The present paper underlines the necessity of valorification for residual waters in the context of using them as source for biogas production inside anaerobic fermentation processes. Relative to this aspect, there will be presented a comparative approach for two types of residual waters from Timisoara city (residual water from the treatment plant and from beer factory), both in combination with residual dehydrated sludge and cow whey. Conclusions will be traced relative to the used materials in terms of general properties (physical and chemical), anaerobic fermentation process and quantity and quality for the produced biogas

Adrian Eugen Cioabla

Lucia Varga

CiteSeerX

http://www.revistadechimie.ro REV.CHIM.(Bucharest)♦ 67♦ No.1♦ 2016174
Comparative Determination of Cofermentation Using Residual
Waters for Biogas Production at Small Scale
LUCIA VARGA, ADRIAN EUGEN CIOABLA*, IOANA IONEL
Politehnica University of Timisoara, Mechanical Engineering Faculty, 1 Mihai Viteazu Av., 300222, Timisoara, Romania
The present paper underlines the necessity of valorification for residual waters in the context of using them
as source for biogas production inside anaerobic fermentation processes. Relative to this aspect, there will
be presented a comparative approach for two types of residual waters from Timisoara city (residual water
from the treatment plant and from beer factory), both in combination with residual dehydrated sludge and
cow whey. Conclusions will be traced relative to the used materials in terms of general properties (physical
and chemical), anaerobic fermentation process and quantity and quality for the produced biogas.
Keywords: residual waters, biogas, anaerobic fermentation
The rapid development of human society increased the
energy demands, which will led to the depletion of
conventional energy sources [1].
Residual biomass as: organic domestic, garden and
agro-industrial wastes, crop residues, manure, wastewater
sludges, offers a huge potential for the production of
renewable energy [2-4]. Anaerobic digestion of residual
biomass has attracted much interest in recent years. This
technology offers great potential for rapid disintegration of
organic matter to produce biogas and save fossil energy
[5-8].
The biogas produced by digestion is a clean and
environmentally friendly fuel, with a CH4 content of about
55–65%. Other constituents include 30–40% of CO2,
fractions of water vapour, traces of H2S and H2, and possibly
other contaminants (e.g. siloxanes).
Anaerobic digestion was first considered as an
inefficient and unreliable treatment process applicable to
a limited number of substrates, but now it has received
increased attention during the last few years [9].
Management of the organic fraction of urban solid waste
using anaerobic procedures will contribute to the reduction
of greenhouse gas emissions, and using biogas, which is a
carbon neutral energy, to generate electrical energy will
eventually help in reducing the combustion of fossil fuels.
The methane content of biogas varies between 50 - 70%
depending on feedstock. It has an energy content
equivalent to about two-third of that of natural gas and can
be burnt in stationary engines or turbines to generate heat
and electricity; in many cases the methane drives an
engine and Combined Heat and Power (CHP) plants
generates electricity and heat as by-product.
Biogas can be compressed and stored, and its quality
can be improved by removing CO2 using chemical
methods.
The production of biogas through anaerobic digestion
offers significant advantages over other forms of waste
treatment, including [5]:
-less biomass sludge is produced in comparison to
aerobic treatment technologies;
-successful in treating wet wastes of less than 40% dry
matter;
-more effective pathogen removal – this is especially
true for multi-stage digesters or if a pasteurization step is
* email: adrian.cioabla@upt.ro
included in the process;
-minimal odor emissions as 99% of volatile compounds
are oxidatively decomposed upon combustion, e.g. H2S
forms SO2;
-high degree of compliance with many national waste
strategies implemented to reduce the amount of
biodegradable waste entering landfill;
-the slurry produced (digestate) is an improved fertilizer
in terms of both its availability to plants and its rheology;
-a source of carbon neutral energy is produced in the
form of biogas.
The composition of these wastewaters depends on the
source and its characteristics, but the main constituents
are: organic matter, nutrients (nitrogen, phosphorus and
potassium), inorganic matter (dissolved minerals), toxic
chemicals and pathogens [10]. Releasing of an untreated
wastewater effluent into environment can have negative
impact on ecosystem and human health. Now, there are
varieties of strategies used to treat the wastewaters [11-
14].
Experimental part
Substrate choices and general information regarding the
used materials
 The base materials used were mixtures composed by
the following:
- first glass vessel: residual water from the treatment
plant, 4% dehydrated sludge from treatment plant and 5%
cow whey;
- second glass vessel: residual water from the beer
factory, 4% dehydrated sludge from treatment plant and
5% cow whey.
The general properties of the two materials are
presented below. The determinations were made
according to standard methods [15-20].
The fermentation process was held between 40 and 50
days in order to observe the pH and gas quantities and
composition in terms of CH4 and CO2 percentages
maintaining a constant temperature between 36 and 37
°C.
In order to correct the pH values during the process, it
was used a solution of NH3, 20% concentration.
The general overview of the small-scale installation is
REV.CHIM.(Bucharest)♦ 67♦ No.1♦ 2016 http://www.revistadechimie.ro 175
presented in figure 1.
The components of the small-scale installation are:
1 – thermal glass vessels with a total volume of 6L used
for dark fermentation;
2 – magnets positioned at the bottom of the glass
vessels used for magnetic stirring of the used material
suspensions; this system allows also the manual stirring /
agitation;
3 – device used for heating the suspension inside the
glass vessels;
4 – thermocouple used for temperature control inside
the fermentation vessels;
5 – system for sampling and pH correction of the
suspensions inside the vessels;
6 – syringe used for sampling and pH correction system;
7 - pH controllers connected to pH sensors inside the
glass vessels in order to determine in real time the pH value
of the suspension;
8 – temperature controller connected with the
thermocouple inside the glass vessel for temperature
control to a determined range;
9 – gas bags with a total volume of 2L dedicated for
sampling the obtained biogas from the fermentation
process.
Results and discussion
The tested batch of material consisted, as described
above, in parallel measurement for a mixture composed
from 91% residual water from the treatment plant, 4%
dehydrated sludge from treatment plant and 5% cow whey
Table 1
 GENERAL CHARACTERISTICS OF
THE USED MATERIALS (PART 1)
Table 2
GENERAL CHARACTERISTICS
OF THE USED MATERIALS
(PART 2)
Fig. 1. Overall view of the small-scale
installation
http://www.revistadechimie.ro REV.CHIM.(Bucharest)♦ 67♦ No.1♦ 2016176
for the first vessel and 91% residual water from the beer
factory, 4% dehydrated sludge from treatment plant and
5% cow whey for the second glass vessel.
The pH of the suspension was corrected with a solution
of NH3 20% concentration and the temperature regime was
held inside the domain of 36 – 37 °C.
The time variation for pH is presented in figure 2.
It can be observed that during the process, the batches
presented a relatively high pH value which made the use
of the NH3 suspension to be made just at the beginning of
the process when the starting pH was not neutral.
During the tests, the produced biogas was measured
both in terms of quality and quantity.
The gas analyzer used for this task was a DELTA 1600 S
IV type, which allows determination of methane and carbon
dioxide composition up to 100% by volume.
The CH4 and CO2 concentrations are presented in figure
3, 4.
It is mentioned that the four values for the first reactor
and the five values consiedered for the second reactor are
corresponding to the mean value read over 10 days of
process, and because of this reason the measurement was
divided in four periods of 10 days each. For the second
reactor there were made two readings in the last period of
measurements.
The produced quantities were about 4 L of gas for the
mixture with 91% residual water from the treatment plant,
4% dehydrated sludge from treatment plant and 5% cow
whey and about 5 L for the batch composed by 91% residual
water from beer factory, 4% dehydrated sludge from
treatment plant and 5% cow whey.
Conclusions
Even if both batches produced biogas, the main
composition of the produced gas until the end of process
was about 60 - 61% CH4 and 38 - 40% CO2 for both batches
of material.
From the determinations it can be observed that the
batch composed by 91% residual water from beer factory,
4% dehydrated sludge from treatment plant and 5% cow
Fig. 2. pH variation
Fig. 3. CH4 and CO2 concentrations for the first vessel (residual
water from the treatment plant, 4% dehydrated sludge from
treatment plant and 5% cow whey)
Fig. 4.
CH4 and CO2
concentrations
for the second
vessel (residual
water from beer
factory, 4%
dehydrated
sludge from
treatment plant
and 5% cow
whey)
whey has a slightly higher biogas quantity produced during
the process, while the first batch composed from 91%
residual water from the treatment plant, 4% dehydrated
sludge from treatment plant and 5% cow whey and about
5 L.
Both biogas quality and quantity depend on the organic
concentration inside the used material, this being a good
indicator that the residual water from beer factory has a
higher concentration in biodegradable materials.
Acknowledgements: This work was supported by a grant of the
Romanian National Authority for Scientific Research and Innovation,
CNCS - UEFISCDI, project number PN-II-RU-TE-2014-4-1043
References
1.ILUÞIU – VARVARA, D. A., Environ. Eng. Manag. J., (EEMJ), 9, no. 6,
2010, p. 813.
2.CIOABLA, A.E., IONEL, I.; TENCHEA, A., DUMITREL, G.A., PODE, V.,
Rev. Chim. (Bucharest), 64, 2013, p. 186.
3.CIOABLA, A.E.; IONEL, I.; BISORCA, D.; NEAMT, I.; DUMITREL, G.A.,
J. Eniron. Prot. Ecol., 14, 2013, p. 1777.
4.CIOABLA, A.E.; IONEL, I.; DUMITREL, G.A.; NEGREA, P.; PODE, V.,
Rev. Chim. (Bucharest), 63, no. 6, 2012, p. 629.
5.WARD, A. J., HOBBS, P. J., HOLLIMAN, P.J., JONES, D. L., Bioresource
Technol., 99, 2008, p. 7928.
6.GERIN, P. A., VLIEGEN, F., JOSSART, J.-M., Bioresource Technol., 99,
2008, p. 2620.
7.ZHANG, R., EL-MASHAD, H. M., HARTMAN, K., WANG, F., LIU, G.,
CHOATE, C., GAMBLE, P., Bioresource Technol., 98, 2007, p. 929.
8.JINGURA, R. M., MATENGAIFA, R., Renew. Sustain. Energy Rev., 13,
2009, p. 1116.
9.HARTMANN, H., AHRING, B. K., Water Res., 39(8), 2005, p. 1543.
10.KALBAR, P. P., KARMAKAR, S., ASOLEKAR, S. R., J. Environ. Manage.,
113, 2012, p. 158.
11.GOGATE, P. R., PANDIT, A. B., Adv. Environ. Res., 8, 3–4, 2004,
p.501.
12.GOGATE, P. R., PANDIT, A. B., Adv. Environ. Res., 8, 3–4, 2004, p.
553.
13.NEGREANU-PIRJOL, B., ZAGAN, S., GORUN, E., MEGHEA, A., ZAGAN,
R., STANCIUREV, G., Rev. Chim. (Bucharest), 61, no. 12, 2010, p. 1261.
14.NICOLAU, M., PATROESCU, V., COSMA, C., DINU, L., BUMBAC, C.,
CONSTANTIN, L., Rev. Chim. (Bucharest), 59, no.10, 2008, p.1106.
15.*** Solid biofuels – Determination of moisture content – Oven dry
method, European Standard EN 14774, 2009.
16.*** Solid biofuels - Determination of ash content, European Standard
EN 14775, 2009.
17.*** Solid biofuels – Determination of calorific value, European
Standard EN 14918, 2010.
18.*** Solid biofuels – Determination of major elements, European
Standard EN 15290, 2011.
19.*** Solid biofuels – Determination of total content of carbon,
hydrogen and nitrogen – Instrumental methods, European Standard
EN 15104, 2011.
20.*** Solid biofuels – Determination of the content of volatile matter,
European Standard EN 15148, 2010.
Manuscript received: 6.08.2015


Comparative Determination of Cofermentation Using Residual Waters for Biogas Production at Small Scale

http://citeseerx.ist.psu.edu/viewdoc/download;jsessionid=6842641FEBCAEA012689EE2467F04552?doi=10.1.1.1078.9156&rep=rep1&type=pdf

Comparative Determination of Cofermentation Using Residual Waters for Biogas Production at Small Scale

Abstract

Similar works

Full text

Available Versions

CiteSeerX