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Claudio J.A. Mota, PhD, is Professor of Chemistry and Chemical Engineering and head of the Institute of Chemistry at the Federal University of Rio de Janeiro, Brazil. He has taught and published extensively on green chemistry, catalysis, biomass conversion, as well as CO2 capture and conversion.
Ana Lúcia de Lima, PhD, is Associate Professor at the Institute of Chemistry, Federal University of Rio de Janeiro, Brazil. Her research concerns synthesis of materials for CO2 capture, biomass conversion, and catalysis.
Daniella R. Fernandes, PhD, is Associate Professor at the Institute of Chemistry, Federal University of Rio de Janeiro, Brazil. Her research concerns development of materials for biomass transformation and carbon capture.
Bianca P. Pinto, PhD, is a researcher at the Laboratory of Reactivity of Hydrocarbons, Biomass and Catalysis, Federal University of Rio de Janeiro, Brazil. She is also the co-founder of CarbonAir Energy, a startup devoted to sustainable energy. Her research focuses on CO2 capture and biomass transformation.
About the Authors ix
Preface xi
1 Levulinic Acid - History, Properties, Global Market, Direct Uses, Safety 1
1.1 History and Properties 1
1.2 Global Market 8
1.3 Direct Uses 10
1.4 Toxicity of Levulinic Acid and Inorganic Levulinates 12
1.5 Concluding Remarks 13
References 15
2 Production and Technological Routes 19
2.1 Production and Technological Routes from Biomass 19
2.2 Pretreatment of Lignocellulosic Biomass 23
2.2.1 Physical Pretreatment 23
2.2.1.1 Mechanical 24
2.2.1.2 Microwave 25
2.2.1.3 Ultrasound 25
2.2.2 Chemical Pretreatment 25
2.2.2.1 Acid Hydrolysis 25
2.2.2.2 Alkaline Hydrolysis 26
2.2.2.3 Ionic Liquids 27
2.2.2.4 Organosolv 27
2.2.3 Physicochemical Pretreatment 28
2.2.3.1 Steam Explosion (SE) 29
2.2.3.2 Liquid Hot Water (LHW) 29
2.2.3.3 Ammonia Fiber Expansion (AFEX) 30
2.2.3.4 Supercritical CO 2 Explosion 30
2.2.4 Biological Pretreatment 31
2.3 Production of Levulinic Acid from Lignocellulosic Biomass 32
2.3.1 Processes for LA Production: Homogeneous Catalysts 35
2.3.2 Processes for LA Production: Heterogeneous Catalysts 38
2.3.3 Processes for LA Production: Biphasic Systems 40
2.3.4 The Biofine Process of LA Production 41
2.3.5 Downstream Process of LA Recovery 42
2.4 Commercial Plants for the Production of LA 44
2.5 Conclusion 47
References 47
3 Levulinate Derivatives - Main Production Routes and Uses of Organic and Inorganic Levulinates Derivatives 65
3.1 Main Production Routes 65
3.1.1 Esterification of Levulinic Acid 65
3.1.2 Direct Production from the Alcoholysis of Polyschacarides 71
3.1.3 Alcoholysis of Furfural 76
3.1.4 Alcoholysis of 5-Hydroxymethyl Furfural 82
3.1.5 Production of Levulinate Inorganic Salts 86
3.2 Importance and Market of the Levulinate Derivatives 87
3.3 Uses of Organic Levulinate Derivatives 88
3.3.1 Food and Cosmetic 88
3.3.2 Fuel Additives 89
3.3.3 Plasticizers 90
3.3.4 Solvents 91
3.4 Uses of Inorganic Levulinate Derivatives 93
3.4.1 Antifreeze Additive 93
3.4.2 Cosmetic, Pharmaceutical, and Food 93
3.4.3 Miscellaneous Applications 94
3.5 Conclusion 95
References 96
4 Levulinic Acid Hydrogenation 107
4.1 Levulinic Acid Hydrogenation Products 107
4.1.1 ¿-Valerolactone (GVL) 107
4.1.1.1 GVL Versus Ethanol 111
4.1.1.2 2-Methyl-tetrahydrofuran (2-MTHF) 111
4.1.1.3 1,4-Pentanediol (1,4-PDO) 112
4.1.1.4 Alkyl Valerates 113
4.2 Performance of GVL as Fuel Additive 113
4.3 Levulinic Acid to ¿-Valerolactone 114
4.3.1 Conversion of GVL into 1,4-PDO and 2-MTHF 115
4.3.2 GVL to Butenes and Hydrocarbons 117
4.4 Homogeneous and Heterogeneous Catalysts for the Efficient Conversion of LA to GVL 121
4.4.1 Precious Metal Catalysts 121
4.4.2 Nonprecious Metal Catalyst 125
4.4.2.1 Copper-Based Catalysts 125
4.4.2.2 Nickel-Based Catalysts 127
4.4.2.3 Zirconium-Based Catalysts 130
4.4.2.4 Iron-Based Catalysts 130
4.5 Heterogeneous Catalysts for the Conversion of LA and GVL to 1,4-PDO and 2-MTHF 132
4.6 Types of Hydrogenating Agents 135
4.7 Patent Search of LA Hydrogenation 137
4.8 Conclusion 138
References 138
5 Carbonyl Reactions of Levulinic Acid - Ketals and Other Derivatives Formed Upon Reaction with the Carbonyl Group of Levulinic Acid. Production Routes, Technologies, and Main Uses 149
5.1 Levulinc Acid Ester Ketals Main Routes 150
5.1.1 Levulinic Acid Ester Ketals Main Uses 153
5.2 Succinic Acid 158
5.2.1 Petrochemical and Biotechnological Routes 158
5.2.2 Levulinic to Succinic Acid 163
5.2.3 Succinic Acid Main Uses 164
5.3 d-Aminolevulinic Acid (DALA) Main Routes 167
5.3.1 d-Aminolevulinic Acid Main Uses 169
5.4 5-Methyl-N-Alkyl-2-Pyrrolidone Main Routes 171
5.4.1 5-Methyl-N-Alkyl-2-Pyrrolidone Main Uses 177
5.5 Diphenolic Acid Main Routes 179
5.5.1 Diphenolic Levulinic Acid Main Uses 181
5.6 Conclusion 185
References 185
6 Levulinic Acid in the Context of a Biorefinery 197
6.1 Biorefinery 197
6.2 Sugar-Based Biorefinery 198
6.3 Levulinc Acid and Levulinates from a Sugar Cane Biorefinery 200
6.4 Production of ¿-Valerolactone in a Sugar Cane Biorefinery 201
6.5 LA in the Context of a Biodiesel Plant 204
6.6 Conclusions 206
References 207
Index 209
The first evidence for the formation of levulinic acid was obtained from the treatment of sugars with dilute acid solutions. The Italian-French Pharmacist Faustino Jovita Malaguti (Figure 1.1) reported, in 1835 [1], the treatment of sucrose with boiling diluted acid solutions, being able to identify formic acid and other ammonia-soluble compounds. In 1840, the Dutch chemist Gerardus Johannes Mulder reported the treatment of fructose with hydrochloric acid and was able to isolate acidic compounds [2]. Although these two scientists did not explicitly identify levulinic acid among the products, they were the first to conduct experiments in which levulinic acid would be formed. Nevertheless, the first identification of levulinic acid from the acid treatment of sugars was reported by Tollens in 1875 [3].
Levulinic acid (LA) is a keto-carboxylic acid bearing carbonyl and carboxyl groups in its structure (Figure 1.2). Therefore, the double functionalization makes it an interesting chemical for multiple purposes. Reactions involving levulinic acid are known since the 1870s, but the development of commercial processes and uses were not significant until the 1940s, mostly because of the high costs of the raw materials at the time, high capital costs, and low yields. With the use of cellulose-based feedstocks [4], the production of levulinic acid became more attractive motivating its general use.
Levulinic acid is the 4-oxo-pentanoic acid according to the International Union of Pure and Applied Chemistry (IUPAC) nomenclature. It may also be regarded as the 4-oxo-valeric acid. In the pure form, it is a solid that melts at 30-33?°C and boils at 245-246?°C at atmospheric pressure. Table 1.1 shows some selected properties of levulinic acid.
The first commercial production of levulinic acid dates from the 1940s when the A.E. Staley Manufacturing Company started a bath production using starch as raw material. The process [5] involves the initial mixing of proper amounts of starch and diluted hydrochloric acid at 100?°C in a preheater system. Then, the reaction mixture was autoclaved at 175-215?°C for a determined period. The effluent was neutralized with soda ash and the humins, which are insoluble by-products, were separated by filtration, whereas water and formic acid, formed as a by-product, were evaporated from the solution and the sodium chloride by centrifugation. Levulinic acid was obtained, like a light-colored liquid, upon vacuum steam distillation (Figure 1.3).
Figure 1.1 Faustino Jovita Malaguti (1802-1878) (https://www.redalyc.org/jatsRepo/1816/181662291006/html/index.html).
Source: CITMATEL.
Figure 1.2 Structure of levulinic acid.
Starch is a biopolymer made of hexoses, mainly glucose, that may be obtained from wheat, potato, and oat among numerous other crops. The chemical pathway from C6 sugars to levulinic acid is depicted in Scheme 1.1. The acid medium dehydrates the carbohydrates to intermediate compounds, like hydroxymethyl furfural (HMF), which can then be converted into levulinic acid also releasing a molecule of formic acid in the process.
Table 1.1 Selected properties of levulinic acid.
In the 1950s, the Quaker Oats Company developed a process to produce levulinic acid based on furfuryl alcohol as raw material. The company started producing furfural from sugarcane bagasse or corn cobs in 1922 [6, 7], upon heating the biomass in an aqueous solution of sulfuric or phosphoric acid. Furfural is an aromatic aldehyde mostly used in the production of resins at that time. In 1934, the company began the production of furfuryl alcohol from the high-pressure hydrogenation of furfural in Memphis, Tennessee, United States [8]. Then, a continuous process was developed, achieving 99% conversion of furfural in furfuryl alcohol with the use of copper-supported catalysts [9]. The production of levulinic acid from furfuryl alcohol began in 1957 and ended in 1972. The process involved the heating of furfuryl alcohol in the presence of aqueous hydrochloric acid, but small alcohol, such as methanol and ethanol, could also be employed affording the respective levulinate esters [10]. In the beginning, the company did not have enough uses for the levulinic acid produced. In 1959, Quaker Oats released [11] a contest for someone to bring a big idea on a commercial use of levulinic acid (Figure 1.4).
The overall chemical pathway to produce levulinic acid from C5 sugars is shown in Scheme 1.2. The pentoses are initially dehydrated to furfural in the acidic medium, usually hydrochloric acid. Then, in a second process, furfural is hydrogenated to furfuryl alcohol, which is further converted to levulinic acid upon acid-catalyzed hydrolysis.
Figure 1.3 Flow diagram of levulinic acid production process.
Scheme 1.1 Schematic reaction pathway for the production of levulinic acid from hexoses.
A biotechnological route to levulinic acid involving multiple steps has also been suggested [12]. It involves the fermentation of sugars, like glucose and fructose, to pyruvic acid as the first step (Scheme 1.3). The next steps may also involve biocatalysts. For instance, acetaldehyde can be produced from pyruvic acid with the use of pyruvate decarboxylase. In the same way, aldolases may be employed in the aldol condensation step. Dehydration of the 2-hydroxy-4-oxo-pentanoic acid, followed by the selective hydrogenation of the intermediate to levulinic acid, may be carried out either through biocatalysis or homogeneous/heterogeneous catalysis. Although technically feasible, this route has not been employed industrially, probably because of the numerous steps, which may require specific reaction conditions and separation procedures, significantly increasing the production costs.
Figure 1.4 Advertisement of the contest for uses of levulinic acid in 1959.
Source: Reproduced with the permission of the American Chemical Society.
Scheme 1.2 Schematic reaction pathway for the production of levulinic acid from pentoses.
Scheme 1.3 Biotechnological route for the synthesis of levulinic acid.
A fossil-based route to levulinic acid has also been developed [13]. The raw material is maleic acid, which is normally obtained from oxidation of benzene [14] or butenes [15]. However, recent developments point out possible routes from renewable feedstocks [16]. Scheme 1.4 shows the steps, which involve the decarboxylation of acetyl succinate.
The DSM company in Linz, Austria, has developed a small-scale process to produce 3?tons per day of levulinic acid from maleic acid, with an overall yield of about 80%. Nevertheless, the company has moved the production of levulinic acid from bio-based raw materials, discontinuing the fossil-based route.
Levulinic acid is a bifunctional molecule, having a keto-carbonyl and a carboxylic acid group. Therefore, it is expected to present the chemical properties of ketones and carboxylic acids. Scheme 1.5 shows the most common transformations of the levulinic acid molecule.
The levulinate esters find applications as fuel additives [17], as well as fragrancies. Inorganic levulinate salts are also important specialty chemicals; sodium levulinate is used in the cosmetic and food industry as preservative [18], whereas calcium levulinate is used in pharmaceutics and as a supplementary source of calcium. Hydrogenation may lead to different products. The ?-valerolactone (GVL) is normally produced upon the hydrogenation of...
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