Deep eutectic solvent-based, microwave-assisted pretreatment is a green, fast, and efficient process for lignocellulosic fractionation and high-purity lignin recovery.
Pretreatment is still the most expensive step in lignocellulosic biorefinery processes. It must be made cost-effective by minimizing chemical requirements as well as power and heat consumption and by using environment-friendly solvents. Deep eutectic solvents (DESs) are key, green, and low-cost solvents in sustainable biorefineries. They are transparent mixtures characterized by low freezing points resulting from at least one hydrogen bond donor and one hydrogen bond acceptor. Although DESs are promising solvents, it is necessary to combine them with an economic heating technology, such as microwave irradiation, for competitive profitability. Microwave irradiation is a promising strategy to shorten the heating time and boost fractionation because it can rapidly attain the appropriate temperature. The aim of this study was to develop a one-step, rapid method for biomass fractionation and lignin extraction using a low-cost and biodegradable solvent.
In this study, a microwave-assisted DES pretreatment was conducted for 60 s at 800 W, using three kinds of DESs. The DES mixtures were facilely prepared from choline chloride (ChCl) and three hydrogen-bond donors (HBDs): a monocarboxylic acid (lactic acid), a dicarboxylic acid (oxalic acid), and urea. This pretreatment was used for biomass fractionation and lignin recovery from marine residues (Posidonia leaves and aegagropile), agri-food byproducts (almond shells and olive pomace), forest residues (pinecones), and perennial lignocellulosic grasses (Stipa tenacissima). Further analyses were conducted to determine the yield, purity, and molecular weight distribution of the recovered lignin. In addition, the effect of DESs on the chemical functional groups in the extracted lignin was determined by Fourier-transform infrared (FTIR) spectroscopy. The results indicate that the ChCl-oxalic acid mixture affords the highest lignin purity and the lowest yield. The present study demonstrates that the DES-microwave process is an ultrafast, efficient, and cost-competitive technology for lignocellulosic biomass fractionation.
Sustainable biorefinery processes integrate biomass processing, its fractionation into molecules of interest, and their conversion to value-added products1. In second-generation biorefining, pretreatment is considered essential for fractionating biomass into its main components2. Traditional pretreatment methods utilizing chemical, physical, or biological strategies have been widely applied3. However, such pretreatment is considered the most expensive step in biorefining and has other disadvantages such as long processing time, high heat and power consumption, and solvent impurities4. Recently, DESs, whose properties are similar to those of ionic liquids3, have emerged as green solvents owing to advantages such as biodegradability, environmental-friendliness, ease of synthesis, and recovery after treatment5.
DESs are mixtures of at least one HBD, such as lactic acid, malic acid, or oxalic acid, and a hydrogen-bond acceptor (HBA) such as betaine or choline chloride (ChCl)6. HBA-HBD interactions enable a catalytic mechanism that permits cleavage of chemical bonds, causing biomass fractionation and lignin separation. Many researchers have reported the DES-based pretreatment of lignocellulosic feedstocks such as ChCl-glycerol on corn's cob and stover7,8, ChCl-urea, and ChCl-oxalic acid on wheat straw9, ChCl-lactic acid on Eucalyptus sawdust10, and ChCl-acetic acid11 and ChCl-ethylene glycol on wood11. To improve DES efficiency, the pretreatment should be combined with microwave treatment to accelerate biomass fractionation5. Many researchers have reported such a combined pretreatment (DES and microwave) of wood8 and of corn stover, switchgrass, and Miscanthus5, which provides new insight into the capacity of DESs for lignocellulosic fractionation and lignin extraction in one easy step over a short period.
Lignin is a phenolic macromolecule valorized as a raw material for the production of biopolymers and presents an alternative for the production of chemicals such as aromatic monomers and oligomers12. In addition, lignin has antioxidant and ultraviolet absorption activities13. Several studies have reported lignin applications in cosmetic products14,15. Its integration in commercial sunscreen products has improved the sun protection factor (SPF) of the product from SPF 15 to SPF 30 with the addition of only 2 wt % lignin and up to SPF 50 with the addition of 10 wt % lignin16. This paper describes an ultrafast approach for lignin-carbohydrate cleavage, assisted by combined DES-microwave pretreatment of Mediterranean biomasses. These biomasses consist of agri-food byproducts, particularly olive pomace and almond shells. Other biomasses that were investigated were those of a marine origin (Posidonia leaves and aegagropile) and those originating from a forest (pinecones and wild grasses). The focus of this study was to test low-cost green solvents to evaluate the effects of this combined pretreatment on feedstock fractionation, to investigate its influence on lignin purity and yield, and to study its effects on the molecular weights and chemical functional groups in the extracted lignin.
1. Preparation of biomasses
2. Microwave-assisted, ultrafast lignin extraction
3. Purity determination of extracted lignin by Klason
4. Nitrogen content in extracted lignin
5. Ash content in extracted lignin
6. Carbohydrate content
7. Chemical functions in extracted lignin (Fourier-transformed infrared)
8. Molecular weight of extracted lignin (gel permeation chromatography)
9. Data treatment and statistical analyses
Figure 2A–C depict the lignin yield of extraction from the six feedstocks, shown in Figure 1A–F, after the combined microwave-DES pretreatment. The results show that the lignin yield obtained with DES1 (ChCl-oxalic acid) (Figure 2A) was lower than the yields obtained with DES2 (ChCl-lactic acid) and DES3 (ChCl-urea) (Figure 2B,C). In addition, lignin yields from pinecones (PC) and olive pomace (OP) were higher at 32.31% and 26.04% for DES1 treatment and 48.72% and 43.76 for DES3, respectively. Lignin yield from alfa leaves (A) was significantly higher than the yields of all other lignins extracted with DES2. Figure 3A–C show that lignin purity exceeded 70% for the three pretreatments of the biomasses, except for DES3 pretreatment of alfa leaves (A), aegagropile (Ag), and almond shells (AS) in the DES3 (ChCl-urea) treatment, which gave a lignin purity of 65%. The highest lignin purity (> 90%) was obtained with the DES1 treatment: alfa leaves (A) 94%, almond shells (AS) 93%, pinecones (PC) 90%, Posidonia leaves (PL) 92%, and olive pomace (OP) 91%.
Lignin purity and yield data were subjected to principal component analysis (PCA) by considering two parameters (yield and purity) and 18 treatments. Figure 4 shows that the correlation circle explained 100% of the total variation. The first component, PCA1, explained 58.09%, and the second component, PCA2, explained 41.91% of the total variation. Lignin purity was positively correlated with DES1 (Ox) treatment. The Pearson correlation coefficients (R) were alfa (A Ox) 0.32, olive pomace (OP Ox) 0.27, pinecones (PC Ox) 0.2, Posidonia leaves (PL Ox) 0.35, almond shells (AS Ox) 0.32, and aegagropile (Ag Ox) 0.05, respectively. However, DES3 treatment was negatively correlated with lignin yield with R-values that oscillated between −0.37 and −0.05. Thus, PCA results confirmed that lignin extracted with DES1 was the purest with the lowest yield.
Lignin was characterized for its sugar, nitrogen, and ash contents (Figure 5A–C). The total sugar content was determined by gas chromatography (GC). The carbohydrate content in lignin was extracted using DES3 (ChCl-urea) was the highest (6-15%). This was followed by lignin extracted using DES2 (ChCl-lactic acid), which had a carbohydrate content of 3-12%. However, the lowest carbohydrate content (1%) was reported for lignin extracted using DES1 (ChCl-oxalic acid). The type of sugars identified differed significantly (Figure 6A-C); D-xylose and D-glucose were the most abundant monosaccharides. These results indicate that DES1 was extremely selective in its extraction of lignin compared with the other two DESs, which extracted not only lignin, but also carbohydrates. In other words, lignin purity was lower after extraction with the lactic acid and urea DESs.
The high selectivity of DES1 to fractionate the lignocellulosic matrix and extract pure lignin is probably because of the high acidity of its hydrogen bonds (alpha = 1.3). Choline chloride contains chloride ions that break the intramolecular interactions of hydrogen bonds, and the carboxylate groups in oxalic acid contribute to dissolve the lignin polymers. Similarly, the nitrogen content of lignin extracted using DES1 was lower than the nitrogen content of lignin extracted using DES2 and DES3, reaching up to 3% (Figure 5A-C). Lignin extracted from alfa leaves had the highest nitrogen content: 2.70, 3.84, and 3.40 for DES1, DES2, and DES3, respectively. These results prove that nitrogenous compounds were extracted and co-precipitated with lignin. Furthermore, lignin calcination in all the samples indicated that lignin extracted using DES2 and DES3 contained a higher inorganic component than lignin extracted using DES1.
These results indicate that DES1 promoted the extraction of lignin with high purity, but with low nitrogen, carbohydrate, and ash contents. In other words, lignin extracted using DES1 (ChCl-oxalic acid) was purer than that extracted using DES2 (ChCl-lactic acid) and DES3 (ChCl-urea), which possesses lower purity and high nitrogen, carbohydrate, and ash contents. Table 1 summarizes the molecular mass distribution of lignin, as analyzed by gel permeation chromatography (GPC) and represented by the number-average molecular weight (Mn), weight-average molecular weight (Mw) and polydispersity index (PDI). The Mw values ranged from 48,123 to 147,233 g mol-1. The lignin extracted by DES2 from alfa leaves, almond shells, and aegagropile had a lower PDI than the lignin extracted by DES1, DES3, and alkali, as well as raw lignin. In contrast, lignin extracted by DES2 from pinecones, olive pomace, and Posidonia leaves showed higher PDI. The lower PDI of the lignin extracted from aegagropile indicates that its molecular weight is more homogenous than that of the lignins extracted from the other biomasses.
The chemical functional groups present in extracted lignin were investigated by FTIR spectroscopy (Figure 7A-F). The strong, broad band between 3,441 and 3,198 cm-1 was attributed to OH stretching vibrations of the alcoholic and phenolic hydroxyl groups involved in hydrogen bonding. The signals in the wavenumber range 2,963-2,852 cm-1 were assigned to alkyl C-H stretching vibrations. Olive pomace, alfa leaves, and almond shells showed more intense bands than the other biomasses. No bands were observed from 2,800 to 1,800 cm-1. The lignin obtained by DES1 and DES2 treatment, had a rising band at 1,708 cm-1, which indicated the presence of unconjugated C=O groups. However, this signal was absent in the solvent spectra (Figure 8B). Lactic and oxalic acid spectra were characterized by a band in the 1,737-1,723 cm-1 range, which indicated the presence of unconjugated C=O groups, whereas the urea spectrum was characterized by two signals in the wavenumber range of 1,660 cm-1 and 1,604 cm-1 attributed to amide groups. The bands at 1,606-1,618 cm-1 were observed in lignin extracted by DES1 and DES2 treatment, associated with ring-conjugated C=C stretch.
The signal at 1,640 cm-1 in lignin extracted by DES3 indicated the presence of C=O stretching vibration in conjugated carbonyl groups of lignin. The signal at 1516 cm-1 arose from the vibrations of the aromatic rings present in lignin, while the band at 1200 cm-1 indicated the presence of ether groups. Bands in the wavenumber range of 1,250-1,200 cm-1 were assigned to C-O stretching of nonaromatic alcohols. The band at 953 cm-1 was assigned to methyl substituents. The results indicate that DES-lignin fractions spectra showed signals at 1,730-1,702 cm-1 and 1,643-1,635 cm-1, assigned to the stretching vibration of unconjugated and conjugated carbonyl groups, respectively. However, these band ranges were absent in three commercial lignins: raw, soda-processed, and alkali-extracted lignins (Figure 8A).This observation indicates that during its extraction and solubilization, some functional groups of lignin were conjugated with oxalic and lactic acid.
Figure 1: Mediterranean biomasses studied. (A) Almond shells, (B) Olive pomace, (C) Cone pines, (D) Aegagropile (Posidonia balls), (E) Posidonia leaves, (F) Alfa leaves. Please click here to view a larger version of this figure.
Figure 2: Lignin yield. (A) Choline chloride + Oxalic acid (DES1), (B) Choline chloride + Lactic acid (DES2), (C) Choline chloride + Urea (DES3). Significant differences were determined with one-way ANOVA and Fisher's post-hoc test (*P < 0.05; **P < 0.01; ***P < 0.001). Abbreviations: A = Alfa leaves, AS = Almond shells, PC = Pinecones, PL = Posidonia leaves, OP = Olive pomace, Ag = Aegagropile; ns = not significant. Please click here to view a larger version of this figure.
Figure 3: Lignin (%). (A) Choline chloride + Oxalic acid (DES1), (B) Choline chloride + Lactic acid (DES2), (C) Choline chloride + Urea (DES3). Significant differences were determined with one-way ANOVA and Fisher's post hoc test (*P < 0.05; **P < 0.01; ***P < 0.001). Abbreviations: A = Alfa leaves, AS = Almond shells, PC = Pinecones, PL = Posidonia leaves, OP = Olive pomace, Ag = Aegagropile; ns = not significant. Please click here to view a larger version of this figure.
Figure 4: Principal component analysis of yield and purity of lignin extracted from Mediterranean biomasses. Hydrogen-bond acceptor (HBA) is choline chloride (ChCl) and hydrogen-bond donors (HBD) are Ox = oxalic acid, Lac : lactic acid, and Urea. PCA = principal component analysis; A = Alfa leaves, AS = Almond shells, PC = Pinecones, PL = Posidonia leaves, OP = Olive pomace, Ag = Aegagropile. Please click here to view a larger version of this figure.
Figure 5: Carbohydrate (%), nitrogen (%), and ash content (%) in lignin samples. (A) Choline chloride + Oxalic acid (DES1), (B) Choline chloride + Lactic acid (DES2), (C) Choline chloride + Urea (DES3). Significant differences were determined with one-way ANOVA and Fisher's post-hoc test (*P < 0.05; **P < 0.01; ***P < 0.001). Abbreviations: A = Alfa leaves, AS = Almond shells, PC = Pinecones, PL = Posidonia leaves, OP = Olive pomace, Ag = Aegagropile; ns = not significant. Please click here to view a larger version of this figure.
Figure 6: Identification of monosaccharides in lignin samples (%). (A) Choline chloride + Oxalic acid (DES1), (B) Choline chloride + Lactic acid (DES2), (C) Choline chloride + Urea (DES3). Significant differences were determined with one-way ANOVA and Fisher's post-hoc test (*P < 0.05; **P < 0.01; ***P < 0.001). Abbreviations: A = Alfa leaves, AS = Almond shells, PC = Pinecones, PL = Posidonia leaves, OP = Olive pomace, Ag = Aegagropile; ns = not significant. Please click here to view a larger version of this figure.
Figure 7: Fourier-transform infrared spectra of lignin samples. (A) Alfa leaves, (B) Almond shells, (C) Pinecones, (D) Posidonia leaves, (E) Olive pomace, (F) Aegagropile. Abbreviations: DES1 = Choline chloride + Oxalic acid, DES2 = Choline chloride + Lactic acid, DES3 = Choline chloride + Urea. Please click here to view a larger version of this figure.
Figure 8: Fourier-transform infrared spectra. (A) Lignin controls, (B) hydrogen bond donors. Please click here to view a larger version of this figure.
Sample | Treatment | Mn | Mw | PDI |
A | Urea | 47558 | 120141 | 2.5 |
Lac | 35241 | 73665 | 2.1 | |
Ox | 35793 | 84312 | 2.4 | |
AS | Urea | 50181 | 105817 | 2.1 |
Lac | 60409 | 104915 | 1.7 | |
Ox | 83112 | 147233 | 1.8 | |
PC | Urea | 34013 | 65181 | 1.9 |
Lac | 55513 | 145963 | 2.6 | |
Ox | 46409 | 102298 | 2.2 | |
PL | Urea | 25696 | 50093 | 1.9 |
Lac | 45530 | 122900 | 2.7 | |
Ox | 28427 | 70726 | 2.5 | |
OP | Urea | 29669 | 70424 | 2.4 |
Lac | 26735 | 66743 | 2.5 | |
Ox | 34161 | 75509 | 2.2 | |
Ag | Urea | 30184 | 48123 | 1.6 |
Lac | 33835 | 52123 | 1.5 | |
Ox | 30025 | 49808 | 1.7 | |
Control | Raw lignin | 23275.3 | 36496.5 | 1.6 |
Alkali-extracted lignin | 22792.6 | 43014.3 | 1.9 |
Table 1: Molecular weights of the lignins. Abbreviations: A = Alfa leaves, AS = Almond shells, PC = Pinecones, PL = Posidonia leaves, OP = Olive pomace, Ag = Aegagropile; Mn = number-average molecular weight; Mw = weight-averaged molecular weight; PDI = polydispersity index; Ox =oxalic acid; Lac = lactic acid.
Figure S1: Lignin. Please click here to download this File.
Figure S2: Samples after being autoclaved (30 mg of lignin + 1 mL of 72% sulfuric acid + 28 mL of distilled water). Please click here to download this File.
Figure S3: Lignin pellets. Please click here to download this File.
Figure S4: Solid residue washed four times to recover maximum lignin content. Please click here to download this File.
Figure S5: Gel permeation chromatograms of lignin controls, raw and alkali-extracted lignins. Please click here to download this File.
Figure S6: Gel permeation chromatograms of lignin samples. Abbreviations: A = Alfa leaves, AS = Almond shells, PC = Pinecones, PL = Posidonia leaves, OP = Olive pomace, Ag = Aegagropile; DES1 = Choline chloride + Oxalic acid, DES2 = Choline chloride + Lactic acid, DES3 = Choline chloride + Urea. Please click here to download this File.
Figure S7: Flowsheet of the deep eutectic solvent (DES)-microwave process for lignin extraction. Please click here to download this File.
This study had many objectives; the first of which was to prepare and use low-cost green solvents with the characteristics of both ionic liquids and organic solvents. The second objective was to fractionate the biomass and extract lignin in a single step, without requiring preliminary steps such as the extraction of extractables using Soxhlet or hemicellulose using alkaline solvents, basic, or thermophysical techniques. The third aim was to recover lignin by simple filtration after the treatment, without adjustment of pH, but simply by adding distilled water. The results of the ultrafast extraction of lignin from six different sources using the microwave-assisted, DES-based process using three different DESs indicate that the extraction yield can vary depending on the biomass and nature of the DES. For example, the highest yield of lignin extraction among all three DESs was from olive pomace. This was followed by the yields from alfa leaves, pinecones, and almond shells. The extraction yields were lower for the leaves and balls of Posidonia oceanica.
The purity of lignin was evaluated using the Klason, Kjeldahl (nitrogen), carbohydrate (GC), and ash methods. As depicted in Figure 3 and Figure 5A–C, the purity of lignin decreased owing to the co-precipitation of nitrogen, carbohydrate, and ash components with lignin. The conditions for lignin extraction with DES1 ensured high purity, but a low yield, indicating that process improvements are necessary for the positive correlation between the yield and purity of lignin. The lignin yield can be improved if the duration of the treatment is longer, the microwave power is increased from 800 W to 1200 W, or the ratio of solid:solvent (1:10) is reduced. Lignin molecular weight data provide an insight into the dissociation or repolymerization of lignin fragments after treatment. An increase in the Mw of lignin for the biomasses was observed after the extraction using microwave-DES, as is evident, for example, in the case of Posidonia leaves (the Mw is 50093 for DES3 and is 70726 for DES1), which demonstrates that depolymerization occurred during the extraction of lignin and was followed by a rapid repolymerization of the carbon-carbon interunit under the action of the DES. This requires the use of a capturing agent, such as formaldehyde, to stabilize the deployment.
In DES pretreatment, lignin dissociation and condensation are the two competing reactions. The PDI of the extracted lignins is lower than that of beech lignin extracted by organic solvents (ethanol/water/H2SO4) reported in the literature17. This indicates that DES treatment improves molecular weight homogeneity in lignin compared to treatment with organic solvents. The FTIR spectra indicate that lignin functional groups are influenced by the DES solvent used. Spectra show signals at 1,730-1,702 cm-1 assigned to the stretching vibration of unconjugated carbonyl groups, whereas peaks at 1,643-1,635 cm-1 indicate the stretching vibration of conjugated carbonyl groups. These results demonstrate the possibility of extracting value-added lignin of high purity from Mediterranean biomasses (which is presently undervalued and used either as feed or as soil amendment) and can help determine the optimal DES solvent while ensuring the purity of lignin. For example, DES1 demonstrated the purest extraction of lignin, though with a lower yield than that observed using the other two DESs.
The proposed method can be applied easily because of the inexpensive and green ChCl-oxalic acid deep eutectic solvent system. Choline chloride is an organic salt and oxalic acid is available as a natural product of plants, which are abundant with low cost. This technique (an ultrafast protocol, which in one step provides biomass fractionation and high-purity lignin recovery) is applicable to any type of lignocellulosic biomass that has a chemical composition similar to that studied here on the laboratory scale using the microwave-DES process or at the pilot scale using the DES-ultrasound process or by convectional heating.
The authors have nothing to disclose.
MK and TB thanks Haitham Ayeb for statistical analyses and figure preparation, Walloon Region (European Regional Development-VERDIR) and Minister of Higher Education and Scientific Research (Taoufik Bettaieb) for funding.
HPLC Gel Permeation Chromatography | Agilent 1200 series | ||
1 methylimadazole | Acros organics | ||
2-deoxy-D-glucose (internal standard) | Sigma Aldrich (St. Louis, USA) | ||
Acetic acid | Sigma Aldrich (St. Louis, USA) | ||
Acetic anhydride | Sigma Aldrich (St. Louis, USA) | ||
Adjustables pipettors | |||
Alkali | alkali-extracted lignin | ||
Arabinose (99%) | Sigma Aldrich (St. Louis, USA) | ||
Autoclave | CERTO CLAV (Model CV-22-VAC-Pro) | ||
Water Bath at 70 °C | |||
Boric acid | Sigma Aldrich (St. Louis, USA) | ||
Bromocresol | Sigma Aldrich (St. Louis, USA) | ||
Catalyst | CTQ (coded A22) (1.5 g K2SO4 + 0.045 g CuSO4.5 H2O + 0.045 g TiO2) | Merck | |
Centrifugation container | |||
Centrifuge | BECKMAN COULTER | Avanti J-E centrifuge | |
Ceramic crucibles | |||
Choline chloride 99% | Acros organics | ||
Column | Agilent PLGel Mixed C (alpha 3,000 (4.6 × 250 mm, 5 µm) preceded by a guard column (TSK gel alpha guard column 4.6 mm × 50 mm, 5 µm) | ||
Column | HP1-methylsisoxane (30 m, 0.32 mm, 0.25 mm) | ||
Crucible porosity N°4 ( Filtering crucible) | Shott Duran Germany | boro 3.3 | |
Deonized water | |||
Dessicator | |||
Dimethylformamide | VWR BDH Chemicals | ||
Dimethylsulfoxide | Acros organics | ||
Erlenmeyer flask | |||
Ethanol | Merck (Darmstadtt, Germany) | ||
Filtering crucibles, procelain | |||
Filtration flasks | |||
Fourrier Transformed Inra- Red | Vertex 70 Bruker apparatus equipped with an attenuated total reflectance (ATR) module. Spectra were recorded in the 4,000–400 cm−1 range with 32 scans at a resolution of 4.0 cm−1 |
||
Galactose (98% | Sigma Aldrich (St. Louis, USA) | ||
Gaz Chromatography | Agilent (7890 series) | ||
Glass bottle 100 mL | |||
Glass tubes ( borosilicate) with teflon caps 10 mL | |||
Glucose (98% | Sigma Aldrich (St. Louis, USA) | ||
Golves | |||
Graduated cylinder 50 mL /100 mL | |||
H2SO4 Titrisol (0.1 N) | Merck (Darmstadtt, Germany) | ||
H2SO4 (95-98%) | Sigma Aldrich (St. Louis, USA) | BUCHI R-114) | |
Hummer cutter equiped with 1 mm and 0.5 mm sieve | Mill Ttecator (Sweden) | Cyclotec 1093 | |
Indulin | Raw lignin control | ||
Kjeldahl distiller | Kjeltec 2300 (Foss) | ||
Kjeldahl tube | FOSS | ||
Kjeldhal rack | |||
Kjeldhal digester | Kjeltec 2300 (Foss) | ||
Kjeldhal suction system | |||
Lab Chem station Software | GC data analysis | ||
Lactic acid | Merck (Darmstadtt, Germany) | ||
Lithium chloride LiCl | Sigma Aldrich (St. Louis, USA) | ||
Mannose (98%) | Sigma Aldrich (St. Louis, USA) | ||
Methyl red | |||
Microwave | START SYNTH MILESTONE Microwave laboratory system | ||
Microwave temperature probe | |||
Microwave container | |||
Muffle Furnace | |||
NaOH | Merck (Darmstadtt, Germany) | ||
Nitrogen free- paper | |||
Opus | spectroscopy software | ||
Oven | GmbH Memmert SNB100 | Memmert SNB100 | |
Oxalic acid | VWR BDH Chemicals | ||
P 1000 | Soda-processed lignin | ||
pH paper | |||
precision balance | |||
Infrared spectroscopy | |||
Quatz cuvette | |||
Rhamnose (98%) | Sigma Aldrich (St. Louis, USA) | ||
Rotary vacuum evaporator | Bucher | ||
Round-bottom flask 500 mL | |||
sodium borohydride NaBH4 | |||
Schott bottle | glass bottle | ||
Sovirel tubes | sovirel | Borosilicate glass tubes | |
Spatule | |||
Special tube | |||
Spectophotometer | UV-1800 Shimadzu | ||
Sterilization indicator tape | |||
Stir bar in teflon | |||
Stirring plate | |||
Syringes | |||
Sodium borohydride | Sigma Aldrich (St. Louis, USA) | ||
Titrisol | Merck | Merck 109984 | 0.1 N H2SO4 |
Urea | VWR BDH Chemicals | ||
Vials | |||
VolumetriC flask 2.5 L /5 L | Bucher | ||
Vortex | |||
Xylose (98%) | Sigma Aldrich (St. Louis, USA) |