Display of Candida antarctica lipase B on Pichia pastoris and its application to flavor ester synthesis

Two alternative cell-surface display systems were developed in Pichia pastoris using the α-agglutinin and Flo1p (FS) anchor systems, respectively. Both the anchor cell wall proteins were obtained originally from Saccharomyces cerevisiae. Candida antarctica lipase B (CALB) was displayed functionally on the cell surface of P. pastoris using the anchor proteins α-agglutinin and FS. The activity of CALB displayed on P. pastoris was tenfold higher than that of S. cerevisiae. The hydrolytic and synthetic activities of CALB fused with α-agglutinin and FS anchored on P. pastoris were investigated. The hydrolytic activities of both lipases displayed on yeast cells surface were more than 200 U/g dry cell after 120 h of culture (200 and 270 U/g dry cell, respectively). However, the synthetic activity of CALB fused with α-agglutinin on P. pastoris was threefold higher than that of the FS fusion protein when applied to the synthesis of ethyl caproate. Similarly, the CALB displayed on P. pastoris using α-agglutinin had a higher catalytic efficiency with respect to the synthesis of other short-chain flavor esters than that displayed using the FS anchor. Interestingly, for some short-chain esters, the synthetic activity of displaying CALB fused with α-agglutinin on P. pastoris was even higher than that of the commercial CALB Novozyme 435.     

Effects of by-products of fermentation of banana pseudostem on ethanol separation by pervaporation

In this work, we performed recovery of ethanol from a fermentation broth of banana pseudostem by pervaporation (PV) as a lower-energy-cost alternative to traditional separation processes such as distillation. As real fermentation systems generally contain by-products, it was investigated the effects of different components from the fermentation broth of banana pseudostem on PV performance for ethanol recovery through commercial flat sheet polydimethylsiloxane (PDMS) membrane. The experiments were compared to a binary solution (ethanol/water) to determine differences in the results due to the presence of fermentation by-products. A real fermented broth of banana pseudostem was also used as feed for the PV experiments. Seven by-products from fermented broth were identified: propanol, isobutanol, methanol, isoamyl alcohol, 1-pentanol, acetic acid, and succinic acid. Moreover, the residual sugar content of 3.02 g/L¹ was obtained. The presence of methanol showed the best results for total permeate flux (0.1626 kg·m⁻²·h⁻¹) and ethanol permeate flux (0.0391 kg·m⁻²·h⁻¹) during PV at 25°C and 3 wt% ethanol, also demonstrated by the selectivity and enrichment factor. The lowest total fluxes of permeate were observed in the experiments containing the acids. Better permeance of 0.1171 from 0.0796 kg·m⁻²·h⁻¹ and membrane selectivity of 9.77 from 9.30 were obtained with real fermentation broth than with synthetic solutions, possibly due to the presence of by-products in the multicomponent mixtures, which contributed to ethanol permeation. The results of this work indicate that by-products influence pervaporation of ethanol with hydrophobic flat sheet membrane produced from the fermented broth of banana pseudostem.     

Fermentation and purification of microbial monomer 4-amminocinnamic acid to produce ultra-high performance bioplastics

Aromatic amines are base materials for generating super-engineering plastics such as polyamides and polyimides. Recombinant Escherichia coli ferments 4-aminocinnamic acid (4ACA) from glucose, and it can be derived to plastics of biomass origin with extreme thermal properties. Here, we scaled-up 4ACA production by optimizing microbial fermentation processes. The initial fermentation of 4-aminophenylalanine (4APhe) using E. coli generated the papABC genes of Pseudomonas fluorescens that produced 4APhe with a volumetric mass transfer coefficient (k_La) of 70 h⁻¹ in 115 L of culture broth, and 334 g of 4APhe at a final concentration of 2.9 g 4APhe L⁻¹. Crude 4APhe prepared from the fermentation broth was bioconverted to 4ACA by an E. coli strain producing phenylalanine ammonia lyase of the yeast Rhodotorula glutinis. The E. coli cells cultured under optimized conditions converted 4APhe to 4ACA at a rate of 0.65 g L⁻¹ 4ACA OD₆₀₀⁻¹. These processes resulted in the final derivation of 4.1 g L⁻¹ of 4ACA from glucose. The 4ACA was purified from the reaction as a hydrochloric acid salt and photodimerized to 4,4’-diaminotruxillic acid, which was polycondensed to produce bioaromatic polyimides. Large-scale 4ACA production will facilitate investigations of the physicochemical properties of biomass-derived aromatic polymers of 4ACA origin.     

Supercritical CO2 as a reaction medium for synthesis of capsaicin analogues by lipase-catalyzed transacylation of capsaicin

Capsaicin analogues having different acyl moiety were synthesized by lipase-catalyzed transacylation of capsaicin with a corresponding acyl donor in supercritical CO₂ as a reaction medium. Transacylation with methyl tetradecanoate using Novozym 435 as a catalyst gave vanillyl tetradecanamide in a 54% yield at 80 °C and 19 MPa over 72 h. Vanillyl (Z)-9-octadecenamide, olvanil, was synthesized from triolein in a 21% yield over 7 d.     

Quantitative physiology of Pichia pastoris during glucose‐limited high‐cell density fed‐batch cultivation for recombinant protein production

Pichia pastoris has become one of the major microorganisms for the production of proteins in recent years. This development was mainly driven by the readily available genetic tools and the ease of high‐cell density cultivations using methanol (or methanol/glycerol mixtures) as inducer and carbon source. To overcome the observed limitations of methanol use such as high heat development, cell lysis, and explosion hazard, we here revisited the possibility to produce proteins with P. pastoris using glucose as sole carbon source. Using a recombinant P. pastoris strain in glucose limited fed‐batch cultivations, very high‐cell densities were reached (more than 200 g_CDW L^?1) resulting in a recombinant protein titer of about 6.5 g L^?1. To investigate the impact of recombinant protein production and high‐cell density fermentation on the metabolism of P. pastoris, we used ¹³C‐tracer‐based metabolic flux analysis in batch and fed‐batch experiments. At a controlled growth rate of 0.12 h^?1 in fed‐batch experiments an increased TCA cycle flux of 1.1 mmol g^?1 h^?1 compared to 0.7 mmol g^?1 h^?1 for the recombinant and reference strains, respectively, suggest a limited but significant flux rerouting of carbon and energy resources. This change in flux is most likely causal to protein synthesis. In summary, the results highlight the potential of glucose as carbon and energy source, enabling high biomass concentrations and protein titers. The insights into the operation of metabolism during recombinant protein production might guide strain design and fermentation development. Biotechnol. Bioeng. 2010;107: 357–368. © 2010 Wiley Periodicals, Inc.     

Decarboxylative aldol reaction catalysed by lipases and a protease in organic co-solvent mixtures and nearly anhydrous organic solvent media

Abstract

The effects of the choice of lipase, reaction medium, immobilization, presence of additives and temperature on conversion and stereoselectivity during a lipase catalysed decarboxylative aldol reaction were examined. It was shown that Candida antarctica lipase B (CALB) catalysed a decarboxylative aldol reaction between 4-nitrobenzaldehyde and ethyl acetoacetate in a 60% acetonitrile–40% aqueous buffer co-solvent mixture. Interestingly, free and immobilized forms of CALB showed opposite enantioselectivity in this media. The addition of 30 mol% imidazole increased the reaction rate from 8.5 to 55.7 μM min^??1 mg^??1. A 98% conversion could be achieved in 14 h (instead of 168 h) by adding imidazole. Other lipases also catalysed this reaction in different reaction media to a varying extent. With Mucor javanicus lipase in 30% DMSO, 20% enantiomeric excess (ee) of the (R)-product was observed. CALB also catalysed this reaction in nearly anhydrous acetonitrile. In the presence of cross-linked protein coated microcrystals of CALB, 90% conversion was obtained in this media in 24 h. A commercially available protease, alcalase, was also found to catalyse this reaction. While low water media gave poor conversion, the reaction in aqueous–60% acetonitrile co-solvent mixture gave 99% conversion in 72 h, provided imidazole was used as an additive.     

Biocatalytic synthesis of vitamin A palmitate using immobilized lipase produced by recombinant Pichia pastoris

In this work, the Candida antarctica lipase B (CALB), produced by recombinant Pichia pastoris , was immobilized and used to synthesize vitamin A palmitate by transesterification of vitamin A acetate and palmitic acid in organic solvent. The reaction conditions including the type of solvent, temperature, rotation speed, particle size, and molar ratio between the two substrates were investigated. It turned out that the macroporous resin HPD826 serving as a carrier showed the highest activity (ca. 9200 U g^?1) among all the screened carriers. It was found that the transesterification kinetic of the immobilized CALB followed the ping pong Bi‐Bi mechanism and the reaction product acetic acid inhibited the enzymatic reaction with an inhibition factor of 2.823 mmol L^?1. The conversion ability of the immobilized CALB was 54.3% after 15 cycles. In conclusion, the present work provides a green route for vitamin A palmitate production using immobilized CALB to catalyze the transesterification of vitamin A acetate and palmitic acid.     

Synthesis of fatty acid ethyl esters with conventional and microwave heating systems using the free lipase B from Candida antarctica

Free Candida antarctica lipase B (Lipozyme, CALB L^®) was used to produce fatty acid ethyl esters (FAEE) from refined soybean oil in solvent-free media using the conventional (CHS) and microwave (MHS) heating systems. Statistical analyses (95% confidence level) for both reaction products, FAEE and free fatty acids (FFA), were performed. An increase in ethanol:oil molar ratio decreased the catalytic performance of CALB L (p?<?.05). The best conditions using the microwave radiation were a molar ratio of ethanol:oil of 3:1, a water content of 20.3?wt.% and an enzyme loading of 3?wt.% and this resulted in a total ester content of 64.7% in 15?min, while the same condition using the conventional heating gave only 21.4%. Moreover, the reaction equilibrium was reached 16 times faster with microwave than with conventional heating. High ethanol:oil molar ratios had a negative effect on FAEE synthesis with both CHS and MHS, probably due to the partial inactivation of the enzymes. MHS improved the reaction performance of CALB L, but other process parameters will have to be optimized to enhance the resulting FAEE yields. The recovery and reuse of CALB L using a MHS was demonstrated. Hence, the use of microwave radiation under the conditions applied in this study was not detrimental to the catalytic performance of CALB L for at least one reuse.     

Chromosome evolution of Escherichia coli Nissle 1917 for high-level production of heparosan

Heparosan is a crucial-polysaccharide precursor for the chemoenzymatic synthesis of heparin, a widely used anticoagulant drug. Presently, heparosan is mainly extracted with the potential risk of contamination from Escherichia coli strain K5, a pathogenic bacterium causing urinary tract infection. Here, a nonpathogenic probiotic, E. coli strain Nissle 1917 (EcN), was metabolically engineered to carry multiple copies of the 19-kb kps locus and produce heparosan to 9.1 g/L in fed-batch fermentation. Chromosome evolution driven by antibiotics was employed to amplify the kps locus, which governed the synthesis and export of heparosan from EcN at 21 mg L⁻¹ OD⁻¹. The average copy number of kps locus increased from 1 to 24 copies per cell, which produced up to 104 mg L^-1 OD⁻¹ of heparosan in the shaking flask cultures of engineered strains. The following in-frame deletion of recA stabilized the recombinant duplicates of chromosomal kps locus and the productivity of heparosan in continuous culture for at least 56 generations. Fed-batch fermentation of the engineered strain EcN8 was carried out to bring the yield of heparosan up to 9.1 g/L. Heparosan from the fermentation culture was further purified at a 75% overall recovery. The structure of purified heparosan was characterized and further modified by N-sulfotransferase with 3′-phosphoadenosine-5′-phosphosulfate as the sulfo-donor. The analysis of element composition showed that heparosan was N-sulfated by over 80%. These results indicated that duplicating large DNA cassettes up to 19-kb, followed by high-cell-density fermentation, was promising in the large-scale preparation of chemicals and could be adapted to engineer other industrial-interest bacteria metabolically.     

Optimization of β-mannanase production by Bacillus subtilis US191 using economical agricultural substrates

The Bacillus subtilis US191 strain producing highly thermostable β-mannanase was previously selected as potential probiotic candidate for application as feed supplement in poultry industry. Initially, the level of extracellular β-mannanase production by this strain was 1.48 U ml⁻¹. To improve this enzyme titer, the present study was undertaken to optimize the fermentation conditions through experimental designs and valorization of agro-industrial byproducts. Using the Plackett–Burman design, in submerged fermentation, a set of 14 culture variables was evaluated in terms of their effects on β-mannanase production. Locust bean gum (LBG), soymeal, temperature, and inoculum size were subsequently optimized by response surface methodology using Box–Behnken design. Under optimized conditions (1 g L⁻¹ LBG, 8 g L⁻¹ soymeal, temperature of 30°C and inoculum size of 10¹⁰ CFU ml⁻¹), a 2.59-fold enhancement in β-mannanase titer was achieved. Next, to decrease the enzyme production cost, the effect of partial substitution of LBG (1 g L⁻¹) by agro-industrial byproducts was investigated, and a Taguchi design was applied. This allowed the attaining of a β-mannanase production level of 8.75 U ml⁻¹ in presence of 0.25 g L⁻¹ LBG, 5 g L⁻¹ of coffee residue powder, 5 g L⁻¹ of date seeds powder, and 5 g L⁻¹ of prickly pear seeds powder as mannans sources. Overall, a 5.91-fold improvement in β-mannanase production by B. subtilis US191 was achieved.     

Identification of Flavone Compounds in Eighteen Gramineae Species

Conditions for tryptophan synthesis from pyruvic acid, indole and NH₄Cl by Enterobacter aerogenes AHU 1540 having a high tryptophanase activity, were investigated using a reaction mixture containing 1.7% of pyruvic acid. Under optimum conditions, 16.4g/liter of tryptophan was accumulated after 24 hr of incubation.

Agaricus campestris AHU 9382 produced pyruvic acid in amounts of 22 ~ 26.5 g/liter from 5% of glucose after 3-days shaking culture. When E. aerogenes was added to this fermentation broth together with indole and NH₄Cl, pyruvic acid produced was rapidly converted to tryptophan and yields of tryptophan as high as 15 g/liter were obtained after 12 hr of incubation. Furthermore, pyruvic acid fermentation by Saccharomyces exiguus AHU 3110 or Corynebacterium sp. 37-3A could also be used as a pyruvic acid source for subsequent tryptophan production.     

Quantitative evaluation of Candia antarctica lipase B displayed on the cell surface of a Pichia pastoris based on an FS anchor system

A new approach is described to quantify the number of enzyme molecules, such as Candia antarctica lipase B, that are displayed on the cell surface of Pichia pastoris. Enhanced green fluorescent protein (EGFP) and Candida antarctica lipase B (CALB) were fused and displayed on the surface of P. pastoris by linking to the anchor flocculation functional domain of FLO1p from Saccharomyces cerevisiae. Confocal laser scanning microscopy, flow cytometry, and fluorescence spectrophotometry were used to monitor the fluorescence intensity of fused EGFP. Combined with the corresponding protein concentration detected in the medium, a standard curve describing the relationship between the fusion protein concentration and fluorescence intensity were obtained and could be used to number CALB displayed on the cell surface. The results showed that approx. 10⁴ molecules of CALB molecules were immobilized on the single P. pastoris cell wall based on FS anchor system.     

Biotransformation of cladribine using a stabilized biocatalyst in calcium alginate beads

Cladribine is a nucleoside analogue widely used in the pharmaceutical industry for the treatment of several neoplasms, including hairy-cell leukemia among others. This compound has also shown efficacy in the treatment of autoimmune diseases such as rheumatoid arthritis and multiple sclerosis. In this work, a green bioprocess for cladribine biosynthesis using immobilized Arthrobacter oxydans was developed. The microorganism was stabilized by entrapment immobilization in the natural matrix alginate. Different reaction parameters were optimized obtaining a biocatalyst able to achieve cladribine bioconversion values close to 85% after 1 hr, the shortest reaction times reported so far. The developed bioprocess was successfully scaled-up reaching a productivity of 138 mg L⁻¹ hr⁻¹. Also, the biocatalyst was stable for 5 months in storage and in 96 hr at operational conditions.     

Optimization of the fermentation parameters for the production of Ganoderma lucidum immunomodulatory protein by Pichia pastoris

Abstract

In order to obtain a better fermentation parameter for the production of recombinant Ganoderma lucidum immunomodulatory protein (rFIP-glu), an engineered Pichia pastoris GS115 was investigated on the fermentation time, temperature, methanol concentration and initial pH of media, while immunomodulatory activities of the rFIP-glu was confirmed. L₉(3³) orthogonal experiment were firstly employed to optimize various fermentation parameters in the shake-flask level. The optimized fermentation parameters were subsequently verified in a 5?L fermenter. Biological activities including cell viability and tumor necrosis factor-alpha (TNF-α) mRNA of the rFIP-glu were evaluated on murine macrophage RAW264.7 cells. The results showed that the yield of rFIP-glu was up to 368.71?μg/ml in the shake-flask, and 613.47?μg/ml in the 5?L fermenter, when the Pichia pastoris was incubated in basic media with the methanol concentration 1.0% and initial pH 6.5, and with constant shaking at 280?rpm for 4?days at 26?°C. In vitro assays of biological activity indicated that rFIP-glu had significant toxicity against RAW264.7 cells, and possessed the ability to induce TNF-α mRNA expression in macrophage RAW264.7 cells. In conclusion, engineered P. pastoris showed a good fermentation property under the optimum fermentation parameters. It could be a candidate industrial strain for further study.     

Nutritional optimization of Arthrospira platensis for starch and Total carbohydrates production

Present study aims to optimize the production of starch and total carbohydrates from Arthrospira platensis. Growing concerns toward unprecedented environmental issues associated with plastic pollution has created a tremendous impetus to develop new biomaterials for the production of bioplastic. Starch-based biopolymers from algae serve as sustainable feedstock for thermoplastic starch production due to their abundant availability and low cost. A. platensis was cultivated in Zarrouk's medium at 32 ± 1°C and exposed to red light with a photoperiod of 12:12 hr light/dark. Growth kinetics studies showed that the maximum specific growth rate (μ_max) obtained was 0.059 day⁻¹ with the doubling time (t_d) of 11.748 days. Subsequently, Zarrouk's medium with different concentrations of sulfur, phosphorus and nitrogen was prepared to establish the nutrient-limiting conditions to enhance the accumulation of starch and total carbohydrates. In this study, the highest starch accumulated was 6.406 ± 0.622 mg L⁻¹ under optimized phosphorus limitation (0.025 g L⁻¹) conditions. Nitrogen limitation (0.250 g L⁻¹) results demonstrated significant influenced (p < 0.05) on total carbohydrates (67.573 ± 2.893 mg L⁻¹) accumulation in A. platensis. The starch accumulation in A. platensis was significantly affected (p < 0.05) by phosphorus limitation (0.0025 g L⁻¹). Subsequently, the optimized phosphorus concentration was coupled with mixotrophic cultivation to further enhance the starch accumulation. The results obtained indicated that, the starch (11.426 ± 0.314 mg L⁻¹) and carbohydrates (43.053 ± 2.986 mg L⁻¹) concentration obtained was significantly high (p < 0.05) under mixotrophic cultivation. Therefore, it shown that nutrient limitation and mixotrophic cultivation are viable strategies to enhance the accumulation of starch and total carbohydrates in A. platensis.     

Bench-scale fermentation of Trichoderma viride on wastewater sludge: Rheology,lytic enzymes and biocontrol activity

Conidiation and lytic enzyme production by Trichoderma viride at different solids concentration of pre-treated municipal wastewater sludge was examined in a 15-L fermenter. The maximum conidia concentration (5.94 × 10⁷ CFU mL⁻¹ at 96 h) was obtained at 30 g L⁻¹ suspended solids. The maximum lytic enzyme activities were achieved around 12–30 h of fermentation. Bioassay against a fungal phytopathogen, Fusarium sp. showed maximum activity in the sample drawn around 96 h of fermentation at 30 g L⁻¹ suspended solids concentration. Entomotoxicity against spruce budworm larvae showed maximum value ≈17290 SBU μL⁻¹ at 30 g L⁻¹ suspended solids concentration at the end of fermentation (96 h). Plant bioassay showed dual action of T. viride, i.e., disease prevention and growth promotion. The rheological analyses of fermentation sludges showed the pseudoplastic behaviour. In order to maintain required dissolved oxygen concentration ≥30%, the agitation and aeration requirements significantly increased at 35 g L⁻¹ compared to 30 and 25 g L⁻¹. The oxygen uptake rate and volumetric oxygen mass transfer coefficient, k_La at 35 g L⁻¹ did not increase in comparison to 30 g L⁻¹ due to rheological complexity of the broth during fermentation. Thus, the successful fermentation operation of the biocontrol fungus T. viride is a rational indication of its potential for mass-scale production for agriculture and forest sector as a biocontrol agent.     

High expression of Trigonopsis variabilis -amino acid oxidase in Pichia pastoris

To explore a new approach of high expression of -amino acid oxidase (DAAO) in Pichia pastoris, a gene encoding DAAO from Trigonopsis variabilis (TvDAAO gene) deleted intron was prepared by PCR amplification and cloned into the intracellular expression vector pPIC3.5K. The expression plasmid pPIC3.5K-DAAO linearized by SalI was transformed into Pichia pastoris strain GS115 (his⁻mut⁺). By means of MM and MD plates and PCR, the recombinant P. pastoris strains (his⁺mut⁺) were obtained. Activity assay and SDS-PAGE demonstrated that DAAO was intracellularly expressed in P. pastoris with the induction of methanol. The recombinant strain PD27 with the highest expression of DAAO was screened through activity assay and its high-density fermentation was carried out in a 1-l fermentor. Activity assay and SDS-PAGE demonstrated that DAAO was intracellularly expressed in P. pastoris with the induction of methanol. The recombinant cells with high expression of DAAO were screened and the high-density fermentation was carried out in a 1-l fermentor. Interestingly, the DAAO expression level reached up to 473 U/g dry cell weight in fermentation yield. Finally, 1-hexanol was used to break recombinant cells and the specific activity of DAAO was 1.46 U/mg protein in crude extraction.     

An efficient method for separation of surfactin from Bacillus amyloliquefaciens fmb50 broth by flocculation

An efficient method for removing microbial cells and macromolecular impurities and purification of surfaction from fermentation broth produced by Bacillus amyloliquefaciens fmb50 was carried out in this study. Among three inorganic flocculants and a macromolecular flocculants, the combination use of CaCl₂ and Na₂HPO₄ was the most effective separation process. Addition of 50% ethanol into fermentation broth could not only disrupt the surfactin micells, but also promote the permeating of surfactin in filtration. The flocculation condition was optimized by an L₉ (3⁴) orthogonal design. The light transmittance, surfactin recovery rate, protein removal rate and filtration flux could reach to 96.3%, 95.31%, 56.59% and 3204.41 L m⁻² h⁻¹ respectively, the surfactin purity reached to 79.5% and the residual protein was 8.1% in separated product under the optimal flocculation condition (flocculants dosage 0.5%, pH 5.0, and temperature 35 °C). Validation test also demonstrated stable results under the optimal conditions. Due to higher efficiency, lower cost and scale-up more easily of flocculation and filtration processes, it is feasible to separate surfactin from fermentation broth.     

Non-carbon loss long-term continuous lactic acid production from mixed sugars using thermophilic Enterococcus faecium QU 50

In this study, a non-sterile (open) continuous fermentation (OCF) process with no-carbon loss was developed to improve lactic acid (LA) productivity and operational stability from the co-utilization of lignocellulose-derived sugars by thermophilic Enterococcus faecium QU 50. The effects of different sugar mixtures on LA production were firstly investigated in conventional OCF at 50°C, pH 6.5 and a dilution rate of 0.20 hr⁻¹. The xylose consumption ratio was greatly lower than that of glucose in fermentations with glucose/xylose mixtures, indicating apparent carbon catabolite repression (CCR). However, CCR could be efficiently eliminated by feeding solutions containing the cellobiose/xylose mixture. In OCF at a dilution rate ca. 0.10 hr⁻¹, strain QU 50 produced 42.6 g L⁻¹ of l -LA with a yield of 0.912 g g⁻¹-consumed sugars, LA yield of 0.655 g g⁻¹ based on mixed sugar-loaded, and a productivity of 4.31 g L⁻¹ hr⁻¹ from simulated energy cane hydrolyzate. In OCF with high cell density by cell recycling, simultaneous and complete co-utilization of sugars was achieved with stable LA production at 60.1 ± 3.25 g L⁻¹ with LA yield of 0.944 g g⁻¹-consumed sugar and LA productivity of 6.49 ± 0.357 g L⁻¹ hr⁻¹. Besides this, a dramatic increase in LA yield of 0.927 g g⁻¹ based on mixed sugar-loaded with prolonged operational stability for at least 500 hr (>20 days) was established. This robust system demonstrates an initial green step with a no-carbon loss under energy-saving toward the feasibility of sustainable LA production from lignocellulosic sugars.