Enzymatic reactions in the production of biomethane from organic waste

Enzymatic reactions in the production of biomethane from organic waste

Journal Pre-proof Enzymatic reactions in the production of biomethane from organic waste ´ Dufour, Joanna Lecka, Brar Topwe Milongwe Mwene-Mbeja, Amel...

4MB Sizes 0 Downloads 86 Views

Journal Pre-proof Enzymatic reactions in the production of biomethane from organic waste ´ Dufour, Joanna Lecka, Brar Topwe Milongwe Mwene-Mbeja, Amelie ´ Satinder Kaur, Celine Vaneeckhaute

PII:

S0141-0229(19)30148-6

DOI:

https://doi.org/10.1016/j.enzmictec.2019.109410

Article Number:

109410

Reference:

EMT 109410

To appear in:

Enzyme and Microbial Technology

Received Date:

7 April 2019

Revised Date:

6 July 2019

Accepted Date:

15 August 2019

Please cite this article as: Mwene-Mbeja TM, Dufour A, Lecka J, Kaur BS, Vaneeckhaute C, Enzymatic reactions in the production of biomethane from organic waste, Enzyme and Microbial Technology (2019), doi: https://doi.org/10.1016/j.enzmictec.2019.109410

This is a PDF file of an article that has undergone enhancements after acceptance, such as the addition of a cover page and metadata, and formatting for readability, but it is not yet the definitive version of record. This version will undergo additional copyediting, typesetting and review before it is published in its final form, but we are providing this version to give early visibility of the article. Please note that, during the production process, errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain. © 2019 Published by Elsevier.

1

Enzymatic reactions in the production of biomethane from organic waste Topwe Milongwe Mwene-Mbejaa, Amélie Dufourb,c, Joanna Leckad, Brar Satinder Kaurd, Céline Vaneeckhauteb,c* a

Department of Chemistry, Faculty of Sciences, University of Lubumbashi, D.

R.

Congo,

E-mail

address:

[email protected]

/

of

Lubumbashi,

[email protected] b

ro

BioEngine - Research team on green process engineering and biorefineries,

Department of Chemical Engineering, Faculty of Science and Engineering,

-p

Université Laval, 1065 avenue de la Médecine, Pavillon Adrien-Pouliot, Québec,

[email protected]

CentrEau, Centre de recherche sur l'eau, Université Laval, 1065 Avenue de la

lP

c

re

QC, Canada, G1V 0A6, E-mail address: [email protected],

Médecine, Québec, QC, Canada, G1V 0A6 d

ur na

Centre Eau Terre Environnement, Institut national de la recherche scientifique, 490

rue de la Couronne, Québec, QC, Canada, G1K 9A9, E-mail address: [email protected], [email protected] *Corresponding author.

Jo

Highlights 

Enzymatic reactions refer to organic reactions catalyzed by enzymes



Enzymatic reactions relative to the production of biomethane are reviewed



The structure of organic compounds and reaction mechanisms are represented

2



Understanding of enzymatic reactions can be used for biomethanation optimization



Understanding of enzymatic reactions can lead to the development of new bioproducts

Abstract

of

Enzymatic reactions refer to organic reactions catalyzed by enzymes. This review

ro

aims to enrich the documentation relative to enzymatic reactions occurring during the anaerobic degradation of residual organic substances with emphasis on the

-p

structures of organic compounds and reaction mechanisms. This allows to

re

understand the displacement of electrons between electron-rich and electron-poor entities to form new bonds in products. The detailed mechanisms of enzymatic

lP

reactions relative to the production of biomethane have not yet been reviewed in the scientific literature. Hence, this review is novel and timely since it discusses the

ur na

chemical behavior or reactivity of different functional groups, thereby allowing to better understand the enzymatic catalysis in the transformations of residual proteins, carbohydrates, and lipids into biomethane and fertilizers. Such understanding allows to improve the overall biomethanation efficiency in industrial applications.

Jo

Keywords: Biomethane; Carbohydrates; Enzymatic reactions; Lipids; Mechanisms; Proteins

1. Introduction

3

Biomethanation is an established technology to convert organic waste into biomethane and digestate fertilizer products under the action of microorganism’s enzymes. The valorization of organic waste through biomethanation contributes to the improvement of hygiene, reduces bad odors as well as the use of synthetic fertilizers and pesticides. It also helps to avoid incineration and the dumping of

of

organic waste in landfills, thereby reducing greenhouse gas emissions such as carbon dioxide and nitrous dioxide [1,2]. Energy from biogas is very important

ro

especially in regions lacking energy infrastructure, for instance in Africa, because it

-p

reduces the use of fossil fuels, limits deforestation and improves people's livelihoods. The aim of this article is to enrich the documentation relative to different

re

enzymatic reactions which occur in the anaerobic degradation (biomethanation) of

lP

residual organic substances, with emphasis on the structures of organic compounds and reaction mechanisms to explain the formation of different products (Figure 1). The detailed mechanisms of enzymatic reactions relative to the production of

ur na

biomethane and biofertilizer have not yet been reviewed in the scientific literature. However, the structures of the organic compounds show different functional groups at which the organic reactions can take place. In order to better understand the

Jo

formation of the various products (biomethane and biofertilizer) in the reaction media, it is important to know which functional groups of enzymes and substrates react with each other. On top of that, the mechanisms of electron displacement and bond formation through anaerobic degradation must be understood. All of this, in

4

turn, can guide future research efforts in terms of biomethanation optimization, for example, by maximizing biomethane production or biofertilizer quality. Concretely, this review briefly describes the function of enzymes (Section 2), after which it presents a collection of organic reactions occurring upon anaerobic digestion, such as hydrolysis, acidification, synthesis of acetate (ethyl acetate or

of

methyl acetate) and synthesis of methane catalyzed by enzymes (Section 3). Various substrates (proteins, carbohydrates, and lipids) are metabolized or

ro

degraded in an anaerobic fashion by specific enzymes, while intermediate products

-p

serve as starting materials for subsequent enzymatic conversion to produce methane and fertilizers. Examples of current industrial applications to improve the

2. Enzymes

lP

re

efficiency of biomethanation by use of enzymes are provided in Section 4.

Enzymes are proteins or organic catalysts present within the cells of

ur na

microorganisms and capable of catalyzing reactions inside or outside their cell. The active center of an enzyme contains amino acids, which help to stabilize the enzyme’s transition state through hydrogen bond formation either with substrates or

Jo

with other amino acid residues. As such, a triad composed of serine, histidine, and aspartate forms a catalytic center of certain proteases and these three amino acids work together to carry out the expected catalytic activity. In the catalytic triad, histidine plays the role of a base (Figure 2) [3,4]. Indeed, amino acids can act as acids, bases, nucleophiles or electrophiles.

5

Proteins are build from amino acids, which are small molecules composed of an amine group, a carboxylic acid group and an organic R group (mostly levorotatory). Those R groups can posses an ionized polar character that influences the shape of the enzyme’s active sites. They facilitate the structural changes of the

of

protein in different physicochemical conditions and are crucial in the process of catalysis. (Figure 3). Indeed, these polar amino acids release protons as acids and

ro

capture protons as bases and being nucleophiles, they transfer electrons to

-p

electrophiles during catalysis (Figure 3) [3,4]. In the active center, the side chains of the polar amino acids participate in the acid and base chemical and covalent

re

catalysis. In other words, they can donate protons in alkaline solution (Figure 3,

lP

reaction 1) or accept protons in acidic solution (Figure 3, reaction 2). In neutral solution (pH 7), the side chains of the amino acids are neutral (Figure 3). The active

[3,4].

ur na

center is thus the biological equivalent of a strong acidic or strong basic solution

3. Enzymatic reactions

Jo

3.1 Hydrolysis

The residual organic substances consist mainly of proteins, sugars, and

lipids. The enzymatic hydrolysis of these macromolecules is the first step in the production of methane and fertilizers. Nucleophilic N-terminal hydrolases constitute a family of enzymes specialized in the breakdown of amide bonds, for instance,

6

serine proteases characterized by the presence of serine, histidine, and aspartate in the active center. The strategic step in the serine protease mechanism is the nucleophilic attack at the carbonyl group of the polypeptide (protein) by the oxygen ion from the hydroxyl group of the serine (Figure 4, reaction 2). The role of aspartate is to remove the proton bound to the nitrogen atom of histidine, while histidine

of

removes the acid proton from the hydroxyl group of serine (Figure 4, reaction 1) [5,6]. Sugars or carbohydrates are organic compounds that act as an energy

ro

reservoir at the level of higher plants. Because humans consume plants, sugars turn

-p

out to be essential constituents of human food. In general, carbohydrates are one of the major chemical groups containing carbon, hydrogen, and oxygen, such as

re

starch, which is an energy reserve substance in the plant cell [7,8]. Starch is a long

lP

chain made up of nonlinear glucose molecules (amylopectin) and linear glucose molecules (amylose) [7,8]. The glucose molecules within the starch can range from a few hundred to a few thousand linked together by alpha-glycoside linkages [7,8].

ur na

During the hydrolysis of starch, it was found that the alpha stereochemistry is maintained in the final product and the plausible catalytic mechanism involves the protonation of the glycosidic oxygen by the proton donor glutamate amino acid

Jo

(Figure 5, reaction 2) [9,10]. This step is followed by the ejection of the leaving group, due to an electron lone pair oriented antiperiplanar to the leaving group, to produce a corresponding cyclic oxocarbonium ion (Figure 5, reaction 2). The latter reacts with a water molecule to generate an intermediate compound, which yields a proton to

7

aspartate and this results in the formation of glucose molecules in the reaction medium (Figure 5, reaction 3) [9,10]. Cellulose is an organic polymer formed by several units of glucose molecules linked together by beta-(1-4)-glycosidic bonds (Figure 6) [9,10]. It is associated with lignin and hemicellulose, which form a protective layer or a shield of the cellulose. It has

of

been observed that lignin and hemicellulose are difficult to hydrolyze with enzymes. For this reason, the cellulosic waste must be treated beforehand, for instance, in

ro

using dilute acids to degrade lignin and hemicellulose and thus promote the

-p

efficiency and rapidity of the enzymatic hydrolysis of cellulose (Figure 6) [9,10]. As hemicellulose is built from different polymers, such as pentoses, hexoses, and

re

sugar/uronic acids, it requires a wide variety of enzymes to be fully hydrolyzed into

lP

free monomers [11,12,13]. In this perspective, it has been reported that the enzyme derived from the fungus Trichoderma viride was capable of transforming the cellulosic waste into fermentable sugars (Figure 6) [9,10]. The authors mentioned

ur na

that the fungus Trichoderma viride produces cellulase, which reacts with a crystalline fraction of a cellulose molecule (Figure 6). The authors also reported that the hydrolysis of cellulosic residues from sugar cane with cellulase produced glucose

Jo

with excellent yield (Figure 6) [9,10].

Cellulase represents a group of different enzymes, in particular, the

endoglucanase enzymes which hydrolyze beta-(1-4)-glycosidic internal bonds, exoglucanase enzymes that hydrolyze beta-(1-4)-glycosidic external bonds and the

8

cellobiase that hydrolyzes the disaccharide cellobiose to produce two molecules of glucose. Experimental studies showed that two amino acids (glutamate and aspartate) constitute the root of the catalytic activity in the hydrolysis of cellulose. In this regard, the glutamate amino acid yields a proton to glycosidic oxygen and the aspartate amino acid acts as a base by accepting the proton of a water molecule,

of

which acts as a nucleophile (Figure 7) [9,10]. According to the theory of stereoelectronic control, the carbon-hydrogen bond of beta-glycoside (equatorial isomer)

ro

is activated by two ion pairs of electrons oxygen antiperiplanar to the carbon-

-p

hydrogen bond (two electronic effects) [9,10]. The proposed hydrolysis mechanism involves the formation of a twist-boat conformation, which allows the substrate to line

re

up an ion pair of oxygen electrons in an antiperiplanar way to the leaving group,

lP

before adopting a chair-like transition state (cyclic oxocarbonium ion) (Figure 7) [9,10]. The nucleophilic attack at the oxocarbonium ion leads to the production of an intermediate adduct, which donates a proton to aspartate to produce the axial isomer

ur na

(alpha-glycoside) and the equatorial isomer (beta-glycoside) (Figure 7) [9,10].

The best-known disaccharide is sucrose obtained from sugarcane juice or

Jo

sugar beet. During enzymatic hydrolysis, sucrose degrades to generate D-(+)glucose and D-(-)-fructose (Figure 8, reaction 1) [14,15]. Concerning the reaction mechanism, Reddy and Maley (1996) [14] have demonstrated the role of the aspartate amino acid as well as that of the glutamate amino acid in the catalytic activity of the enzyme invertase (Figure 8) [14,15]. The carboxylate group of the side

9

chain of aspartate acts as nucleophile, while the carboxylic group of the glutamate amino acid acts as an acid (donor of the proton) (Figure 8, reaction 2). The conjugate base accepts the proton of the water (Figure 8, reaction 3). The latter acts also as a

ro

of

nucleophile (Figure 8, reaction 3) [14,15].

Lipids are triglycerides or esters of fatty acids and glycerol containing long (R)

-p

chains which are insoluble in water (Figure 9). From an environmental point of view, lipids are important organic constituents in wastewater, which contribute enormously

re

to environmental pollution. If they are not removed, the lipids form a layer on the

lP

surface of the water and thus prevent diffusion of oxygen from the air into the water. This result in the death of aquatic living beings. In this regard, it has been shown that lipases are potential catalysts that can be used to hydrolyze oils from industrial

ur na

effluents, slaughterhouses and frying oils [16]. Experimental observations have shown that the lipases catalyze the hydrolysis of the ester bonds to produce fatty acids and glycerol (Figure 9, reaction 1) [17]. These enzymes contain serine,

Jo

histidine and aspartate amino acid in the active center. It has been found that the aspartate amino acid can be replaced by the glutamate amino acid in the case of Geotrichum candidum lipase [17]. This enzyme uses the glutamate residue to specifically hydrolyze the fatty acids having cis double bonds in the hydrocarbon side

10

chains [17]. The reaction mechanism of the lipases is thus similar to that of serine protease (Figure 9, reaction 2).

The catalytic activity of the lipases is influenced by the water molecules present in the structure of these enzymes. From this point of view, it has been observed that

of

when the lipases are dehydrated, they lose the ability to catalyze esterification

ro

reactions involving congested alcohols. This could be explained by the fact that the absence of water affects the mobility necessary to bind the substrates in the active

-p

center [18,19]. Hence, lipases are less active in solvents which are miscible with

re

water because they extract water integrated into the structure of the enzyme [20,21].

lP

3.2 Acidification

The products of hydrolysis are used by microorganisms as substrates to

ur na

produce acids, alcohols and carbon dioxide (Figure 10). At this level of biomethanation, amino acids could be used as a source of energy for microorganisms. Rupasinghe and his colleagues reported on an enzymatic method for producing glucose, ethanol and acetic acid from apple residues (Figure 10)

Jo

[18,19]. The cellulose was pretreated with acidified aqueous conditions and the hydrolysis was optimized by using commercial enzymes (beta-glucosidase and pectinase). The glucose was fermented using Saccharomyces cerevisiae to produce ethanol. The bioconversion of ethanol to acetic acid was carried out using acetobacter aceti [18,19].

11

The enzymatic oxidation of ethanol to acetaldehyde is catalyzed by alcohol dehydrogenase (Figure 10, reaction 2) [22,23]. On the other hand, the oxidation of acetaldehyde to acetic acid is catalyzed by the aldehyde dehydrogenase (Figure 10, reaction 3). These enzymes use nicotinamide adenine dinucleotide (NAD) as coenzyme and glutamate plays the role of a base in the active center of the enzyme

of

(dehydrogenase) [22,23]. Regarding the dehydrogenation of ethanol, the mechanism involves the transfer of the hydride ion to NAD+ (oxidized form of NAD)

ro

and this results in the formation of NADH (reduced form of NAD) and the desired

-p

product (acetaldehyde) (Figure 10, reaction 2). Dehydrogenation of acetaldehyde involves the nucleophilic attack by a water molecule upon the electrophilic carbon of

re

acetaldehyde. This step is followed by the removal of the proton by glutamate and

reaction 3) [22,23]. 3.3 Synthesis of acetate

lP

the transfer of the hydride ion at the level of the oxidized form of NAD (Figure 10,

ur na

It has previously been observed that the majority of methane is produced from acetate (Figure 1) [24]. In this context, it has been demonstrated that lipase catalyzes the reaction between acetic acid and ethanol to produce volatile natural ethyl acetate

Jo

and water as by-product [25,26]. Because of the reversibility of the reaction, it is important to remove water to optimize the formation of the product. Concerning the mechanism, the lipase utilizes serine, histidine and aspartate amino acid to catalyze the production of acetate from acetic acid and alcohol (ROH). Aspartate amino acid donates a proton to the hydroxyl group of acetic acid (Figure 11, reaction 2). This

12

step is followed by serine nucleophilic attack, resulting in the loss of one molecule of water and formation of an intermediate adduct, which in turn reacts with the alcohol (ethanol or methanol) to produce the corresponding acetate (Figure 11, reaction 3) [27].

of

3.4 Synthesis of methane Bacteria degrade ethyl acetate to produce ethanol and acetic acid. The latter

ro

is then metabolized to produce methane and carbon dioxide with the assistance of

-p

decarboxylase as a catalyst. It has been reported that decarboxylation involves the formation of negatively charged intermediate compounds. In this perspective, the

re

electrophilic substitution of carbon dioxide by a proton involves the loss of carbon

lP

dioxide to form a carbanion (methyl anion), which accepts a proton from the catalytic amino acid residue, in this case, lysine, to generate the desired product (methane) (Figure 12) [25,28]. It has been observed that lysine and cysteine are at the center

ur na

of catalytic activity of decarboxylase (Figure 12) [26].

4. Current industrial applications to optimize biomethanation efficiency

Jo

Cellulosic materials have relatively low cost and plentiful supply. Organisms that are producing cellulolytic enzymes, hydrolysis of biomass, and fermentation of resulting sugars to desired products are considered for “consolidated bioprocessing” (CBP). Biological hydrogen and methane production biomass able to convert lignocellulose into biofuels show great potential as a promising alternative to

13

conventional hydrogen and methane production methods, but utilization of these materials is limited due to their low degradability. As hydrolysis is the first step of anaerobic digestion, preliminary degradation of lignocellulose is crucial for efficient bioconversion of biomass to biofuels [29,30]. The low rate of hydrolysis of lignocellulose results in the slowdown of the entire process. Therefore, the

of

lignocellulosic material requires special preliminary treatment before further processing [31], which may be carried out by physical, chemical and biological

ro

methods including, but not limited to, e.g., comminution, acid hydrolysis, ammonia

-p

fiber expansion, steam explosion [32].

Increase in the biogas yield production from hemicelluloses using anaerobic

re

digestion and decrease in the time of this process can be achieved by several

lP

pretreatment technologies [31,33,34,35,36]. Pretreatments with enzymes that will convert lignocellulosic biomass into biogas are necessary also for elimination of structural barriers like crystalline cellulose structure [37,38,39,40]. In the literature,

ur na

two enzymatic pretreatment strategies for lignocelluloses have been reported: 1) helping to degrade cellulose by addition of laccases and peroxidises, 2) reinforcing cellulose and other polysaccharides metabolism by addition of cellulosic enzymes.

Jo

The first strategy utilizes enzymes from various fungi. Anaerobic fungi, belonging to the phylum Neocallimastigomycota, key players in the digestive system of various animals, produce a plethora of plant carbohydrate hydrolysing enzymes that can degrade both amorphous and crystalline cellulose [41].

14

Combined with the invasive growth of their rhizoid system their contribution to cell wall polysaccharide decomposition may greatly exceed that of bacteria [42,43]. The yield of end-products of enzymes used as pretreatment depend on species, sources and substrates of fungi [44,45]. Anaerobic fungi have widely been isolated from wild and domestic ruminants, such as Holstein steers rumen, ovine rumen,

of

cattle rumen, cattle faeces, buffalo rumen or faeces, goats, wild bluebull, elephants, deer, zebras, grazing sheep [46,47,48,49,51]. Sijtsma and Tan (1993) reported that

ro

Neocallimastix isolate from the yaks faeces could secrete enzymes that degrade the

-p

cell wall, including exoglucanase [52].

Some studies suggest that anaerobic fungi and methanogens, e.g.

re

methanogenic Archaea, a diverse group of strictly anaerobic Euryarchaeota, can

lP

form stable co-cultures that have higher ability to degrade lignocellulose than pure anaerobic fungi [53,54]. Such co-culture changes metabolism pathways of fungi, resulting in the production of methane and more acetate and ATP, but less lactate,

ur na

ethanol and succinate, since it can provide more energy for fungi by enhancing cellulose fermentation kinetics [54]. The strength of such cooperation was confirmed in the study of Wei et al. (2016) showing that the anaerobic fungi and associated

Jo

indigenous methanogens in the rumen of grazing yaks have a strong capability to degrade lignocellulose [55]. Another practical example are extremophile-derived enzymes (enzymes

present

in

Extremophilic

microorganisms

called

thermophiles

and

hyperthermophiles). Due to their optimal activity and stability under extreme

15

conditions, these enzymes are able to catalyze chemical reactions under harsh conditions similar to those found in industrial processes. Those organisms are found in environments where temperatures are above 100°C such as hot springs and deep sea vents, geysers and highly geothermal volcanic areas [56,57] Hyperthermophiles, e.g., Methanocaldococcus jannaschii, posses the anaerobic metabolic pathways

of

used for production of methane from hydrogen and carbon dioxide [58]. From an industrial viewpoint, hyperthermophilic enzymes possess certain advantages: their

ro

enzymes are active and efficient under high temperatures (above 100°C), extreme

-p

pH values (4.0 to 7.5), high substrate concentrations, high pressure and are highly

re

resistant to denaturing agents and organic solvents [59, 60, 61] Unfortunately, the costs of using enzymatic processes in industrial applications are

lP

very high, which increases the cost of waste conversion to biogas. Nevertheless, efforts to improve the cost efficiency are growing. DuPont Org., winner in the

ur na

European Community project DEMETER (Demonstrating More Efficient Enzyme Production To Increase Biogas Yields, January 2016) provides a good best practice example. They developed and applied a fungal expression technology for producing enzymes that break down plant fibers (carbohydrates such as cellulose and

Jo

hemicellulose) and protein-rich materials, resulting in sugars and amino acids more suitable for biogas-producing microorganisms [62].

5. Conclusions and perspectives

16

Proteins, carbohydrates, and lipids are essential constituents of domestic, agricultural and industrial organic waste. These organic molecules have functional groups, at which hydrolysis, acidification and decarboxylation reactions catalyzed by specific enzymes take place. This paper explains in an understandable way the different steps of enzymatic reactions involved in the production of methane and

of

fertilizer from residual organic substances. This allows guiding future research efforts in terms of biomethanation optimization, e.g., by maximizing biomethane production

ro

and biofertilizer quality. Knowledge of enzymatic mechanisms involved in

lP

Conflict of interest statement

re

reinforce the process of methane production.

-p

biomethanation can help to define precisely the pretreatment strategies that will

We declare that we do not have a conflict of interest regarding the publication of this

ur na

paper.

Acknowledgements

Céline Vaneeckhaute is funded by the Natural Science and Engineering

Jo

Research Council of Canada (NSERC) through the award of an NSERC Discovery Grant (RGPIN-2017-04838) and by the Fonds de Recherche du Québec Nature et Technologies (FRQNT) through the award of a Research Support for New Academics Grant (2019-NC-253483).

17

References [1] Chen, T.-C., Lin, C.-F. J., 2008. Greenhouse gases emissions from waste management practices using Life Cycle Inventory model. J. of Hazardous Materials. 155, 23-31. [2] Pham, C. H., Triolo, J. M., Cu, T. T. T., Pedersen, L., Sommer, S. G., 2013.

of

Validation and Recommendation of Methods to Measure Biogas Production Potential of Animal Manure. Asian Australas. J. Anim. Sci. 26, 864-873.

ro

[3] Yang, Y. L., Ramaswamy, S. G., Jakoby, W. B., 1998. Enzymatic Hydrolysis of

[4] Zhou, Y.,

-p

Organic Cyclic Carbonates. J. Biol. Chem. 273, 7814-7817.

Wang, S., Zhang, Y., 2010. Catalytic Reaction Mechanism of

re

Acetylcholinesterase Determined by Born-Oppenheimer ab initio QM/MM Molecular

lP

Dynamics Simulations. J. Phys. Chem. B. 114, 8817-8825.

[5] Hedstrom, L., 2002. Serine Protease Mechanism and Specificity. Chem. Rev.

ur na

102, 4501-4524.

[6] Neitzel, J. J., 2010. Enzyme catalysis: the serine proteases. Nat. Edu. 3, 21.

[7] Kobayashi, K., K Kimura, S., Togawa, E., Wada, M., 2013.Thermal expansion behavior of hydrate paramylon in the low-temperature region. Carbohydrate Poly.

Jo

91, 543-548.

18

[8] Ring, S. G., Gee, J. M., Whittam, M., Orford, P., Johnson, I. T., 1988. Resistant starch: Its chemical form in foodstuffs and effect on digestibility in vitro. Food Chem. 28, 97-109. [9] Azevedo, H. S., Gama, F. M., Reis, R. L., 2003. In Vitro Assessment of the Enzymatic Degradation of Several Starch Based Biomaterials. Biomacromolecules.

of

4, 1703-1712.

ro

[10] Deslongchamps, P., 1993. Intramolecular strategies and stereoelectronic effects. Glycosides hydrolysis revisited. Pure Appl. Chern. 65, 1161-1178.

-p

[11] Gírio F.M., Fonseca, C., Carvalheiro, F., Duarte, L.C., Marques, S., Bogel-

re

Lukasik, R., 2010. Hemicelluloses for fuel ethanol: A review. Bioresour Technol. 101, 4775–4800.

lP

[12] Laureano-Perez, L., Teymouri, F., Alizadeh, H., Dale, B. E., 2005. Understanding factors that limit enzymatic hydrolysis of biomass. Appl Biochem

ur na

Biotechnol. 124, 1081–1099.

[13] Saha BC., 2003. Hemicellulose bioconversion. J Ind Microbiol Biotechnol. 30, 279–291.

Jo

[14] Reddy, A., Maley, F., 1996. Studies on identifying the catalytic role of Glu-204 in the active site of yeast invertase J. Biol. Chem. 271, 13953-13958. [15] Heinzerling, P., Schrader, F., Schanze, S., 2012. Measurement of Enzyme Kinetics by Use of a Blood Glucometer: Hydrolysis of Sucrose and Lactose. J. Chem. Educ. 89, 1582-1586.

19

[16] Mendes, A. A., De Castro, H. F., 2005. Effect on the enzymatic hydrolysis of lipids from dairy wastewater by replacing Gum Arabic emulsifier for sodium chloride. Braz. Arch. Biol. Technol. 48, 135-142. [17] Mala, J. G. S., Takeuchi, S., 2008. Understanding Structural Features of Microbial Lipases—An Overview. Anal. Chem. Insights. 3, 9-19.

of

[18] Philippidis, G. P., Smith, T. K., Wyman, C. E., 1993. Study of the Enzymatic

ro

Hydrolysis of Cellulose for Production of Fuel Ethanol by the Simultaneous Saccharification and Fermentation Process Biotechnol. Bioeng. 41, 846-853.

-p

[19] Zhang, R., Pan, Z., Zheng, Y., 2009. Overview of biomass pretreatment for

re

cellulosic ethanol production. Int. J. Agric. Biol. Eng. 2, 51-68.

[20] Krishna, S. H., Karanth, N. G., 2002. Lipases and lipase-catalyzed esterification

lP

reactions in nonaqueous media. Catalysis Rev.: Sci. Eng. 44, 499-591.

ur na

[21] Tundo, P., Selva, M., Bomben, A. Org. Synth. Coll. 2004, 10, 640. [22] Muzio, G., Maggiora, M., Paiuzzi, E., Oraldi, M., Canuto, R. A., 2012. Aldehyde dehydrogenases and cell proliferation. Radic. Biol. Med. 52, 735-746. [23] Marchitti, S. A., Brocker, C., Stagos, D., Vasiliou, V., 2008. Non-P450 aldehyde

Jo

oxidizing enzymes: the aldehyde dehydrogenase superfamily. Expert Opin Drug Metab Toxicol. 4, 697-720. [24] Morvai, L., Miháltz, P., Holló, J., 1992. Comparison of the kinetics of acetate biomethanation by raw and granular sludges. Appl. Microbiol. Biotechnol. 36, 561567.

20

[25] Richard, J. P., 2011. Enzymatic catalysis of proton transfer and decarboxylation reactions, Pure Appl. Chem. 83, 1555-1565. [26] Lee, Y.; Cho, Y., 2001. Identification of essential active-site residues in ornithine decarboxylase of Nicotiana glutinosa decarboxylating both L-ornithine and L-lysine. Biochem. J. 360, 657-665.

of

[27] Bélafi-Bako, K., Kabiri Badr, A., Nemestothy, N., Ehrenstein, U., Gubicza, L.,

ro

2003. Kinetics of Ethyl Acetate Formation by Lipase in Organic Solvent and SolventFree System. Chem. Papers. 57, 278-281.

-p

[28] Hollenstein, M., 2013. Deoxynucleoside triphosphates bearing histamine,

Org. Biomol. Chem. 11, 5162-5172.

re

carboxylic acid, and hydroxyl residues – synthesis and biochemical characterization.

lP

[29] Sun, Y., Cheng, J., 2002. Hydrolysis of lignocellulosic materials for ethanol production: a review. Bioresource Technology. 83, 1-11.

ur na

[30] O’Sullivan, C., Burrell, P.C., Clarke, W.P., Blackall, L.L., 2007. A survey of the

Jo

relative abundance of specific groups of cellulose degrading bacteria in anaerobic

21

environments using fluorescence in situ hybridization. Journal of Applied Microbiology. 103, 1332-1343. [31] Taherzadeh, M.J. and Karimi, K., 2008. Pretreatment of Lignocellulosic Wastes to Improve Ethanol and Biogas Production: A Review. Int. J. Mol. Sci. 9, 1621-1651. [32] Sanchez, C., 2009. Lignocellulosic residues: Biodegradation and bioconversion

of

by fungi. Biotechnol Adv. 27, 185-194.

ro

[33] Zheng Y., Zhao, Y., Xu, F., Li, Y., 2014. Pretreatment of lignocellulosic biomass

-p

for enhanced biogas production. Prog. Energy Combust. Sci. 42, 35–53. [34] Ariunbaatar J., Panico, A., Esposito, G., Pirozzi, F., Lens, P.N.L., 2014.

re

Pretreatment methods to enhance anaerobic digestion of organic solid waste. Appl.

lP

Energy. 123, 143–56.

[35] Chandra R.P., Bura R., Mabee W.E., Berlin A., Pan X., Saddler J.N., 2007. Pretreatment:

The

Jo

ur na

Substrate

Key

to

Effective

Enzymatic

Hydrolysis

of

22

Lignocellulosics?, In: Olsson, L. (eds) Biofuels. Advances in Biochemical Engineering/Biotechnology, vol 108. Springer, Berlin, pp. 67-93. [36] Hendriks A.T.W.M. and Zeeman G., 2009. Pretreatments to enhance the digestibility of lignocellulosic biomass. Bioresour. Technol. 100, 10–18. [37] Christopher L.P., Yao, B., Ji, Y., 2014. Lignin biodegradation with laccase-

of

mediator systems. Front. Energy Res. 2, 1–13.

ro

[38] Sawatdeenarunat C., Surendra, K.C., Takara, D., 2015. Anaerobic digestion of lignocellulosic biomass: Challenges and opportunities. Bioresour. Technol. 178,

-p

178–186.

re

[39] Ellenrieder J., Schieder, D., Mayer, W., 2010. Combined mechanical enzymatic pretreatment for an improved substrate conversion when fermenting biogenic

lP

resources. Eng. Life Sci. 10, 544–551.

[40] Kim I.J., Lee, H.J., Choi, I-G., Kim, K.H., 2014. Synergistic proteins for the

ur na

enhanced enzymatic hydrolysis of cellulose by cellulase. Appl. Microbiol. Biotechnol. 98, 8469–8480.

[41] Youssef, N.H., Couger, M.B., Struchtemeyer, C.G., Liggenstoffer, A.S., Prade,

Jo

R.A., Najar, F.Z., Atiyeh, H.K., Wilkins, M. R. and Elshahed, M. S., 2013. The Genome of the Anaerobic Fungus Orpinomyces sp. Strain C1A Reveals the Unique

23

Evolutionary History of a Remarkable Plant Biomass Degrader. Appl. Environ. Microbiol. 79, 4620–4634. [42] Liggenstoffer, A.S., Youssef, N.H., Couger, M.B., Elshahed, M.S., 2010. Phylogenetic diversity and community structure of anaerobic gut fungi (phylum Neocallimastigomycota) in ruminant and non-ruminant herbivores, The ISME

of

Journal. 4, 1225–1235.

ro

[43] Lee S.M., Guan, L.L., Eun, J.-S., Kim, C.-H., Lee, S.J., Kim, E.T., Lee, S.S., 2014. The effect of anaerobic fungal inoculation on the fermentation characteristics

-p

of rice straw silages. J. Appl. Microbiol. 118, 565–573.

re

[44] Boxma, B., Voncken, F., Jannink, S., Alen, T.V., Akhmanova, A., Weelden, S.W.H.V., Hellemond, J.J.V., Ricard, G., Huynen, M., Tielens, A.G.M., Hackstein,

lP

J.H.P., 2004. The anaerobic chytridiomycete fungus Piromyces sp. E2 produces ethanol via pyruvate:formate lyase and an alcohol dehydrogenase E. Mol. Microbiol.

ur na

51, 1389–1399.

[45] Marvin-Sikkema, F.D., Rees, E., Kraak, M.N., Gottschal, J.C., Prins, R.A., 1993. Influence of Metronidazole, CO, CO2, and Methanogens on the Fermentative

Jo

Metabolism of the Anaerobic Fungus Neocallimastix sp. Strain L2. Appl. Environ. Microbiol. 59, 2678–2683. [46] Yang, H., Yue, Q., Cao, Y.C., Zhang, D.F., Wang, J.Q., 2009. Effects of crude feruloyl

and

acetyl

esterase

solutions

of

Neocallimastix

sp.

YQ1

and Anaeromyces sp. YQ3 isolated from Holstein steers on hydrolysis of Chinese

24

wildrye grass hay, wheat bran, maize bran, wheat straw and corn stalks. Anim. Feed. Sci. Tech. 154, 218–227. [47] Gordon, G. and Phillips, M.W., 1989. Degradation and utilization of cellulose and straw by three different anaerobic fungi from the ovine rumen. Appl. Environ. Microbiol. 55, 1703–1710.

of

[48] Sirohi, S.K., Choudhury, P.K., Dagar, S.S., Puniya, A.K., Singh, D., 2013.

ro

Isolation, characterization and fibre degradation potential of anaerobic rumen fungi from cattle. Ann. Microbiol. 63, 1187–1194.

-p

[49] Thareja, A., Puniya, A.K., Goel, G., Nagpal, R., Sehgal, J.P., Singh, P.K., Singh,

re

K., 2006. In vitro degradation of wheat straw by anaerobic fungi from small ruminants. Arch. Anim. Nutr. 60, 412–417.

lP

[50] Paul, S.S., Kamra, D.N., Sastry, V.R.B., 2010. Fermentative characteristics and fibrolytic activities of anaerobic gut fungi isolated from wild and domestic ruminants.

ur na

Arch. Anim. Nutr. 64, 279–292.

[51] Nagpal, R., Puniya, A.K., Sehgal, J.P., Singh, K., 2011. In vitro fibrolytic potential of anaerobic rumen fungi from ruminants and non-ruminant herbivores.

Jo

Mycoscience. 52, 31–38.

[52] Sijtsma, L., Tan, B., 1993. Degradation and utilization of grass cell walls by anaerobic fungi isolated from yak, llama and sheep. Anim. Feed Sci. Tech. 44, 221– 236.

25

[53] Thauer, R.K., Kaster, A.-K., Seedorf, H., Buckel, W., Hedderich, R., 2008. Methanogenic archaea: ecologically relevant differences in energy conservation. Nat. Rev. Microbiol. 6, 579–591. [54] Bauchop, T., Mountfort, D.O., 1981. Cellulose Fermentation by a Rumen Anaerobic Fungus in Both the Absence and the Presence of Rumen Methanogens.

of

Appl. Environ. Microbiol. 42, 1103–1110.

ro

[55] Wei, Y.-Q., Yang, H.-J., Luan, Y., Long, R.-J., Wu, Y.-J., Wang, Z.-Y., 2016. Isolation, identification and fibrolytic characteristics of rumen fungi grown with

-p

indigenous methanogen from yaks (Bos grunniens) grazing on the Qinghai‐Tibetan

re

Plateau. J. Applied Microbiology. 120, 571–587.

[56] Cowen, D.A., 2004. The upper temperature of life – where do we draw the line?

lP

Trends Microbiol. 12, 58–60.

[57] Takai, K., Nakamura, K., Toki, T., Tsunogai, U., Miyazaki, M., Miyazaki, J., 2008.

Jo

ur na

Cell proliferation at 122 °C and isotopically heavy CH4 production by a

26

hyperthermophilic methanogen under high-pressure cultivation. Proc. Natl. Acad. Sci. U.S.A. 105, 10949–10954. [58] Bult, C. J., White, O., Olsen, G. J., Zhou, L., Fleischmann, R. D., Sutton, G. G., 1996. Complete genome sequence of the methanogenic archaeon, Methanococcus jannaschii. Science 273, 1058–1073.

of

[59] Niehaus, F., Bertoldo, C., Kahler, M., Antranikian, G., 1999. Extremophiles as a

ro

source of novel enzymes for industrial application. Appl. Microbiol. Biotechnol. 51,

-p

711–729.

[60] Larsson, L., Olsson, G., Holst, O., Karlsson, H.T., 1990. Pyrite oxidation by

re

thermophilic archaebacteria. Appl. Environ. Microbiol. 56, 697–701.

lP

[61] Kletzin, A., Urich, T., Muller, F., Bandeiras, T.M., and Gomes, C.M., 2004. Dissimilatory oxidation and reduction of elemental sulfur in thermophilic archaea. J.

ur na

Bioenerg. Biomembr. 36, 77–91.

Jo

[62] DuPont, 2019. Available from: www.biofuels.dupont.com.

27

Carbohy drates

Lipids

Amino acids

Sugars

Fatty acids

Acidific ation

Acetate synthesis

-p

Acetate Water

of

Acids Alkohold

ro

Hydrol ysis

Polypep tides

Methane synthesis

re

Methan e

ur na

lP

Figure 1 – Processes involved in anaerobic digestion and products obtained.

Jo

Figure 2 – Triad of amino acids forming the catalytic center of certain proteases.

-p

ro

of

28

re

Figure 3 – Examples of reactions with polar amino acids occurring in the catalytic center of an enzyme: 1) Donation of protons in alkaline solution, 2)

Jo

ur na

neutral solution.

lP

Acceptance of protons in acidic solution, 3) Neutrality of the side chains in

29

of

Figure 4 – Serine protease mechanism: 1) Reaction between aspartate,

Jo

ur na

lP

re

-p

ro

histidine and serine, 2) Nucleophilic attack of the polypeptide by the serine.

re

-p

ro

of

30

lP

Figure 5 – 1) Hydrolysis of starch, 2) Catalytic mechanism involving glutamate and formation of the cyclic oxocarbonium ion, 3) Reaction of the ion with water

Jo

ur na

and aspartate to produce glucose.

Figure 6 – Hydrolysis of cellulose with cellulase produced by the fungus Trichoderma viride.

re

-p

ro

of

31

ur na

lP

Figure 7 – Hydrolysis mechanisms of cellulose.

Jo

Figure 8a – Degradation of sucrose with the enzyme invertase.

Jo

ur na

lP

re

-p

ro

of

32

Figure 8b – Reaction mechanisms for sucrose hydrolysis: 1) Formation of D(+)-glucose, 2) Formation of D-(-)-fructose.

ro

of

33

-p

Figure 9 – Hydrolysis of lipids with lipase: 1) Formation of fatty acids and

Jo

ur na

lP

re

glycerol, 2) Reaction of the triglyceride with serine.

34

of

Figure 10 – 1) Formation of carbon dioxide and ethanol from glucose, 2)

ro

Oxidation of ethanol to acetaldehyde, 3) Oxidation of acetaldehyde to acetic

Jo

ur na

lP

re

-p

acid.

35

Figure 11 – Formation of acetate from acetic acid and ethanol: 1) Basic reaction, 2) Enzymatic reaction between acetic acid and aspartate amino acids,

lP

re

-p

ro

of

3) Enzymatic reaction of serine to form acetate.

Jo

ur na

Figure 12 – Reaction mechanisms for the formation of methane with lysine.