, access to electricity in rural areas is relatively scarce [13].
Biogas is a substitute for firewood and cattle dung that can meet the energy needs of the rural population [14,15]. Biogas is a renewable source of energy that can be used as a substitute for natural gas or liquefied petroleum gas [16]. There are different models to assess the energy content of different energy sources, which includes water boiling test, controlled cooking test and kitchen performance test [17]. The energy content of 1.0 m3 of purified biogas is equal to 1.1 L of gasoline, 1.7 L of bioethanol, or 0.97 m3 of natural gas [16]. The application for rural and urban waste biogas production is widely spread. It is a challenge for engineers and scientists to build an efficient domestic digesters with the materials available, at the same time taking the local and economical considerations into the account. Although many digesters have been built, additional research and awareness are needed to meet the changing needs and conditions [18].
Biogas production can be carried out in very small reactors ranging from 100-mL serum bottles in the lab up to 10,000 m3 large digesters as normally used, for example, in Europe. This review deals with a summary of different household biogas digesters, their operating parameters, cost and materials used to build them, startup, and maintenance, the variety of applications employed, and associated social and environmental effects.

1.1. Biogas

Biogas, the metabolic product of anaerobic digestion, is a mixture of methane and carbon dioxide with small quantities of other gases such as hydrogen sulfide [19,20]. Methane, the desired component of biogas, is a colorless, blue burning gas used for cooking, heating, and lighting [21]. Biogas is a clean, efficient, and renewable source of energy, which can be used as a substitute for other fuels in order to save energy in rural areas [22]. In anaerobic digestion, organic materials are degraded by bacteria, in the absence of oxygen, converting it into a methane and carbon dioxide mixture. The digestate or slurry from the digester is rich in ammonium and other nutrients used as an organic fertilizer [11,23,24,25,26,27].
Methane formation in anaerobic digestion involves four different steps, including hydrolysis, acidogenesis, acetogenesis, and methanogenesis. Different bacterial/archaea communities work in a syntrophic relationship with each other to form methane. In hydrolysis, complex carbohydrates, fats, and proteins are first hydrolyzed to their monomeric forms by exoenzymes and bacterial cellulosome. In the second phase (acidogenesis), monomers are further degraded into short-chain acids such as: acetic acid, propionic acid, butyric acid, isobutyric acid, valeric acid, isovaleric acid, caprionic acid, alcohols, hydrogen, and carbon dioxide. During acetogenesis, these short-chain acids are converted into acetate, hydrogen, and carbon dioxide. In the last phase, methanogens convert the intermediates produced into methane and carbon dioxide. Almost one-third of methane formation is due to reduction of carbon dioxide by hydrogen [28].

1.2. Digestion Factors

Anaerobic digestion depends on several different parameters for an optimum performance. Different groups of microorganisms are involved in the methane production, and suitable conditions have to be established to keep all the microorganisms in balance. Some of these parameters are: pH, temperature, mixing, substrate, C/N ratio, and hydraulic retention time (HRT). Digestion is a slow process and it takes at a minimum of three weeks for the microorganisms to adapt to a new condition when there is a change in substrate or temperature [28].
A symbiotic relationship is necessary between the hydrogen-producing acetogenic microorganisms and the hydrogen-consuming methanogens. Furthermore, a neutral pH is favorable for biogas production, since most of the methanogens grow at the pH range of 6.7–7.5. Temperature is also an important factor in the biogas production. Most of the acid forming microorganisms grows under mesophilic conditions; however, for methanogens, a higher temperature is favorable [28]. Mixing is also an essential parameter for biogas production. Too much mixing stresses the microorganisms and without mixing foaming occurs. Methane-forming microorganisms grow slowly, with a doubling time of around 5–16 days. Therefore, the hydraulic retention time should be at least 10–15 days, unless these bacteria are retained by, for example, entrapment. Substrate and the balance of carbon sources with other nutrients such as nitrogen, phosphorus, and sulfur is also important. The substrate should be slowly digested, otherwise easily degradable substrates may cause a sudden increase in acid content. The carbon and nitrogen ratio should be around 16:1–25:1. Too much increase or decrease in the carbon/nitrogen ratio affects biogas production. The concentration of solids in the digester should vary between 7% and 9%. Particle size is not an important factor compared to other parameters such as pH and temperature. However, the size of the particles used affects the degradation and ultimately the biogas production rate [28,29,30].

1.3. A Brief Global View on Small Anaerobic Digesters

Unlike other renewable fuels such as biodiesel and bioethanol, biogas production is relatively simple and can operate under any conditions and is not monopolistic [31,32]. Dung is a potential substrate for biogas production, seen only as a floor polish and fertilizer in the garden for hundreds of years. Biogas for rural energy is sustainable, affordable, and has no negative effect on people’s health or the environment, if handled properly [33,34]. Complicated construction, difficult operation of the systems, high investment, and maintenance costs have pushed farmers to adopt cheaper and simpler anaerobic systems [35].
There are currently more than 30 million household digesters in China, followed by India with 3.8 million, 0.2 million in Nepal, and 60,000 in Bangladesh [36,37,38]. China has increased its investments in biogas infrastructure very rapidly. By 2020, 80 million households in China are expected to have biogas digesters serving 300 million people [39]. India is implementing one of the world’s largest renewable-energy programs with different scales of technologies. One of the strategies is to promote biogas plants [40,41]. India began the project half a century ago, and was further supported by the National Project on Biogas Development in 1982. Similar trends were more or less observed in other Asian countries. For instance, SNV, a Non Governmental Organization (NGO) from The Netherlands has installed 23,300 plants in Vietnam [42].
In America, 162 farm scale plants were in operation by 2010, providing energy for 41,000 homes; in addition, 17 plants were operating in Canada. The number of farm scale digesters in Europe has increased drastically. At the end of 2011, the number of these digesters was more than 4000 in Germany, 350 in Austria, 72 in Switzerland, 65 in the United Kingdom followed by Denmark with 20 community type and 35 farm scale plants, and Sweden had 12 plants [43,44,45,46].
The level of biogas technology for household purposes is very low in many African countries [47]. Kenya has 1884 household biogas plants and Ethiopia has more than 1140 plants [48]. Small-scale biogas plants are located throughout Africa, but only a few are working. Poor technical quality of construction and material used, inexperienced contractors, insufficient knowledge on the system in practice as well as in research institutes and universities are some of the reasons responsible for the failure [49]. Although the potential need is very high in Africa, the technology is at embryonic stage with the countries struggling to meet their energy demands [2,49,50].

2. Household Digesters

It is always difficult to adopt one particular type of digester for household purposes. Design of the digesters is varied based on the geographical location, availability of substrate, and climatic conditions. For instance, a digester used in mountainous regions is designed to have less gas volume in order to avoid gas loss. For tropical countries, it is preferred to have digesters underground due to the geothermal energy [51]. Out of all the different digesters developed, the fixed dome model developed by China and the floating drum model developed by India have continued to perform until today [52]. Recently, plug flow digesters are gaining attention due to its portability and easy operation.

2.1. Fixed Dome Digesters

The fixed dome digesters (Figure 1) also called “Chinese” or “hydraulic” digesters are the most common model developed and used mainly in China for biogas production [27]. The digester is filled through the inlet pipe until the level reaches the bottom level of the expansion chamber. The produced biogas is accumulated at the upper part of the digester called storage part. The difference in the level between slurry inside of the digester and the expansion chamber creates a gas pressure. The collected gas requires space and presses a part of the substrate into an expansion chamber. The slurry flows back into the digester immediately after gas is released [53].
Fixed dome digesters are usually built underground [27]. The size of the digester depends on the location, number of households, and the amount of substrate available every day. For instance, the size of these digesters can typically vary between 4 and 20 m3 in Nepal [54], between 6 and 10 m3 in China [55], between 1 and 150 m3 in India [56] and in Nigeria it is around 6 m3 for a family of 9 [57]. Instead of having a digester for each individual home, a large volume digester is used to produce biogas for 10–20 homes, and is called community type biogas digesters. In countries where houses are clustered as in Nigeria, these types of biogas digesters are more feasible [58].
Figure 1. Schematic sketch of (a) a janta model fixed dome digester and its modifications, (b) a deenbandhu model fixed dome digester and its modifications, and (c) a modified fixed dome digester with straight and curved inlet and outlet tube.
Figure 1. Schematic sketch of (a) a janta model fixed dome digester and its modifications, (b) a deenbandhu model fixed dome digester and its modifications, and (c) a modified fixed dome digester with straight and curved inlet and outlet tube.
Energies 05 02911 g001
Fixed dome models developed in India include the janta and deenbandhu models. The janta model was introduced in 1978 (Figure 1a). It consists of a shallow well with a dome roof on top. The inlet and outlet were kept above the dome with the gas pipe fitted on top of the dome. The disadvantages of the janta model includes short circulating path of the slurry, escape of undigested slurry at the top and less volume of gas produced due to the increased gas pressure [59]. Action for Food Production (AFPRO) launched a modified janta model called the deenbandhu model in 1984 (Figure 1b). It consists of two spheres of different diameters. The lower sphere acts as a fermentation unit, while the upper one is the storage unit. This model was developed to reduce the price without decreasing the efficiency of the process [1].
Many countries have modified the basic shape of the fixed dome model. For instance, the Chinese digester was modified into a hemispherical shape with a wall in the middle as shown in Figure 1a [60,61], and the deenbandhu model was modified with a smaller gas holding capacity and reducing the diameter of the arch (Figure 1b) [62]. In mountainous regions, loss of biogas during the winter months is less in the modified model than the deenbandhu model. Jash and Basu [63] modified the dome with a vertical cylinder and a gas holder in a bell shape. The cylindrical vessel was partitioned into two using bricks. Since the inlet and outlet tubes were long and straight, some of the heavy particles got stuck, resulting in a modification with a bent inlet and outlet tube (Figure 1c). Fixed dome digesters were surrounded by a steel drum containing biomass to avoid the loss in temperature, which is also called French type digesters [64]. Another modification is to cover the gas storage part of the fixed dome digester with an expanding plastic bag. A wood roof is placed on top of the cover in order to protect the fragile plastic bag against the sunlight and at the same time increase the gas pressure by its weight [53].

2.2. Floating Drum Digesters

Khadi and Village Industries Commission (KVIC) is the name of a floating drum digester model developed in 1962 (Figure 2). Even though the model is pretty old, it is one of the most widely accepted and used designs for household purposes in India. The design includes a movable inverted drum placed on a well-shaped digester. An inverted steel drum that acts as a storage tank is placed on the digester, which can move up and down depending on the amount of accumulated gas at the top of the digester. The weight of this inverted drum applies the pressure needed for the gas flow through the pipeline for use [1].
Floating drum digesters produce biogas at a constant pressure with variable volume [33]. From the position of the drum, the amount of biogas accumulated under the drum is easily detectable. However, the floating drum needs to be coated with paint in a constant interval to avoid rust. Additionally, fibrous materials will block the movement of digester. Hence, their accumulation should be avoided if possible [65]. In Thailand, the floating dome has been modified with two cement jars on either side of the floating drum. The average size of these kinds of digesters is around 1.2 m3 [66]. For a small-medium size farms the size varies from around 5–15 m3 [65]. Singh and Gupta [67] compared 14 different biogas plants with a floating drum model. The size of each digester was about 85 m3. The ratio of the waste fed to the plant in one day to the capacity of the plant is called plant utilization factor (PUF), and it was found to be 0.36. This result suggests that the full capacity of the plant was not utilized.
Figure 2. Schematic sketch of a floating drum digester.
Figure 2. Schematic sketch of a floating drum digester.
Energies 05 02911 g002

2.3. Plug Flow Digesters

The disadvantage with the fixed dome and floating drum models is, once installed they are difficult to move. Hence, portable models built over the ground called tubular or plug flow digesters were developed (Figure 3).
Figure 3. Schematic sketch of a plug flow digester.
Figure 3. Schematic sketch of a plug flow digester.
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Plug flow digesters have a constant volume, but produce biogas at a variable pressure [33]. The size of such digesters varies from 2.4 to 7.5 m3. Plug-flow digesters consist of a narrow and long tank with, an average length to width ratio of 5:1. The inlet and outlet of the digester are located at opposite ends, kept above ground, while the remaining parts of the digester is buried in the ground in an inclined position. As the fresh substrate is added from the inlet, the digestate flows towards the outlet at the other end of the tank. The inclined position makes it possible to separate acidogenesis and methanogenesis longitudinally, thus producing a two-phase system. In order to avoid temperature fluctuations during the night and maintain the process temperature, a gable or shed roof is placed on top of the digester to cover it, which acts as an insulation both during day and night [68,69,70,71,72,73,74].
The popularity of tubular digesters has increased recently in Peru, due to its portability and low cost [68]. The usefulness of these digesters includes easy installation, easy handling, and adaptation to extreme conditions at high altitudes with low temperatures. The transportation costs for the material to build the digester in hilly areas are high, leading to a high capital cost. On the other hand, plug flow digesters are easy to transport, which ultimately reduces the cost of the digester [68]. It is also difficult to dig a large volume under the ground to build digesters in high altitudes [75].
51% of all digesters installed by United States Environmental Protection Agency (USEPA) were plug flow digesters [76]. Plug flow designs are suitable for manure, and operating semi-continuously with a HRT between 20 and 30 days, and a solid contents varying between 11 and 14%. These digesters do not have moving parts, reducing risks for failure [77,78,79]. Out of 99 digesters installed by the Bureau of Animal Industry in the Philippines, only one did not produce gas, and three had delayed gas production [80].

2.4. Comparisons of Different Digesters

Hamad et al. [81] compared the performance of the modified Indian digester and the Chinese fixed dome models for the conditions prevailing in Egypt. None of the digesters were suitable for the local conditions, and for the conditions present in Egypt, the plug flow digester and the digester with a solar heater were reported to be more efficient. Biogas production decreased by 70% in the rubber balloon digester compared to 17% in the deenbandhu model during winter. It is not advisable to use the rubber balloon model in hilly areas as it is affected by the ambient temperatures. The fluctuation in temperature changes the microflora in the reactor between lower mesophilic in summer to psycrophilic in winter, affecting the process parameters. Compared to the conventional plant (fixed dome digesters), rubber balloon reactors in hilly areas maintain 2–3 °C lower temperatures during the winter and 2–3 °C higher temperatures during the summer [82]. Mohammad [64] compared the vertical plant (modified floating drum), horizontal (with two partitions), community type, Chinese dome, French type, rubber tube, and polyethylene bag using a common substrate (buffalo dung). The results suggest that the community model was somewhat expensive, but it was very effective.

2.5. Other Digesters

Singh and Anand [83] aimed to decrease the water consumption in domestic digesters. Thus, a solid-state digester (SSD) was built out of a cylindrical vertical vessel with a cone at the bottom. This digester was welded to a tripod for balance. Lagoons with a floating cover could also be used as a digester, which is very cheap for farmers [84]. Qi et al. [85] designed and studied an integrated system of biogas production, using a greenhouse for growing vegetables and a pigsty for feeding the pigs in Laiwu, Shandong province, North of China. The biogas produced from swine manure and urine was used for cooking, lighting, or to maintain the temperature inside the greenhouse for optimum vegetable growth and the digestate were used as a fertilizer to replace chemical fertilizers. During winter, the low temperature and sunlight levels increases the application of chemical fertilizers. This frequent use of chemical fertilizer not only increased the cost of expenses but also decreased the vegetable quality during the winter. However, the substitution of chemical fertilizer with digestate increased the vegetable yield by 18.4% and 17.8% for cucumber and tomato respectively.

3. Parameters in Digesters Operation

3.1. Materials for Construction

Materials for construction of household digesters depend on geological, hydrological, local conditions, and locally available materials [18]. With technological advances, different materials with improved properties and lower costs have been introduced to the market in recent years. In India, underground biogas household digesters are very popular. Stone or bricks are used as the material for construction of these kinds of digesters [86]. High investment costs are required to build fixed structure digesters, which is the main constraint to low-income farmers. Taiwanese engineers in 1960 started to develop digesters from cheaper, locally available materials. Although nylon and neoprene were used initially, this proved to be expensive. With the development of technology, PVC and polyethylene were used instead, since they are relatively cheap [72]. Different construction materials with their advantages and disadvantages are summarized in Table 1.
Table 1. Different materials used for construction of digesters with their advantages and disadvantages.
Table 1. Different materials used for construction of digesters with their advantages and disadvantages.
MaterialModificationsAdvantagesDisadvantagesReference
Poly vinyl chloride (PVC)Red mud PVC (mixed with aluminum)Less weight
Easily portable
Short life span of plastics[59,68,70,72,73,87,88,89,90]
Polyethylene (PE)PE with UV filterPE is much cheaper compared to PVC
Neoprene and rubberReinforced with nylonWeather resistance elasticExpensive
Low pressure
Less life span
[72,82,91]
Bricks and concretePre fired earthen rings,
lime concrete,
slag concrete,
fired clay, bricks,
reinforced concrete,
Ferro cement (crack proof)
Everlasting, less maintenance costsGas could escape through concrete pores when pressure increases.
Built underground. Difficult to clean. Occupies more space.
[18,52,63,86,92,93]
Bamboo and wood supportsUsually a support material, Reinforced with flaxLocally available materialCan break easily[54]
Steel drum Produce gas at a constant flow
Leak proof
Corrosion
Heavy weight of gas holder
[64,91]

3.2. Effect of Temperature

One of the important and difficult parameters to maintain in domestic biogas digesters is the temperature. Methanogens are active, even at a very low temperature [70,94,95,96], while the biogas production increases by tenfold upon increasing the temperature from 10 to 25 °C. According to some observations, the amount of biogas produced by high temperature (mesophilic) and low HRT is comparable to the biogas produced with low temperature (psycrophilic) and high HRT [70]. People living in mountain valleys or outside of tropical regions suffer from low digestion rates during the winter season, when the temperature drops below 15 °C [86]. Different techniques and methods have been developed around the world to maintain the temperature inside the digester. Solar energy could be used as a heating source to increase the temperature of the digester [18]. Misra et al. [97] developed a solar-based heating device, but the efficiency decreased during the wintertime in hilly areas. To keep the temperature as constant as possible, most of the digesters were built underground [98]. Ramana and Singh [99] reported that geothermal energy helped in maintaining the temperature in the digester when buried underground.
Anand and Singh [86] proposed using a charcoal coating on top of the digester. This method increased the temperature by 3 °C and gas production by 7%–15%, but the digester had to be coated every one and a half months. This method is however economical as farmers can prepare charcoal by burning wood pieces. To maintain the temperature in the reactor, it is not enough to only blacken or glaze (coating). Some part of the biogas produced should also be burnt to maintain the temperature in the digester [100]. Paddy husk placed on top of the digester can also help in maintaining the temperature during winter [101]. Singh et al. [102] reported that the decrease of biogas yield during winter could be overcome by providing insulation on the inner surface of the gas holder. A shallow, solar-pond water-heater also reduced the heat loss inside the digester.
The French type digester covered with a polyethylene bag containing municipal solid waste did not affect the temperature drop [64]. Anjan [59] compared the janta model and the plug flow type of digester. The biogas production was more in the summer than in the winter, and the plug flow digester was less influenced by the temperature. Hamad et al. [81] compared the Indian model and the Chinese fixed dome digester. The Chinese dome digester had better insulation properties compared to the Indian type. In the Indian model the temperature decreased with decrease in height. A long-term testing of a biogas digester shows that the digester worked in the lower mesophilic range for almost eight months out of the year and in the psychrophilic range for the remaining part of the year [75].
In order to maintain the temperature in the reactor, the digester is covered by certain insulation materials. The insulation materials include: composites made of glass wool, sawdust, and plaster of Paris in ratio 1:2:2; black cloth coated with pitch, sodium peroxide, glass wool, and a mixture of thermocol and sawdust. The composite and black cloth coating was able to hold the temperature for more than 70 h, but the thermocol-sawdust mixture could only maintain it for 36 h [97].

3.3. Substrate Consumption

Almost all biomass is degraded to biogas in theory [103]. However, the choice of substrate will depend on the availability of the raw material, type of the digester, and its operating conditions. [64]. Cattle manure was a traditional source for biogas production in the past. The methane content was high in pig manure, around 60%, followed by cow dung with 50% [89]. Kitchen wastes and crop residues are some underexploited substrates for the domestic biogas production. Kitchen wastes contain a high amount of fat in the form of animal fat and cooking oil. This high-fat content can enhance the biogas production [90,103].
Combinations of different substrates often have a synergistic effect on biogas production [104,105]. Co-digestion can improve the nutrient balance, maintains the pH, and results in positive synergisms [106,107,108]. Moreover, in several studies co-digestion had a higher methane yield compared to mono substrate digestion [90,109,110,111,112,113]. Different substrates used for biogas production, dry matter, ash content, total digestible nutrients and biogas yield for household digesters are listed in Table 2.
Table 2. Different substrates with corresponding dry matter, ash content, total digestible nutrients and biogas yield used in the household biogas digesters [28,65,114].
Table 2. Different substrates with corresponding dry matter, ash content, total digestible nutrients and biogas yield used in the household biogas digesters [28,65,114].
Main substrateSubstrate classificationDry matter (%)Ash (%)Total digestible nutrients (%)Biogas yieldReferences
ManureCow3814920.6–0.8 m3/kg TS[54,60,61,66,67,68,75,86,89,92,110,112,113,115]
Pig20–25NANA0.27–0.45 m3/kg TS[70,89,112,116,117]
Buffalo14NANANA[81,89]
Poultry8933380.3–0.8 m3/kg TS[64,118,119]
Horse28NANA0.4–0.6 m3/kg TS[120]
Fecal matterHuman excreta20NANANA[27,54]
Night soilNANANANA[93,94,121]
Agricultural residuesRice straw9113400.55–0.62 m3/kg TS[93]
Wheat straw918430.188 m3/kg VS[64,122]
Maize straw86NANA0.4–1.0 m3/kg TS[28]
Grass886580.28–0.55 m3/kg VS[55,118,119]
Mango leavesNANANA0.6 m3/kg TS[92]
Foliage of partheniumNANANANA
Coffee pulp288NA0.300– 0.450 m3/kg VS[118,119,123]
Corn stalk807540.350–0.480 m3/kg VS
Cassava peels (residues)NANANA0.661 m3/kg VS (0.132 m3/kg VS)[88,124,125,126]
Food wastesHousehold grease [111]
Whey941082NA
Vegetable waste5–20NANA0.4 m3/kg TS[16,54,69]
Fruit wastes(apple)17270NA[64,69]
Kitchen/restaurant wastes27/1313/8NA0.506/0. 650 m3 CH4/kg VS[110,111,127,128,129,130,131]
Left over’s food14–18NANA0.2–0.5 m3/kg TS[28]
Egg waste25NANA0.97–0.98 m3/kg TS[28]
Cereals85–90NANA0.4–0.9 m3/kg TS[28]
Aquatic plants or sea weedsAlgaeNANANA0.38–0.55 m3/kg VS[132]
Water hyacinth7NANA0.2–0.3 m3/kg VS[93,133]
Giant kelpNANANANA[118,119]
CabomaNANANA0.221 m3/kg VS[133]
SalviniaNANANA0.155 m3/kg VS[133]
* NA- Not Available.

3.4. Loading Rate and Yield of Biogas Produced

The solids concentration in the household biogas digesters varies between 5% and 10% [64,69,89,92,103]. Increasing the solids concentration to 19% decreased the biogas production considerably [92]. The common organic loading rate (OLR) of the digester is 2–3 kgVS/m3/day under mesophilic conditions. Nevertheless, it could be possible to achieve higher OLRs if the sludge concentration is over 10% [101]. Anjan [59] reported a maximum of 10.4–10.6 kgVS/m3/day in the janta model and the modified plug flow reactor. The average biogas production in the domestic biogas digester was in the range of 0.26–0.55 m3/kgVS/day [67,84,89].
Hydraulic retention times (HRT) vary between 20 and 100 days for mesophilic household digesters [70,71,89,103]. Studies show that decreasing HRT from 90 days to 60 day and increasing the OLR by diluting the substrate from 1:4 to 1:2 would be beneficial for the better performance of the digester [68]. Many household digesters do not have a stirrer to mix the digester content, which creates stagnant regions in the digesters. Due to these stagnant regions, the digester HRT is decreased compared to its calculated HRT, leading to wash out of the microorganisms [81,134,135].

3.5. Biogas Storage and Maintenance of Digesters

Storing the biogas produced is often a major concern. Biogas can be transported directly to the kitchen or stored in a pressurized tank, floating drum storage, gas cylinders, and gasbags. Storing the biogas reduces the problem of low flow rate during cooking. Biogas can be transported from one place to another by using gasbags [18,52,72,136,137,138]. The excess pressure in the storage container can be released using a ‘T’ shaped valve [72,139].
The amount of biogas produced in the digester depends on the material fed, type of the material, C/N ratio, digestion time, and temperature [50,140,141]. For instance, highly concentrated influent slows down the fermentation, and diluted influent causes scum formation. To keep the solids concentration, the amount of water and biomass added should be in equal proportion [11,142,143,144]. The digester should be fed every day. However, free fermentable carbohydrates will increase the volatile fatty acids concentration, which affects the methane forming bacteria. Usually, the steady state of biogas production is observed after two months of operation with a constant OLR [33,145].

4. Applications of Biogas in Household Digesters

4.1. Cooking and Heating

Biogas produced from the household digesters is mainly used for cooking [54,70]. The amount of biogas used for cooking purposes usually varies between 30 and 45 m3 per month. This number can be compared with other commonly used fuels such as kerosene where the consumption is between 15 and 20 L, and Liquefied Petroleum Gas (LPG) between 11 and 15 kg per month, respectively. The energy equivalent was around 300, 200, and 150 kWh for biogas, kerosene, and LPG, respectively [66,146,147]. The surplus biogas in the domestic digester could be used for water and space heating [148,149,150].

4.2. Biogas Stoves

Biogas burning is not possible in commercial butane and propane burners because of its physiochemical properties. However, it is possible to use these burners after some modifications [103]. Burners are changed in the gas injector, its cross-section, and mixing chambers. The biogas burners are designed to meet a mixture of bio-gas and air in the ratio of 1:10 [101]. Different burners like vertical flame diffuser, horizontal flame diffuser, and no diffuser with biogas have been examined. A vertical flame diffuser had a high heat transfer efficiency compared to other diffusers [68]. The efficiency is obtained by calculating the heat gained by the water subjected for heating and the amount of fuel consumed during this process. The efficiency of the heat entering the vessel from the stove was high for biogas with 57.4%, followed by LPG, kerosene, and wood with 53.6%, 49.5%, and 22.8%, respectively [151]. The biogas consumption and the thermal efficiency in the biogas stoves varied between 0.340–0.450 m3/h and 59–68% [67,145,152,153,154].

4.3. Fertilizer

The digestate left over from the digester is rich in nitrogen, phosphorus, and potassium, and can be used as a fertilizer [54,73]. Digestate increased the potato cultivation by 27.5% and forage by 1.5% compared to no added fertilizer. Due to the anaerobic digestion of organic matter, these nutrient concentrations were easily taken up by plants [71,116]. The effluent can be directly used as a fertilizer in farming [92]. Digestate has a high commercial value when exported. The dried effluent could also be used as an adsorbent to remove lead from industrial wastewater [155]. Biogas slurry could be helpful in growing algae, water hyacinth [101], duck weed [156], and fish poly-aquaculture [157,158].

4.4. Lighting and Power Generation

The other major application of household biogas is for lighting and power generation. In many developed countries, biogas from the digesters is sent to a combustion engine to convert it into electrical and mechanical energy [64]. Biogas requires a liquid fuel to start ignition [13]. Diesel fuel can also be combined with biogas for power generation [159,160,161,162,163]. For instance, in Pura (India), a well-studied community biogas digester can fuel a modified diesel engine and run an electric generator [164]. Bari [160] reported that carbon dioxide up to 40% will not decrease the engine performance using biogas as a fuel. Biogas can also be used to power engines when mixed with petrol or diesel, and it can also help in pumping water for irrigation [66,165,166,167]. Cottage/small scale industries use biogas for pumping, milling, and for some other production activities [168].
For a medium-sized farm in Jordan, the monthly energy consumption for various purposes is about 1282 kWh. The biogas required for producing 982 kWh is around 6.7 m3/day, and for water-heating 2 m3/day. The use of 1 kW generator proved that half of the energy needed could be met by using a domestic digester. Satisfactory results were observed when tested for water-heating and electricity generation from biogas [60,61]. In Earth University (USA), electricity from biogas is used for milking operations [169]. Biogas is blended with jatropha oil in a 12 kW diesel engine generator to act as a dual fuel for rural electrification. Jatropha seeds remain as a waste product after oil production. This waste gets converted into biogas. The oil and biogas is combined in a duel fuel engine for electricity generation [13]. The fertilizer from biogas is used for jatropha plantation. Hence, the nutrients are in the closed cycle, which can act as a bio-refinery [170]. Biogas conversion into electricity using fuel cells is a hot research topic nowadays. However, it is not commercially affordable due to the requirement of clean gas and the cost of fuel cells [103].
Biogas lamps are more efficient than the kerosene powered lamps, but the efficiency is quite low compared to electric-powered lamps. However, the light intensity of the biogas lamp compared to a kerosene lamp or an electric light bulb, was in the power range of 25–75 W [145]. One cubic meter of biogas is equal to lighting 60–100 watt bulb for 6 h, or cooking three meals a day for 5–6 persons. In contrast, 0.7 kg of petrol can run 1 hp motor for 2 h or generate 1.25 kW for electricity [171]. To provide electricity for a home with a family of five, about 0.25 to 0.5 m3 biogas is needed [66]. Until recently, many of the rural areas in India depended on kerosene lamps for lighting due to the energy shortage. Using these kerosene-powered lamps was inefficient as well costly. Battery-operated solar panels were also an expensive means for lighting. This resulted in research to design a digester, which could provide lighting to a home. A mini-biogas digester developed especially for lighting purposes. This digester could produce 0.5 m3/day biogas which is enough for 4 h of use [63].

4.5. Other Applications

Besides common applications, domestic biogas is also utilized for other purposes. Gas-powered refrigerators or a chicken incubator can run on household biogas, which is a well known application in Kenya [98,145]. In India, around 4600 public toilets are connected to biogas digesters by a local NGO to improve social living conditions of the people. Similarly, in Nepal, public toilets are connected to biogas digesters to light these toilets [98,172].

5. Disadvantages

Despite the various advantages of household biogas digesters, there are a few disadvantages to overcome as well. Anaerobic digestion is a slow process, and it requires a long HRT (>30 days) [16]. This increases the volume and cost of the digester. Low loading rates and slow recovery after a failure are other limitations in biogas production [173]. Another limitation is the fluctuation in temperature throughout the year. The decrease in biogas production during the winter months makes it difficult for cold countries to adapt this technology [30]. In the long-run, people often stop using the household digesters due to lack of knowledge, gas leakage, slow recovery, low gas production, and inadequate supply of substrate [174]. Research into these issues is needed. For instance, straw is a potential substrates for household biogas digesters, but it demands more research and development [175].
Leakage from biogas digesters increases emissions of methane and carbon dioxide into the environment. Fire explosions in households are another disadvantage when methane leaks from the digester [40].
Individual economic status is also a concern in biogas technology [176]. Sibisi and Green [98] installed a floating drum digester in a school to meet their energy needs. However, it was impossible for the school to spend a capital investment unless a governmental subsidy was provided. In Thailand, high investment, lack of financial resources, lack of information, and lack of skilled labor are barriers towards adopting biogas stoves, and household biogas digesters [177,178].
Developments in technology can help to rectify these problems by making biogas sustainable for rural energy production. However, low functionality of biogas plants due to defective components, lack of technical knowledge, not adopting a proper size and model based on locality and availability of raw materials, poor supervision, and lack of NGO involvement continue to present obstacles to technology dissemination [91]. It is important to spread basic knowledge among farmers and local people in order to train and educate them about the potential of biogas technology [179].

6. Economics and Policies

Most biogas digesters have lifetimes of 25–35 years [180,181]. The cost of these digesters varies from 200 to 400 USD. For instance, in Thailand a fixed dome model called cement water jar with a size of 1.2 m3 costs around 180 USD [66], in Peru a PVC tubular digester of volume 0.225 m3 costs around 250 USD [70] and a plug flow digester with a size of 0.250 m3 costs 300 USD in Costa Rica [90]. In India, the floating drum model of size 1–6 m3 costs from 200 to 400 USD respectively [66,70,88,90,182]. The payback period (PBP) for different digesters, including deenbandhu, KVIC, and janta models was calculated. The deenbandhu model had a lower PBP around 4.7 and 1.6 years for a digester of size 1 and 6 m3, followed by the janta model with 11.3 and 3.2, PBP and years, respectively, for the same size. The floating drum model had a high PBP of 26.6 for a 1 m3 digester [1]. Amigun and von Blottnitz [47] calculated the capital cost for different sizes of biogas digesters by using the Lang factor (fL). The results revealed that the fL value of 2.63 and 1.79 gives a better prediction for small/medium digesters and large plants, respectively. Rubab and Kandpal [183] calculated the capital cost using different methodologies, including economies of scale, ratio of size of a reference plant cost, cost of constituents, and the last method included factors like retention time and other important factors for capital cost calculations.
Different economic models to predict the cost of a digester and the cost of benefits obtained using a household biogas digester have been developed in the recent past. An economic model to assess the cost-effectiveness of domestic biogas plants was developed by [35,184,185], which is summarized in Equations (1), (2) and (4). The cost calculation of a biogas digester based on a reference plant is given in Equation (3). In Laboratory of Agricultural Structures (LAS) of the Agricultural University of Athens, an improved version of the original Basic Economic Evaluation Model were developed called Modified Basic Economic Evaluation Model (MBEEM). This model involves many parameters and a computer model was developed in order to facilitate the application of the MBEEM. According to the model, the optimum retention time from an economical point of view would be 20 days. The net present benefit increases with the increase in government subsidies, increase in fuel wood cost, and decrease in the cost of the digester. However, net present benefit gets affected if the interest rate is high. The financial stability of the digesters is increased with the increase in digester size. Cooking with firewood suppresses biogas cooking if the efficiency is more than 25%. The biogas plants will be in a critical position, if the cost of wood fuel decreases or the cost of dung increases. Ciotola et al. [169] conducted an energy analysis to assess the sustainability and environmental impact of small-scale digesters. They found that it was better to use biogas for cooking, but not for producing electricity using a generator. Environmental Sustainability Index (ESI) is a way to measure the total sustainability of a process and Environmental Loading Ratio (ELR) is a method to estimate how much impact a process has on the environment. A high ELR corresponds to a high environmental stress. ESI was reduced from 5.67 to 2.22 due to production of electricity from biogas. At the same time, ELR was increased from 0.52 to 0.93.
Equation 1. Model for net present benefit for the digesters in Bangladesh, where PW- present worth of the incremental net benefit, Ag—Annual incremental benefit from using biogas as cooking fuel, Af—Annual incremental benefit from using treated slurry as fertilizer, C—Cost of digester, N—Plant life, and W—Inflation rate/Interest rate [184]:
P W = ( A g + A f ) n = 1 N W n C n = 1 N m n W n
Equation 2. Model for the cost benefit analysis in India for floating drum model, where NPV—Net Present Value, Ab—Annual benefits, Ac—Annual operating costs, i—interest rate, t—life time of the plant, C—Cost of the digester [185].
N P V = ( A b A c ) [ 1 ( 1 + i ) t ] i C
Equation 3. Generalized cost calculation for a biogas digester, C—Cost of the digeter, CO—Cost of the reference plant, a and b are constants, V—Volume of the digester, Vo—Volume of the reference digester [185]:
C = C 0 [ a + b ( V V 0 ) ]
Equation 4. Modified basic economical evaluation model for Greece, where NPV—Net Present Value (Euro), NCF—Net Cash Flow, r—discount rate, j—operational life span of installation (year), I—capital investment [35]:
N P V = j = 1 n [ N C F j × ( 1 + r ) j ] I
Pütz et al. [186] developed a morphological matrix to sell the biogas produced from the digester to the low-income farmers. Using the right methods to transport and sell biogas can yield a profit to both the seller and the buyer. Li et al. [5] calculated the ecological and environmental benefits by building a biogas digester by using a quantitative model. The equation to calculate economical and environmental benefits is given in Equations (5) and (6), respectively. The results showed that families that have a biogas digester could benefit by about 100 USD/digester. Peter et al. [187] developed an empirical model for the adoption of biogas technology, and the results showed that the adoption of technology is increasing with high income, more cattle owned, bigger homes and hike in fuel price. However, the adoption for biogas technology decreased with an increase in remote location and area of the household. Van Groenendaal and Gehua [188] analyzed the internal benefits which revealed that 58.5% of people who used a biogas digester could cook three meals a day and most of the people had improved health conditions. Feng et al. [189] calculated the efficiency of energy use for the rural households in Tibet. The comparison of the present scenario and the futuristic change revealed the importance of the biogas not only economically, but also by building a healthier and sustainable society.
Equation 5. Calculation for economical benefits of a digester, Tc—cost of economical benefits for a household, m—items consuming energy, n—kinds of energy resources, j—type of usage, i—type of resource, Ci—unit price for the type of energy [5]:
T c = j = 1 m   i = 1 n C i x i j ( i = 1 , 2 n , j = 1 , 2 m )
Equation 6. Calculations for environmental benefits of a digester, Ts—cost of environmental benefits for a household, m—items consuming energy, n—kinds of energy resources, j—type of usage, i—type of resource, S1i—Environmental costs in a hill, S2i—environmental costs in a slope [5]:
T s = j = 1 m   i = 1 n x i j ( S 1 i + S 2 i ) ( i = 1 , 2 n , j = 1 , 2 m )
Politicians and policymakers must promote efficient ways to meet energy needs in rural areas [190]. By having government subsidy plans and loan or credit schemes, the biogas program for rural households will be more attractive to people [33]. In China, the government pays two-thirds of the digester cost and the farmer pay the remaining amount. However, the construction of digesters decreased when the government reduced the subsidy to one-third of the cost [55]. Millions of people have benefited from this technology, and its popularity is still increasing [54]. Domestic biogas digester programs could be alive with the microfinance schemes available in the developing countries. This could help farmers and poor people to reduce the burden on capital cost investments [191].

7. Environmental and Social Aspects of Biogas Digesters

Climate change is one of the major environmental challenges facing the World today. Unsustainable energy consumption in past has contributed to global warming that needs to be addressed [192]. Household digesters could reduce the pressure on the environment by reducing deforestation and greenhouse gas emissions, soil erosion, loss of cultivable land [54].
A major contributor to global warming are greenhouse gases (GHG), emitted to the atmosphere mainly from burning fossil fuels such as coal, oil and natural gas. Rural biogas production can partially reduce global warming [193]. By utilizing biogas for rural households, environmental, economical, and social benefits were obtained [194]. Even though, both methane and carbon dioxide are major contributors to the greenhouse effect, the global warming potential of methane is 21 times higher than that of carbon dioxide [195]. However, the comparison of the houses equipped with and without biogas systems, including the leakage of gases in the biogas systems revealed that the households with biogas plants have 48% less emissions compared to households without biogas systems [196]. It is worth mentioning that only 10% of households had methane leakage [194]. Studies show that by replacing firewood and coal with biogas, the emission of CO2 and SO2 would be reduced by 397–4193 thousand tons, and 21.3–62.0 thousand tons, respectively [193]. Pathak et al. [193] reported that the global warming mitigation potential from a 3 m3 family size biogas plant in India using dung from four cattles was about 9.7 tons CO2 equivalent per year. The government of India targeted to install 12.34 million digesters by 2010. This target mitigation potential is equal to 120 million tons CO2 equivalent per year.
Hamburg [197] did a pilot-scale study on the emission of H2S and SO2 by using crop stalks, coal, and biogas for cooking in the regions of Henan province in China. The study revealed that the emission of SO2 using crop stalks and coal for cooking was four times higher than that of biogas. Additionally, no significant level of H2S was found. Khoiyangbam et al. [198] compared the methane emission effect of fixed dome biogas plants installed in the hilly areas of India. The studies showed that methane emission was higher for the janta model compared to the deenbandhu model. A family size biogas plant is a substitute for 316 L of kerosene, 5535 kg of wood and 4400 kg of cattle dung as fuels reducing emissions like NOx, SO2, CO, and volatile compounds into the atmosphere by 16.4, 11.3, 987.0, and 69.7 kg/year, respectively [199].
The slurry from the biogas digesters, if not used properly, becomes an active place for insects to spread diseases [200]. Biogas slurry could be used as a valuable resource for earthworm culture. Slurry mixed with plant rich materials, is also a suitable substrate for vermicomposting [201,202].
A comprehensive study to analyze the rural energy development in China using household-scale biogas digesters and green house gas emission reduction was done by Yu et al [22]. The greenhouse gas emissions from energy sources including straw, fuel wood, coal, refined oil, electricity, LPG, natural gas, and coal gas were compared to emissions from biogas. Biogas as a substitute for other energy sources reduced the greenhouse gases by 73.157 megatons CO2 equivalents based on the amount of consumption between the years 1991 to 2005.
Another study in the Peruvian Andes by Garfi et al [88] involving 12 rural families in a project to substitute biogas with firewood, showed a decrease of firewood consumption by 50%–60% and cooking time by 1 h. The results are based on a survey which included technical aspects such as type of fuel and time for cooking, environmental aspects such as number of cows in the households and amount of firewood used to cook and economical aspects including income of the family and the expenditure for fuel and fertilizer and social aspects such as time for collecting wood. The effect of the price on firewood, kerosene and fertilizer before and after installing the biogas plant from 2001 to 2005 in India is shown in Figure 4.
Cattle dung is usually used as compost or dung cakes for cooking, which is neither hygienic nor economical [1]. Burning dung cakes does not only creates pollution but also leads to loss of a valuable fertilizer. On the other hand, if the dung cake is applied directly to the field it would also cause total loss of fuel, besides the pollution [184]. Anaerobic digestion is a secure and high-profit yielding way to dispose of this cattle dung [1].
Figure 4. Costs of firewood, kerosene and fertilizer before and after installing the biogas digester from 2001 to 2005 in India [190].
Figure 4. Costs of firewood, kerosene and fertilizer before and after installing the biogas digester from 2001 to 2005 in India [190].
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In addition to environmental benefits, there are a number of social and health benefits using biogas as a fuel. Improved health conditions and change in lifestyle for women in the households were observed after installation of a biogas digester [33]. Hiremath et al. [203] mentioned that India could meet their energy demands by a decentralized energy planning. Using the locally available materials, they could fulfill their energy needs in a sustainable way. One of the possible alternatives to producing energy for rural India is biogas. The basic seven goals are: cost minimization, efficiency maximization, employment generation, system reliability, minimization of petroleum product, maximization use of local resource, and minimization of emissions. Biogas can improve sanitation considerably, when linked to a public toilet where waste is no longer stored [204,205]. Green foods (crops grown using fertilizer from biogas plants) were developed by connecting a biogas plant to a toilet and pigpen. This kind of integrated model is very popular in southern China [175]. One-third of the dung produced in India is enough to run 12 million biogas plants [206]. Use of biogas digesters by the rural people could help them financially as well as improve the living conditions such as improved air quality for the health benefits of the people [66].
For instance, burning firewood for cooking also creates a lot of smoke and soot particles. The smoke and soot contributes to air pollution which in turn causes health issues such as respiratory illness [54]. However, Zhang et al. [10] reported that more than 420,000 premature babies died in China every year due to indoor air pollution. Most of the pollution is due to poor combustion fuels and emitted greenhouse gases. The main reason for infant mortality and deaths in developing countries is respiratory diseases. Most of these diseases are due to pollution emission from cooking. In contrast, biogas is a clean fuel compared to biomass or coal combustion. Cleanliness here refers to the cooking vessel not turning black in the bottom of the vessel, when biogas is used for cooking. Air pollution in biogas will be less because they have few larger hydrocarbons. Increase in the concentration of hydrogen sulfide leads to headaches, dizziness, blurry vision, nausea, and vomiting. Sulfur dioxide emissions lead to choking and sneeze-inducing effects [197]. Sustainable energy production for rural-needs and proper sanitation has a significant difference on control of parasitic diseases [204,205]. Figure 5 shows the environmental and social benefits obtained by using a biogas digester.
Figure 5. Environmental and social benefits in using biogas digesters.
Figure 5. Environmental and social benefits in using biogas digesters.
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8. Discussion

Access to energy resources, economic development and environmental pollution, which in turn threaten human health, are major challenges facing developing countries today [207]. Economically feasible and efficient small scale biogas digesters could be the answer of solving some of these problems and needs. By enhancing energy availability and simultaneously protect the surrounding environment such as soil, water and air, a lots of benefits could be gained. Most of small-scale digesters are concentrated in developing countries with India and China as leading countries accounting for the highest share.
More or less, every biodegradable organic waste can be treated in a biogas digester, providing energy for cooking, lighting and heating along with increased of dissolved nutrient concentration in the digestate, thus, providing farmers with an improved organic fertilizer. Many of small scale digesters do not require high maintenance and are more or less adaptable to the climate and condition of many of developing countries [73]. However, adopting of biogas digesters is low in many countries despite the great potential to gain a wide verity of benefits, both from socioeconomic and environmental point of View. Possible negative impacts are suggested such as the potential for pathogens, limitation of economic and material resources, and pollution through losses from damaged digesters, and possible leakage of incomplete combustion of methane to CO2. Additionally several practical problem have also been suggested as limiting the uptake of small-scale digesters including unaffordable initial investment costs, accessibility of proper materials to avoid leakage in digester construction, lack of efficient functioning digesters in different climate condition, sufficient production of fuel to meet the needs, social acceptability of the fuel produced, etc. [208].
Studies showed that political measures are required to support adoption of the household digesters, by subsidy plans, including training and capacity building to keep up the interest in adopting the household digesters. However, the interesting paradox is, despite all the benefits that could be gained, the interest fades as soon as the governmental subsidy support is reduced, as the case in China which is the one of leading countries in adopting the biogas digesters. It seems the benefit from implementation of biogas digester alone is not enough to increase the attention. Further, full analysis are needed with a new approach to facilitate communication between the experts from different fields such as engineering, hydrology, biology, social science, economics and systems-modeling to identify and find the best possible optimum solution and strategies needed in implementing household biogas digesters in rural communities [208]. Furthermore, interest is growing slowly in many poor countries and effort should be made to increase the awareness and to introduce affordable and more efficient digesters tailored to take full advantage of the local possibilities in order to succeed.

9. Conclusions

Household digesters represent a boon for farmers and rural people to meet their energy needs. These digesters help in two ways: one is to reduce waste, and the other is to provide valuable energy. Although they have been used for many years, modernization is needed to overcome the drawbacks in the long run. The awareness by people of their technical issues, and governmental subsidy plans could provide even more benefits from household digesters.

Acknowledgments

This work was financed by the Sparbank foundation in Sjuhärad, Borås Energi and Environment AB and FOV Fabrics AB in Sweden.

References

  1. Singh, K.J.; Sooch, S.S. Comparative study of economics of different models of family size biogas plants for state of punjab, India. Energy Convers. Manag. 2004, 45, 1329–1341. [Google Scholar] [CrossRef]
  2. Amigun, B.; Sigamoney, R.; Von Blottnitz, H. Commercialisation of biofuel industry in Africa: A review. Renew. Sustain. Energy Rev. 2008, 12, 690–711. [Google Scholar] [CrossRef]
  3. Pagar Savita, D. Design, Development and Performance Evaluation of Biogas Stoves; Maharana Pratap University of Agriculture and Technology: Udaipur, India, 2008. [Google Scholar]
  4. Zhou, Z.; Wu, W.; Chen, Q.; Chen, S. Study on sustainable development of rural household energy in northern China. Renew. Sustain. Energy Rev. 2008, 12, 2227–2239. [Google Scholar] [CrossRef]
  5. Li, G.Z.; Niu, S.W.; Liang, Y.H. Estimate on the Ecological and Economic Benefits of Rural Household Biogas Construction Project in Loess Hilly Region, China. In Proceedings of International Conference on Wireless Communications: Networking and Mobile Computing, 21–25 September 2007; Volume 1–15, pp. 5075–5078.
  6. Li, G.; Niu, S.; Ma, L.; Zhang, X. Assessment of environmental and economic costs of rural household energy consumption in loess hilly region, gansu province, China. Renew. Energy 2009, 34, 1438–1444. [Google Scholar] [CrossRef]
  7. Parikh, J.K.; Parikh, K.S. Mobilization and impacts of bio-gas technologies. Energy 1977, 2, 441–455. [Google Scholar] [CrossRef]
  8. Starke, L. State of the World 2004; World Watch Institute: Washington, DC, USA, 2004. [Google Scholar]
  9. Ravindranath, N.H. Renewable Energy and Environment: A Policy Analysis for India; Tata McGraw-Hill Pub. Co.: Uttar Pradesh, India, 2000. [Google Scholar]
  10. Zhang, J.; Mauzerall, D.L.; Zhu, T.; Liang, S.; Ezzati, M.; Remais, J.V. Environmental health in China: Progress towards clean air and safe water. Lancet 2010, 375, 1110–1119. [Google Scholar] [CrossRef] [PubMed]
  11. NAS. Methane Generation from Human, Animal and Agricultural Waste; National Academy of Sciences: Washington, DC, USA, 1977. [Google Scholar]
  12. Bioenergylists. Available online: http://www.stoves.bioenergylists.org (accessed on 25 March 2012).
  13. Luijten, C.C.M.; Kerkhof, E. Jatropha oil and biogas in a dual fuel ci engine for rural electrification. Energy Convers. Manag. 2011, 52, 1426–1438. [Google Scholar] [CrossRef]
  14. Bhattacharya, S.C.; Abdul Salam, P.; Sharma, M. Emissions from biomass energy use in some selected asian countries. Energy 2000, 25, 169–188. [Google Scholar]
  15. Xiaohua, W.; Jingfei, L. Influence of using household biogas digesters on household energy consumption in rural areas—A case study in Lianshui County in China. Renew. Sustain. Energy Rev. 2005, 9, 229–236. [Google Scholar]
  16. Martins das Neves, L.C.; Converti, A.; Vessoni Penna, T.C. Biogas production: New trends for alternative energy sources in rural and urban zones. Chem. Eng. Technol. 2009, 32, 1147–1153. [Google Scholar] [CrossRef]
  17. VITA. Testing the Efficiency of Wood Burning Stoves: International Standards; Volunteers in Technical Assitance, Inc.: Arlington, TX, USA, 1985. [Google Scholar]
  18. Shian, S.-T.; Chang, M.-C.; Ye, Y.-T.; Chang, W. The construction of simple biogas digesters in the province of Szechwan, China. Agric. Wastes 1979, 1, 247–258. [Google Scholar] [CrossRef]
  19. McKendry, P. Energy production from biomass (part 2): Conversion technologies. Bioresour. Technol. 2002, 83, 47–54. [Google Scholar] [CrossRef] [PubMed]
  20. Hiremath, R.B.; Kumar, B.; Balachandra, P.; Ravindranath, N.H.; Raghunandan, B.N. Decentralised renewable energy: Scope, relevance and applications in the Indian context. Energy Sustain. Dev. 2009, 13, 4–10. [Google Scholar] [CrossRef]
  21. Itodo, I.N.; Agyo, G.E.; Yusuf, P. Performance evaluation of a biogas stove for cooking in nigeria. J. Energy S. Afr. 2007, 18, 14–18. [Google Scholar]
  22. Yu, L.; Yaoqiu, K.; Ningsheng, H.; Zhifeng, W.; Lianzhong, X. Popularizing household-scale biogas digesters for rural sustainable energy development and greenhouse gas mitigation. Renew. Energy 2008, 33, 2027–2035. [Google Scholar] [CrossRef]
  23. Singh, R.B. Bio-Gas Plant: Design with Specifications; Gobar Gas Research Station: Ajitmal, India, 1973. [Google Scholar]
  24. Singh, R.B. Bio-Gas Plant: Generating mEthane from Organic Wastes; Gobar Gas Research Station: Ajitmal, India, 1974. [Google Scholar]
  25. Sathianathan, M.A. Bio-Gas: Achievements & Challenges; Association of Voluntary Agencies for Rural Development: New Delhi, India, 1975. [Google Scholar]
  26. Meynell, P.J. Methane: Planning A Digester; Sochen Books: Prison Stable Court: Dorset, Clarington, ON, Canada, 1976. [Google Scholar]
  27. Santerre, M.T.; Smith, K.R. Measures of appropriateness: The resource requirements of anaerobic digestion (biogas) systems. World Dev. 1982, 10, 239–261. [Google Scholar] [CrossRef]
  28. Deublein, D.; Steinhauser, A. Biogas from Waste and Renewable Resources; Wiley Online Library: Weinheim, Germany, 2008. [Google Scholar]
  29. Gerardi, M.H. The Microbiology of Anaerobic Digesters; John Wiley & Sons: Chichester, UK, 2003; Volume 3. [Google Scholar]
  30. Yadvika; Santosh; Sreekrishnan, T.R.; Kohli, S.; Rana, V. Enhancement of biogas production from solid substrates using different techniques––A review. Bioresour. Technol. 2004, 95, 1–10. [Google Scholar] [CrossRef] [PubMed]
  31. Gijzen, H.J. Anaerobic digestion for sustainable development: A natural approach. Water Sci. Technol. 2002, 45, 321–328. [Google Scholar] [PubMed]
  32. Gijzen, H.J. Anaerobes, aerobes and phototrophs: A winning team for wastewater management. Water Sci. Technol. 2001, 44, 123–132. [Google Scholar] [PubMed]
  33. Green, J.M.; Sibisi, M.N.T. Domestic Biogas Digesters: A Comparative Study. In Proceedings of Domestic Use of Energy Conference, Cape Town, South Africa, 2–3 April 2002; pp. 33–38.
  34. Hall, D.O.; Moss, P.A. Biomass for energy in developing countries. Geojournal 1983, 7, 5–14. [Google Scholar] [CrossRef]
  35. Georgakakis, D.; Christopoulou, N.; Chatziathanassiou, A.; Venetis, T. Development and use of an economic evaluation model to assess establishment of local centralized rural biogas plants in Greece. Appl. Biochem. Biotechnol. 2003, 109, 275–284. [Google Scholar] [CrossRef] [PubMed]
  36. Jiang, X.; Sommer, S.G.; Christensen, K.V. A review of the biogas industry in China. Energy Policy 2011, 39, 6073–6081. [Google Scholar] [CrossRef]
  37. Thien Thu, C.T.; Cuong, P.H.; Hang, L.T.; Chao, N.V.; Anh, L.X.; Trach, N.X.; Sommer, S.G. Manure management practices on biogas and non-biogas pig farms in developing countries—Using livestock farms in Vietnam as an example. J. Clean. Prod. 2012, 27, 64–71. [Google Scholar] [CrossRef]
  38. Austin, G.; Morris, G. Biogas Production in Africa. In Bioenergy for Sustainable Development in Africa; Springer Netherlands: Dordrecht, The Netherlands, 2012; pp. 103–115. [Google Scholar]
  39. NDRC. Medium and Long-Term Development Plan for Renewable Energy in China; National Development and Reform Commission: Beijing, China, 2007.
  40. Khoiyangbam, R.S. Environmental implications of biomethanation in conventional biogas plants. Iran. J. Energy Environ. 2011, 2, 181–187. [Google Scholar]
  41. Sarkar, A.N. Research and development work in biogas technology. J. Sci. Ind. Res. 1982, 41, 279–291. [Google Scholar]
  42. Snv World. Available online: http://www.snvworld.org (accessed on 23 March 2012).
  43. U.S. Farm Anaerobic Digestion Systems: A 2010 Snapshot; EPA: Washington, DC, USA, 2010.
  44. Wilkinson, K.G. A comparison of the drivers influencing adoption of on-farm anaerobic digestion in Germany and Australia. Biomass Bioenergy 2011, 35, 1613–1622. [Google Scholar] [CrossRef]
  45. Raven, R.P.J.M.; Gregersen, K.H. Biogas plants in denmark: Successes and setbacks. Renew. Sustain. Energy Rev. 2007, 11, 116–132. [Google Scholar] [CrossRef]
  46. Iea-biogas. Available online: http://www.iea-biogas.net (accessed on 25 March 2012).
  47. Amigun, B.; von Blottnitz, H. Capital cost prediction for biogas installations in africa: Lang factor approach. Environ. Prog. Sustain. Energy 2009, 28, 134–142. [Google Scholar] [CrossRef]
  48. Africa Biogas. Available online: http://africabiogas.org (accessed on 23 March 2012).
  49. Parawira, W. Biogas technology in Sub-Saharan Africa: Status, prospects and constraints. Rev. Environ. Sci. Biotechnol. 2009, 8, 187–200. [Google Scholar] [CrossRef]
  50. Omer, A.M.; Fadalla, Y. Biogas energy technology in sudan. Renew. Energy 2003, 28, 499–507. [Google Scholar] [CrossRef]
  51. Bin, C. The current status of agricultural geothermal utilization in China. Biomass 1989, 20, 69–76. [Google Scholar] [CrossRef]
  52. Zhang, D. An analysis of domestic biogas storage installations in China. Biomass 1989, 20, 61–67. [Google Scholar] [CrossRef]
  53. Sasse, L.; Kellner, C.; Kimaro, A. Improved Biogas Unit for Developing Countries; Deutsche Gesellschaft für Technische Zusammenarbeit (GTZ) GmbH; Vieweg & Sohn Verlagsgesellschaft Braunschweig: Nairobi, Kilimani, 1991. [Google Scholar]
  54. Gautam, R.; Baral, S.; Herat, S. Biogas as a sustainable energy source in nepal: Present status and future challenges. Renew. Sustain. Energy Rev. 2009, 13, 248–252. [Google Scholar] [CrossRef]
  55. Daxiong, Q.; Shuhua, G.; Baofen, L.; Gehua, W. Diffusion and innovation in the Chinese biogas program. World Dev. 1990, 18, 555–563. [Google Scholar] [CrossRef]
  56. Tomar, S.S. Status of biogas plant in India. Renew. Energy 1994, 5, 829–831. [Google Scholar] [CrossRef]
  57. Adeoti, O.; Ilori, M.O.; Oyebisi, T.O.; Adekoya, L.O. Engineering design and economic evaluation of a family-sized biogas project in Nigeria. Technovation 2000, 20, 103–108. [Google Scholar] [CrossRef]
  58. Akinbami, J.F.K.; Ilori, M.O.; Oyebisi, T.O.; Akinwumi, I.O.; Adeoti, O. Biogas energy use in nigeria: Current status, future prospects and policy implications. Renew. Sustain. Energy Rev. 2001, 5, 97–112. [Google Scholar] [CrossRef]
  59. Anjan, K.K. Development and evaluation of a fixed dome plug flow anaerobic digester. Biomass 1988, 16, 225–235. [Google Scholar] [CrossRef]
  60. Aburas, R.; Hammad, M.; Abu-Reesh, I.; Hiary, S.E.; Qousous, S. Construction and operation of a demonstration biogas plant, problems and prospects. Bioresour. Technol. 1995, 53, 101–104. [Google Scholar] [CrossRef]
  61. Aburas, R.; Hammad, M.A.; Hiary, S.E.; Qousous, S.; Abu-Reesh, I. Construction and operation of a demonstration biogas plant, problems and prospects. Energy Convers. Manag. 1996, 37, 611–614. [Google Scholar] [CrossRef]
  62. Kanwar, S.S.; Gupta, R.K.; Guleri, R.L.; Singh, S.P. Performance evaluation of a 1 m3 modified, fixed-dome Deenbandhu biogas plant under hilly conditions. Bioresour. Technol. 1994, 50, 239–241. [Google Scholar] [CrossRef]
  63. Jash, T.; Basu, S. Development of a mini-biogas digester for lighting in India. Energy 1999, 24, 409–411. [Google Scholar] [CrossRef]
  64. Mohammad, N. Biogas plants construction technology for rural areas. Bioresour. Technol. 1991, 35, 283–289. [Google Scholar] [CrossRef]
  65. Werner, U.; Stöhr, U.; Hees, N. Biogas Plants in Animal Husbandry; Deutsches Zentrum für Entwicklungstechnologien-GATE: Bonn, Germany, 1989. [Google Scholar]
  66. Gosling, D. Biogas for thailand’s rural development: Transferring the technology. Biomass 1982, 2, 309–316. [Google Scholar]
  67. Singh, N.; Gupta, R.K. Community biogas plants in India. Biol. Wastes 1990, 32, 149–153. [Google Scholar] [CrossRef]
  68. Ferrer, I.; Garfí, M.; Uggetti, E.; Ferrer-Martí, L.; Calderon, A.; Velo, E. Biogas production in low-cost household digesters at the Peruvian Andes. Biomass Bioenergy 2011, 35, 1668–1674. [Google Scholar] [CrossRef]
  69. Bouallagui, H.; Ben Cheikh, R.; Marouani, L.; Hamdi, M. Mesophilic biogas production from fruit and vegetable waste in a tubular digester. Bioresour. Technol. 2003, 86, 85–89. [Google Scholar] [CrossRef] [PubMed]
  70. Ferrer, I.; Gamiz, M.; Almeida, M.; Ruiz, A. Pilot project of biogas production from pig manure and urine mixture at ambient temperature in Ventanilla (Lima, Peru). Waste Manag. (Oxf.) 2009, 29, 168–173. [Google Scholar] [CrossRef]
  71. Garfí, M.; Gelman, P.; Comas, J.; Carrasco, W.; Ferrer, I. Agricultural reuse of the digestate from low-cost tubular digesters in rural andean communities. Waste Manag. (Oxf.) 2011, 31, 2584–2589. [Google Scholar] [CrossRef]
  72. An, B.X.; Rodriguez, L.; Sarwatt, S.V.; Preston, T.R.; Dolberg, F. Installation and performance of low-cost polyethylene tube biodigesters on small-scale farms. Rev. Mond. Zootech. 1997, 88, 38–47. [Google Scholar]
  73. Lansing, S.; Botero, R.B.; Martin, J.F. Waste treatment and biogas quality in small-scale agricultural digesters. Bioresour. Technol. 2008, 99, 5881–5890. [Google Scholar] [CrossRef] [PubMed]
  74. Karagiannidis, A. Waste to Energy: Opportunities and Challenges for Developing and Transition Economies (Green Energy and Technology); Springer: Berlin, Germany, 2012. [Google Scholar]
  75. Kalia, A.K.; Kanwar, S.S. Long-term evaluation of a fixed dome Janata biogas plant in hilly conditions. Bioresour. Technol. 1998, 65, 61–63. [Google Scholar] [CrossRef]
  76. Agstar Guide to Operational Systems; U.S. Environmental Protection Agency: Washington, DC, USA, 2007.
  77. Lusk, P.D. Methane Recovery from Animal Manures: The Current Opportunities Casebook; National Renewable Energy Laboratory Colarado: Golden, CO, USA, 1998; Volume 3.
  78. Cantrell, K.B.; Ducey, T.; Ro, K.S.; Hunt, P.G. Livestock waste-to-bioenergy generation opportunities. Bioresour. Technol. 2008, 99, 7941–7953. [Google Scholar] [CrossRef] [PubMed]
  79. Beddoes, J.C.; Bracmort, K.S.; Burn, R.B.; Lazarus, W.F. An Analysis of Energy Production Costs from Anaerobic Digestion Systems on Us Livestock Production Facilities; Natural Resources Conservation Service: Washington, DC, USA, 2007.
  80. Moog, F.A.; Avilla, H.F.; Agpaoa, E.V.; Valenzuela, F.G.; Concepcion, F.C. Promotion and utilisation of polyethylene biodigester in smallhold farming systems in the Philippines. Livest. Res. Rural Dev. 1997, 9. [Google Scholar]
  81. Hamad, M.A.; Abdel Dayem, A.M.; El Halwagi, M.M. Evaluation of the performance of two rural biogas units of Indian and Chinese design. Energy Agric. 1981, 1, 235–250. [Google Scholar] [CrossRef]
  82. Kanwar, S.S.; Guleri, R.L. Performance evaluation of a family-size, rubber-balloon biogas plant under hilly conditions. Bioresour. Technol. 1994, 50, 119–121. [Google Scholar] [CrossRef]
  83. Singh, R.; Anand, R.C. Comparative performances of Indian small solid-state and conventional anaerobic digesters. Bioresour. Technol. 1994, 47, 235–238. [Google Scholar] [CrossRef]
  84. Safley, L.M., Jr.; Westerman, P.W. Performance of a low temperature lagoon digester. Bioresour. Technol. 1992, 41, 167–175. [Google Scholar] [CrossRef]
  85. Qi, X.; Zhang, S.; Wang, Y.; Wang, R. Advantages of the integrated pig-biogas-vegetable greenhouse system in north China. Ecol. Eng. 2005, 24, 175–183. [Google Scholar] [CrossRef]
  86. Anand, R.C.; Singh, R. A simple technique, charcoal coating around the digester, improves biogas production in winter. Bioresour. Technol. 1993, 45, 151–152. [Google Scholar] [CrossRef]
  87. Lansing, S.; Víquez, J.; Martínez, H.; Botero, R.; Martin, J. Quantifying electricity generation and waste transformations in a low-cost, plug-flow anaerobic digestion system. Ecol. Eng. 2008, 34, 332–348. [Google Scholar] [CrossRef]
  88. Garfí, M.; Ferrer-Martí, L.; Velo, E.; Ferrer, I. Evaluating benefits of low-cost household digesters for rural andean communities. Renew. Sustain. Energy Rev. 2012, 16, 575–581. [Google Scholar] [CrossRef]
  89. Xavier, S.; Nand, K. A preliminary study on biogas production from cowdung using fixed-bed digesters. Biol. Wastes 1990, 34, 161–165. [Google Scholar] [CrossRef]
  90. Lansing, S.; Martin, J.F.; Botero, R.B.; da Silva, T.N.; da Silva, E.D. Methane production in low-cost, unheated, plug-flow digesters treating swine manure and used cooking grease. Bioresour. Technol. 2010, 101, 4362–4370. [Google Scholar] [CrossRef] [PubMed]
  91. Singh, S.P.; Vatsa, D.K.; Verma, H.N. Problems with biogas plants in himachal pradesh. Bioresour. Technol. 1997, 59, 69–71. [Google Scholar] [CrossRef]
  92. Shyam, M.; Sharma, P.K. Solid-state anaerobic digestion of cattle dung and agro-residues in small-capacity field digesters. Bioresour. Technol. 1994, 48, 203–207. [Google Scholar] [CrossRef]
  93. Polprasert, C.; Edwards, P.; Rajput, V.S.; Pacharaprakiti, C. Integrated biogas technology in the tropics 1. Performance of small-scale digesters. Waste Manag. Res. 1986, 4, 197–213. [Google Scholar] [CrossRef]
  94. Singh, L.; Maurya, M.S.; Ramana, K.V.; Alam, S.I. Production of biogas from night soil at psychrophilic temperature. Bioresour. Technol. 1995, 53, 147–149. [Google Scholar] [CrossRef]
  95. Singh, L.; Maurya, M.; Ram, M.S.; Alam, S. Biogas production from night soil: Effects of loading and temperature. Bioresour. Technol. 1993, 45, 59–61. [Google Scholar] [CrossRef]
  96. Stevens, M.A.; Schulte, D.D. Low temperature anaerobic digestion of swine manure. J. Environ. Eng. Div. 1979, 105, 33–42. [Google Scholar]
  97. Misra, U.; Singh, S.; Singh, A.; Pandey, G.N. A new temperature controlled digester for anaerobic digestion for biogas production. Energy Convers. Manag. 1992, 33, 983–986. [Google Scholar] [CrossRef]
  98. Sibisi, N.T.; Green, J.M. A floating dome biogas digester: Perceptions of energising a rural school in Maphephetheni, Kwazulu-Natal. J. Energy S. Afr. 2005, 16, 45–52. [Google Scholar]
  99. Ramana, K.V.; Singh, L. Microbial degradation of organic wastes at low temperatures. Def. Sci. J. Newdelhi 2000, 50, 382–390. [Google Scholar]
  100. Jayashankar, B.C.; Kishor, J.; Goyal, I.C.; Sawhney, R.L.; Sodha, M.S. Solar assisted biogas plants iv: Optimum area for blackening and double glazing over a fixed-dome biogas plant. Int. J. Energy Res. 1989, 13, 193–205. [Google Scholar] [CrossRef]
  101. Subramanian, S.K. Bio-Gas Systems in Asia; Management Development Institute: Newdelhi, India, 1977; Volume 11. [Google Scholar]
  102. Singh, D.; Singh, K.K.; Bansal, N.K. Heat loss reduction from the gas holder/fixed gas dome of a community-size biogas plant. Int. J. Energy Res. 1985, 9, 417–430. [Google Scholar] [CrossRef]
  103. Bond, T.; Templeton, M.R. History and future of domestic biogas plants in the developing world. Energy Sustain. Dev. 2011, 15, 347–354. [Google Scholar] [CrossRef]
  104. Shah, N. The role of bio-energy utilisation in sustainable development. Int. J. Glob. Energy Issues 1997, 9, 365–381. [Google Scholar]
  105. Mata-Alvarez, J.; Macé, S.; Llabrés, P. Anaerobic digestion of organic solid wastes. An overview of research achievements and perspectives. Bioresour. Technol. 2000, 74, 3–16. [Google Scholar] [CrossRef]
  106. Yen, H.-W.; Brune, D.E. Anaerobic co-digestion of algal sludge and waste paper to produce methane. Bioresour. Technol. 2007, 98, 130–134. [Google Scholar] [CrossRef] [PubMed]
  107. Murto, M.; Björnsson, L.; Mattiasson, B. Impact of food industrial waste on anaerobic co-digestion of sewage sludge and pig manure. J. Environ. Manag. 2004, 70, 101–107. [Google Scholar] [CrossRef]
  108. Gelegenis, J.; Georgakakis, D.; Angelidaki, I.; Mavris, V. Optimization of biogas production by co-digesting whey with diluted poultry manure. Renew. Energy 2007, 32, 2147–2160. [Google Scholar] [CrossRef]
  109. Llabrés-Luengo, P.; Mata-Alvarez, J. Influence of temperature, buffer, composition and straw particle length on the anaerobic digestion of wheat straw-pig manure mixtures. Resour. Conserv. Recycl. 1988, 1, 27–37. [Google Scholar] [CrossRef]
  110. Li, R.; Chen, S.; Li, X.; Saifullah Lar, J.; He, Y.; Zhu, B. Anaerobic codigestion of kitchen waste with cattle manure for biogas production. Energy Fuels 2009, 23, 2225–2228. [Google Scholar] [CrossRef]
  111. Lansing, S.; Martin, J.F.; Botero, R.B.; Nogueira da Silva, T.; Dias da Silva, E. Wastewater transformations and fertilizer value when co-digesting differing ratios of swine manure and used cooking grease in low-cost digesters. Biomass Bioenergy 2010, 34, 1711–1720. [Google Scholar] [CrossRef]
  112. Garfí, M.; Ferrer-Martí, L.; Perez, I.; Flotats, X.; Ferrer, I. Codigestion of cow and guinea pig manure in low-cost tubular digesters at high altitude. Ecol. Eng. 2011, 37, 2066–2070. [Google Scholar] [CrossRef]
  113. Levi, K.L.; Dorothy, M. Assessment of the effect of mixing pig and cow dung on biogas yield. Agric. Eng. Int.: CIGR J. 2009, 11, 1–7. [Google Scholar]
  114. Preston, R.L. Feed composition tables. Beef Mag. 2010, 47–54. [Google Scholar]
  115. Khandelwal, K.C.; Maithani, P.C. Guide to Family Size Biogas Plants; Department of Non-Conventional Energy Sources: New Delhi, India, 1989.
  116. Garfí, M.; Ferrer-Martí, L.; Villegas, V.; Ferrer, I. Psychrophilic anaerobic digestion of guinea pig manure in low-cost tubular digesters at high altitude. Bioresour. Technol. 2011, 102, 6356–6359. [Google Scholar] [CrossRef] [PubMed]
  117. An, B.X.; Preston, T.R. Gas production from pig manure fed at different loading rates to polyethylene tubular biodigesters. Livest. Res. Rural Dev. 1999, 11. [Google Scholar]
  118. Nijaguna, B.T. Biogas Technology; New Age International: Delhi, India, 2006. [Google Scholar]
  119. Staffen, R.; Sudar, O.; Braun, R. Feedstock for Anaerobic Digestion; AD-NETT: Herning, Denmark, 2000. [Google Scholar]
  120. Kalia, A.K.; Singh, S.P. Horse dung as a partial substitute for cattle dung for operating family-size biogas plants in a hilly region. Bioresour. Technol. 1998, 64, 63–66. [Google Scholar] [CrossRef]
  121. Sai Ram, M.; Singh, L.; Alam, S. Effect of sulfate and nitrate on anaerobic degradation of night soil. Bioresour. Technol. 1993, 45, 229–232. [Google Scholar] [CrossRef]
  122. Chandra, R.; Takeuchi, H.; Hasegawa, T.; Kumar, R. Improving biodegradability and biogas production of wheat straw substrates using sodium hydroxide and hydrothermal pretreatments. Energy 2012, 43, 273–282. [Google Scholar] [CrossRef]
  123. Carlsson, M.; Uldal, M. Substrathandbok för Biogasproduktion; Svenskt Gastekniskt Center: Malmö, Sweden, 2009. [Google Scholar]
  124. Zvinavashe, E.; Elbersen, H.W.; Slingerland, M.; Kolijn, S.; Sanders, J.P.M. Cassava for food and energy: Exploring potential benefits of processing of cassava into cassava flour and bioenergy at farmstead and community levels in rural mozambique. Biofuels Bioprod. Biorefining 2011, 5, 151–164. [Google Scholar] [CrossRef]
  125. Cuzin, N.; Farinet, J.L.; Segretain, C.; Labat, M. Methanogenic fermentation of cassava peel using a pilot plug flow digester. Bioresour. Technol. 1992, 41, 259–264. [Google Scholar] [CrossRef]
  126. Zhang, Q.; He, J.; Tian, M.; Mao, Z.; Tang, L.; Zhang, J.; Zhang, H. Enhancement of methane production from cassava residues by biological pretreatment using a constructed microbial consortium. Bioresour. Technol. 2011, 102, 8899–8906. [Google Scholar] [CrossRef] [PubMed]
  127. De Baere, L. Anaerobic digestion of solid waste: State-of-the-art. Water Sci. Technol. 2000, 283–290. [Google Scholar]
  128. Pang, Y.Z.; Liu, Y.P.; Li, X.J.; Wang, K.S.; Yuan, H.R. Improving biodegradability and biogas production of corn stover through sodium hydroxide solid state pretreatment. Energy Fuels 2008, 22, 2761–2766. [Google Scholar] [CrossRef]
  129. Zhang, R.; El-Mashad, H.M.; Hartman, K.; Wang, F.; Liu, G.; Choate, C.; Gamble, P. Characterization of food waste as feedstock for anaerobic digestion. Bioresour. Technol. 2007, 98, 929–935. [Google Scholar] [CrossRef] [PubMed]
  130. Hessami, M.A.; Christensen, S.; Gani, R. Anaerobic digestion of household organic waste to produce biogas. Renewable Energy 1996, 9, 954–957. [Google Scholar] [CrossRef]
  131. Christensen, S. Appropriate Technology Methods for the Anaerobic Digestion of Organic Household Waste; Monash University: Clayton, Australia, 1995. [Google Scholar]
  132. Muñoz, R.; Guieysse, B. Algal–bacterial processes for the treatment of hazardous contaminants: A review. Water Res. 2006, 40, 2799–2815. [Google Scholar] [CrossRef] [PubMed]
  133. O’Sullivan, C.; Rounsefell, B.; Grinham, A.; Clarke, W.; Udy, J. Anaerobic digestion of harvested aquatic weeds: Water hyacinth (Eichhornia crassipes), Cabomba (Cabomba caroliniana) and Salvinia (Salvinia molesta). Ecol. Eng. 2010, 36, 1459–1468. [Google Scholar] [CrossRef]
  134. Jash, T.; Ghosh, D.N. Studies on residence time distribution in cylindrical and rectangular biogas digesters. Energy 1990, 15, 987–991. [Google Scholar] [CrossRef]
  135. Martí-Herrero, J. Reduced hydraulic retention times in low-cost tubular digesters: Two issues. Biomass Bioenergy 2011, 35, 4481–4484. [Google Scholar] [CrossRef]
  136. Ezekoye, V.A.; Okeke, C.E. Design, construction, and performance evaluation of plastic biodigester and the storage of biogas. Pac. J. Sci. Technol. 2006, 7, 176–184. [Google Scholar]
  137. Moulik, T.K.; Srivastava, U.K.; Shingi, P.M. Bio-Gas System in India: A Socio-Economic Evaluation; Centre for Management in Agriculture, Indian Institute of Management: Ahmedabad, India, 1978. [Google Scholar]
  138. Aguilar, F.X. How to Install a Polyethylene Biogas Plant; Royal Agricultural College: Cirencester, UK, 2001. [Google Scholar]
  139. Rodriguez, L.; Preston, T. Biodigester Installation Manual; Food & Agriculture Organization: Roma, Italia, 2001. [Google Scholar]
  140. Chynoweth, D.P.; Owens, J.M.; Legrand, R. Renewable methane from anaerobic digestion of biomass. Renew. Energy 2001, 22, 1–8. [Google Scholar] [CrossRef]
  141. Schwart, R.; Jackson, R.; Herbst, B.; Whitney, R.; Lacewell, R.; Mjelde, J. Methane Generation; Department of Agricultural Economics, Texas A&M University: Galveston, TX, USA, 2005. [Google Scholar]
  142. Barnett, A.; Pyle, L.; Subramanian, S.K. Biogas Technology in the Third World: A Multi-Disciplinary Review; International Development Research Centre: Ottawa, Canada, 1978. [Google Scholar]
  143. Buren, A.V. A Chinese Biogas Manual; Intermediate Technology Publications: Rugby, UK, 1979. [Google Scholar]
  144. Van Buren, A.; Pyle, L.; Crook, M. A Chinese Biogas Manual: Popularising Technology in the Countryside; Intermediate Technology Publications: Rugby, UK, 1979. [Google Scholar]
  145. Laichena, J.K.; Wafula, J.C. Biogas technology for rural households in Kenya. OPEC Rev. 1997, 21, 223–244. [Google Scholar] [CrossRef]
  146. Heltberg, R. Household Fuel and Energy Use in Developing Countries—A Multicountry Study; Oil and Gas Policy Division, The World Bank: Washington, DC, USA, 2003. [Google Scholar]
  147. United Nations Development Programme (UNDP). Access of the Poor to Clean Household Fuels in India; The World Bank: Washington, DC, USA, 2003; p. 94. [Google Scholar]
  148. Axaopoulos, P.; Panagakis, P. Energy and economic analysis of biogas heated livestock buildings. Biomass Bioenergy 2003, 24, 239–248. [Google Scholar] [CrossRef]
  149. Tasdemiroglu, E. Economics of biogas space heating systems in rural Turkey. Bioresour. Technol. 1991, 36, 147–155. [Google Scholar] [CrossRef]
  150. He, P.J. Anaerobic digestion: An intriguing long history in China. Waste Manag. (Oxf.) 2010, 30, 549–550. [Google Scholar] [CrossRef]
  151. CES. Efficiency Measurement of Biogas, Kerosene and Lpg Stoves; Tribhuvan University: Kathmandu, Nepal, 2001. [Google Scholar]
  152. Chan, U.S. State of the Art Review on the Integrated Use of Anaerobic Processes in China; International Reference Center for Waste Disposal: Dubendorf, Switzerland, 1982. [Google Scholar]
  153. Chandra, A.; Tiwari, G.N.; Srivastava, V.K.; Yadav, Y.P. Performance evaluation of biogas burners. Energy Convers. Manag. 1991, 32, 353–358. [Google Scholar] [CrossRef]
  154. Kurchania, A.K.; Panwar, N.L.; Pagar, S.D. Development of domestic biogas stove. Biomass Convers. Biorefin. 2011, 1, 99–103. [Google Scholar] [CrossRef]
  155. Namasivayam, C.; Yamuna, R. Waste biogas residual slurry as an adsorbent for the removal of Pb (ii) from aqueous solution and radiator manufacturing industry wastewater. Bioresour. Technol. 1995, 52, 125–131. [Google Scholar] [CrossRef]
  156. Rodríguez, L.; Preston, T.R. Use of effluent from low-cost plastic biodigesters as fertilizer for duck weed ponds. Livest. Res. Rural Dev. 1996, 8. Number 2. [Google Scholar]
  157. Balasubramanian, P.; Kasturi Bai, R. Biogas-plant effluent as an organic fertiliser in fish polyculture. Bioresour. Technol. 1994, 50, 189–192. [Google Scholar] [CrossRef]
  158. Integrated Agriculture-Aquaculture: A Primer; Food & Agriculture Organization, International Center for Living Aquatic Resources Management and International Institute of Rural Reconstruction: Silang, Philippines, 2001.
  159. Duc, P.M.; Wattanavichien, K. Study on biogas premixed charge diesel dual fuelled engine. Energy Convers. Manag. 2007, 48, 2286–2308. [Google Scholar] [CrossRef]
  160. Bari, S. Effect of carbon dioxide on the performance of biogas/diesel duel-fuel engine. Renew. Energy 1996, 9, 1007–1010. [Google Scholar] [CrossRef]
  161. Henham, A.; Makkar, M.K. Combustion of simulated biogas in a dual-fuel diesel engine. Energy Convers. Manag. 1998, 39, 2001–2009. [Google Scholar] [CrossRef]
  162. Tippayawong, N.; Promwungkwa, A.; Rerkkriangkrai, P. Long-term operation of a small biogas/diesel dual-fuel engine for on-farm electricity generation. Biosyst. Eng. 2007, 98, 26–32. [Google Scholar] [CrossRef]
  163. Tippayawong, N.; Promwungkwa, A.; Rerkkriangkrai, P. Durability of a small agricultural engine on biogas/diesel dual fuel operation. Iran. J. Sci. Technol. 2010, 34, 167–177. [Google Scholar]
  164. Reddy, A.K.N. Lessons from the pura community biogas project. Energy Sustain. Dev. 2004, 8, 68–73. [Google Scholar] [CrossRef]
  165. Jawurek, H.H.; Lane, N.W.; Rallis, C.J. Biogas/petrol dual fuelling of si engine for rural third world use. Biomass 1987, 13, 87–103. [Google Scholar] [CrossRef]
  166. Khadi and Village Industries Commission and Its Non-Conventional Energy Programmes; Khadi and Village Industries Commission: Bombay, India, 1993.
  167. Lichtman, R.J. Biogas Systems in India; Volunteers in Technical Assistance: Arlington, VA, USA, 1983. [Google Scholar]
  168. Vijay, V.K.; Prasad, R.; Singh, J.P.; Sorayan, V.P.S. A case for biogas energy application for rural industries in India. Renew. Energy 1996, 9, 993–996. [Google Scholar] [CrossRef]
  169. Ciotola, R.J.; Lansing, S.; Martin, J.F. Emergy analysis of biogas production and electricity generation from small-scale agricultural digesters. Ecol. Eng. 2011, 37, 1681–1691. [Google Scholar] [CrossRef]
  170. Butterworth, B. Biofuels from waste: Closed-loop sustainable fuel production. Refocus 2006, 7, 60–61. [Google Scholar] [CrossRef]
  171. Kristoferson, L.A.; Bokalders, V. Renewable Energy Technologies—Their Application in Developing Countries; ITDG Publishing: London, UK, 1991. [Google Scholar]
  172. Batzias, F.; Sidiras, D.; Spyrou, E. Evaluating livestock manures for biogas production: A GIS based method. Renew. Energy 2005, 30, 1161–1176. [Google Scholar] [CrossRef]
  173. Tang, W.Z. Physicochemical Treatment of Hazardous Wastes; Lewis publisher: Boca Raton, FL, USA, 2004. [Google Scholar]
  174. Wijesinghe, L.C.A.D.S.; Chandrasiri, J.A. Operating experience with biogas plants in Sri Lanka. Nat. Resour. Forum 1986, 10, 221–229. [Google Scholar] [CrossRef]
  175. Chen, Y.; Yang, G.; Sweeney, S.; Feng, Y. Household biogas use in rural China: A study of opportunities and constraints. Renew. Sustain. Energy Rev. 2010, 14, 545–549. [Google Scholar] [CrossRef]
  176. Ni, J.Q.; Nyns, E.J. New concept for the evaluation of rural biogas management in developing countries. Energy Convers. Manag. 1996, 37, 1525–1534. [Google Scholar] [CrossRef]
  177. Limmeechokchai, B.; Chawana, S. Sustainable energy development strategies in the rural thailand: The case of the improved cooking stove and the small biogas digester. Renew. Sustain. Energy Rev. 2007, 11, 818–837. [Google Scholar] [CrossRef]
  178. Day, D.L.; Chen, T.H.; Anderson, J.C.; Steinberg, M.P. Biogas plants for small farms in Kenya. Biomass 1990, 21, 83–99. [Google Scholar] [CrossRef]
  179. Ru-Chen, C. The development of biogas utilization in China. Nat. Resour. Forum 1981, 5, 277–282. [Google Scholar] [CrossRef]
  180. Mukherjee, K.K. Gobar Gas Plant—A Study; Gandhi Peace Foundation: New Delhi, India, 1974. [Google Scholar]
  181. Three Cubic-Meter Bio-Gas Plant: A Construction Manual; Volunteers in Technical Assistance: Arlington, VA, USA, 1979.
  182. Hyman, E.L. Fuel substitution and efficient woodstoves-are they the answers to the fuelwood supply problem in northern nigeria. Environ. Manag. 1994, 18, 23–32. [Google Scholar] [CrossRef]
  183. Rubab, S.; Kandpal, T.C. Cost of anaerobic digestion technology: Household biogas plants in India. Int. J. Energy Res. 1995, 19, 675–685. [Google Scholar] [CrossRef]
  184. Bala, B.K.; Hossain, M.M. Economics of biogas digesters in bangladesh. Energy 1992, 17, 939–944. [Google Scholar] [CrossRef]
  185. Kandpal, T.C.; Joshi, B.; Sinha, C.S. Economics of family sized biogas plants in India. Energy Convers. Manag. 1991, 32, 101–113. [Google Scholar] [CrossRef]
  186. Pütz, K.; Asfaw, A.; Leta, B.; Müller, J. Biogas as Business-Biogas Transport Technology and Economic Concept for Developing Countries. In Proceedings of Conference on International Research on Food Security, Natural Resource Management and Rural Development, Bonn, Germany, 5–7 October, 2011.
  187. Peter, N.W.; Mugisha, J.; Drake, L. Biogas energy from family-sized digesters in Uganda: Critical factors and policy implications. Energy Policy 2009, 37, 2754–2762. [Google Scholar] [CrossRef]
  188. Van Groenendaal, W.; Gehua, W. Microanalysis of the benefits of China’s family-size bio-digesters. Energy 2010, 35, 4457–4466. [Google Scholar] [CrossRef]
  189. Feng, T.; Cheng, S.; Min, Q.; Li, W. Productive use of bioenergy for rural household in ecological fragile area, panam county, tibet in China: The case of the residential biogas model. Renew. Sustain. Energy Rev. 2009, 13, 2070–2078. [Google Scholar] [CrossRef]
  190. Agoramoorthy, G.; Hsu, M.J. Biogas plants ease ecological stress in India’s remote villages. Hum. Ecol. 2008, 36, 435–441. [Google Scholar] [CrossRef]
  191. Sunderasan, S. Positive externalities of domestic biogas initiatives: Implications for financing. Renew. Sustain. Energy Rev. 2008, 12, 1476–1484. [Google Scholar] [CrossRef]
  192. Bilen, K.; Ozyurt, O.; Bakırcı, K.; Karslı, S.; Erdogan, S.; Yılmaz, M.; Comakl, O. Energy production, consumption, and environmental pollution for sustainable development: A case study in Turkey. Renew. Sustain. Energy Rev. 2008, 12, 1529–1561. [Google Scholar] [CrossRef]
  193. Pei-dong, Z.; Guomei, J.; Gang, W. Contribution to emission reduction of CO2 and SO2 by household biogas construction in rural China. Renew. Sustain. Energy Rev. 2007, 11, 1903–1912. [Google Scholar] [CrossRef]
  194. Yang, J.; Chen, W.; Chen, B. Impacts of biogas projects on agro-ecosystem in rural areas—A case study of gongcheng. Front. Earth Sci. 2011, 5, 1–6. [Google Scholar] [CrossRef]
  195. Cuéllar, A.D.; Webber, M.E. Cow power: The energy and emissions benefits of converting manure to biogas. Environ. Res. Lett. 2008, 3. [Google Scholar] [CrossRef]
  196. Dhingra, R.; Christensen, E.R.; Liu, Y.; Zhong, B.; Wu, C.-F.; Yost, M.G.; Remais, J.V. Greenhouse gas emission reductions from domestic anaerobic digesters linked with sustainable sanitation in rural China. Environ. Sci. Technol. 2011, 45, 2345–2352. [Google Scholar] [CrossRef] [PubMed]
  197. Hamburg, R.A. Household cooking fuel hydrogen sulfide and sulfur dioxide emissions from stalks, coal and biogas. Biomass 1989, 19, 233–245. [Google Scholar] [CrossRef]
  198. Khoiyangbam, R.S.; Kumar, S.; Jain, M.C.; Gupta, N.; Kumar, A.; Kumar, V. Methane emission from fixed dome biogas plants in hilly and plain regions of northern India. Bioresour. Technol. 2004, 95, 35–39. [Google Scholar] [CrossRef] [PubMed]
  199. Pathak, H.; Jain, N.; Bhatia, A.; Mohanty, S.; Gupta, N. Global warming mitigation potential of biogas plants in India. Environ. Monit. Assess. 2009, 157, 407–418. [Google Scholar] [CrossRef] [PubMed]
  200. Surindra, S. Potential of domestic biogas digester slurry in vermitechnology. Bioresour. Technol. 2010, 101, 5419–5425. [Google Scholar] [CrossRef] [PubMed]
  201. Suthar, S. Bioremediation of agricultural wastes through vermicomposting. Biorem. J. 2009, 13, 21–28. [Google Scholar]
  202. Suthar, S. Nutrient changes and biodynamics of epigeic earthworm Perionyx excavatus (Perrier) during recycling of some agriculture wastes. Bioresour. Technol. 2007, 98, 1608–1614. [Google Scholar] [CrossRef] [PubMed]
  203. Hiremath, R.B.; Kumar, B.; Balachandra, P.; Ravindranath, N.H. Sustainable bioenergy production strategies for rural India. Mitig. Adapt. Strateg. Glob. Chang. 2010, 15, 571–590. [Google Scholar] [CrossRef]
  204. Remais, J.; Chen, L.; Seto, E. Leveraging rural energy investment for parasitic disease control: Schistosome ova inactivation and energy co-benefits of anaerobic digesters in rural China. PLoS One 2009, 4, e4856. [Google Scholar] [CrossRef] [PubMed]
  205. Biogas Digest; Information and Advisory Service on Appropriate Technology, Deutsche Gesellschaft für Technische Zusammenarbeit: Eschborn, Germany, 1999.
  206. Kashyap, D.R.; Dadhich, K.S.; Sharma, S.K. Biomethanation under psychrophilic conditions: A review. Bioresour. Technol. 2003, 87, 147–153. [Google Scholar] [CrossRef] [PubMed]
  207. Zhang, Z. Digester Comparison Study; The California Energy Commission and Commonwealth Energy Corporation: Santa Ana, CA, USA, 2003. [Google Scholar]
  208. Smith, J.U. The Potential of Small-Scale Biogas Digesters to Alleviate Poverty and Improve Long Term Sustainability of Ecosystem Services in Sub-Saharan Africa; University of Aberdeen, Institute of Biological and Environmental Science: Aberdeen, UK, 2012. [Google Scholar]

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Rajendran, K.; Aslanzadeh, S.; Taherzadeh, M.J. Household Biogas Digesters—A Review. Energies 2012, 5, 2911-2942. https://doi.org/10.3390/en5082911

AMA Style

Rajendran K, Aslanzadeh S, Taherzadeh MJ. Household Biogas Digesters—A Review. Energies. 2012; 5(8):2911-2942. https://doi.org/10.3390/en5082911

Chicago/Turabian Style

Rajendran, Karthik, Solmaz Aslanzadeh, and Mohammad J. Taherzadeh. 2012. "Household Biogas Digesters—A Review" Energies 5, no. 8: 2911-2942. https://doi.org/10.3390/en5082911

APA Style

Rajendran, K., Aslanzadeh, S., & Taherzadeh, M. J. (2012). Household Biogas Digesters—A Review. Energies, 5(8), 2911-2942. https://doi.org/10.3390/en5082911

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