Designing a cocktail containing redox enzymes to improve hemicellulosic hydrolysate fermentability by microorganisms.

Bioproducts production using monomeric sugars derived from lignocellulosic biomass presents several challenges, such as to require a physicochemical pretreatment to improve its conversion yields. Hydrothermal lignocellulose pretreatment has several advantages and results in solid and liquid streams. The former is called hemicellulosic hydrolysate (HH), which contains inhibitory phenolic compounds and sugar degradation products that hinder microbial fermentation products from pentose sugars. Here, we developed and applied a novel enzyme process to detoxify HH. Initially, the design of experiments with different redox activities enzymes was carried out. The enzyme mixture containing the peroxidase (from Armoracia rusticana) together with superoxide dismutase (from Coptotermes gestroi) are the most effective to detoxify HH derived from sugarcane bagasse. Butanol fermentation by the bacteria Clostridium saccharoperbutylacetonicum and ethanol production by the yeast Scheffersomyces stipitis increased by 24.0× and 2.4×, respectively, relative to the untreated hemicellulosic hydrolysates. Detoxified HH was analyzed by chromatographic and spectrometric methods elucidating the mechanisms of phenolic compound modifications by enzymatic treatment. The enzyme mixture degraded and reduced the hydroxyphenyl- and feruloyl-derived units and polymerized the lignin fragments. This strategy uses biocatalysts under environmentally friendly conditions and could be applied in the fuel, food, and chemical industries.

A robotic platform to screen aqueous two-phase systems for overcoming inhibition in enzymatic reactions.

Aqueous two-phase systems (ATPS) can be applied to enzymatic reactions that are affected by product inhibition. In the biorefinery context, sugars inhibit the cellulolytic enzymes in charge of converting the biomass. Here, we present a strategy to select an ATPS (formed by polymer and salt) that can separate sugar and enzymes. This automated and miniaturized method is able to determine phase diagrams and partition coefficients of solutes in these. Tailored approaches to quantify the solutes are presented, taking into account the limitations of techniques that can be applied with ATPS due to the interference of phase forming components with the analytics. The developed high-throughput (HT) platform identifies suitable phase forming components and the tie line of operation. This fast methodology proposes to screen up to six different polymer-salt systems in eight days and supplies the results to understand the influence of sugar and protein concentrations on their partition coefficients.

Techno-economic analysis of the industrial production of a low-cost enzyme using E. coli: the case of recombinant ß-glucosidase.

BACKGROUND: The enzymatic conversion of lignocellulosic biomass into fermentable sugars is a promising approach for producing renewable fuels and chemicals. However, the cost and efficiency of the fungal enzyme cocktails that are normally employed in these processes remain a significant bottleneck. A potential route to increase hydrolysis yields and thereby reduce the hydrolysis costs would be to supplement the fungal enzymes with their lacking enzymatic activities, such as ß-glucosidase. In this context, it is not clear from the literature whether recombinant E. coli could be a cost-effective platform for the production of some of these low-value enzymes, especially in the case of on-site production. Here, we present a conceptual design and techno-economic evaluation of the production of a low-cost industrial enzyme using recombinant E. coli. RESULTS: In a simulated baseline scenario for ß-glucosidase demand in a hypothetical second-generation ethanol (2G) plant in Brazil, we found that the production cost (316 US$/kg) was higher than what is commonly assumed in the literature for fungal enzymes, owing especially to the facility-dependent costs (45%) and to consumables (23%) and raw materials (25%). Sensitivity analyses of process scale, inoculation volume, and volumetric productivity indicated that optimized conditions may promote a dramatic reduction in enzyme cost and also revealed the most relevant factors affecting production costs. CONCLUSIONS: Despite the considerable technical and economic uncertainties that surround 2G ethanol and the large-scale production of low-cost recombinant enzymes, this work sheds light on some relevant questions and supports future studies in this field. In particular, we conclude that process optimization, on many fronts, may strongly reduce the costs of E. coli recombinant enzymes, in the context of tailor-made enzymatic cocktails for 2G ethanol production.

Improvement on sugar cane bagasse hydrolysis using enzymatic mixture designed cocktail.

The aim of this work was to study cocktail supplementation for sugar cane bagasse hydrolysis, where the enzymes were provided from both commercial source and microorganism cultivation (Trichoderma reesei and genetically modified Escherichia coli), followed by purification. Experimental simplex lattice mixture design was performed to optimize the enzymatic proportion. The response was evaluated through hydrolysis microassays validated here. The optimized enzyme mixture, comprised of T. reesei fraction (80%), endoglucanase (10%) and ß-glucosidase (10%), converted, theoretically, 72% of cellulose present in hydrothermally pretreated bagasse, whereas commercial Celluclast 1.5L converts 49.11%±0.49. Thus, a rational enzyme mixture designed by using synergism concept and statistical analysis was capable of improving biomass saccharification.

Transcriptome profile of Trichoderma harzianum IOC-3844 induced by sugarcane bagasse.

Profiling the transcriptome that underlies biomass degradation by the fungus Trichoderma harzianum allows the identification of gene sequences with potential application in enzymatic hydrolysis processing. In the present study, the transcriptome of T. harzianum IOC-3844 was analyzed using RNA-seq technology. The sequencing generated 14.7 Gbp for downstream analyses. De novo assembly resulted in 32,396 contigs, which were submitted for identification and classified according to their identities. This analysis allowed us to define a principal set of T. harzianum genes that are involved in the degradation of cellulose and hemicellulose and the accessory genes that are involved in the depolymerization of biomass. An additional analysis of expression levels identified a set of carbohydrate-active enzymes that are upregulated under different conditions. The present study provides valuable information for future studies on biomass degradation and contributes to a better understanding of the role of the genes that are involved in this process.

Sodium citrate and potassium phosphate as alternative adsorption buffers in hydrophobic and aromatic thiophilic chromatographic purification of plasmid DNA from neutralized lysate.

The number of studies on gene therapy using plasmid vectors (pDNA) has increased in recent years. As a result, the demand for preparations of pDNA in compliance with recommendations of regulatory agencies (EMEA, FDA) has also increased. Plasmid DNA is often obtained through fermentation of transformed Escherichia coli and purification by a series of unit operations, including chromatography. Hydrophobic interaction chromatography (HIC) and thiophilic aromatic chromatography (TAC), both using ammonium sulfate buffers, are commonly employed with success. This work was aimed at studying the feasibility of utilizing alternative salts in the purification of pDNA from neutralized lysate with phenyl-agarose (HIC) and mercaptopyrimidine-agarose (TAC) adsorbents. Their selectivity toward sc pDNA was evaluated through adsorption studies using 1.5 mol/L sodium citrate and 2.0 mol/L potassium phosphate as adsorption buffers. Chromatography with mercaptopyrimidine-agarose adsorbent and 1.5 mol/L sodium citrate was able to recover 91.1% of the pDNA with over 99.0% removal of gDNA and endotoxin. This represents a potential alternative for the primary recovery of sc pDNA. However, the most promising result was obtained using 2.0 mol/L potassium phosphate buffer and a mercaptopyrimidine-agarose column. In a single chromatographic step, this latter buffer/adsorbent system recovered 68.5% of the pDNA with 98.8% purity in accordance with the recommendations of regulatory agencies with regard to RNA and endotoxin impurity.

Stabilization of naked and condensed plasmid DNA against degradation induced by ultrasounds and high-shear vortices.

Micrometre-sized aggregates of a 6050-bp plasmid obtained by the addition of 1.5-3.0 mM CaCl2 and 20% (v/v) t-butanol or 0.3-1.0% (v/v) APG (aluminium phosphate gel) were subjected to degradation induced by sonication or vortex flows. Dynamic light scattering revealed that the plasmid hydrodynamic radius increases from 116 nm to >1300 nm and approx. 1000 nm, when formulated with CaCl2/t-butanol and APG respectively. CD showed that addition of CaCl2/t-butanol leads to transition in plasmid structure from B-DNA to a psi-DNA negative form, whereas no detectable transitions were observed for APG formulations. The ability of the condensing agents to stabilize supercoiled plasmid isoforms subjected to sonication or turbulent Taylor vortices was assessed by agarose-gel electrophoresis. Although naked plasmid was completely fragmented after 5 s of sonication, condensing agents increased the plasmid stability dramatically [e.g. up to 80% after 30 s with 1.5 mM CaCl2+20% (v/v) t-butanol]. In the case of the vorticular flow system, the extent of degradation correlated well with the shear stress associated with flow of the solutions being processed. Overall, the results from the present study demonstrate that condensing agents such as CaCl2/t-butanol and APG can effectively stabilize plasmids against shear-induced degradation; the extent of protection, however, depends on both the condensing agents and the shear-inducing system used.

Alternatives for the intermediate recovery of plasmid DNA: performance, economic viability and environmental impact.

Robust cGMP manufacturing is required to produce high-quality plasmid DNA (pDNA). Three established techniques, isopropanol and ammonium sulfate (AS) precipitation (PP), tangential flow filtration (TFF) and aqueous two-phase systems (ATPS) with PEG600/AS, were tested as alternatives to recover pDNA from alkaline lysates. Yield and purity data were used to evaluate the economic and environmental impact of each option. Although pDNA yields > or = 90% were always obtained, ATPS delivered the highest HPLC purity (59%), followed by PP (48%) and TFF (18%). However, the ability of ATPS to concentrate pDNA was very poor when compared with PP or TFF. Processes were also implemented by coupling TFF with ATPS or AS-PP. Process simulations indicate that all options require large amounts of water (100-200 tons/kg pDNA) and that the ATPS process uses large amounts of mass separating agents (65 tons/kg pDNA). Estimates indicate that operating costs of the ATPS process are 2.5-fold larger when compared with the PP and TFF processes. The most significant contributions to the costs in the PP, TFF and ATPS processes came from operators (59%), consumables (75%) and raw materials (84%), respectively. The ATPS process presented the highest environmental impact, whereas the impact of the TFF process was negligible.

Selective purification of supercoiled plasmid DNA from clarified cell lysates with a single histidine-agarose chromatography step.

The ability to isolate sc (supercoiled) pDNA (plasmid DNA) isoform should be one of the features of a pDNA purification process, eliminating sample contaminants such as RNA, gDNA (genomic DNA), proteins and endotoxins. A process is described that uses a single histidine-agarose chromatography step to purify sc pDNA from other isoforms and Escherichia coli impurities present in a clarified lysate. The histidine-agarose support combines the mild hydrophobic characteristics of an epoxy spacer arm with a pseudo-affinity histidine ligand. The 6 kb DNA vaccine backbone pVAX1-LacZ was used as a model target. Following loading at high salt [2.3 M (NH4)2SO4], the different species were eluted by a series of reverse salt step gradients (2.0, 1.5 and 0 M (NH4)2SO4). Open circular pDNA and gDNA was eluted at 2.3 M, sc pDNA was isolated as a single peak at 2.0 M and RNA was eluted at 1.5 M (NH4)2SO4 and lower. The underlying mechanism is thought to involve not only hydrophobic interactions between the support and pDNA molecules, but also non-specific biorecognition of nucleic acid bases by the histidine ligand. Control analysis showed that the isolated sc pDNA conforms to specifications in terms of gDNA (3.4 ng/microg of pDNA), endotoxins (0.02 endotoxin unit/microg of pDNA), RNA and proteins (undetectable) and pDNA homogeneity (approximately 100% sc). Furthermore, the transfection efficiency of Chinese-hamster ovary cells (50%) was significantly higher when compared with the efficiency (25%) of a pDNA control. The present study confirms the possibility of using a single histidine-agarose chromatography step to purify sc pDNA from other isoforms and host contaminants present in a clarified E. coli lysate.