Bioenergy production from different kinds of wastewaters

Methanogenic anaerobic digestion is a classical anaerobic bioconversion process that has been practiced for over a century and used in full-scale facilities worldwide. This is a complicated process that involves a mixture of population of microorganisms and several gasses and liquid products, thus strict process control and product purification are required. Biogas production have been demonstrated in numerous studies with great success like can see in the Table 6 (Gavrilescu, 2005).

COD

CH4 Yield

Wastewater

Reactor

HRT

OLR

removal

(%)

Reference

Type

(days)

(kg COD/m3-d)

(m3/kg COD)

Brewage

UASB

16.5-44.0

80

16.5

Shin et al.,

distillery

(1992)

Cane-

molasses

AFB

5.6-32

4.65-20

85

0.168

Yeoh

stillage

(1997)

Cheese whey

Hybrid

10

98

Malaspina

and dairy

reactor

et al (1996)

Cheese whey

Hybrid

0.97-2.82

91-97

0.28-0.35

Strydom et

and dairy

reactor

al (1997)

Cheese whey

CSTR

2.0

5

90

Ince

and dairy

(1998)

Cheese whey and dairy

CSTR

4-7

0.55

Yilmazer y Yeningum (1999)

Landfill

leachate

AFB

4.7-16

2.41-7.98

>90

Lin (1990)

Table 6. Typical performance of anaerobic reactor used for wastewater treatment (Gavrilescu, 2005)

3. Biogas production from agro-industrial wastewaters

3.1 Case vinasses of tequila

Tequila is a Mexican regional alcoholic beverage obtained from the fermentation of sugars from the cooked stems of blue agave (Agave tequilana Weber var. azul). Its production and

commercialization is verified and certified by the Mexican Tequila Regulatory Council (CRT) (NOM-006-SCFI-2005, 2006). In 2008 the CRT registered 139 producers and 1,018 brands of Tequila (bottled in Mexico and in foreign countries, CRT 2008). Based on the number of employees, only 7% are large factories and the rest are small and medium factories, with a grand total of around 30,500 direct employees (National Tequila Industry Chamber, CNIT 2009). Therefore, this industry represents an important economic activity for the 180 Mexican municipalities within the appellation d’origine controlee granted in 1995 for Tequila.

Tequila production has had an important increase from 2004 to 2008, as it is shown in Fig. 3. In 2010 about 187.3 million liters of Tequila (55% Alc. Vol.) has been produced with a projection for annual growth of at least 10% (CNIT 2010); there is also a decrease in production of Tequila between 2000 and 2003, due to the agave crisis (Dalton 2005). Although exhaustive reviews regarding the treatment of different distillery wastewaters are published elsewhere (Satyawali and Balakrishnan 2008; Mohana et al. 2009), it is considered that special attention should be paid to distillery effluents from the Tequila industry due to their complex composition. This section present the potential generation of energy from wastewater treatments to generate biogas from the Tequila industry.

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rSb d djb <& А Л A8 rh flo A fib rib ilb

& & & & & # &

Year

Fig. 3. Dynamics of Tequila production (55% Alc. Vol.). (calculated from CNIT 2010)

The production of Tequila generates large quantities of bagasse and vinasses. Bagasse is a residual solid; it is generated in the elaboration of Tequila and is produced during the extraction of juice from the cooked heads of agave. Vinasses are the liquid residues that are generated and remain in the bottom of the still after the distillation of the must of fermented agave.

liter of Tequila produced, 1.4 kg of bagasse and 10-12 L of vinasses are generated. Under this basis of calculation, it is estimated that the production of Tequila in 2010 generated 262.2 million kilograms of bagasse and 1,873.0 million liters of vinasses.

In the majority of the Tequila factories, bagasse is converted into compost, which is also done in the agave plantations. However, approximately 80% of the vinasses are discharged directly into water bodies (rivers, streams, lakes, reservoirs) and municipal sewer systems or directly onto the soil without receiving adequate treatment for discharge. This common practice causes a deterioration of different degrees to the water bodies receiving the discharges due to low pH, high temperature and elevated concentrations of both BOD and COD of these effluents. On the contrary, if the vinasses receive appropriate treatment and management, they can be used as a source of nutrients and organic matter in agricultural activities; they can also be a potential source of renewable energy. A summary of the physicochemical characteristics of the vinasses generated from the process of producing traditional Tequila (100% agave) is shown in Table 7 (Lopez-Lopez, 2010).

Parameter

Value

ph

3.4-4.5

Oils and fats (mg/L)

10-100

Total COD (mg/L)

60,000-100,000

Soluble COD (mg/L)

40,000-80,000

Total BOD (mg/L)

35,000-60,000

Soluble BOD (mg/L)

25,000-50,000

Total solids (mg/L)

25,000-50,000

Total suspended solids (mg/L)

2,000-8,000

Fixed suspended solids (mg/L)

10-500

Volatile suspended solids (mg/L)

1,990-7,500

Total dissolved solids (mg/L)

23,000-42,000

Settleable solids (mL/L)

10-900

Total alkalinity (mg/L)

< 6.00

Total acidity (mg/L)

1,500-6,000

Fixed acidity (mg/L)

1,480-5,800

Volatile acidity (mg/L)

20-200

Ca (mg/L)

200-1,100

Mg (mg/L)

100-300

K (mg/L)

150-650

Phosphates (mg/L)

100-700

Total nitrogen (mg/L)

20-50

NH4+-nitrogen (mg/L)

15-40

Organic nitrogen (mg/L)

5.0-10

Total reducing sugars (% w)

0.5-2.0

Direct sugars (% w)

0.4-1.0

Cu (mg/L)

< 3.0

Fe (mg/L)

< 45

Ni (mg/L)

< 0.02

Zn (mg/L)

< 1.0

Table 7. Physicochemical characteristics of Tequila vinasses (Lopez-Lopez 2010)

The anaerobic biological process has been utilized for treating Tequila vinasses on laboratory, pilot and industrial scales due to technical and economical advantages over aerobic processes (Linerio and Guzman 2004; Mendez, et al. 2009). On a laboratory scale, Lopez-Lopez and coworkers (2011), Mendez and coworkers (2009) showed an anaerobic digester capable of removing 90-95% of organic material as COD; generating significant amounts of biogas rich in methane. The most common system found at an industrial level in treating Tequila vinasses is of anaerobic type. Fig.4 shows the amount of energy that can be generated if the entire volume of vinasses is treated.

image014

Fig. 4. Production of biogas from Tequila vinasses as a source of energy