| Literature DB >> 35267704 |
Antonio M Borrero-López1, Concepción Valencia1, José M Franco1.
Abstract
The present review is devoted to the description of the state-of-the-art techniques and procedures concerning treatments and modifications of lignocellulosic materials in order to use them as precursors for biomaterials, biochemicals and biofuels, with particular focus on lignin and lignin-based products. Four different main pretreatment types are outlined, i.e., thermal, mechanical, chemical and biological, with special emphasis on the biological action of fungi and bacteria. Therefore, by selecting a determined type of fungi or bacteria, some of the fractions may remain unaltered, while others may be decomposed. In this sense, the possibilities to obtain different final products are massive, depending on the type of microorganism and the biomass selected. Biofuels, biochemicals and biomaterials derived from lignocellulose are extensively described, covering those obtained from the lignocellulose as a whole, but also from the main biopolymers that comprise its structure, i.e., cellulose, hemicellulose and lignin. In addition, special attention has been paid to the formulation of bio-polyurethanes from lignocellulosic materials, focusing more specifically on their applications in the lubricant, adhesive and cushioning material fields. High-performance alternatives to petroleum-derived products have been reported, such as adhesives that substantially exceed the adhesion performance of those commercially available in different surfaces, lubricating greases with tribological behaviour superior to those in lithium and calcium soap and elastomers with excellent static and dynamic performance.Entities:
Keywords: adhesives; biochemicals; biofuels; biomaterials; cellulose; cushioning materials; lignin; lignocellulose; lubricating greases; rheology
Year: 2022 PMID: 35267704 PMCID: PMC8912558 DOI: 10.3390/polym14050881
Source DB: PubMed Journal: Polymers (Basel) ISSN: 2073-4360 Impact factor: 4.329
Composition of representative lignocellulosic feedstocks [12].
| Feedstocks | Carbohydrate Composition (% Dry Weight) | ||
|---|---|---|---|
| Cellulose | Hemicellulose | Lignin | |
| Barley hull | 24 | 36 | 19 |
| Barley straw | 36–43 | 24–33 | 6.3–9.8 |
| Bamboo | 49–50 | 18–20 | 23 |
| Banana waste | 13 | 15 | 14 |
| Corn cob | 32.3–45.6 | 39.8 | 6.7–13.9 |
| Corn stover | 35.1–39.5 | 20.7–24.6 | 11.0–19.1 |
| Cotton | 85–95 | 5–15 | 0 |
| Cotton stalk | 31 | 11 | 30 |
| Coffee pulp | 33.7–36.9 | 44.2–47.5 | 15.6–19.1 |
| Douglas fir | 35–48 | 20–22 | 15–21 |
| Eucalyptus | 45–51 | 11–18 | 29 |
| Hardwood stems | 40–55 | 24–40 | 18–25 |
| Rice straw | 29.2–34.7 | 23–25.9 | 17–19 |
| Rice husk | 28.7–35.6 | 11.96–29.3 | 15.4–20 |
| Wheat straw | 35–39 | 22–30 | 12–16 |
| Wheat bran | 10.5–14.8 | 35.5–39.2 | 8.3–12.5 |
| Grasses | 25–40 | 25–50 | 10–30 |
| Newspaper | 40–55 | 24–39 | 18–30 |
| Sugarcane bagasse | 25–45 | 28–32 | 15–25 |
| Sugarcane tops | 35 | 32 | 14 |
| Pine | 42–49 | 13–25 | 23–29 |
| Poplar wood | 45–51 | 25–28 | 10–21 |
| Olive tree biomass | 25.2 | 15.8 | 19.1 |
| Jute fibres | 45–53 | 18–21 | 21–26 |
| Switchgrass | 35–40 | 25–30 | 15–20 |
| Winter rye | 29–30 | 22–26 | 16.1 |
| Oilseed rape | 27.3 | 20.5 | 14.2 |
| Softwood stem | 45–50 | 24–40 | 18–25 |
| Oat straw | 31–35 | 20–26 | 10–15 |
| Nut shells | 25–30 | 22–28 | 30–40 |
| Sorghum straw | 32–35 | 24–27 | 15–21 |
| Tamarind kernel powder | 10–15 | 55–65 | - |
| Water hyacinth | 18.2–22.1 | 48.7–50.1 | 3.5–5.4 |
| Miscanthus * | 37 | 29 | 10 |
| Oat husks ** | 23 | 35 | 25 |
* Adapted from [15]. ** Adapted from [16].
Figure 1Main monolignol units. p-coumaryl alcohol, coniferyl alcohol and sinapyl alcohol, from left to right.
Figure 2Resonance units of the radical intermediates of the diverse monolignol units during lignin synthesis.
Figure 3Main lignin structures identified by NMR. (R may indicate both aliphatic and aromatic chains.) (A) β-O-4 alkyl-aryl ethers; (A’) β-O-4 alkyl-aryl ethers with acylated γ’-OH with p-coumaric acid; (B) resinols; (B’) di-c-acylated mono-tetrahydrofuran structure formed by β–β’ coupling and subsequent a-O-a’ bonding (R, acetyl/p-coumaroyl); (C) phenylcoumarans; (I) p-hydroxycinnamyl alcohol end-groups; (C/C’) γ-acetylated phenylcoumaran (R, acetyl) (J) spirodienones (β-1′); (PCA) p-coumarates; (PB) p-hydroxybenzoate; (FA) ferulates; (T) tricin incorporation into the lignin polymer through a G-type β-O-4 linkage; (E) α,β-diaryl ethers (α-O-4/β-O-4).
Approximate percentages of linkages found in softwood and hardwood lignin [33].
| Linkage Type | Approximate Percentage (%) | |
|---|---|---|
| Softwood | Hardwood | |
| β-O-4 | 45–50 | 60 |
| 5–5 | 18–25 | 5 |
| β-5 | 9–12 | 6 |
| 4-O-5 | 4–8 | 7 |
| β-1 | 7–10 | 7 |
| β-β | 3 | 3 |
Scheme 1Main pretreatments of lignocellulose and products obtained, with special attention to the enzymes involved in both fungi and bacterial biological processes of cellulose and lignin degradation.
Enzymes involved in the hydrolysis of complex heteroarabinoxylans.
| Enzyme | Objective |
|---|---|
| Endo-β-l,4-xylanase | β-1,4-xylose linkage hydrolysation of the xylan backbone |
| Exo-xylanase | β-1,4-xylose linkage hydrolysation, releasing xylobiose |
| β-Xylosidase | Release short-chain xylooligosaccharides and xylose from xylobiose |
| α-L-Arabinofuranosidase | Terminal non-reducing α-arabinofuranose hydrolysation from arabinoxylans |
| α-Glucuronidase | Release glucuronic acid from glucuronoxylans |
| Acetylxylan esterase | Acetylester bond hydrolysation in acetyl xylans |
| Ferulic acid esterase | Feruloylester bond hydrolysation in xylans |
| ρ-Coumaric acid esterase | ρ -coumaryl ester bond hydrolysation in xylans |
Aromatic products detected from lignin breakdown [51,65,66].
| Compound | Fungal Lignin Degrader | Bacterial Lignin Degrader | |
|---|---|---|---|
| Benzoic acid | 4-hydroxy |
| |
| 4-hydroxy-3-methoxy |
|
| |
| 4-hydroxy-3-methoxy-6-carboxy |
| ||
| 4-hydroxy-3-methoxy-5-carboxy | |||
| 3,4-dimethoxy |
| ||
| 3,4-dimethoxy-2-carboxy |
| ||
| 2-hydroxy-3-methoxy |
| ||
| 2,3-dihydroxy | |||
| 2,3,4-trihydroxy |
| ||
| Benzaldehyde | 4-hydroxy-3-methoxy |
| |
| 3,4,5-trimethoxy |
| ||
| Cinnamic acid | 4-hydroxy |
| |
| 4-hydroxy-3-methoxy | |||
| Biphenyl-5,5′-dicarboxylic acid, 2,2′-dihydroxy, 3,3′-dimethoxy |
|
| |
| Diphenyl ether |
| ||
| Propiophenone-3′-hydroxy | 4-hydroxy-3-methoxy | ||
| Acetophenone | 4-hydroxy-3-methoxy | Soil metabolite | |
| Phenol | 2-methoxy | Soil metabolite | |
| 2-methoxy-4-vinyl | Soil metabolite | ||
| Vanillin |
Comparison of the different pretreatment methods used for lignocellulosic degradation methods. Good or bad performance regarding cost, toxic byproduct formation and applicability are marked by 🗸 and ×, respectively [61].
| Pretreatment | Cost | Toxic Byproduct | Applicable to a Wide Range of Biomass | Remarks |
|---|---|---|---|---|
| Acid pretreatment | 🗸 | × | 🗸 | Inhibitors limited by dilute acid use |
| Freezing | 🗸 | 🗸 | × | Freezing/thawing cycles |
| Milling | 🗸 | 🗸 | 🗸 | Used for bioethanol and biogas production |
| Liquid hot water | 🗸 | 🗸 | × | High water and energy inputs |
| Organic solvent (Organosolv) | × | × | 🗸 | Low boiling point of the solvent. Solvent recycling is required |
| Oxidation | × | 🗸 | 🗸 | High cost of ozone generation. Ozone handling is required |
| Steam explosion | × | × | 🗸 | High cost of steam generation |
| Extrusion | 🗸 | 🗸 | 🗸 | Hydrolysis efficiency is improved |
| Wet oxidation | × | 🗸 | × | Less water use as no washing is required |
| CO2 explosion | × | 🗸 | 🗸 | High cost for pressure maintenance |
| Microwave irradiation | × | 🗸 | 🗸 | More effective than conventional heating |
| Ultrasound | × | 🗸 | 🗸 | Low temperature and time required |
| Ammonium fibre expansion | × | 🗸 | 🗸 | Less effective for biomass with high lignin contents |
| Ionic liquid | × | 🗸 | 🗸 | Stability and reuse. Instability may cause contamination |
| Biological pretreatment | 🗸 | 🗸 | 🗸 | Increases delignification. Able to reduce polymerisation |
| Hydrothermal liquefaction | × | 🗸 | 🗸 | Lignocellulosic materials are depolymerised into bio-oil, biogas, biochar and water-soluble compounds |
Scheme 2Main procedures, products and fields of application of biofuels, biochemicals and biomaterials derived from lignocellulose.
Main biofuels, the associated energy and corresponding processing routes reported in the literature.
| Biofuel | Lower Heating Value | References |
|---|---|---|
| Biodiesel | 32.6 MJ/L | [ |
| Bioethanol | 21.2 MJ/L | [ |
| Biocrude | 35.0 MJ/kg | [ |
| Bio-oil | 40 MJ/kg | [ |
| Biogas | 13–17 MJ/m3 | [ |
| Biohydrogen | 13 MJ/m3 | [ |
| Biobutanol | 27.8 MJ/L | [ |
Main building blocks and their derivatives obtained from cellulose and hemicellulose [84].
| Compound | Production | Derived Products |
|---|---|---|
| Succinic, fumaric and malic acid | Biofermentation | Tetrahydrofuran (THF), 1,4-butanediol, 2-pyrrolidone, o-butyrolactone, N-methyl-2-pyrrolidone (NMP) |
| 2,5-Furan dicarboxylic acid | Chemical (oxidative dehydration of glucose) and biological | (2,5-Bis(aminomethyl)-tetrahydrofuran, 2,5-dihydroxymethyl-tetrahydrofuran, 2,5-dihydroxymethyl-furan |
| 3-Hydroxy propionic acid | Biofermentation | 1,3-Propanediol, acrylic acid, acrylamide |
| Aspartic acid | Chemical and biological pathways | 2-Amino-1,4-butanediol, aspartic anhydride, 3-aminotetrahydrofuran, amino-γ-butyrolactone |
| Glucaric acid | Chemical (starch oxidation by nitric acid or bleach) | Glucaro-γ-lactone, polyhydroxypolyamides, glucarodilactone, glucaro-δ-lactone |
| Glutamic acid | Biofermentation | Glutaminol, glutaric acid, norvoline, 1,5-pentandiol, 5-amino-1-butanol |
| Itaconic acid | Chemical and biofermentation | 3-Methylpyrrolidine, 3- & 4-methyl NMP, 3-methyl THF, 2-methyl-1,4-butanediol. |
| Levulinic acid | Chemical (acid decomposition of six-carbon sugars) | Diphenolic acid, 2-methyl-THF, b-acetylacrylic acid, 1,4-pentanediol |
| 3-Hydroxybutyrolactone | Chemical (oxidative degradation of starch) | 3-Hydroxytetrahydrofuran, 3-aminotetrahydrofuran, acrylate-lactone |
| Glycerol | Transesterification (via chemical or biological pathways) | Glyceric acid, 1,3-propanediol, propylene glycol |
| Sorbitol | Chemical (glucose hydrogenation) | Isosorbide, propylene glycol, ethylene glycol, 1,4-sorbitan |
| Xylitol/arabinitol | Chemical (hydrogenation of xylose and arabinose) and biological | Xylaric acid, propylene glycol, ethylene glycol, lactic acid |
Main procedures from lignin depolymerisation along with main products obtained.
| Depolymerisation | Procedures | Products | Refs |
|---|---|---|---|
| Non-reductive depolymerisation | Thermal, hydrothermal, oxidative, acid and base catalysed, solvolytic | Vanillin, syringaldehyde, acetosyringone, guaiacylacetone, p-hydroxylated phenol acetovanillone, syringol, guaiacol, phenol, catechol, alkylcatechols, creosol, p-hydroxybenzaldehyde, vanillic, protocatechuic, syringic, homovanillic and p-hydroxybenzoic acid, aliphatic carboxylic acids (succinic, acetic and formic acid) | [ |
| Reductive depolymerisation | Hydroprocessing, liquid phase reforming | Cresol, xylenol, phenol with long alkyl chains, p-substituted methoxyphenols, | [ |
Glucomannan-based materials, characterisation performed and future application prospects in various fields [236].
| Components | Potential Applications |
|---|---|
| Chitosan/Konjac glucomannan (KGM) | Membrane with superior dehydration |
| KGM/Chitosan | Food industry, biomaterial matrix, biomedical material |
| KGM/Ethyl cellulose | Films for food packaging |
| Glucomannan–Chitosan–Nisin | Active packaging material |
| KGM/Gellan gum | Food packaging material |
| KGM/Poly(acrylic acid) | Specific drug delivery |
| KGM/Polyacrylamide/Sodium xanthate | Hydrogels for drug delivery |
| KGM/poly(methacrylic acid) | Specific drug delivery |
| KGM/Polyvinyl alcohol | Pervaporation dehydration, food package film |
| KGM/Xanthan gum | Gels for delivery systems, specific drug delivery |
| KGM/Alginate/Chitosan | Controlled release |
| KGM/Carboxymethyl cellulose | Emulsion stabiliser |
| KGM/Curdian | Food films and coatings |
| KGM/Poly(aspartic acid) | Carrier for drug delivery |
| KGM/Cellulose | Separation |
| KGM/Whey protein | Edible food films |
| KGM/Sodium alginate | Food films |
| KGM/Gelatin | Specific drug delivery |
| KGM/Starch | Edible food films & coatings |
| KGM/Poly(diallydimethylammonium chloride) | Antibacterial in biomedicine |
| KGM/xanthan gum | Drug delivery |
| KGM-graft-Polyacrylamide-co-sodium xanthate | Flocculant |
| KGM | Coating |
Most-used base oils and thickeners for lubricating greases.
| Base Oils | Thickeners |
|---|---|
| Mineral oil | Sodium soap |
| Synthetic oil | Calcium soap |
| Diester | Lithium soap |
| Silicone liquid | Aluminium soap |
| Phosphate ester | Lithium complex |
| Fluorinated silicone | Calcium complex |
| Chlorinated silicone | Aluminium complex |
| Polyglycol | Bentonite |
| Castor oil | Silicon oxide |
| Carbon/graphite | |
| Polyurea | |
| Polyethylene | |
| Indanthrene dye | |
| Phthalocyanine dye |
Lubricating grease evolution through history [277,278].
| Date | Event |
|---|---|
| About 1400 BC | The use of animal fat and limestone for lubrication of axes of Hittite chariots was started. In the same period, lubricants based on olive oil and limestone were used in Ancient Egypt |
| 1845 | A lubricant consisting of mineral oil, animal fat and limestone was invented in the United States |
| 1853 | The first sodium lubricant based on beef fat appeared in the United Kingdom |
| 1912 | The production of calcium lubricants with the dispersion medium based on mineral oil was started in Japan |
| 1938 | Lithium lubricants were developed. They quickly conquered the world and were used as multipurpose lubricants |
| 1954 | Invention of complex aluminium lubricants for operation at high temperatures |
| 1955 | Invention of urea greases in the United States |
| 1960–Present | Resurgence of vegetable-oil-based lubricating greases |
Figure 4Main bio-polyurethanes studied, i.e., adhesives, lubricating greases and elastomers, from left to right, with testing or application as background.