High solid fed‐batch butanol fermentation with simultaneous product recovery: Part II—process integration

In these studies, liquid hot water (LHW) pretreated and enzymatically hydrolyzed Sweet Sorghum Bagasse (SSB) hydrolyzates were fermented in a fed‐batch reactor. As reported in the preceding paper, the culture was not able to ferment the hydrolyzate I in a batch process due to presence of high level of toxic chemicals, in particular acetic acid released from SSB during the hydrolytic process. To be able to ferment the hydrolyzate I obtained from 250 g L^?1 SSB hydrolysis, a fed‐batch reactor with in situ butanol recovery was devised. The process was started with the hydrolyzate II and when good cell growth and vigorous fermentation were observed, the hydrolyzate I was slowly fed to the reactor. In this manner the culture was able to ferment all the sugars present in both the hydrolyzates to acetone butanol ethanol (ABE). In a control batch reactor in which ABE was produced from glucose, ABE productivity and yield of 0.42 g L^?1 h^?1 and 0.36 were obtained, respectively. In the fed‐batch reactor fed with SSB hydrolyzates, these productivity and yield values were 0.44 g L^?1 h^?1 and 0.45, respectively. ABE yield in the integrated system was high due to utilization of acetic acid to convert to ABE. In summary we were able to utilize both the hydrolyzates obtained from LHW pretreated and enzymatically hydrolyzed SSB (250 g L^?1) and convert them to ABE. Complete fermentation was possible due to simultaneous recovery of ABE by vacuum. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:967–972, 2018     

Lactic acid production by Lactobacillus sp. RKY2 in a cell-recycle continuous fermentation using lignocellulosic hydrolyzates as inexpensive raw materials

Continuous lactic acid fermentations were conducted using lignocellulosic hydrolyzates and corn steep liquor as inexpensive raw materials. Lactic acid concentrations decreased with increases in the dilution rate, whereas the residual substrate concentrations increased. However, lactic acid yields were maintained at more than 0.90 g g⁻¹ over all cases experimented. The cell-recycle cultivation system exerted positive effects on fermentation efficiency, including volumetric productivity, which is attributable to the retention of cells in the bioreactor. The cell-recycle continuous fermentation of lignocellulosic hydrolyzates yielded a lactic acid productivity of 6.7 g l⁻¹ h⁻¹ for a dilution rate of 0.16 h⁻¹ using 30 g l⁻¹ of corn steep liquor and 1.5 g l⁻¹ of yeast extract as nutrients. The productivity (6.7 g l⁻¹ h⁻¹) acquired by the cell-recycle continuous fermentation of lignocellulosic hydrolyzates was 1.6 times higher than the lactic acid productivity yielded in the continuous fermentation without cell-recycle system.     

Isolation, purification and characterization of antioxidant peptidic fractions from a bovine liver sarcoplasmic protein thermolysin hydrolyzate

Sarcoplasmic proteins isolated from bovine livers were hydrolyzed using the enzyme thermolysin at 37 ?C for 2 h. The hydrolyzates were filtered through molecular weight cut off membranes (MWCO) and filtrates were obtained. The water activity (a_w) of unhydrolysed sarcoplasmic protein, full hydrolyzates, 10-kDa and 3-kDa filtrates were below the limit necessary for microbial growth. The antioxidant activities of both filtrates and fractions were assessed using the 2,2-diphenyl-1-picrylhydrazyl (DPPH) radical scavenging activity assay, the ferric ion reducing antioxidant power (FRAP) assay and the Fe²⁺ chelating ability assay. RP-HPLC was used for purification of the full hydrolyzates, the 10-kDa and the 3-kDa filtrates. The peptidic content of the full hydrolyzates, the 10-kDa and the 3-kDa filtrates were assessed using the Dumas method and peptide contents of each fraction were characterized using electrospray quadrupole time-of-flight (ESI-Q-TOF) mass spectrometry with the resultant spectrum analysed using the software programmes Protein Lynx Global Server 2.4. and TurboSEQUEST. Similarities between the amino acid composition of characterized peptides from each fraction and previously reported antioxidant peptides were found. This study demonstrates that meat by-product such as liver can be utilised as raw material for the generation of bioactive peptides with demonstrated antioxidant activities in vitro using the enzyme thermolysin. It is significant as it presents a potential opportunity for meat processors to use their waste streams for the generation of bioactive peptides for potential functional food use.     

Amino acid and peptide ratio in protein hydrolysates for parenteral feeding

Using the method of amino acid analysis and routine methods of protein biochemistry, the ratio of amino acids and peptides in acid and enzyme protein hydrolyzates was determined. Depending on the production procedure, the hydrolyzates under study contained various amounts of free amino acids and peptides in which the number of amino acid residues varied from 2 to 7. Additional hydrolysis of these preparations by leucine aminopeptidase led to a decrease in the peptide content and to an increase in the amino acid content. This may have a beneficial effect on the quality of protein hydrolyzates.     

Potential of biotechnological conversion of lignocellulose hydrolyzates by Pseudomonas putida KT2440 as a model organism for a bio‐based economy

Lignocellulose‐derived hydrolyzates typically display a high degree of variation depending on applied biomass source material as well as process conditions. Consequently, this typically results in variable composition such as different sugar concentrations as well as degree and the presence of inhibitors formed during hydrolysis. These key obstacles commonly limit its efficient use as a carbon source for biotechnological conversion. The gram‐negative soil bacterium Pseudomonas putida KT2440 is a promising candidate for a future lignocellulose‐based biotechnology process due to its robustness and versatile metabolism. Recently, P. putida KT2440_xylAB which was able to metabolize the hemicellulose (HC) sugars, xylose and arabinose, was developed and characterized. Building on this, the intent of the study was to evaluate different lignocellulose hydrolyzates as platform substrates for P. putida KT2440 as a model organism for a bio‐based economy. Firstly, hydrolyzates of different origins were evaluated as potential carbon sources by cultivation experiments and determination of cell growth and sugar consumption. Secondly, the content of major toxic substances in cellulose and HC hydrolyzates was determined and their inhibitory effect on bacterial growth was characterized. Thirdly, fed‐batch bioreactor cultivations with hydrolyzate as the carbon source were characterized and a diauxic‐like growth behavior with regard to different sugars was revealed. In this context, a feeding strategy to overcome the diauxic‐like growth behavior preventing accumulation of sugars is proposed and presented. Results obtained in this study represent a first step and proof‐of‐concept toward establishing lignocellulose hydrolyzates as platform substrates for a bio‐based economy.     

Share of carbohydrates in the humus substances composition

The effect of different concentrations of hydrochloric acid on the qualitative an quantitative content of carbohydrates in humus fraction hydrolyzates was investigated. Three humic acid preparations were subjected to the usual procedure for obtaining fractions of humic and hymatomelanic acids. The carbohydrate content of the hydrolyzates was determined after their Chromatographic separation on Whatman 1, using the Partridge system and detection with acid anilin phtalate. The results showed that the qualitative carbohydrate content in the hydrolyzates of most humus fractions of samples used was identical. With increasing acid concentrations the amount of hydrolyzable carbohydrates usually increased, the total amount of carbohydrate in the hydrolyzate not exceeding 4% . The difference in the carbohydrate content as between hydrolysis with 0-9N and 5-3N HC1 was sometimes fourfold. A higher content of hexoses than of pentoses was generally found.     

Glycine Serine Interconversion in the Rooster

Serine was isolated by the column chromatography from the hydrolyzates of proteins of the serum, the liver and the pectoral muscle which were obtained from the roosters fed a diet containing 2-¹⁴C glycine for 16–17 days. The carbon chain of serine was cut off by treating with sodium periodate. The specific activity of each carbon (as barium carbonate) was estimated. Carboxyl carbon had little radioactivity. The specific activity of hydroxymethyl carbon was 10–19% of that of methylen carbon. Glycine isolated from the same hydrolyzates was degraded by ninhydrin oxidation. Formaldehyde produced from 2-C was oxidized to carbon dioxide by treating with mercuric chloride. Carboxyl carbon had little radioactivity. The specific activities of 2-C of glycine and 2-C of serine in the same tissue protein were compared. The ratio of serine 2-C/glycine 2-C was between 0.7 – 1.5. These results seem to indicate that glycine directly converts to serine in the rooster. The quantitative significance of the pathways of glycine (serine) biosynthesis is discussed.     

Detoxification requirements for bioconversion of softwood dilute acid hydrolyzates to succinic acid

In this work an Escherichia coli metabolically engineered to ferment lignocellulosic biomass sugars to succinic acid was tested for growth and fermentation of detoxified softwood dilute sulfuric acid hydrolyzates, and the minimum detoxification requirements were investigated with activated carbon and/or overliming treatments. Detoxified hydrolyzates supported fast growth and complete fermentation of all hydrolyzate sugars to succinate at yields comparable to pure sugar, while untreated hydrolyzates were unable to support either growth or fermentation. Activated carbon treatment was able to remove significantly more HMF and phenolics than overliming. However, in some cases, overliming treatment was capable of generating a fermentable hydrolyzate where activated carbon treatment was not. The implications of this are that in addition to the known organic inhibitors, the changes in the inorganic content and/or composition due to overliming are significant to the hydrolyzate toxicity. It was also found that any HMF remaining after detoxification was completely metabolized during aerobic cell growth on the hydrolyzates that were capable of supporting growth.     

Quantitative analysis of sugars in wood hydrolyzates with H NMR during the autohydrolysis of hardwoods

The focus of this work was to determine the utility of ¹H NMR spectroscopy in the quantification of sugars resulting from the solubilization of hemicelluloses during the autohydrolysis of hardwoods and the use of this technique to evaluate the kinetics of this process over a range of temperatures and times. Yields of residual xylan, xylooligomers, xylose, glucose, and the degraded products of sugars, i.e., furfural and HMF (5-hydroxymethyl furfural), were determined. The monosaccharide and oligomer contents were quantified with a recently developed high resolution ¹H NMR spectroscopic analysis. This method provided precise measurement of the residual xylan and cellulose remaining in the extracted wood samples and xylose and glucose in the hydrolyzates. NMR was found to exhibit good repeatability and provided carbohydrate compositional results comparable to published methods for sugar maple and aspen woods.     

Acetaldehyde stimulation of the growth of Saccharomyces cerevisiae in the presence of inhibitors found inlignocellulose-to-ethanol fermentations

The addition of small quantities of acetaldehyde to fermentations containing inhibitory concentrations of furfural, acetate and other compounds typically present in lignocellulosic hydrolyzates significantly reduced the lag phase of yeast growth and stimulated ethanol production. Similar effects were observed when acetaldehyde (0.06 g l⁻¹) was added to fermentations of a birch wood hydrolyzate produced by steam/acid pretreatment. Acetaldehyde addition appears to have potential as a low-cost alternative (or adjunct) to current procedures for medium detoxification in lignocellulose-to-ethanol fermentations, particularly those in which high inhibitor concentrations are generated through recycling of the culture broth. Journal of Industrial Microbiology & Biotechnology (2000) 25, 104–108. Received 18 March 2000/ Accepted in revised form 02 June 2000     

Enzymatic Synthesis of α-Linked Galactooligosaccharides Using the Reverse Reaction of a Cell-bound α-Galactosidase from Candida guilliermondii H-404

α-Linked galactooligosaccharides (α-GOS A from galactose, and α-GOS B from lactose hydrolyzates) were synthesized using the reverse reaction of α-galactosidase from Candida guilliermondii H-404. The α-GOS A and B were isolated and their structures were identified by methylation analysis. The main product of the disaccharides in α-GOS A and α-GOS B was the (1, 6)-isomer. The remaining disaccharides consisted of (1, 3)-, (1, 2)-, and (1, 1)-isomers. Conditions for synthesis of α-GOS B from lactose hydrolyzates were examined. The yield of α-GOS B was approximately 20% when the mixture of heat-treated cells containing a-galactosidase (60U/g galactose) and 85% lactose hydrolyzates was incubated for 90 h at pH 4.5 and 50°C. The α-GOS A and B were available as the donor substrates in transgalactosylation of α-galactosidase in the same manner as melibiose.     

Purification and characterization of a novel anticancer peptide derived from Ruditapes philippinarum

The aim of this study was to purify a novel peptide from Ruditapes philippinarum and investigate its anticancer activities. For the aim, eight proteases were applied for enzymatic hydrolysis. α-Chymotrypsin hydrolyzates, which showed clearly superior cytotoxicity activity on prostate cancer cells, were further purified using a flow filtration system and consecutive chromatographic methods. Finally, a novel anticancer peptide was purified, and the sequence was identified as Ala-Val-Leu-Val-Asp-Lys-Gln-Cys-Pro-Asp at N-terminal. The peptide from R. philippinarum effectively induced apoptosis on prostate, breast and lung cancer cells but not on normal liver cells. This is the first report of an anticancer peptide purified from the hydrolyzates of R. philippinarum.     

2,3-Butanediol production using Klebsiella oxytoca ATCC 8724: Evaluation of biomass derived sugars and fed-batch fermentation process

For this study, 2,3-butanediol (BD) fermentation from pure and biomass-derived sugar were optimized in shake-flask and 5-L bioreactor levels using Klebsiella oxytoca ATCC 8724. The results showed that 70 g/L of single sugar (glucose or xylose) and 90 g/L of mixed-sugar (glucose:xylose = 2:1) were optimum concentrations for efficient 2,3-BD fermentation. At optimum sugar concentrations, 2,3-BD productivities were 1.03, 0.64 and 0.50 gL⁻¹ h⁻¹, and yields were 0.43, 0.36 and 0.35 g/g in glucose, xylose and mixed-sugar medium, respectively. The lack of simultaneous utilization of glucose and xylose led to the lowest productivity in the mixed-sugar medium. Detoxification of biomass hydrolyzates was necessary for efficient 2,3-BD fermentation when sugar concentrations in the medium was 90 g/L or higher, but not with sugar concentrations of 30 g/L or less. A fed-batch fermentation using glucose medium led to an increase 2,3-BD titer to 79.4 g/L and yields 0.47 g/g, while productivity decreased to 0.79 gL⁻¹ h⁻¹. However, the fed-batch process was inefficient using mixed-sugar and biomass hydrolyzates because of poor xylose utilization. These results indicated that appropriate biomass processing technologies must be developed to generate separate glucose and xylose streams to produce high 2,3-BD titer from biomass-derived sugar using a fed-batch process.     

Inactivation of E. coli RNA polymerase by pyridoxal 5'-phosphate: identificationof a low pKa lysine as the modified residue.

The inactivation of E. coli RNA polymerase (3.3 × 10^?7M) by pyridoxal 5′-phosphate (1 × 10^?4M to 5 × 10^?4M) is a first order process with respect to the remaining active enzyme. Studies of the variation of the first order rate constant with the concentration of pyridoxal 5′-phosphate show that the inactivation reaction follows saturation kinetics. The formation of a reversible enzyme-inhibitor intermediate is postulated. Kinetic studies at different pH values indicate that the inactivation rate constant depends on the mole fraction of one conjugate base with pK_a 7.9. The apparent equilibrium constant (association) for the inactivation reaction is independent of the pH and is 1.8 × 10⁴ M^?1. By electrophoretic and chromatographic analysis of enzyme hydrolyzates after pyridoxal 5′-phosphate and NaBH₄ treatment only N-ε-pyridoxyllysine was found. It is postulated that a lysine ε-amino group with a low pK_a is critical for the activity of the enzyme.     

Identification of 3-hydroxy-6-methyl-2H-pyran-2-one from pyrolysis of phosphoric acid-treated cellulosic materials

The hydrogen isotope-effect that occurs in vitro during myo-inositol 1-phosphate synthase-catalyzed conversion of d-[5-³H]glucose 6-phosphate into myo-[2-³H]inositol 1-phosphate has been used to compare the functional role of the nucleotide sugar oxidation-pathway with that of the myo-inositol oxidation-pathway in germinating lily pollen. Results reveal a significant difference between the ³H/¹⁴C ratios of glucosyl and galactosyluronic residues from pectinase-amyloglucosidase hydrolyzates of the 70 % ethanol-insoluble fraction of d-[5-³H, 1-¹⁴-C]glucose-labeled, germinating lily pollen. This isotope effect at C-5 of d-glucose that occurred during its conversion into d-galactosyluronic residues of pectic substance is not explained by loss of ³H when UDP-d-[5-³H, 1-¹⁴C]glucose is oxidized by UDP-d-glucose dehydrogenase from germinating lily pollen. The evidence obtained from this study favors a functional role for the myo-inositol oxidation pathway during in vivo conversion of glucose into galactosyluronic residues of pectin in germinating lily pollen.     

13C metabolic flux analysis for larger scale cultivation using gas chromatography-combustion-isotope ratio mass spectrometry

¹³C-based metabolic flux analysis (¹³CMFA) is limited to smaller scale experiments due to very high costs of labeled substrates. We measured ¹³C enrichment in proteinogenic amino acid hydrolyzates using gas chromatography-combustion-isotope ratio mass spectrometry (GC-C-IRMS) from a series of parallel batch cultivations of Corynebacterium glutamicum utilizing mixtures of natural glucose and [1-¹³C] glucose, containing 0%, 0.5%, 1%, 2%, and 10% [1-¹³C] glucose. Decreasing the [1-¹³C] glucose content, kinetic isotope effects played an increasing role but could be corrected. From the corrected ¹³C enrichments in vivo fluxes in the central metabolism were determined by numerical optimization. The obtained flux distribution was very similar to those obtained from parallel labeling experiments using conventional high labeling GC-MS method and to published results. The GC-C-IRMS-based method involving low labeling degree of expensive tracer substrate, e.g. 1%, is well suited for larger laboratory and industrial pilot scale fermentations.     

Gas chromatographic assay of iduronic and glucuronic acids as aldonic acid butaneboronates

A gas chromatographic procedure has been developed for the analysis of uronic acids as aldonic acid butaneboronates. With these derivatives, aldoses frequently accompanying uronic acids in polysaccharide hydrolyzates are readily separated and measured. The method has been applied to the assay of iduronic and glucuronic acid released by enzymes associated with various mucopolysaccharidoses.     

Multiple resins for analysis of amino acids and ninhydrin-positive compounds in hydrolyzates and physiological fluids

The newly available spherical cation-exchange resins HP-AN 90 and HP-B 80 are capable of performing various analyses of amino acids and peptides at low backpressures. These multipurpose resins can perform: a 2 or 4 hr simple (approximately 20 amino acids) procedure used with protein hydrolyzates, or a complex (50 or more amino acids) technical procedure (for physiological fluids), or a rapid screening procedure dealing with specific amino acids as they relate to clinical disease or biomedical studies, or the analysis of peptide samples.     

Optimization of Pseudoalteromonas sp. JYBCL 1 culture conditions, medium composition and extracellular β-agarase activity

Extracellular agarase produced by the Pseudoalteromonas strain JYBCL 1 is used in a variety of applications in the biotechnology, pharmaceutical, cosmetic, and food industries. The optimization of culture conditions for agarase-producing microbes and agarase activity is thus an important consideration in many industrial applications. In this study, the optimum medium composition and culture conditions for the JYBCL 1 strain were determined using the ??one factor at a time?? (OFAT) method and a Plackett-Burman design. Optimal cell growth was obtained at a temperature of 25°C and when 10 g/L tryptone was present in the culture medium. Optimal agarase activity occurred at a temperature of 40°C and at pH 6. The presence of carbonyl groups in the extracellular agarase hydrolysis products was verified using FT-IR. LC-MS identified the hydrolyzates as neoagarohexaose, neoagarotetraose, and neoagarobiose. The extracellular agarase produced by the JYBCL 1 strain used in this study was identified as ??-agarase by ¹³C-NMR spectroscopy.     

Acid hydrolysis of sunflower seed husks for production of single cell protein

Summary Sunflower seed husks were chosen as a typical lignocellulosic waste product of low value. This model substrate was hydrolyzed with sulphuric acid at 120°C. The hydrolysis was carried out in two steps: hydrolysis of the pentosan fraction and subsequent hydrolysis of the cellulose fraction. The pentosan fraction was nearly quantitatively hydrolyzed. For the cellulose hydrolysis the yield was 79% of the theoretical yield. The hydrolyzates were neutralized to pH 5 with solid calcium hydroxide and used for preparation of growth media forCandida yeasts andPaecilomyces variotii. For the pentosan hydrolyzates the yields of yeast biomass were 35–36 g per 100 g available reducing sugars (supplied to the medium). In cellulose hydrolyzates the corresponding yields were 45–48 g withCandida utilis andC. tropicalis and about 30 g withC. pseudotropicalis. P. variotii was noticeably superior to the yeasts. In pentosan hydrolyzates it produced 63 g dry mycelium from 100 g reducing sugars supplied; in cellulose hydrolyzates, 94 g. This suggests that it must be an effective utilizer of a wide range of compounds, for example, organic acids in the medium.