Pretreatment of microcrystalline cellulose in organic electrolyte solutions for enzymatic hydrolysis

Background

Biomass use for the production of bioethanol or platform chemicals requires efficient breakdown of biomass to fermentable monosaccharides. Lignocellulosic feedstocks often require physicochemical pretreatment before enzymatic hydrolysis can begin. The optimal pretreatment can be different for different feedstocks, and should not lead to biomass destruction or formation of toxic products.

Methods

We examined the influence of six mild sulfuric acid or water pretreatments at different temperatures on the enzymatic degradability of sugar-beet pulp (SBP).

Results

We found that optimal pretreatment at 140°C of 15 minutes in water was able to solubilize 60% w/w of the total carbohydrates present, mainly pectins. More severe treatments led to the destruction of the solubilized sugars, and the subsequent production of the sugar-degradation products furfural, hydroxymethylfurfural, acetic acid and formic acid. The pretreated samples were successfully degraded enzymatically with an experimental cellulase preparation.

Conclusions

In this study, we found that pretreatment of SBP greatly facilitated the subsequent enzymatic degradation within economically feasible time ranges and enzyme levels. In addition, pretreatment of SBP can be useful to fractionate functional ingredients such as arabinans and pectins from cellulose. We found that the optimal combined severity factor to enhance the enzymatic degradation of SBP was between log R'₀ = -2.0 and log R'₀ = -1.5. The optimal pretreatment and enzyme treatment solubilized up to 80% of all sugars present in the SBP, including ≥90% of the cellulose.     

Ethanol production from seaweed (Undaria pinnatifida) using yeast acclimated to specific sugars

Ethanol production from Undaria pinnatifida (Sea mustard, Miyuk) was performed using yeast acclimated to specific sugars. Pretreatment conditions were optimized by thermal acid hydrolysis and enzyme treatment to increase the monosaccharide yield. Pretreatment by thermal acid hydrolysis was carried out using seaweed powder at 8 ～ 17% (w/v) solid content with a treatment time of 30 ～ 60 min. Enzyme treatment was carried out with 1% (v/v) Viscozyme L (1.2 FGU/mL), 1% (v/v) Celluclast 1.5 L (8.5 EGU/mL), 1% (v/v) AMG 300 L (3.0 AGU/mL), and 1% (v/v) Termamyl 120 L (0.72 KNU/mL). All enzymes except Termamyl 120 L, which was applied during pretreatment, were treated at 45°C for 24 h following pretreatment. Optimal pretreatment and enzyme conditions were determined to be 75 mM H₂SO₄, 13% (w/v) slurry, and 2.88 KNU/mL Termamyl 120 L at 121°C for 60 min. A maximum monosaccharide concentration of 33.1 g/L with 50.1% theoretical yield was obtained. To increase the ethanol yield, Pichia angophorae KCTC 17574 was acclimated to a high concentration (120 g/L) of galactose and mannitol at 30oC for 24 h. Ethanol production of 12.98 g/L with 40.12% theoretical yield was obtained from U. pinnatifida through fermentation with 0.35 g dry cell weight/L P. angophorae KCTC 17574 acclimated to mannitol and galactose.     

Butanol production from sweet sorghum bagasse with high solids content: Part I—comparison of liquid hot water pretreatment with dilute sulfuric acid

In these studies, we pretreated sweet sorghum bagasse (SSB) using liquid hot water (LHW) or dilute H₂SO₄ (2 g L^?1) at 190°C for zero min (as soon as temperature reached 190°C, cooling was started) to reduce generation of sugar degradation fermentation inhibiting products such as furfural and hydroxymethyl furfural (HMF). The solids loading were 250–300 g L^?1. This was followed by enzymatic hydrolysis. After hydrolysis, 89.0 g L^?1 sugars, 7.60 g L^?1 acetic acid, 0.33 g L^?1 furfural, and 0.07 g L^?1 HMF were released. This pretreatment and hydrolysis resulted in the release of 57.9% sugars. This was followed by second hydrolysis of the fibrous biomass which resulted in the release of 43.64 g L^?1 additional sugars, 2.40 g L^?1 acetic acid, zero g L^?1 furfural, and zero g L^?1 HMF. In both the hydrolyzates, 86.3% sugars present in SSB were released. Fermentation of the hydrolyzate I resulted in poor acetone‐butanol‐ethanol (ABE) fermentation. However, fermentation of the hydrolyzate II was successful and produced 13.43 g L^?1 ABE of which butanol was the main product. Use of 2 g L^?1 H₂SO₄ as a pretreatment medium followed by enzymatic hydrolysis resulted in the release of 100.6–93.8% (w/w) sugars from 250 to 300 g L^?1 SSB, respectively. LHW or dilute H₂SO₄ were used to economize production of cellulosic sugars from SSB. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:960–966, 2018     

Sequential Thermochemical Hydrolysis of Corncobs and Enzymatic Saccharification of the Whole Slurry Followed by Fermentation of Solubilized Sugars to Ethanol with the Ethanologenic Strain <Emphasis Type="Italic">Escherichia coli</Emphasis> MS04

Interest in the use of corncobs as feedstock for bioethanol production is growing. This study assesses the feasibility of sequential thermochemical diluted sulfuric acid pretreatment of corncobs at moderate temperature to hydrolyze the hemicellulosic fraction, followed by enzymatic hydrolysis of the whole slurry, and fermentation of the obtained syrup. The total sugar concentration after enzymatic hydrolysis was 85.21 g/l, i.e., 86 % of the sugars were liberated from the polymeric fractions, together with a low amount of furfural (0.26 g/l) and 4.01 g/l of acetic acid. The syrups, which contained 36.3, 40.9, 4.47, and 1.84 g/l of xylose, glucose, arabinose, and mannose, respectively, were fermented (pH 7, 37 °C, 150 rpm) to ethanol with the metabolically engineered acetate-tolerant Escherichia coli strain MS04 under non-aerated conditions, producing 35 g/l of ethanol in 18 h (1.94 g_EtOH/l/h), i.e., a conversion yield greater than 80 % of the theoretical value based on total sugars was obtained. Hence, using the procedures developed in this study, 288 l of ethanol can be produced per metric ton of dry corncobs. Strain MS04 can ferment sugars in the presence of acetate, and the amount of furans generated during the sequential thermochemical and enzymatic hydrolysis was low; hence, the detoxification step was avoided. The residual salts, acetic acid, and solubilized lignin present in the syrup did not interfere with the production of ethanol by E. coli MS04 and the results show that this strain can metabolize mixtures of glucose and xylose simultaneously.     

Enhancement of hydrolysis of <Emphasis Type="Italic">Chlorella vulgaris</Emphasis> by hydrochloric acid

Chlorella vulgaris is considered as one of the potential sources of biomass for bio-based products because it consists of large amounts of carbohydrates. In this study, hydrothermal acid hydrolysis with five different acids (hydrochloric acid, nitric acid, peracetic acid, phosphoric acid, and sulfuric acid) was carried out to produce fermentable sugars (glucose, galactose). The hydrothermal acid hydrolysis by hydrochloric acid showed the highest sugar production. C. vulgaris was hydrolyzed with various concentrations of hydrochloric acid [0.5–10 % (w/w)] and microalgal biomass [20–140 g/L (w/v)] at 121 °C for 20 min. Among the concentrations examined, 2 % hydrochloric acid with 100 g/L biomass yielded the highest conversion of carbohydrates (92.5 %) into reducing sugars. The hydrolysate thus produced from C. vulgaris was fermented using the yeast Brettanomyces custersii H1-603 and obtained bioethanol yield of 0.37 g/g of algal sugars.     

Hydrolysis of soy isoflavone glycosides by recombinant β-glucosidase from hyperthermophile <Emphasis Type="Italic">Thermotoga maritima</Emphasis>

A recombinant Thermotoga maritima β-glucosidase A (BglA) was purified to homogeneity for performing enzymatic hydrolysis of isoflavone glycosides from soy flour. The kinetic properties K _m, k _cat, and k _cat/K _m of BglA towards isoflavone glycosides, determined using high-performance liquid chromatography, confirmed the higher efficiency of BglA in hydrolyzing malonylglycosides than non-conjugated glycosides (daidzin and genistin). During hydrolysis of soy flour by BglA at 80°C, the isoflavone glycosides (soluble form) were extracted from soy flour (solid state) into the solution (liquid state) in thermal condition and converted to their aglycones (insoluble form), which mostly existed in the pellet to be separated from BglA in the reaction solution. The enzymatic hydrolysis in one-step and two-step approaches yielded 0.38 and 0.35 mg genistein and daidzein per gram of soy flour, respectively. The optimum conditions for conversion of isoflavone aglycones were 100 U per gram of soy flour, substrate concentration 25% (w/v), and incubation time 3 h for 80°C.     

Advantages of a two-step enzymatic process for cotton–polyester blends

Cotton fabric samples were treated with a formulation of a total crude Trichoderma reesei cellulase in a two-step procedure. In the first step, samples were treated at a low liquor ratio by padding through the enzyme formulation at 21°C and 55°C with a wet pickup of 100% and batched for 12 h. The samples were then treated at a high liquor ratio (1:25) with an identical enzyme formulation at 55°C, with intensive agitation. The pre-treatment influenced the overall weight loss and rate of hydrolysis in samples, and the protein concentration in the liquor of the second step. The overall weight loss was 25–28% (w/w) in the two-step procedure compared to a weight loss of 22% (w/w) in the one-step batch hydrolysis.     

Autohydrolysis extraction process as a pretreatment of lignocelluloses for their enzymatic hydrolysis

Autohydrolysis was studied as a pretreatment to enhance sugar yields from enzymatic hydrolysis of wheat and rape straw, beech, birch and poplar sawdust. Reaction temperatures were 185°C to 212°C and the reaction time 20 min. The pretreated slurries were hydrolyzed with “Novo” cellulase and Fusarium sp. 27 cellulase at 45°C and pH 4.8 for 24 h with addition of Fusarium sp. 27 cellbound cellobiase. From 85% to 90% sugar content of substrates were converted to reducing sugars after 24 h enzymatic hydrolysis, with exception of poplar wood. 10.8 g biomass was obtained after cultivation of Fusarium sp. 27 with water solution hemicellulose fraction from 100 g beech sawdust autohydrolyzed at 200°C during 20 min.     

Enantioconvergent hydrolysis of racemic styrene oxide at high concentration by a pair of novel epoxide hydrolases into (<Emphasis Type="Italic">R</Emphasis>)-phenyl-1,2-ethanediol

Objectives

To prepare (R)-phenyl-1,2-ethanediol ((R)-PED) with high enantiomeric excess (ee _p) and yield from racemic styrene oxide (rac-SO) at high concentration by bi-enzymatic catalysis.

Results

The bi-enzymatic catalysis was designed for enantioconvergent hydrolysis of rac-SO by a pair of novel epoxide hydrolases (EHs), a Vigna radiata EH3 (VrEH3) and a variant (AuEH2^A250I) of Aspergillus usamii EH2. The simultaneous addition mode of VrEH3 and AuEH2^A250I, exhibiting the highest average turnover frequency (aTOF) of 0.12 g h^?1 g^?1, was selected, by which rac-SO (10 mM) was converted into (R)-PED with 92.6% ee _p and 96.3% yield. Under the optimized reaction conditions: dry weight ratio 14:1 of VrEH3-expressing E. coli/vreh3 to AuEH2^A250I-expressing E. coli/Aueh2 ^A250I and reaction at 20 °C, rac-SO (10 mM) was completely hydrolyzed in 2.3 h, affording (R)-PED with 98% ee _p. At the weight ratio 0.8:1 of rac-SO to two mixed dry cells, (R)-PED with 97.4% ee _p and 98.7% yield was produced from 200 mM (24 mg/ml) rac-SO in 10.5 h.

Conclusions

Enantioconvergent hydrolysis of rac-SO at high concentration catalyzed by both VrEH3 and AuEH2^A250I is an effective method for preparing (R)-PED with high ee _p and yield.

     

Enhancement of the enzymatic digestibility of sugarcane bagasse by steam pretreatment impregnated with hydrogen peroxide

Sugarcane bagasse was subjected to steam pretreatment impregnated with hydrogen peroxide. Analyses were performed using 2³ factorial designs and enzymatic hydrolysis was performed at two different solid concentrations and with washed and unwashed material to evaluate the importance of this step for obtaining high cellulose conversion. Similar cellulose conversion were obtained at different conditions of pretreatment and hydrolysis. When the cellulose was hydrolyzed using the pretreated material in the most severe conditions of the experimental design (210°C, 15 min and 1.0% hydrogen peroxide), and using 2% (w/w) water‐insoluble solids (WIS), and 15 FPU/g WIS, the cellulose conversion was 86.9%. In contrast, at a milder pretreatment condition (190°C, 15 min and 0.2% hydrogen peroxide) and industrially more realistic conditions of hydrolysis (10% WIS and 10 FPU/g WIS), the cellulose conversion reached 82.2%. The step of washing the pretreated material was very important to obtain high concentrations of fermentable sugars. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

Efficient chemical and enzymatic saccharification of the lignocellulosic residue from <Emphasis Type="Italic">Agave tequilana</Emphasis> bagasse to produce ethanol by <Emphasis Type="Italic">Pichia caribbica</Emphasis>

Bagasse of Agave tequilana (BAT) is the residual lignocellulosic waste that remains from tequila production. In this study we characterized the chemical composition of BAT, which was further saccharified and fermented to produce ethanol. BAT was constituted by cellulose (42%), hemicellulose (20%), lignin (15%), and other (23%). Saccharification of BAT was carried out at 147°C with 2% sulfuric acid for 15 min, yielding 25.8 g/l of fermentable sugars, corresponding to 36.1% of saccharificable material (cellulose and hemicellulose contents, w/w). The remaining lignocellulosic material was further hydrolyzed by commercial enzymes, ~8.2% of BAT load was incubated for 72 h at 40°C rendering 41 g/l of fermentable sugars corresponding to 73.6% of the saccharificable material (w/w). Mathematic surface response analysis of the acid and enzymatic BAT hydrolysis was used for process optimization. The results showed a satisfactory correlation (R ² = 0.90) between the obtained and predicted responses. The native yeast Pichia caribbica UM-5 was used to ferment sugar liquors from both acid and enzymatic hydrolysis to ethanol yielding 50 and 87%, respectively. The final optimized process generated 8.99 g ethanol/50 g of BAT, corresponding to an overall 56.75% of theoretical ethanol (w/w). Thus, BAT may be employed as a lignocellulosic raw material for bioethanol production and can contribute to BAT residue elimination from environment.     

Heart valve cryopreservation: protocol for addition of dimethyl sulphoxide and amelioration of putative amphotericin B toxicity

Aim

To investigate the need for stepwise addition of dimethyl sulphoxide to heart valves and amelioration of putative amphotericin B toxicity.

Methods

There were four groups: an untreated control (Group 1) and three experimental groups. For the latter, porcine heart valves were exposed to the antibiotic/antimycotic mixture used for disinfecting heart valves in the Bristol Heart Valve Bank, for 24 h at 22 °C. Dimethyl sulphoxide (Me₂SO, 10% v/v) was added either in two steps (5% then 10%) (Group 2) or in a single step. For single-step addition, valves were either first placed in Hanks’ balanced salt solution for 10 min before transfer to the cryoprotectant solution (Group 3) or immersed directly in the 10% cryoprotectant solution (Group 4). The valve leaflets were dissected from the valves and frozen in 10% Me₂SO in multi-well tissue culture plates at 1 °C/min to −80 °C. After storage overnight, the valve leaflets were warmed at approximately 11 °C/min and the cryoprotectant was removed by single-step dilution in excess Hartmann’s solution. Each leaflet was then divided into four pieces, which were placed in separate wells of a culture plate. Outgrowth of cells from the explants was monitored daily and graded according to the extent of cell growth.

Results

After freezing and thawing, only 77% of the explants from valves placed directly into 10% Me₂SO (Group 4) showed outgrowth of cells after freezing compared with 89% with two-step addition of Me₂SO (Group 2) and 95% with one-step addition after the extra rinse in Hanks’ solution (Group 3) (χ², p = 0.001). 92% of unfrozen control explants showed outgrowth of cells (Group 1). Only 37% of Group 4 explants reached confluence compared with 63 and 56%, respectively, of Groups 2 and 3 explants (χ², p = 0.007). The rates of cell growth in Group 2 (two-step addition of Me₂SO) and Group 3 (one-step addition of Me₂SO with additional Hanks’ solution rinse) were similar and faster than the Group 4 (one-step addition of Me₂SO without the additional Hanks’ rinse).

Conclusion

Single-step addition of Me₂SO before freezing gave similar results to two-step addition provided an additional rinse in Hanks’ solution was introduced after exposure to the antibiotic/antimycotic mixture. This suggests that antibiotic/antimycotic carryover may have been harmful during freezing and that the additional rinse in Hanks before one-step addition of Me₂SO, and the 5% Me₂SO step in the two-step protocol, merely served to reduce this carryover.     

Pomegranate peels waste hydrolyzate optimization by Response Surface Methodology for Bioethanol production

Unwanted agricultural waste is largely comprised of lignocellulosic substrate which could be transformed into sugars. The production of bioethanol from garbage manifested an agreeable proposal towards waste management as well as energy causation. The goal of this work is to optimize parameters for generation of bioethanol through fermentation by different yeast strains while Saccharomyces cerevisiae used as standard strain. The low cost fermentable sugars from pomegranate peels waste (PPW) were obtained by hydrolysis with HNO₃ (1 to 5%). The optimum levels of hydrolysis time and temperature were elucidated via RSM (CCD) ranging from 30 to 60 min and 50 to 100 °C respectively. The result shows that optimum values (g/L) for reducing sugars was 61.45 ± 0.01 while for total carbohydrates was 236 ± 0.01. These values were found when PPW was hydrolyzed with 3% HNO₃, at 75 °C for one hour. The hydrolyzates obtained from the dilute HNO₃ pretreated PPW yielded a maximum of 0.43 ± 0.04, 0.41 ± 0.03 g ethanol per g of reducing sugars by both Metchnikowia sp. Y31 and M. cibodasensis Y34 at day 7 of ethanologenic experiment. The current study exhibited that by fermentation of dilute HNO₃ hydrolyzates of PPW could develop copious amount of ethanol by optimized conditions.     

Production of hemicellulosic sugars and glucose from residual corrugated cardboard

Corrugated cardboard samples were subjected to two-step saccharification. A first prehydrolysis stage was carried out to solubilise the hemicellulosic fraction as hemicellulosic sugars, and the solid phase from prehydrolysis was used as a substrate for the enzymic hydrolysis of cellulose. The prehydrolysis step was carried out for 0–180 min in media containing 1–3 wt.% of H₂SO₄ and the fraction of solid recovered after treatments and the compositions of solid and liquid phases from treatments were measured. The susceptibility of prehydrolysed solids towards the enzymic hydrolysis was assessed in further experiments. Under selected prehydrolysis conditions (3% H₂SO₄, 180 min), 78.2% of initial hemicelluloses was saccharified, leading to liquors containing up to 10 g hemicellulosic sugars/l and 9.2 g glucose/l. The corresponding solid phase, enriched in cellulose, showed good susceptibility towards enzymatic hydrolysis, leading to solutions containing up to 17.9 g glucose/l (conversion yield=63.6%) and a glucose/total sugar ratio of 0.93 g/g. Mathematical models assessing the effects of the operational conditions on both the prehydrolysis stage and the susceptibility of substrates towards enzymic hydrolysis have been developed.     

Study of the Ultrastructure of <Emphasis Type="Italic">Eucalyptus globulus</Emphasis> Wood Substrates Subjected to Auto-Hydrolysis and Diluted Acid Hydrolysis Pre-treatments and Its Influence on Enzymatic Hydrolysis

Dilute acid hydrolysis (DAH) and auto-hydrolysis (AU) have demonstrated to be optimal pre-treatments for the generation of biofuels from wood. Recent studies have highlighted the importance of ensuring the accessibility of cellulose enzymes during the enzymatic hydrolysis (EH) of pre-treated materials. In this work, the microscopic and nanoscopic structures of Eucalyptus globulus samples pre-treated by AU and DAH were evaluated by different techniques to understand the effect of the ultrastructure of samples on the enzymatic conversion and cellulose accessibility for bioethanol production. Microscopic techniques revealed changes in the physical characteristics of pre-treated fibers, coalescence at microscopic level, and differences in the chemical distribution of lignocellulosic components depending on the severity and type of pre-treatment. The atomic force microscopy-based nanoscopic study of samples showed differences in the effect of the pre-treatments on the ultrastructure of samples, with DAH pre-treatment producing major changes in the secondary cell wall with respect to AU samples at comparable severities, and a positive effect of the DAH ultrastructure changes to increase the EH yield.     

Comparison of SHF and SSF processes for the bioconversion of steam-exploded wheat straw

Two processes for ethanol production from wheat straw have been evaluated — separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF). The study compares the ethanol yield for biomass subjected to varying steam explosion pretreatment conditions: temperature and time of pretreatment was 200°C or 217°C and at 3 or 10 min. A rinsing procedure with water and NaOH solutions was employed for removing lignin residues and the products of hemicellulose degradation from the biomass, resulting in a final structure that facilitated enzymatic hydrolysis. Biomass loading in the bioreactor ranged from 25 to 100 g l⁻¹ (dry weight). The enzyme-to-biomass mass ratio was 0.06. Ethanol yields close to 81% of theoretical were achieved in the two-step process (SHF) at hydrolysis and fermentation temperatures of 45°C and 37°C, respectively. The broth required addition of nutrients. Sterilisation of the biomass hydrolysate in SHF and of reaction medium in SSF can be avoided as can the use of different buffers in the two stages. The optimum temperature for the single-step process (SSF) was found to be 37°C and ethanol yields close to 68% of theoretical were achieved. The SSF process required a much shorter overall process time (≈30 h) than the SHF process (96 h) and resulted in a large increase in ethanol productivity (0.837 g l⁻¹ h⁻¹ for SSF compared to 0.313 g l⁻¹ h⁻¹ for SHF). Journal of Industrial Microbiology & Biotechnology (2000) 25, 184–192. Received 02 December 1999/ Accepted in revised form 20 July 2000     

Comparative performance of precommercial cellulases hydrolyzing pretreated corn stover

Background

Cellulases and related hydrolytic enzymes represent a key cost factor for biochemical conversion of cellulosic biomass feedstocks to sugars for biofuels and chemicals production. The US Department of Energy (DOE) is cost sharing projects to decrease the cost of enzymes for biomass saccharification. The performance of benchmark cellulase preparations produced by Danisco, DSM, Novozymes and Verenium to convert pretreated corn stover (PCS) cellulose to glucose was evaluated under common experimental conditions and is reported here in a non-attributed manner.

Results

Two hydrolysis modes were examined, enzymatic hydrolysis (EH) of PCS whole slurry or washed PCS solids at pH 5 and 50°C, and simultaneous saccharification and fermentation (SSF) of washed PCS solids at pH 5 and 38°C. Enzymes were dosed on a total protein mass basis, with protein quantified using both the bicinchoninic acid (BCA) assay and the Bradford assay. Substantial differences were observed in absolute cellulose to glucose conversion performance levels under the conditions tested. Higher cellulose conversion yields were obtained using washed solids compared to whole slurry, and estimated enzyme protein dosages required to achieve a particular cellulose conversion to glucose yield were extremely dependent on the protein assay used. All four enzyme systems achieved glucose yields of 90% of theoretical or higher in SSF mode. Glucose yields were reduced in EH mode, with all enzymes achieving glucose yields of at least 85% of theoretical on washed PCS solids and 75% in PCS whole slurry. One of the enzyme systems ('enzyme B') exhibited the best overall performance. However in attaining high conversion yields at lower total enzyme protein loadings, the relative and rank ordered performance of the enzyme systems varied significantly depending upon which hydrolysis mode and protein assay were used as the basis for comparison.

Conclusions

This study provides extensive information about the performance of four precommercial cellulase preparations. Though test conditions were not necessarily optimal for some of the enzymes, all were able to effectively saccharify PCS cellulose. Large differences in the estimated enzyme dosage requirements depending on the assay used to measure protein concentration highlight the need for better consensus methods to quantify enzyme protein.

     

Extraction of indole alkaloids fromCatharanthus roseus by using supercritical carbon dioxide

Summary Indole alkaloids, particularly vindoline and catharanthine, were extracted from the leaves ofCatharanthus roseus by supercritical extraction with CO₂. The contents of vindoline and catharanthine in the extracts were determined by HPLC and identified by LC/MS. About 52 %(w/w) of the initial vindoline content, 1.5 mg vindoline/g dry wt leaves, was recovered after extracting this material for 10 h with the CO₂ flow rate of 400 ml/min at 40°C and 150 bar. Vindoline concentration in the extract was 67 %(w/w).     

Optimization of pineapple pulp residue hydrolysis for lipid production by Rhodotorula glutinis TISTR5159 using as biodiesel feedstock

The higher lipid productivity of Rhodotorula glutinis TISTR5159 was achieved by optimizing the pineapple pulp hydrolysis for releasing the high sugars content. The sequential simplex method operated by varied; solid-to-liquid ratio, sulfuric acid concentration, temperature, and hydrolysis time were successfully applied and the highest sugar content (83.2 g/L) evaluated at a solid-to-liquid ratio of 1:10.8, 3.2% sulfuric acid, 105 °C for 13.9 min. Moreover, the (NH₄)₂SO₄ supplement enhanced the lipid productivity and gave the maximum yields of biomass and lipid of 15.2 g/L and 9.15 g/L (60.2%), respectively. The C16 and C18 fatty acids were found as main components included oleic acid (55.8%), palmitic acid (16.6%), linoleic acid (11.9%), and stearic acid (7.8%). These results present the possibility to convert the sugars in pineapple pulp hydrolysate to lipids. The fatty acid profile was also similar to vegetable oils. Thus, it could be used as potential feedstock for biodiesel production.     

Enzymatic Saccharification of Pretreated Wheat Straw by T. Reesei Cellulases and A. Niger β-Glucosidase

Three methods of wheat straw treatment (with NaOH, H₂O₂ and butylamine) and its subsequent saccharification by Trichoderma reesei cellulases and Aspergillus niger β-glucosidase are reported. The treatment of straw with NaOH for 1 h in the autoclave (120°C) caused a great loss of the hemicellulose content and a partial removal of lignin, provoking an increase of the cellulose content (from 24% to 69%) in the residue. When the straw was pre-treated with H₂O₂ at 25°C for 20 h, the relative content of cellulose in the straw increased (from 24% to 52%) due to the solubilisation of hemicellulose.

The effect of varying the hydrolysis parameters (enzyme and substrate concentration, temperature and pH) was studied in order to maximise the yield of sugars. Under the best conditions and after 48 h with a mixture of 2:1 (w/w) cellulase/β-glucosidase (with a concentration of 7 and 0.1 U ml^-1, respectively) the native, NaOH-treated and H₂O₂-treated straw material were degraded to reducing sugars for 28%, 89% and 97% respectively.