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Brazilian Archives of Biology and Technology

versão impressa ISSN 1516-8913versão On-line ISSN 1678-4324

Braz. arch. biol. technol. vol.61 no.spe Curitiba  2018  Epub 22-Out-2018 

Smart Energy

Storage of purified biogas (biomethane) at low pressure

Michael Feroldi1  3  * 

Andressa Caroline1  3 

Neves, Carlos Eduardo Borba2 

Mabel Karina Arantes3 

Alves Helton José1  3 

1Universidade Estadual do Oeste do Paraná - Mestrado em Engenharia de Energia na Agricultura, Departamento de Energia na Agricultura, Cascavel, Paraná, Brasil.

2Universidade Estadual do Oeste do Paraná - Departamento de Engenharia Química, Toledo, Paraná, Brasil.

3Universidade Federal do Paraná - Laboratório de Catálise e Produção de Biocombistíveis, Palotina, Paraná, Brasil.


The global use of fossil energy sources has led to the need to develop technologies capable of mitigating its consequences. One such option is anaerobic biodigestion, which is already scientifically well-established, although the use of its main products (biogas and biomethane) still requires further development before they can be employed in automotive vehicles, largely due to technical issues concerning their storage. The storage of methane using adsorption (Adsorbed Natural Gas - ANG) is a technology that requires less energy and moderate pressures and temperatures. However, the main storage techniques continue to be those that involve high pressures and/or cryogenic temperatures. The present work evaluates the performance of an unprecedented prototype developed by UFPR for the storage of methane by adsorption, employing commercial activated carbon. The factorial design (2²) indicated that the storage capacity of the system was 39.41 V /V using activated carbon, and the desorption process was effective at 60ºC. Thus, the use of adsorbents of low cost and easy access can provide very interesting results (>100 V / V), which contributes to make the technology viable.

Keywords: Adsorption; biogas; vehicle fuel


The problems associated with the dependence on fossil energy sources, especially petroleum and its derivatives, has increasingly stimulated the development of technologies capable of using biomass for energy production.

Biogas, which can be obtained from a variety of raw materials, is mainly used in direct combustion or in generators for electric power production, and its use in the transport sector has been studied in recent years1.

There are many processes in which biogas could be used, but there is an urgent need to resolve the difficulties likely to hinder its viable implementation. The calorific value of biogas is the key factor for its use in energy conversion, and for this reason, different purification techniques are used for methane enrichment, especially involving the removal of CO2 and H2S 2.

When the methane content reaches around 96%, the properties of biogas become similar to those of natural gas (a fossil fuel). Therefore, purified biogas can be easily employed as a substitute or together with natural gas in automotive vehicles3.

Despite the slow pace of development, the vehicular use of purified biogas (biomethane) has great technological potential, since systems that currently use natural gas (CNG) could shift to the use of biomethane4,5,6.

In order to achieve advances in this industrial sector, it is necessary to develop and improve technologies for the transportation and storage of gaseous fuels including natural gas and methane. Among these techniques, adsorption on porous adsorbent solids (ANG - Adsorbed Natural Gas) has attracted considerable interest, since it is less expensive due to the use of moderate pressures and room temperature.

Many solid adsorbent materials can be used for the storage of natural gas/methane, although activated carbon is most extensively used industrially, because it is readily available and can be produced from a wide range of precursor materials7.

Advances in research in Brazil are needed in various areas of fuel production and use, considering the needs of small-scale industries and consumers. Adsorbents that are sufficiently abundant and accessible for use in small-scale systems are of particular interest, and one option is the use of activated carbon for methane storage, which is the focus of the present work.


Given the need for development of the use of gaseous fuels in the vehicular sector, the aims of this work were to construct a methane storage system and to evaluate the storage of methane fuel on activated carbon, considering operational loading/unloading parameters of the system.


Methane storage tests were performed using commercial activated carbon with particle diameter of 3-5 mm (6x10 mesh). The material was dried in an oven at 100ºC for 24 h prior to each storage test, in order to avoid interference from moisture.


N 2 Physisorption

The textural characteristics of the carbon used were determined by adsorption/desorption isotherms obtained at liquid nitrogen temperature, employing a Quantachrome Nova 2000e instrument. The samples were pretreated at 200ºC for 4 h under vacuum in order to remove any moisture and/or organic species adsorbed on the surface of the material. Determination of the predominant porous structure (microporous, mesoporous, or macroporous) employed the specific surface area and pore volume, using the BET (Brunauer-Emmett-Teller) method, and pore diameter was determined by the BJH (Barrett- Joyner-Halenda) adsorption method.

Scanning Electron Microscopy

Scanning electron microscopy was used to determine the morphology and average size of the particles. The powdered samples were spread onto a double-sided carbon tape attached to the sample holder, then dried and sputter-coated with a thin layer of gold. The micrographs were obtained at several magnifications, in backscattering mode.


The tests were performed in the Laboratory of Catalysis and Biofuels Production (LabCatProBio) of the Federal University of Paraná (Palotina Sector). Pure commercial methane was injected into an unprecedented storage system consisting of a cylinder and a low volume compressor pump, and was subsequently released by heating in an oven at 60ºC for total desorption of the gas. The storage tests employed a maximum pressure of 10 bar. The pressure and temperature were controlled and measured with a manometer and thermocouples, respectively, connected to the cylinder filled with the adsorbent.

The tests were carried out according to a 2² factorial design with triplicates at the central point, varying the adsorption temperature and the rate of methane injection, as shown in Table 1.

Table 1 2² factorial design for the adsorption tests 

Test Temperature Flow rate
Codified ºC Codified mL s -1
1 -1 20 -1 3.65
2 +1 40 -1 3.65
3 -1 20 +1 7.3
4 +1 40 +1 7.3
5 0 30 0 5.54
6 0 30 0 5.54
7 0 30 0 5.54

After reaching the required pressure (10 bar), the amount of gas stored was obtained by weighing the system, recording the mass difference between the cylinder + adsorbent and the cylinder + adsorbent + CH4, after which the cylinder was emptied. The mass values were transformed into the volume of methane stored according to the volume of the cylinder (V/V). Finally, the system was heated at the previously established temperature of 60 ºC for total removal of the adsorbed methane molecules from the pores of the adsorbent, regenerating the material for a subsequent adsorption cycle.


Figure 1 shows the particles of activated carbon, and Table 2 provides their textural characteristics.

Figure 1 Activated carbon (6x10 mesh). 

Table 2 Textural properties of the activated carbon 

Sample S BET (m 2 g -1 ) Pore volume (cm 3 g -1 ) Average pore width (Å) (BJH)
6X10 774.84 0.4532 35.62

It can be seen from Table 2 that the activated carbon had a high specific area, which could be attributed to the high pore volume. The average pore diameter was in the mesopore range, according to the IUPAC classification8(mesopores: 20-500 Å), but with close proximity to the micropore range. Figure 2 shows the isotherms obtained for the activated carbon, which could be classified as type IV, characteristic of mesoporous solids.

Figure 2 Adsorption/desorption isotherms for the activated carbon. 

The pore volume distribution was monomodal, with a well-defined maximum (Fig. 3). The pore diameters were concentrated in the range below 200 Å, with the greatest frequency at around 35 Å, as also found in the BJH textural analysis.

Figure 3 Pore volume distribution of the activated carbon (dV (logD) cm3 g -1 ). 

The SEM micrographs (Fig. 4) revealed that the activated carbon consisted of particles ranging from 1 to 20 µm in size, with irregular shapes.

Figure 4 SEM images of the activated carbon at magnifications of (A) 5000x and (B) 10000x. 

After application of the factorial design in the experiments, the adsorbed methane mass storage capacities were obtained, which were converted to the volume of methane adsorbed according to the volume of the cylinder (V/V), as shown in Table 3, which also provides the results for the test using an empty cylinder (in the absence of adsorbent).

Table 3 Storage capacity of the activated carbon for methane (V/V) 

Test Sample
1 32.84
2 22.99
3 39.41
4 26.28
5 31.04
6 29.56
7 29.66
Empty Cylinder 13.14

The volume of the storage cylinder was approximately 0.465 L and the tests using the activated carbon enabled attainment of a final volume of methane of 18.3 L (Test 3) at a pressure of 10 bar. In comparison with the test using an empty cylinder (without adsorbent), CH4 storage tripled, confirming the contribution of the bed filled with activated carbon.

A preliminary study of the efficiency of gas release was performed in order to determine the lowest temperature capable of achieving complete desorption of methane from the gas-solid system. This study showed that successful desorption was obtained at 60ºC.

In order to analyze the performance of the adsorption study and to determine the effects of the variables tested (temperature and flow rate), Pareto charts and response surface graphs were generated for the values (in liters) obtained in the tests, as shown in Figures 5 and 6.

Figure 5 Pareto chart for the experimental design using activated carbon. 

Figure 6 Response surface for the experimental design using activated carbon. 

The statistical analyses revealed the significance of both variables in the methane storage assays, according to the Pareto chart (Fig. 5), while the interaction of the variables did not show any significant positive effect. The best results were mainly achieved at lower temperatures, which could be explained by the exothermic nature of the adsorption process, with decrease of the temperature of the adsorption system thermodynamically favoring maintenance of the strengths of the active sites present in the carbon used.

A study was also undertaken to determine the performance of the activated carbon in sequential tests at 10 bar, using analyses of surface area and pore volume. After the tests, there was loss of only about 1.5% of the pore volume available for storage of CH4. These results indicated that there were no substantial changes in the structural characteristics of the carbon after the CH4 storage tests, and that the material could be reused without loss of its adsorption capacity.


Since activated carbons possess highly porous structures, typically with specific areas varying between 500 and 3000 m2 g-1, they are widely used in adsorption processes9. In the specific case of gas adsorption, as in this work (adsorption of methane), the activated carbon should present both micropores and mesopores, in order to facilitate the phenomenon of gas-solid diffusion. According to Antoniou et al.10, this characteristic favors a high capacity for adsorption of methane molecules.

The present findings also demonstrated that even after several sequential tests at 10 bar pressure, the carbon presented excellent mechanical resistance, since there were no significant losses in terms of specific area or pore volume, evidencing the potential for reuse of the material.

Therefore, the activated carbon met the requirements for a satisfactory methane adsorption process, since the average pore diameter was around 35 Å, corresponding to the lower mesopore range, with the additional presence of micropores.

Various studies have described the use of carbon as adsorbent in the methane adsorption process, but the systems used operated under pressures (around 35 bar) higher than employed in the present work. Here, an alternative low cost technique is proposed, suitable for small-scale operations, and the low working pressure (10 bar) provided a high storage yield, compared to other studies. For example, Prauchner and Rodríguez-Reinoso11and Perrin et al.12achieved storage capacities of ~75 and 95 V/V, respectively, using activated carbon at 35 bar pressure, while in the present work the capacity achieved was ~48 and ~38% of the earlier values, respectively, but using only 28.6% of the pressure.

Another aspect of adsorption systems that should be considered is the desorption efficiency, since desorption is an endothermic process that requires a source of energy. After a preliminary study of desorption, a temperature of 60 ºC was considered ideal for total desorption of the methane present in the activated carbon. It should be noted that high efficiencies are more difficult to achieve in larger-scale systems, as described by Sahoo et al.13, who reported efficiencies below 93% using a temperature of 80ºC.


This work reports the successful storage of CH4 at low pressure (10 bar) on a low cost adsorbent, tripling the storage capacity of the cylinder. In addition, the activated carbon could be effectively reused in sequential cycles, without showing any significant alterations in its structural characteristics.

The best CH4 storage capacities were obtained at lower temperatures, due to the exothermic nature of the adsorption phenomenon.

The findings are important for the development of potential biogas/biomethane applications, especially in the vehicular sector, opening a range of possible scenarios for use of these fuels and contributing to the development of the sector.


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Received: December 21, 2017; Accepted: August 01, 2018

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