\r\n\tThe book also covers the more specialized areas of energy consumption, riding comfort, noise and vibration.
\r\n\tEscalators and passengers conveyors should also be addressed, as these devices complement elevator system in moving passenger around the building.
\r\n\tModern developments are hope to be covered within the relevant chapters, some of which are listed as follows: Modern electrical safety systems,Modern shaft and motor feedback devices, Modern electrical drive system, Two elevator cars in the same shaft, Multiple elevator car systems in the same shaft, Evacuation systems using elevators, Modern calculation and simulation tools and software packages, Ropeless elevator systems.
",isbn:"978-1-83968-177-6",printIsbn:"978-1-83968-176-9",pdfIsbn:"978-1-83968-178-3",doi:null,price:0,priceEur:0,priceUsd:0,slug:null,numberOfPages:0,isOpenForSubmission:!0,hash:"8d5766ef86475867198610aeb050233c",bookSignature:"Dr. Lutfi Al-Sharif",publishedDate:null,coverURL:"https://cdn.intechopen.com/books/images_new/10040.jpg",keywords:"Elevator Traffic Engineering, Simulation, Elevator Mechanical Engineering, Safety Gear System, Drive Systems, Control Systems, Energy Consumption, Power, Riding Comfort, Noise and Vibration, Escalators, Passenger Conveyors",numberOfDownloads:null,numberOfWosCitations:0,numberOfCrossrefCitations:null,numberOfDimensionsCitations:null,numberOfTotalCitations:null,isAvailableForWebshopOrdering:!0,dateEndFirstStepPublish:"November 14th 2019",dateEndSecondStepPublish:"December 5th 2019",dateEndThirdStepPublish:"February 3rd 2020",dateEndFourthStepPublish:"April 23rd 2020",dateEndFifthStepPublish:"June 22nd 2020",remainingDaysToSecondStep:"11 days",secondStepPassed:!0,currentStepOfPublishingProcess:3,editedByType:null,kuFlag:!1,editors:[{id:"314726",title:"Dr.",name:"Lutfi",middleName:null,surname:"Al-Sharif",slug:"lutfi-al-sharif",fullName:"Lutfi Al-Sharif",profilePictureURL:"https://mts.intechopen.com/storage/users/314726/images/system/314726.jpg",biography:"Lutfi Al-Sharif is currently Professor of Building Transportation Systems at of the Department of Mechatronics Engineering, The University of Jordan. He received his Ph.D. in lift traffic analysis in 1992 from UMIST (Manchester, U.K.). He worked for 9 years for London Underground, London, United Kingdom in the area of lifts and escalators.\r\nIn 2002, he formed Al-Sharif VTC Ltd, a vertical transportation consultancy based in London, United Kingdom. He has over 30 papers published in peer reviewed journals the area of vertical transportation systems and is co-inventor of four patents and co-author of the 2nd edition of the Elevator Traffic Handbook.\r\nHe is also a visiting professor at the University of Northampton (UK), member of the scientific committee of the annual Symposium on Lift & Escalator Technologies and a member of the editorial board of the journal Transportation Systems in Buildings. \r\nHe is a passionate believer in making higher education simple and accessible for engineering students and has a You Tube channel on engineering that has around 50 000 subscribers and around 7 million views. He has also been working as a member of the METHODS Project that aims to improve teaching methods in higher education in Jordan and Palestine. 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From chapter submission and review, to approval and revision, copyediting and design, until final publication, I work closely with authors and editors to ensure a simple and easy publishing process. I maintain constant and effective communication with authors, editors and reviewers, which allows for a level of personal support that enables contributors to fully commit and concentrate on the chapters they are writing, editing, or reviewing. I assist authors in the preparation of their full chapter submissions and track important deadlines and ensure they are met. I help to coordinate internal processes such as linguistic review, and monitor the technical aspects of the process. As an ASM I am also involved in the acquisition of editors. 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Venkateswarlu",coverURL:"https://cdn.intechopen.com/books/images_new/371.jpg",editedByType:"Edited by",editors:[{id:"58592",title:"Dr.",name:"Arun",surname:"Shanker",slug:"arun-shanker",fullName:"Arun Shanker"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}}]},chapter:{item:{type:"chapter",id:"53189",title:"Production of Biofuel via Hydrogenation of Lignin from Biomass",doi:"10.5772/66108",slug:"production-of-biofuel-via-hydrogenation-of-lignin-from-biomass",body:'\nBiomass is a potential source of fuel consists of organic materials and considered as renewable and sustainable for energy development. With fossil fuel remaining unstable in terms of cost and sustainability, the need to generate biomass-based energy is becoming more imperative and feasible in economical point of view [1, 2]. One of the main benefits of biomass-based fuel (sometimes called as biofuel) is zero carbon dioxide release as compared to fossil fuel [3]. Furthermore, the dramatic rise of carbon dioxide concentration in the atmosphere has triggered researchers to find viable alternatives to fossil-based fuels.
\nOne type of biomass which covers mostly of plant molecules is lignocellulosic biomass. Structurally, it composes of cellulose, hemicellulose and lignin. Cellulose and hemicellulose are mainly monomeric sugar linked to form polymer [4]. However, lignin consists of phenylpropane units, which cross-linked with tight and varied chemical bonds [4]. Thus, lignin complexity makes it difficult to be degraded as compared to almost unified type of bonding of cellulose and hemicellulose. Nonetheless, a few researchers have found ways to enhance degradability of lignin through recent pretreatment technologies [4, 5].
\nLignin is separated from cellulose and hemicelluloses during kraft process, and only partial is utilised in combustion application as energy source [6]. In addition, through development of bioethanol production, it is expected that more lignin is produced as by-product which is also added to the mass number of lignin. Through advances of pretreatment technology and valorisation, lignin can be used as an alternative source for fine chemicals and raw material for fuel.
\nIn the progress of lignin utilisation for fuel production, hydrogenation of lignin becomes one of viable methods. Lignin contains functional phenolic compounds, but the difficulties of extracting the compounds remain a bottleneck to unlock this potential material for fuel production. For example, the degree of interaction between monomers (phenolic compound)varied due to the heterologous nature of each individual monomers [7]. Another reason would be the feasibility of pretreatment technologies that are needed to be strategised and to fully utilise the monomers present [7]. In addition, the monomers have to be separated from the strong linkages within lignin structure, so that conversion to fuel can be executed efficiently.
\nIn this chapter, lignin will be discussed of its structure and its different functional phenolic compounds. In addition, lignin depolymerisation or valorisation process to obtain individual monomers will also be presented. Further discussion will also include hydrogenation of lignin and the mechanism involved in the process. At the final part of this chapter, the future perspective of lignin hydrogenation that may lead to more innovative applications is discussed.
The present development of biomass conversion to energy and chemicals together with individual types of abundant biomass in nature has been discussed in terms of its source, availability, types of biomass and chemical characteristics.
\nIn the abundance of biomass in the world’s nature, traditional utilisation of biomass in order to survive has long been established. Primitively, when man knows how to create fire, biomass utilisation evolved from domestic usage to even larger application such as building houses, clothes production, paper making, etc. Yet the biomass utilisation seems endless and continues to produce more relevant products.
\nHenry Ford was the first to design a model car that runs using ethanol, and it was also reported that Rudolph Diesel intended on using vegetable oil to power his car engine [8]. However, at the time of World War II, fossil fuels were more practical based on supply, price and efficiency which caused biofuel to be unpopular. In contrast, in the late 1990s, high intensity of research and investment were made to produce biofuel from biomass due to reverse effect on supply and price of fossil fuel which is unpredictable.
\nThe first biomass used was in solid form—wood—which was used to produce fire and oil derived from plants and animals that has been turned to a useful medium to light up lamp [9, 10]. In the present day, biofuel is derived from food crops like sugar beets, grains and vegetable oils or, namely, first-generation biomass [11]. However, the impact on the global food supply and sustainability of land led to non-food stock for energy sources and the second generation of energy sources such as cellulosic biomass, inedible oil and algae-derived oil [11, 12]. Microalgae can reproduce in a mass rapidly per day and have been found enriched of high level of oil in total dry biomass [13]. However, regardless the high growth rates or high oil content, algae-derived oil production faces challenges that needed attention such as strain isolation, nutrient sourcing or availability, on-site management in production and handling and residual biomass or waste management [14].
\nMeanwhile, biobutanol, another type of fuel, has becoming popular in recent years that surpass bioethanol. Biobutanol is referred as the next generation of biofuels that offers many advantages. It can be produced directly with few combinations of physical, chemical and biological processes from food crops such as cereal crops, sugar beets and sugar cane. The first synthesis of biobutanol was achieved during 1912–1914 by acetone-butanol-ethanol (ABE) fermentation using Clostridium species as catalysts [15].
In developing technologies to fine tune biomass conversion to chemicals or fuels, many combinations of physical, chemical and biological approaches have been utilised. The strategy is to enhance accessibility to the main target component such as cellulose and hemicellulose or to separate main recalcitrant of the biomass which is lignin from the other component and treated individually as precursor for fuel.
\nFor starter, all biomass should undergo pretreatment in order to achieve maximum conversion. During the past decades, the target is to produce fermentable sugar from complex lignocellulosic biomass which includes separating lignin from the complex biomass [16]. Figure 1 shows a schematic flow of basic biomass conversion into value-added products.
Schematic flow of general conversion of biomass to value-added products. Adapted from Ref. [17] with permission from Elsevier.
During the course of chemical or biochemical conversion, an effective pretreatment is needed for maximum utilisation of the biomass. To summarise, a few criteria have been highlighted to achieve efficient pretreatment as indicated below:\n
Preservation of hemicelluloses fractions, in order to have high yield of fermentable sugars;
Minimising the building up of inhibitors due to degradation;
Minimising the use of high energy in the process;
Cost-effective pretreatment processes.
The above criteria become a basis for choosing the right method of pretreatment of biomass in order to maximise its efficiency. Further details on pretreatment will not be discussed here and can be found intensively discussed in other publications [18].
\nMeanwhile, as the complexity of the biomass dissolved through pretreatment processes, the next step is to choose the right method to directly convert the simpler form of the material to the desired product based on physical, chemical and biological processing methods.
\nIn this method, for some biomass, pretreatment sometimes will not be necessary. For example, woody biomass through combustion process will produce heat and electricity. The initial combustion will produce steam at high pressure and eventually the steam is used to activate turbine plants that in turn will generate electricity. Such biomass-fired steam turbine plants are located at the industrial sites that commonly where the biomass is produced. Another example is gasification process, where the biomass is directly heated and broken down into flammable gas. The gas or called ‘biogas’ will be drawn into filtration system to clean and refine before subjected to usage for electricity production.
\nThe fact that major biomass components such as cellulose, hemicellulose and lignin can be fractionated based on different temperatures is exploited with the merging technology of pyrolysis [19–21]. The process involves three stages or heat-based degradation. The first stage includes water elimination, structural deformation and alkyl group formation which is also called pre-pyrolysis. The second stage involves decomposition of components and formation of pyrolysis products. Finally, the last stage produces carbon residuals and bio-oil from charred biomass. Mainly, pyrolysis dealt with cellulose and hemicellulose component conversion, but very little is known about the contribution of this process to lignin fraction. The lignin is merely converted to low concentration of phenolics and char. As it becomes more evident that large amounts of hydrolytic lignin will be produced in future bioethanol plants, lignin has gained interest as a chemical feedstock or aromatic compounds such as catechols, guaiacol, syringol, phenol, furfural, and acetic acid [22, 23].
In a chemical approach, cellulose in a raw biomass can be converted to biofuel. Another new process has been introduced to convert cellulose to chemical 5-hydroxymethylfurfural (HMF). Cellulose, through catalytic conversion, can be converted to HMF [24], and recently formation of HMF through catalytic conversion in ionic liquid produced more than 50% of HMF [25–28]. HMF is oxygen rich and hydrogen deficient that can be used for biofuel production through a reduction process that led to the production of 2,5-hexanedione (HD) [29]. Meanwhile, recently one report indicates that direct electrochemical method to convert HMF to HD without any means of catalysis or hydrogen. Instead HD is produced using water and metal electrode to open up furan ring in HMF and selectively in one-step mode [30].
\nThere is another process called ‘thermochemical’ that involves thorough deconstruction of feedstock and develops the resulting intermediates into different types of fuels and fine chemicals. Thermochemical process consists of three processing parts which include gasification or devolatilisation to produce raw syngas, syngas conditioning and removal of other residual gases such as H2S and CO2 and finally conversion of syngas to fine chemicals such as olefins, aromatic mixed alcohols and fuel for transportation [31].
In general, biological process-based conversion involves cellulosic or hemicellulosic sugar conversion to fuel. Most popular ever known is biofuel such as bioethanol production using microorganism(s) as the catalyst in the bioconversion process. There are two-step processes which include fermentation and pretreatment to obtain the primary sugars [32]. In many publications, cellulose and hemicellulose conversion to biofuel production have been discussed thoroughly and can be read elsewhere [32, 33], and it is necessary to briefly discussed on lignin bioconversion.
\nThough it has inhibitory effect on any cellulose/hemicellulose conversion, if present, lignin can be converted to value-added products such as stand-alone feedstock. Recently, a Rhodococusc sp. can convert lignin into triacylglycerols under nitrogen-limiting conditions [34]. Furthermore, it was demonstrated that lignin valorisation can be channelled by different catabolic pathways of few aromatic catabolising bacteria to produce precursors for fuel production [3]. However, the thermal properties of each aromatic bonding in lignin need an integrated thermochemical process in order to penetrate the bonds [35].
Biomass is usually derived from trees, forest residues, grasses, aquatic plants and crops. They are very important feedstock to produce valuable chemicals and fuel. These plants undergo photosynthesis process to convert carbon dioxide and water to primary and secondary metabolites. Primary metabolites include carbohydrates and lignin which presents in large concentration in biomass. The carbohydrates are simple sugar, cellulose and hemicellulose which take up more than 50% of the content of the biomass. However, some researchers divided the biomass in different moisture contents [36]. The high moisture content biomass includes aquatic plants and manures which have to undergo ‘wet’ processing techniques to convert it to energy. For example, conversion of these materials to biofuel commonly involves degradation of the materials using microorganisms or fermentation. Meanwhile, woody plants or dry biomass involves physical techniques such as gasification, pyrolysis or physical combustion.
Lignin is one of the major components in lignocellulosic biomass together with cellulose and hemicellulose. It intertwined with the cellulose-hemicellulose structural linkage that poses barriers for any physical or biological disturbance through the strong structure of lignin. The structural chemistry of lignin has been discussed and detailed of each of its monomers also presented. In addition, lignin conversion to fine chemicals and fuel has been added and mostly focuses on the present available data.
\nThrough the binding of arrays of carbon-carbon and ether linkages, a single intermonomeric bonding scaffold was formed which is also known as lignin matrix [37]. This complex heterogenous structure of lignin consists essentially from three aromatic alcohols: p-coumaryl, coniferyl and sinapyl alcohols. These monolignols form phenolic substructures such as guaiacyl (G, from coniferyl alcohol), p-hydroxyphenyl (H, from coumaryl alcohol) and syringyl (S, from sinapyl alcohol) as shown in Figure 2. Each chemical structure confers a distinctive characteristic to lignin. Lignins composed mostly of G-units are usually softwood lignins, while lignins with different ratios of G- and S-units are hardwood lignins [37–40].
A segment of lignin polymer structure with monolignols involved in lignin biosynthesis: p-coumaryl alcohol (1), coniferyl alcohol (2) and sinapyl alcohol (3). Possible phenolic structures: guaiacyl (G), p-hydroxyphenyl (H) and syringyl (S). Reprinted from Ref. [38] with permission from Hindawi.
There are few types of native lignin substructures and interunit for different biomass sources as seen in Figure 3. The β-O-4′ (aryl ether) interunit linkage has been identified as a major lignin substructure where it provides a foundation for polymeric framework deconstruction in industrial processes. Some are known to have some resistant to chemical degradation such as β-5′, β-β′, 5-5′, 5-O-4′ and β-1′ [37, 41]. Thus, lignin usually appears in a complicated macromolecule form due to the diversity functional groups and various kinds of linkage of lignin substructures [42]. Lignin usually exists in the form of lignin-carbohydrate complexes (LCCs) resulted from dehydrogenation of G, S and H monolignols. Hence, the covalently linked to hemicellulose lignin and the occurrence of lignin cross-linked to polysaccharides provide mechanical strength to plant cell wall and additional protection to other structures from external [37].
Common interunit linkages in lignin polymeric framework. Reprinted from Ref. [41] with permission of The Royal Society of Chemistry.
High value compound can be produced through biological and chemical conversion of lignin. Processes such as gasification, hydrolysis, oxidation and pyrolysis are a well-known chemical conversion process. A wide range of polymers, chemicals and building blocks can be synthesised from chemically converted lignin [40]. Hydrodeoxygenation (HDO) is an example of chemical conversion method. It involves the removal of oxygen from oxygen-containing molecules in the presence of catalysts with high-pressure hydrogen at moderate temperature. Oxygen is removed to form water via hydrogenolysis reaction and then saturated by hydrogenation reaction [37]. Catalytic HDO of guaiacol (2-methoxyphenol), an oxygen-rich lignin model compound, has been investigated by Aqsha et al. for production of deoxygenated products. Guaiacol conversion products are mainly determined by methoxy, hydroxyl and benzene ring [43].
\nAlternatively, lignin converted from biological process such as enzymatic oxidation and microbial conversion involves living organisms [40]. Lignin-degrading microbes such as ligninolytic peroxidase enzymes or laccase enzymes have been exploited to oxidise aromatic units within lignin complex molecules [44].
Yi-Lin Chung et al. developed a catalytic and solvent-free method for synthesis of a lignin-poly (lactic acid) copolymer. The g-type poly(lactic acid) (PLA) copolymer, synthesised from graft polymerisation of lactide onto lignin, is catalysed by triazabicyclodecene (TBD) as depicted in Figure 4. It displays a glass transition temperature range from 45 to 85°C with multiphase melting behaviour. It also can be used to enhance UV absorption and reduce brittleness without sacrificing its elasticity [45].
Ring-opening polymerisation of lactide (LA) on lignin using triazabicyclodecene (TBD) catalyst scheme. Reprinted with permission from Ref. [45]. Copyright (2013) American Chemical Society.
Barta and Ford devised a novel catalytic system to produce organic liquids from renewable lignocellulose feedstock. Supercritical methanol was used as reaction medium in a single-stage reactor at operating temperature of 300–320°C at 160–220 bar using copper-doped porous metal oxide. This system was tested on organosolv lignin solution (deep brown colour). As summarised in Figure 5, no char was formed during reaction, and the gaseous products were mainly hydrogen gas. The average molecular weight of liquid-phase product is within range of the monomer, and dimer units indicate that organosolv lignin was fully converted [46].
Quantitative analysis of product streams from organosolv lignin substrate. Reprinted with permission from Ref. [46]. Copyright (2014) American Chemical Society.
It is a continuation of previous section, but in this section, the focus is more on hydrogenation process of lignin. In this section, examples of recent literatures reported so far on the hydrogenation of lignin and details on the methods will be discussed.
\nLignin valorisation is an approach or strategy to convert lignin obtained from any sources, especially biomass, into value-added products as shown in Figure 6[47]. Scientists have studied this strategy for many decades through variation of thermal, catalytic and biological approaches in order to break lignin down into its constituent monomers and oligomers as well as upgrading the resulting monomers to fuels or chemicals [48].
Summary of lignin conversion process (note: the abscissa represents the typical temperature range of the lignin conversion processes). Reprinted with permission Ref. [47]. Copyright (2015) American Chemical Society.
The strategy usually involved one or more processes in order to achieve maximum lignin conversion. For example, Gianpaolo Chieffi et al. studied the efficiency of integrating smart recycle and upcycle of biomass-derived waste stream with strategies for the preparation of functional carbonaceous and composite materials using Fe and Ni (cheap and abundant metal precursors) [49].
\nLignin valorisation can be roughly categorised into two sections: (1) upstream which involved separation and isolation process of lignin (e.g. pyrolysis, hydrogenolysis and hydrolysis) and (2) downstream, where valorised products are obtained through depolymerisation and chemical modification of the isolated lignin (e.g. hydrodeoxygenation, catalytic cracking, hydrogenation and dehydrogenation) [50]. In this section, we focus on the downstream process which is to convert the lignin monomers to the fuels and chemicals via hydrogenation.
Hydrogenation is one of the depolymerisation strategies of lignin which utilise hydrogen as a reductant to yield aromatic products with lower oxygen content and higher stability than other strategies (c.f. Figure 6) [47]. This process operates in mild condition affording high-value fine chemicals. However, it is extremely difficult to selectively yield products towards aromatic such as C=C, linear C=C, C=O, C=C, etc. due to the nature of catalysts and reaction conditions. In this process, the selection of the suitable catalysts is the critical parameter to ensure the desired products can be achieved.
Consumption of fossil fuels would decrease significantly by implementing this approach of hydrogenating lignin to obtain the desirable products. Nevertheless, factors such as product selectivity, cost and the conversion efficiency of using commercially available catalysts are still unsatisfactory [51]. Hence, endless research has been carried out in order to overcome these difficulties.
\nYu et al. [52] proposed an in situ catalytic hydrogenation system as relative to conventional method for converting lignin depolymerisation compounds to alcohols. In this work, The Raney Ni has been used for hydrogenation process. They found guaiacol conversion and cyclohexanol selectivity to be 99% and 93.74%, respectively, for 7 h time on stream (TOS). These results were obtained under the optimal conditions of 220°C, initial pressure of 3.0 MPa and mole ratio of H2O/CH3OH/feedstock = 20:5:0.8. Thus, this technique offers a new alternative method for hydrogenation of lignin.
\nThe recent work of Shu et al. [53] utilised a highly efficient and selective hydrogenation process for phenolic compounds at a mild condition over step by step precipitated Ni/SiO2 catalyst. Almost a complete conversion of guaiacol to cyclohexanol was obtained at 120°C, 2.0 MPa for 2 h TOS. The step by step precipitated Ni/SiO2 preparation method thus significantly improved the conversion of the guaiacol (c.f. Figure 7). The structure of catalysts has been significantly modified by increasing the specific surface area and high Ni metal dispersion on the support that translated into high catalytic activity. Furthermore, this method also provides an appropriate acidity of catalyst and, hence, improves the catalytic performance significantly. Interestingly, this method also improves the longevity of the catalyst with an excellent recyclability.
Conversion of guaiacol hydrogenation for different Ni/SiO2 catalysts under 120°C, 2 MPa H2 atmosphere for 2 h. Adapted from Ref. [52] with permission of The Royal Society of Chemistry.
Pd also exhibits a good metal to be doped with Al2O3 as a catalyst for hydrogenation process using wet impregnation technique. The work of Yi et al. (2016) [54] employed 3 wt.%Pd/Al2O3 to convert 4-ethylphenol to cyclohexanols under mild reaction conditions in an aqueous phase. The reaction exhibits 100% conversion at 60°C for 12 h TOS. The catalysts also exhibit water resistance and stability even after recycling four times. This catalyst may provide a new catalyst’s formulation to selectively produce cyclohexanol at mild reaction conditions.
\nOverall, the choice of catalysts is very imperative steps in determining the product selectivity. For example, Raney Ni has been extensively used in hydrogenation of lignin in past decades and regarded as the most common catalysts in hydrogenation process. However, there is not much study in bimetallic catalysts that might be worth to be investigated in order to enhance the product conversion and catalyst’s longevity.
The development of lignin valorisation or degradation remains open for new ideas and approaches. The energy and environmental crises which modern world is experiencing are forcing to re-evaluate the efficient utilisation or finding alternative uses for natural, renewable resources and using clean technologies. In this regard, lignocellulosic biomass holds considerable potential to meet the current energy demand and to overcome the excessive dependence on fossil fuels. Further advanced biotechnologies are crucial for discovery and produce biofuels and bio-chemicals. In current scenario, future trends are being directed to lignocellulosic biotechnology and genetic engineering for improved processes and products [55]. To overcome the current energy problems, it is predicted that lignocellulosic biomass in addition of green biotechnology will be the main focus of the future research [18].
\nCurrently, lignocellulose is processed to product through three steps that include pretreatment, saccharification and fermentation [56]. The chemical pretreatment process has shown it important in the subsequent enzymatic hydrolysis and conversion of cellulosic feedstock to valuable products in the process of fermentation. An analysis of the chemical pretreatment method result shows that the composition of biomass such as hardwood, softwood or grass is the main factor in the selection of pretreatment method [55]. However, any chemical pretreatment that requires lower-cost chemical reagents and conditions and yield more sugar is preferable. The chemical pretreatment process can be divided into six types: acidic pretreatment, alkaline pretreatment, wet oxidation, ionic liquids, oxidative delignification and organosolv [55]. However, it has been reported that chemical pretreatment process adds significantly to the cost of feedstock hydrolysates by consuming energy, expensive catalysts and chemicals while potentially hindering the downstream bioprocess [56, 57], thus requires more research effort, such as the hydrogenolysis of lignin in methanol, however, produced mostly phenols. This clearly shows that the solvent plays an essential role in directing catalytic selectivity and, thus, it must be taken into consideration in the design of catalytic systems for lignin conversion [57].
\nThe necessity of chemical pretreatment of lignin-containing biomass represents a major barrier to downstream fermentation [56] especially involving physical and thermochemical processes that alter the physiochemical recalcitrance of biomass that enhances downstream enzyme digestibility [58–62]. In addition, it has been reported that pretreatment processes modify the polysaccharide matrix reducing overall yield of fermentable sugar or generating by-products that inhibit enzyme hydrolysis and fermentation [63, 64].
\nAlternatively, it has been reported that microbes with tolerance to the inhibitory compounds produced during pretreatment are of industrial interest as fermenters of sources of saccharolytic enzymes and enhances downstream fermentation capabilities, thus potentially eliminate thermochemical pretreatment steps [18]. Indeed, biological pretreatment processes are an environmental-friendly alternative to thermochemical pretreatments, improving biorefinery economics by reducing pretreatment costs, easing inhibitor formation and increasing downstream fermentation [65–67], as reported that a few fungi suitable for wheat straw biological pretreatment and increased sugar recoveries [67].
In a nutshell, the hydrogenation of lignin can potentially become a breakthrough route for production of biofuel if we can unlock the lignin functionality. With the recent findings, it is interesting to observe that the exploitation of lignin valorisation shall make this route become viable and efficient to produce biofuel via hydrogenation of lignin. Further advanced biotechnologies are crucial for discovery such as more efficient biological pretreatment system, bioprospecting and development of stable genetically engineering microorganisms, improved gene cloning and sequencing technologies, characterisation of new enzymes and production in homologous or heterologous systems and ultimately lead to low-cost conversion of lignocellulose biotechnology for improved processes and productions based on economies of scale more efficient and cost-effective conversions of lignin into value-added products. To overcome the current energy problems, it is envisaged that lignocellulosic biomass in addition of green biotechnology will be the main focus of the future research.
The constant necessity of looking for new alternatives to produce sustainable versions of products has led to the discovery and development of new technique and biological models. Organisms with the potential of producing molecules that can be used for the development of bioproducts in different areas (food, beauty, health, and biodiesel, among others) have led to the discovery, study, and use of new organisms. Algae and microalgae have become potential and promising model organisms to be used for carbohydrate production and use, but besides that, it is also deeply studied due to its lipids, proteins, and photosynthetic activity, making them a prospective source of bioenergy production [1, 2].
\nThe problems associated to the first- and second-generation feedstock for biofuels have seen to become more and more complicated to solve considering the food crisis and complex conversion of lignocellulosic materials [3] researchers, has led to the exploration of a third-generation feedstock, mostly represented by photosynthetic organisms, primarily algae/microalgae [4].
\nMicroalgae are considered to have the potential to produce third-generation biodiesel (due to its capability of fixing carbon dioxide (CO2), which is eventually converted to biomass and other products), which can also be referred as third-generation feedstock, providing mainly lipids, proteins, and carbohydrates. The utilization of these molecules in a sequential way allows the treatment of biomass in biorefineries, including its use in fermentative production of a range of platform biochemical [5]. Through this process, carbohydrates are used as a fundamental piece for the production of certain products.
\nBesides the cell wall and reserves of photosynthetic reaction, the carbohydrates can be excreted by the cell. The exopolysaccharides (EPS) are complex carbohydrates produced from some microalgae, which are long chains composed of sugar derivative structures, mucilaginous and with reactive functional groups, such as sulfate, hydroxyl, or carboxylic [6]. The major components of EPS include mainly the polysaccharides and others as proteins, nucleic acid, and lipids [7]. Addition of these molecules is considered to be of extreme importance for enriching the nutritional value of food items [8]. Although these characteristics are beneficial, the extraction of these compounds from microalgae becomes a real challenge. In this context, several treatments can be performed for the disruption of microalgal cells, including chemical modifications and mechanical, thermal, or ultra-sonication processes [9].
\nAlthough promising, it is still hard to manage the cost and work that developing new technologies have for investors (in the industry for applied approaches and academia for basic development and standardization), which presents some limitations for the advance of research in this area. On the long run, an implementation of the use of microalgae as a substitute for many of the other crop options still used will have an important impact on the economics, environment, and more sustainable practices.
\nDue to the vast diversity of species of microalgae, we present an analysis of the current trends and importance and potential of the use of carbohydrates present in microalgae. The aim of highlighting these points is to bring awareness and present new alternatives of methods that will allow the use of carbohydrates in microalgae without the breakdown of these carbohydrates, as a way of improving and lowering cost and making the use of these organisms a more feasible way of developing new products and technologies [10]. The main topics that will be discussed in this chapter can be seen in Figure 1.
\nDiagram of the main topics involved in the harnessing of microalgae carbohydrates.
Carbohydrates from microalgae are considered to have a great application in industry, which has led to the development of new techniques and studies but that has exposed new challenges to industry [11, 12]. The diversity of microalgae, the composition, and cell organization are some of the few trials that many scientists are currently facing.
\nCarbohydrates are poly- or oligosaccharides that can be present in vacuoles and cell walls or that could also be excreted as exopolysaccharides (EPS) [13]. Microalgae come to be an interesting key organism to study due to the high content of carbohydrates that some of them have. Some examples are Desmodesmus spp. (41%) from wastewater and landfill leachate treatment [14], Chlorella stigmatophora (~55%) [5], or Chlorella vulgaris (60% [15] or >52% [16]) cultivated under conditions of nitrogen depletion.
\nSimilarly, indigenous microalgae species have been bioprospected in nitrogen-depleted environments, such as Desmodesmus sp. (57%), an unidentified one with more carbohydrate content (70%) [17], and Arthrospira platensis that accumulated up to 74% of carbohydrates [18].
\nDespite their vast potential, using different species imposes a few challenges when trying to establish a consistent methodology for extraction and use. Based on the differences in metabolism that each species presents, a possible and feasible approach is to consider that they all have reserves made out of polymers of glucose (glucans), such as chrysolaminarin (1:11), laminarin (3:1) (β-1,3 and β-1,6 branches), paramylon(β-1,3), glycogen-type, cyanophycean, floridean (semi-amylopectin: α-1,4 and α-1,6 branches), and amylose-type starch (α-1, 4) or both (Figure 2). The external covering of cell with polysaccharides could be peptidoglycan matrices, cellulosic wall, and galactose polymer matrix, and others [18, 19, 20].
\nGlucose polymers found in microalgae.
The potential of using microalgae for the development of various products, using carbohydrates as the main source, exposes some of the challenges that using these organisms can have. The main of it is the process of extraction of the diverse saccharides present in each species, but in comparison with plant-derived products, it is actually a much easier path, since they do not present lignification of the cell wall [11, 21]. In the same way, having various species together as a main feedstock source may require adaptations to a proper and more efficient method of extraction.
\nMicroalgae use for development of new products that could be beneficial to multiple industries has raised many questions in the quest of finding what will be the next technology that will be developed, what products will change our industries, and how this could benefit populations. As we know, the use of microalgae carbohydrates could be a solution to many current limitations that agriculture, pharmacy, nutrition, and other areas are facing while trying to develop better solutions to fulfill the needs of people [22].
\nOne of the main reasons for the development of new technologies and the arise of trends is to be able to satisfy the demands of the public and produce the income that the market will like to have in return for investing in these areas. Unfortunately, it is still a difficult task since there is still a long way to go for developments of products outside of the food industry.
\nCarbohydrates/starch is considered to be a positive/beneficial step for the chemical development of products, and when produced in high quantities, its use for fermentation is considered a better option. To date, the most common way to induce the production of specific molecules (in this case, carbohydrates and starch) is by creating stress conditions in the environment where the alga is growing, mainly by altering nutrient concentrations or by changing light, temperature, and other parameters [23, 24].
\nPhotosynthetic electron transport approach seems to be the most researched area [25] since genetic modification of algae becomes challenging due to the great variety of species. Cyanobacteria are being used more for genetic engineering, but no complete success has come out it yet. Besides the interest cyanobacteria, some algae species have been explored as potential species for biofuel production through modification of metabolic pathways that could increase the production of carbohydrates, lipids, and other compounds, but the progress in this area has seen to be slow, which although discouraging is still considered one of the main focus for the future of biotechnologies in microalgae [26].
\nMicrobiome studies of microalgae populations seem to focus more on the ecology aspects and the importance of their use in multiple biological processes. Toxicity of waters seems to attract the attention of most research groups. Its importance lies in not only the understanding of structure communities and safety of fresh water resources (which is the main source of drinking water for the world) but also the discovery of new species that may be hard to culture through regular isolation practices.
\nSimilarly, human microbiome studies seem to be interested in the potential use of carbohydrates (including exopolysaccharides) derived from microalgae, due to its prebiotic potential, improving the health of adults and infants that cannot consume breast milk in their early stages, strengthening their immune responses [12, 27].
\nSome microalgae species are capable of accumulating a large amount of intracellular starch and have structural polysaccharides in their cell walls [28]. However, the development of standard analytical procedures for the characterization of microalgae biomass has been difficult because of the existence of several microalgae species with different cellular structures and chemical compositions [28]. Even a specific microalgae species may present variability in their chemical composition because they can strongly be affected by factors of cultivation conditions such as temperature, salinity, and nutrient availability [9]. Thereby, sample preparation for the determination of carbohydrates in microalgae is very complex.
\nThe analytical method applied depends on the intended usage of the algal carbohydrates. Some require the qualitative or quantitative composition of the monosaccharides and others the total carbohydrate analysis [29].
\nIn algal biomass, the carbohydrate profile analysis requires preliminary acid hydrolysis. Acid hydrolysis allows depolymerizing the intracellular starch and structural polysaccharides into their monomers, which are then further quantified [28]. The optimal hydrolysis conditions (acid, temperature, and time) should ensure complete hydrolysis of the polysaccharides and at the same time avoid excessive degradation of monosaccharides [29].
\nIn this context, the selective cleaving of algal polysaccharides by enzymatic hydrolysis is another promising approach once the formation of degradation products like furfural or hydroxymethylfurfural is avoided [29]. However, for some microalgae species, the composition of the cell wall is complicated and unknown; also, some enzymes are very expensive [30]. The cell wall present in the microalgae limits extraction yields of high-value products or results in a low bioavailability of intracellular components [9, 30].
\nThe methodology widely employed in acid hydrolysis is the procedure published by the National Renewable Energy Laboratory (NREL) based on two-step hydrolysis using H2SO4 [31, 32]. Despite being a reliable method, it is a multistep procedure, increasing the chance of experimental errors, and also presents a high time of sample preparation. Northcote et al. [33] proposed another method based on one-step acid hydrolysis with dilute H2SO4 and use smaller biomass samples.
\nOther methods use chemical extraction method like alkaline pretreatment [34] and physical method, such as hot-water treatment, microwave-assisted extraction, and ultrasonic-assisted extraction [30, 35]. The choice of extraction method is that the pretreatment is effective qualitatively and quantitatively, and the technology is simple to operate and economical for scale-up [30].
\nZhao’s research team [30] investigated three methods of conventional solvent extraction (CSE), fluidized bed extraction (FBE), and ultrasonic-assisted extraction (UAE) to obtain an effective extraction method of carbohydrates/glucose. The CSE employed lyophilized microalgae extracted with distilled water and agitation in a vortex. For FBE, the Chlorella sp. culture was harvested and washed with distilled water and then diluted using distilled water and added into a fluidized reactor with air aeration. To UAE, the algal cells were harvested and washed with distilled water, diluted, and taken to the ultrasonic processor. The ultrasonic-assisted extraction was more effective than the other methods.
\nInformation in the literature related to the amount of cell wall microalgae polysaccharides is scarce. Usually, the quantification of polysaccharides in microalgal is made by analyzing the total carbohydrate, thus including storage polysaccharides (SPS) and cell wall-related polysaccharides, which exhibit different functions in the microalgal cell [9].
\nAccording to Bernaerts et al. [9], the insight into the composition of cell wall-related polysaccharides, such as the monosaccharide profile or the degree of sulfation, is not only desired in terms of process optimization but also as a potential for several biotechnological. Thereby, the authors investigated to apply a universal procedure for extraction of the total cell wall-related polysaccharides, including cell wall polysaccharides (CWPS) and extracellular polymeric substances (EPMS), of 10 commercially available microalgae species followed by a characterization of the monosaccharide profile, uronic acid content, and sulfate [9]. Initially, the procedure consisted of dry biomass suspended in saline solution incubated for 16 h at 25°C, followed by a two-step centrifugation. Afterward, the supernatant was submitted for extraction of EPMS and the residual biomass (pellet) for extraction of CWPS. Ethanol was added to the supernatant precipitating EPMS; the solution was vacuum filtered, and the insoluble residue was dialyzed against demineralized water for 48 h, and finally, the extracts were lyophilized.
\nIn the extraction of CWPS, the pellets were suspended in MOPS buffer, and the cells were disrupted using UHPH after cold ethanol was added to the suspensions and for pellet recovery. Lipids were removed by addition of hexane/isopropanol to the pellet, mixed and centrifuged to remove the upper solvent layer. Afterward, SPS and protein were enzymatically removed using endo-β-1,3-glucanase or a combination of α-amylase/amyloglucosidase and Subtilisin A protease, respectively. The mixtures were incubated and after addition of cold ethanol they were centrifuged. The pellet was finally washed in acetone, vacuum filtered, and dried overnight at 40°C, and this residue was considered as CWPS. Monosaccharide and uronic acid composition of CWPS and EPMS were hydrolyzed according to De Ruiter et al. [36] using methanolysis combined with trifluoroacetic acid (TFA) hydrolysis.
\nAfter sample preparation, carbohydrate analysis is a very complex field. Usually, after microalgal acid hydrolysis, the total carbohydrate content of the hydrolysate can be determined using colorimetric procedures like the phenol-sulfuric acid [37, 38, 39] or anthrone-based [40, 41, 42]. These methods are available, giving excellent and robust results with low effort in a very short time. Nevertheless, detailed information about the monosaccharide composition cannot be generated [29]. Qualitative investigations can be performed using TLC methods with silica-based separation materials making the separation of most monosaccharides possible. However, quantification with the TLC methods is not possible [29], and for quantification of monosaccharides, analytical methods such as high performance liquid chromatography (HPLC) are often used. The HPLC equipped with a refractive index detector (RID) [32] and HPLC combined with pulsed amperometric detection (HPAEC-PAD) [9, 28] and liquid chromatography mass spectrometer (LC–MS) [29] were related.
\nThe trends for carbohydrate analysis are the exploration of methods that study both cell wall polysaccharides and extracellular polymeric substances. The developed methods always aim to use small amounts of sample, reagents, and shorter analysis. Liquid chromatography has been highlighted in the carbohydrate determination since it presented a good separation and quantification of these compounds. Although it is a more expensive analytical technique, it provides data on the composition of individual monomeric sugars that make it of interest for this type of analysis.
\nMicroalgae have several types of polysaccharides in their composition, such as phycocolloids, agar, alginate, carrageenan, fucoidan, ulvana, and cellulose, among others. phycocolloids can be formed by different monomers such as glucose, galactose, mannuronic acid, guluronic acid, mannitol, and laminarin. These carbohydrates can be inserted into functional beverages and food products such as functional bread, ready to serve soups, functional snack foods and a variety of sauces, creams, bakery products, and additional food products [43, 44].
\nDue to the high carbohydrate content, poultry and aquaculture feed is one of the main study targets for the use of microalgae biomass. In 2007, around 30% of the world’s current algae production was sold for animal feed application [8]. Microalgae are also a suitable alternative for growing fish, larvae, and zooplankton. Chlorella is one of the main examples of microalgae that can play a key role in food and feed due to the properties of its biomass, which can simultaneously provide high concentrations of carbohydrates, vitamins, and proteins [45]. Besides Chlorella, other species used in aquaculture can be highlighted: Tetraselmis, Isochrysis, Pavlova, Phaeodactylum, Chaetoceros, Nannochloropsis, Skeletonema, and Thalassiosira. Spirulina and Chlorella microalgae can be applied in the feeding of cats, dogs, aquarium fish, ornamental birds, horses, birds, cows, and breeding bulls. The most common genera of larval microalgae include Chaetoceros, Thalassiosira, Tetraselmis, Isochrysis, and Nannochloropsis [46].
\n1,3-β-glucan is an important carbohydrate present in microalgae composition due to its applications in the food industry as a thickener, and health applications, especially in the protection against infections and also to inhibit cancer cell growth in vivo [44, 47]. According to [48], the global β-glucan market was valued at USD 307.8 million in 2016, and it is predicted that in 2022, the global carbohydrate market could reach up to USD 476.5 million, which indicates the huge potential for development in many different types of applications.
\nAccording to Koller et al. [49], sulfated polysaccharides produced by microalgae can be applied in therapies against bacterial infections. Carrageenan polysaccharide, also known as food additive E407, can be used in pharmaceutical applications. Marine carbohydrates have been widely used in the cosmetics industries due to their chemical and physical properties. Brown algal fucoidans/alginates, green algal ulcers, and red algal carrageenans/agar are used as gelling, thickening, and stabilizing agents. In addition, marine carbohydrates have potential skin benefits, and biological activities are linked to their structure as determined by molecular weights or the presence of sulfate groups and other sugars [50].
\nRed algae, such as Chondrus sp., Gigartina sp. Eucheuma sp., Hypnea sp., and Furcellaran sp., are widely used for the production of carrageenan. This compound can be used in food and pharmaceutical industries for applications in fruit gel, fruit juices, sweets, and jellies, among others. Another carbohydrate group molecule is fucoidan, which is associated with brown algal cell wall components (Phaeophyceae). Among the bioactivities derived from this molecule, the anticoagulant, antitumor, antivirus, and antioxidant properties stand out, making it attractive for pharmaceutical applications [51].
\nBesides these applications, the remaining biomass of microalgae presents carbohydrate-rich molecules, which have been widely used in the production of bioplastics, agar, sugars, and other high-added value chemicals. However, despite being a growing area, the biorefinery stage must be studied in order to extend its applicability on an industrial scale [51]. According to Mihranyan [52], the rheological behavior of cellulose found in Cladophora algae is similar to micro fibrillated cellulose. Because this cellulose is very robust and not susceptible to chemical reactions, the properties of cellulose found in these algae provide excellent rheological properties making this material interesting in food, pharmaceuticals, paints, dressings, and biodegradable plastic applications.
\nThe high carbohydrate content and low-ash values make microalgae more suitable for conversion to biofuels [43]. The production of bioethanol from microalgae gained importance due to their high biomass productivity, diversity, variable chemical composition, and high photosynthetic rates of these organisms [53]. Due to the large amount of carbohydrates/polysaccharides and cellulose walls, these microorganisms become favorable for the production of this biofuel [54, 55]. In many countries, ethanol is produced on a large scale from crops containing sugars and starches in its composition through fermentation. The biomass is ground, and the starch is converted into sugars by different methods. Polysaccharide starch is also accessible as a storage material for various algal species and can be anaerobically converted into bioethanol [49].
\nMicroalgae biomass conversion technologies involve carbohydrates as the main source in the production of biofuels and other compounds of high commercial value. Changes in metabolic pathways aiming at increased carbohydrate production are seen as a potential for enhancing microalgae biotechnology. Extraction methods and trends in analytical methodologies focus on microalgae cell wall polysaccharides and the polymers excreted by these microorganisms. The high carbohydrate content makes microalgae excellent candidates for the production of numerous biocomposites, especially beta-glucan, which is on the international market, indicating its strong potential for its use in different biotechnological applications.
\nThis is a brief overview of the main steps involved in publishing with IntechOpen Compacts, Monographs and Edited Books. Once you submit your proposal you will be appointed a Author Service Manager who will be your single point of contact and lead you through all the described steps below.
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\\n\\nPlease complete the publishing proposal form. The completed form should serve as an overview of your future Compacts, Monograph or Edited Book. Once submitted, your publishing proposal will be sent for evaluation, and a notice of acceptance or rejection will be sent within 10 to 30 working days from the date of submission.
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\n\nPlease complete the publishing proposal form. The completed form should serve as an overview of your future Compacts, Monograph or Edited Book. Once submitted, your publishing proposal will be sent for evaluation, and a notice of acceptance or rejection will be sent within 10 to 30 working days from the date of submission.
\n\n2. SUBMIT YOUR MANUSCRIPT
\n\nAfter approval, you will proceed in submitting your full-length manuscript. 50-130 pages for compacts, 130-500 for Monographs & Edited Books.Your full-length manuscript must follow IntechOpen's Author Guidelines and comply with our publishing rules. Once the manuscript is submitted, but before it is forwarded for peer review, it will be screened for plagiarism.
\n\n3. PEER REVIEW RESULTS
\n\nExternal reviewers will evaluate your manuscript and provide you with their feedback. You may be asked to revise your draft, or parts of your draft, provide additional information and make any other necessary changes according to their comments and suggestions.
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\n\nIf the manuscript is formally accepted after peer review you will receive a formal Notice of Acceptance, and a price quote.
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