Interest in lignocellulosic biomass conversion technologies has increased recently because of their potential to reduce the dependency on non-renewable feedstocks. Residues from a variety of crops are the major source of lignocellulose, which is being produced in increasingly large quantities worldwide. The commercial exploitation of crop residues as feedstocks for biorefineries which could be used to produce a variety of goods such as biofuels, biochemicals, bioplastics, and enzymes is an attractive approach not only for adding value to residues but also for providing renewable products required by the expanding bioeconomy market. Moreover, the implementation of biorefineries in different regions has the potential to add value to the specific crop residues produced in the region. In this review, several aspects of crop residue application in biorefineries are discussed, including the role of crop residues in the bioeconomy and circular economy concepts, the main technical aspects of crop residue conversion in biorefineries, the main crop residues generated in different regions of the world and their availability, the potential value-added bioproducts that can be extracted or produced from each crop residue, and the major advantages and challenges associated with crop residue utilization in biorefineries. Despite their potential, most biomass refining technologies are not sufficiently advanced or financially viable. Several technical obstacles, especially with regard to crop residue collection, handling, and pre-treatment, prevent the implementation of biorefineries on a commercial scale. Further research is needed to resolve these scale-up-related challenges. Increased governmental incentives and bioeconomic strategies are expected to boost the biorefinery market and the cost competitiveness of biorefinery products.
Corresponding Author(s):
Edivaldo Ximenes FERREIRA FILHO
引用本文:
. [J]. Frontiers in Energy, 2022, 16(2): 224-245.
Maria Carolina ANDRADE, Caio de Oliveira GORGULHO SILVA, Leonora Rios de SOUZA MOREIRA, Edivaldo Ximenes FERREIRA FILHO. Crop residues: applications of lignocellulosic biomass in the context of a biorefinery. Front. Energy, 2022, 16(2): 224-245.
China (25%), India (22%), USA (15%), Pakistan (8%), Brazil (5%)
6.54E+ 07
9.81E+ 07
Cotton sheets, cotton stalks
80
*
*
[37–39]
Rice
China (19%), India (18%), Indonesia (8%), Bangladesh (6%), Vietnam (4%)
7.41E+ 08
1.10E+ 07
Rice straw, rice hulls
25.1–38
27–37.1
8–15.2
[16,37,38,40]
Coffee
Brazil (33%), Vietnam (16%), Colombia (8%), Indonesia (7%), Ethiopia (5%)
9.22E+ 06
3.67E+ 06
Coffee husks, coffee pulp, wastewater
37.2
24.9
*
[37,38,41]
Sugarcane
Brazil (41%), India (18%), China (6%), Thailand (5%), Pakistan (3%)
1.89E+ 09
4.73E+ 08
Sugarcane bagasse, cane straw
43 –39
26 – 30
22–25
[16,37,38,40]
Barley
Russia (20%), Germany (11%), France (11%), Australia (11%), Ukraine (10%)
1.41E+ 08
1.78E+ 06
Barley straw
39.6
24.7
17.2
[16,37,38]
Beans
Myanmar (19%), India (14%), Brazil (10%), USA (5%), United Republic of Tanzania (4%)
2.68E+ 07
3.66E+ 05
Peel beans
*
*
*
[37,38]
Orange
Brazil (24%), China (12%), India (10%), USA (7%), Mexico (6%)
7.32E+ 07
4.29E+ 07
Orange peel, orange bagasse
*
*
*
[37,38]
Apple
China (50%), USA (5%), Poland (4%), Turkey (3%), India (3%)
8.93E+ 07
5.85E+ 07
Apple pomace
*
*
*
[37,38,42]
Corn
USA (36%), China (22%), Brazil (6%), Argentina (4%), Mexico (3%)
1.06E+ 09
7.49E+ 08
Corncobs, corn straw
37.3
25.5
13.8 – 16.7
[15,16,37,38,43]
Soybean
USA (35%), Brazil (28%), Argentina (17%), India (4%), China (3%)
3.35E+ 08
2.98E+ 08
Soybean hull
25
11.9
17.6
[16,37,38]
Sorghum
USA (19%), Nigeria (11%), Sudan (10%), Mexico (8%), Ethiopia (7%)
6.39E+ 07
3.54E+ 07
Sorghum straw
36
18
15.5
[16,37,38]
Wheat
China (17%), India (12%), Russia (10%), USA (8%), Canada (3%)
7.69E+ 08
1.13E+ 07
Wheat straw
35–37.3
24–28.7
17.8–25
[16,37,38,40]
Grape
China (19%), Italy (11%), USA (9%), France (8%), Spain (8%)
7.74E+ 07
1.24E+ 07
Grape pomace
*
*
*
[37,38]
Tab.1
Fig.4
Residue
Application
Conversion process
Reference
Coffee silverskin
Production of levulinic acid
Water-soluble phenolics were extracted from CS through hydrothermal pre-treatment in a microwave reactor. Pretreated CS was then subjected to diluted hydrochloric acid treatment in a microwave reactor with varying biomass loadings, acid concentrations and reaction temperature/time to produce levulinic acid
[79]
Coffee silverskin
Production of a-amylase
SSF process using a fungal strain Neurospora crassa CFR 308
[80]
Coffee wastes
Production of biogas
Alkaline and acid pre-treatments of a mixture composed of coffee seed skin, seed refuse and coffee product refuse followed by the inoculum of cow and chicken manure and an anaerobic sludge taken from a domestic water treatment system
[89]
Coffee wastewater
Production of bioethanol
Batch fermentation using Hanseniaspora uvarum UFLA CAF76 as inoculum in ground coffee pulp mixed with coffee wastewater
[90]
Coffee husks
Production of endoglucanase
Steam-exploded coffee husks were used as substrate for cellulase production using Rhizopus stolonifer CFR 307 under SSF. Fermentation parameters (pH, moisture and fermentation time) were optimized through response surface methodology (RSM). Enzymes thus produced were applied in ethanol production from coffee husks and as additive in detergent formulation
[86]
Coffee husks
Production of gibberellic acid
SSF and SmF fermentation of alkali pretreated coffee husks and cassava bagasse (7:3, dry wt) employing Gibberella fujokuroi LPB-06
[91]
Coffee husks
Production of carotenoids
Alkaline-pretreated coffee husks were used as substrate for Rhodotorula mucilaginosa CCMA0156 as carotenoid-producing strain under SmF. Intracellular carotenoids were extracted with different organic solvents
[92]
Coffee husks
Production of xylanase and cellulase
Multispecies SSF process applying a specialized consortium of microorganisms (Pseudoxanthomonas taiwanensis, Sphingobacterium composti, Cyberlindnera jardinii and Barnettozyma californica among others)
[81]
Coffee pulp
Cultivation of mushrooms
Six strains of Pleurotus were grown in a mixture of coffee pulp and wheat straw
[93]
Coffee pulp
Production of pectinase
SSF process employing Aspergillus niger AW96 and SmF process employing A. niger AW99
[82]
Spent coffee ground
Production of biodiesel
Oil was extracted from SCG with hexane. Oil transesterification reaction was performed with ethanol or methanol via enzymatic catalysis with three commercial enzymes (Lipozymes RM 1M, TL 100L, and CALBL)
[73]
Tab.2
Residue
Application
Conversion process
Reference
Soybean hulls
Production of protease, b- amylase, a-amylase
SSF process using a fungal strain Penicillium spp. LEMIA 38221 in different conditions (pH, temperature and substrate concentration)
[98]
Soybean hulls
Production of ethanol
Soybean residue was pretreated with dilute H2SO4 and subjected to separate hydrolysis and fermentation employing commercial cellulase cocktails (a mixture of C-Tec 2 and Viscozyme L) and S. cerevisiae (wild-type strain or the KCCM 1129 strain adapted to high galactose concentrations)
[94]
Soybean hulls and citric pulp
Production of gibberellic acid
SSF performed with Fusarium moniliforme LPB 03 optimized for physical and chemical conditions (pH, initial humidity and composition of nutritive solution)
[97]
Soybean oil deodorizer distillate
Production of biodiesel
CaO obtained from calcined duck eggshell was used as catalyst for the esterification of SODD with methanol
[19]
Soybean straw
Production of biogas
Solid-state anaerobic digestion (SS-AD) of soybean processing waste (consisting of soybeans, soybean straw and soybean oil extraction residues) and hay with the effluent from a mesophilic liquid anaerobic digester as inoculum
[102]
Okara
Production of b-glucosidase
Fresh and heat-treated okara were subjected to SSF process using Saccharomyces cerevisiae r.f. bayanus
[96]
Okara
Production of probiotic
A probiotic creamy sauce was produced with Lactobacillus acidophilus LA3-fermented okara flour plus soymilk and different types of gelling components
[104]
Okara
Production of citric acid
Solid-state mixed fermentation of okara with Aspergillus terreus (involved in okara saccharification) and Aspergillus niger (responsible for citric acid production)
[105]
Soybean meal
Production of lipase
SSF process applying DCCR design to evaluate spore concentration, cultivation and humidity parameters affecting the enzymatic production by Penicillium sp. S4
[99]
Soybean meal
Production of cellulase
Cellulase production by Chaetomium globosum BCC5776 was performed under SmF conditions in optimized medium containing 1% soybean meal, 1% empty palm fruit bunch and 2% Avicel®. Home-made enzyme system was supplemented with commercial b-glucosidase (Novozyme® 188) and hemicellulases (Accellerase® XY) for the efficient hydrolysis of alkaline-pretreated rice straw
[106]
Soybean residues
Production of bioethanol
Two residues, i.e. skim (protein-rich fraction) and insoluble fiber (carbohydrate-rich fraction), generated from soybean oil extraction were used as additives in dry-grind corn fermentation for ethanol production. The addition of skim and/or insoluble fiber enhanced ethanol production by decreasing the corn fermentation time, increased corn distillers oil recovery from this tillage and increased the protein content while reducing fiber and oil contents of distillers dried grains
[107]
Tab.3
Residue
Application
Conversion process
Reference
Sugarcane bagasse and citrus residues
Production of glycosyl hydrolases
RSM methodology to select the best enzyme inducing biomass (sugarcane bagasse, soybean bran, wheat bran, apple bagasse or citrus bagasse) using Annulohypoxylon stygium in SmF process
[127]
Sugarcane bagasse
Production of xylanases
Pretreated SCB was used as substrate for Aspergillus terreus in SmF
[128]
Sugarcane bagasse
Production of xylanase
SmF process employing pretreated SCB and Emericella nidulans
[13]
Sugarcane bagasse
Production of endoglucanase
Enzymatically liquefied sugarcane bagasse was used as substrate for endoglucanase production by Aspergillus niger A12. The produced enzymes were then applied to liquefy sugarcane bagasse for later use as substrate for enzyme production in a closed-loop strategy
[12]
Sugarcane bagasse
Production of cellulase, b-glucosidase and xylanase
Mathematical model describes enzyme production by Trichoderma harzianum P4P11 through variation of substrate concentration, cell growth and induction of different enzyme classes (cellulases, b-glucosidases and xylanases) using steam-exploded and alkali-pretreated SCB
[116]
Sugarcane bagasse
Production of biobutanol
Biorefinery model was created based on Aspen Plus® simulations to produce sugar, ethanol and butanol (25:50:25 configuration) employing strains of Saccharomyces cerevisiae, Clostridium saccharoperbutylacetonicum or mutant strain Clostridium beijerinckii BA101
[126]
Sugarcane bagasse
Production of levulinic acid
Biorefinery model that fractionates SCB and wheat straw using liquid hot water pre-treatment and enzymatic hydrolysis with commercial cocktail Cellic® CTec2
[119]
Sugarcane straw
Production of bioethanol
Application of the semi-mechanistic model using SS hydrothermal pretreated with and without alkali delignification with 4% NaOH and enzymatic hydrolysis employing Cellic® CTec2
[129]
Sugarcane straw
Production of lignin
Lignin with high degree of purity (>98%) and low sulfur content (<2%) was extracted from sugarcane straw through SO2-ethanol-water fractionation at different temperatures (135°C–160°C)
[123]
Sugarcane straw
Production of xylitol
The hemicellulosic hydrolysate obtained through dilute acid pre-treatment of sugarcane straw with 1% H2SO4 was fermented with Candida guillermondii FT20037 using three nutritional supplementation conditions
[64]
Tab.4
Residue
Application
Conversion process
Reference
Corn stover
Production of methane
Chicken manure supplemented with corn stover or maize silage was used as substrate for methane production via anaerobic digestion
[141]
Corncobs
Production of prebiotic xylooligosaccharides
Milled corncobs were alkaline pretreated with various concentrations (2%, 4%, 8% and 12%) of NaOH or KOH following incubation with Enterococcus faecium TCD3, E. fecalis CCD10, Lactobacillus maltromicus MTCC108 and Lactobacillus viridiscens NCIM2167
[142]
Corncobs
Production of biosorbent
Biosorbents were prepared by treating corncobs with H3PO4, H2SO4, HNO3, NaOH, or Na2CO3
[134]
Corncobs
Production of biogas
Corncobs were subjected to alkaline extrusion pre-treatment (0.4% NaOH) and hydrolyzed with commercial endoglucanase (Novozymes Ultraflo® L) or crude enzyme extract from Aspergillus terreus CECT 2808 grown on corncobs under SSF condition. A mesophilic anaerobic sludge was used as inoculum for biogas production through anaerobic digestion of hydrolyzed corncobs
[143]
Corncobs
Production of microcrystalline cellulose
Steam explosion pre-treatment of cotton gin wastes and corncobs followed by 20% NaOH extraction, 25% H2O2 bleaching and microcrystalline cellulose conversion with HCl, H2SO4 and Spezyme CP® cellulase enzyme preparation
[138]
Corncobs
Production of cellulase
SSF process employing Trichoderma reesei ZU-02
[144]
Tab.5
Residue
Application
Conversion process
Reference
Wheat straw
Production of bioethanol
H2SO4-catalyzed steam explosion pre-treatment of wheat straw followed by SSF process employing Novozymes A/S cellulase/b-glucosidase cocktail and Kluyveromyces marxianus CECT 10875
[147]
Wheat straw
Production of biogas
Pre-treatment of wheat straw with N-methylmorphine, N-oxide, ethanol (Organosolv) or NaOH followed by anaerobic digestion using a digestate from local manure and dairy residue anaerobic digestion plant as inoculum
[148]
Wheat straw
Biosorption of cadmium and copper
Wheat straw was pretreated with 10% HNO3 and neutralized with 1N NaOH before being used as an efficient biosorbent of Cd2+ and Cu2+
[150]
Wheat straw
Production of bacterial cellulose
Wheat straw was pretreated with ionic liquid [(AMIM)Cl] under optimized conditions, saccharified with commercial cellulase and the straw hydrolysate was employed as the carbon source for the production of bacterial cellulose by Gluconacetobacter xylinus ATCC 23770
[151]
Wheat straw
Production of levulinic acid
The production of levulinic acid from acid hydrolysis of wheat straw was optimized with RSM methodology (effects of temperature, sulfuric acid concentration, reaction time of production and liquid: solid ratio were analyzed to increase yield)
[152]
Wheat straw
Mushroom cultivation
Rice and wheat straw without supplementation were used as a substrate for growing Pleurotus sajor-caju where relative humidity, temperature and ventilation were strictly controlled
[153]
Wheat straw
Production of bioethanol
Native non-adapted Saccharomyces cerevisiae are often used in a combination of physicochemical pre-treatments of wheat straw
[146]
Tab.6
Residue
Application
Conversion process
Reference
Rice straw
Production of cellulase
SmF process employing milled straw treated with 1.25% or 5% NH4OH using Trichoderma reesei ATCC-66589 and Humicola insolens ATCC-26908 as enzyme producers
[158]
Rice straw
Production of biochar
Straw and rice husks of two different varieties (Koshihikari and IR50404) were exposed to high pyrolysis temperatures (300°C–800°C)
[166]
Rice straw
Production of biobutanol
The enzymatic hydrolysate of non-pretreated rice straw was used as carbon source for ABE fermentation with Clostridium saccharoperbutylacetonicum N1-4 for biobutanol production. High initial cell concentration under non-sterile conditions achieved the similar butanol yields obtained under sterile conditions
[168]
Rice straw
Production of bioelectricity
Impregnation of rice straw with FeCl3 solution (10% w/v) followed by heat pre-treatment and enzymatic hydrolysis with enzyme pool from Aspergillus niger and Trichoderma reesei. The fuel cell reactor was loaded with the diluted hydrolysate in an anode compartment including dissolved air as the final electron acceptor
[169]
Rice residues (straw and husk)
Production of nanosilica
Rice residues were burned until ash generation and treated with sodium hydroxide. Sodium silicate was precipitated with HCl or H2SO4, washed, dried and burned at 575°C to obtain nanosilica powder
[167]
Rice straw
Production of lignin-degrading enzymes
Myrothecium roridum LG7 was employed for the biological pre-treatment (delignification) of a mixture of rice straw and herbaceous weed Parthenium sp. under SSF condition. Partially delignified biomass was more susceptible to saccharification with commercial cellulase enzymes (Accellerase® 1500) than untreated biomass
[162]
Rice husk
Production of lignin, cellulose nanocrystals and silica
Sequential acid leaching (HCl) and alkaline extraction (NaOH) were used to recover high purity lignin from rice husks. The remaining cellulose-rich solids were bleached with chlorine free treatment to yield cellulose nanocrystals. Silica was also recovered from the aqueous supernatant of lignin extraction
[170]
Tab.7
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