Recovery of lactic acid from simultaneous saccharification and fermentation media using anion exchange resins

The physicochemical properties (capacity, kinetics and selectivity) of the ion exchange resins Amberlite IRA900, IRA400, IRA96 and IRA67 were determined to evaluate their comparative suitability for lactic acid recovery. Both the kinetics of lactic acid sorption from aqueous solutions and the equilibrium were assessed using mathematical models, which provided a close interpretation of the experimental results. The best resins (Amberlite IRA96 and IRA67) were employed in further fixed-bed operation using aqueous lactic acid solutions as feed. In this set of experiments, parameters such as capacity, regenerant consumption, percentage of lactic acid recovery and product concentration were measured. Amberlite IRA67, a weak base resin, was selected for lactic acid recovery from SSF (simultaneous saccharification and fermentation) broths. Owing to the presence of nutrients and ions other than lactate, a slightly decreased capacity was determined when using SSF media instead aqueous lactic acid solutions, but quantitative lactic acid recoveries at constant capacities were obtained in four sequential load/regeneration cycles.     

Selective recovery of acidic and lactonic sophorolipids from culture broths towards the improvement of their therapeutic potential

Sophorolipids (SLs) were produced by Starmerella bombicola. The separation and purification of SLs are a complex process, since they are produced as a mixture of compounds with few structural differences. Solvent extraction is commonly used in downstream processing. In this work, an environmental friendly approach was developed for SLs recovery and purification, based on neutral polymeric sorbents, Amberlite XAD16N^TM, XAD18^TM, and XAD1600N^TM. In batch microassays, key parameters of sorption/desorption process (e.g., contact time, temperature, sorbents, and SLs concentrations) were optimized for separation of acidic and lactonic SLs. Sorption equilibrium was reached after 2–3 h, for all the sorbents tested. Among them XAD1600N^TM showed a higher sorption capacity (q _max 230 mg g^?1), a higher removal (≈100 %) of acidic and lactonic SLs [1 and 2.5 % (w/v)], and the best selectivity. Methanol, ethanol, and acetone were suitable for SLs elution. A selective desorption of SLs was attained with acetonitrile aqueous solutions (v/v): (1) 25 % led to 88.3 % of acidic SLs and (2) 55 % followed by methanol solution (100 %) led to 93.2 % of purified lactonic SLs. This achievement was particularly important regarding SLs potential therapeutic applications, since acidic and lactonic SLs show different biologic activities. In fact, acid SLs show higher virucidal and pro-inflammatory cytokine activity, while lactonic SLs show stronger spermicidal and anti-cancer activity.     

Simultaneous determination of volatile and non-volatile acidic fermentation products of anaerobes by capillary gas chromatography

A method previously used for the analysis of organic acids in silage has been applied to the detection and quantification of acidic fermentation products (C₁ to C₆ volatile fatty acids, lactic and succinic acid) of rumen bacteria and anaerobic fungi grown in pure culture. The acids were converted to tertiary butyldimethylsilyl derivatives prior to separation on a 30 m DB1 capillary gas chromatographic column. The quantitative recoveries of formic and succinic acids were found to be comparable to the recoveries of other acids reported in the original study. The quantitative recovery of lactic acid was found to be dependent on storage of the samples at ambient temperature for at least 24 h following derivatization. The simultaneous determination of a wide range of volatile and non-volatile acidic products is an important feature of this method.     

Utilization of corn silage juice by Klyuveromyces marxianus

Corn silage juice was found to be a favorable substrate for production of fodder yeasts. Kluyveromyces marxianus NRRL Y-610 yielded significantly more cell dry weight than other cultures examined. In shake-flask experiments, the yeast produced over 13 g of cell dry weight per liter of corn silage juice and completely consumed the organic pollutants (lactic acid, acetic acid, and ethanol). The yeast settled rapidly and had a yeast volume index of 21 ml/g. The results indicate that K. marxianus NRRL Y-610 could be used to efficiently remove lactic acid and other organic compounds from corn silage juice with the concomitant production of fodder yeast.     

Effects of organic phase, fermentation media, and operating conditions on lactic Acid extraction

Lactic acid has extensive uses in the food, pharmaceutical, cosmetic and chemical industry. Lately, its use in producing biodegradable polymeric materials (polylactate) makes the production of lactic acid from fermentation broths very important. The major part of the production cost accounts for the cost of separation from very dilute reaction media where productivity is low as a result of the inhibitory nature of lactic acid. The current method of extraction/separation is both expensive and unsustainable. Therefore, there is great scope for development of alternative technology that will offer efficiency, economic, and environmental benefits. One of the promising technologies for recovery of lactic acid from fermentation broth is reactive liquid-liquid extraction. In this paper the extraction and recovery of lactic acid based on reactive processes is examined and the performance of a hydrophobic microporous hollow-fiber membrane module (HFMM) is evaluated. First, equilibrium experiments were conducted using organic solutions consisting of Aliquat 336/trioctylamine (as a carrier) and tri-butyl phosphate (TBP)/sunflower oil (as a solvent) The values of the distribution coefficient were obtained as a function of feed pH, composition of the organic phase (ratio of carrier to solvent), and temperature (range 8-40 degrees C). The optimum extraction was obtained with the organic phase consisting of a mixture of 15 wt % tri-octylamine (TOA) and 15% Aliquat 336 and 70% solvent. The organic phase with TBP performed best but is less suitable because of its damaging properties (toxicity and environmental impact) and cost. Sunflower oil, which performed moderately, can be regarded as a better option as it has many desirable characteristics (nontoxic, environment- and operator-friendly) and it costs much less. The percentage extraction was approximately 33% at pH 6 and at room temperature (can be enhanced by operating at higher temperatures) at a feed flow rate of 15-20 L/h. These results suggest that the hollow-fiber membrane process yields good percentage extraction at the fermentation conditions and its in situ application could improve the process productivity by suppressing the inhibitory effect of lactic acid.     

Applying slow-release biocatalysis to the asymmetric reduction of ethyl 4-chloroacetoacetate

Amberlite XAD 2 resin enhanced the asymmetric reduction of ethyl 4-chloroacetoacetate (ECA) to S-4-chloro-3-hydroxybutyric acid ethyl ester as catalyzed by Saccharomyces cerevisiae. The absorbed ECA was released slowly to the solution during the reaction so that the substrate inhibition and the spontaneous chemical hydrolysis of ECA were considerably lessened. With 75 g resin l^–1 and ECA at 74 mM, the reaction yield and the product's optical purity increased from 75% to 84% and from 88% to 93%, respectively.     

Extraction of organic acids from kiwifruit juice using a supported liquid membrane process

In order to extract or remove organic acids from kiwifruit juice, we evaluated their separation and transport rates through supported liquid membranes (SLMs). The liquid membrane consisted of an organic solution composed of a carrier (Aliquat 336/Alamine 336) and a linear alcohol (oleyl alcohol) and was loaded on a microporous polypropylene support (commercial grade Celgard 2500/2400). These SLMs were evaluated (i) in a batch cell to determine the permeability and (ii) in a continuous spiral membrane module to study the effects of various process parameters – flow of feed and strip solutions, membrane composition, recycling mode of operation and kiwifruit juice at natural pH. It was observed that there exists an optimum for each system: pH?2.5–?3.0 for Alamine 336/oleyl alcohol and pH?4.5 for Aliquat 336/oleyl alcohol. At this pH?the flux rates of citric acid and malic acid was greater (6–8 times) than that of quinic acid. The flux rates decreased (greatly for citric acid) with the flow rate of feed and strip solutions and increased (considerably for citric acid) with the SLM composition . The recycling of feed and strip solutions significantly improved the removal efficiency. The SLM system retained its performance over a period of a few days. The SLM process allowed extraction of the above three organic acids (ascorbic acid was removed in trace amounts) from kiwifruit juice at a rate of a few percent (5%) in a single-pass processing.     

Lactate from cultures of Lactobacillus casei recovered in a fluidized bed column using ion exchange resin

Summary Lactic acid produced by continuous culture of L.casei in an upflow packed bed reactor, was recovered with Amberlite IRA 400 in a fluidized bed column. Bed expansions of 1.25 and 2.25 were applied. Reutilization did not alter the capability of net recovery of 0.048 ± 0.01 g lactic acid/g resin. When 2200 cm/h of ascensional velocity was used, (bed expansion of 2.25), the resin adsorbed 39.3% of the initial lactic acid and 63.5% was eluted. This resin supported the highest exchange capacity of 0.126 g lactic acid/g resin. Applying high flow rates, the process has potential industrial applications due to the short time employed.     

Ion exchange separation of ascorbic acid and isolation of the 2,4-dinitrophenylosazone

A method has been developed for the separation of small amounts of ascorbic acid from the neutral and basic constituents of rat urine by adsorption on Amberlite IR-4B anion-exchange resin and subsequent elution with hydrochloric acid. The procedure separates the ascorbic acid from the nonacidic substances present, with an over-all recovery of 85–90% of the ascorbic acid originally present. A detailed study of optimum conditions for the formation of the ascorbic acid 2,4-dinitrophenylosazone was made, resulting in a method which permits osazone formation to be complete in 3 hr. The ascorbic acid 2,4-dinitrophenylosazone was shown to be chemically and radioactively pure by accepted standards, including data for the near ultraviolet, visible, and infrared absorption spectra.     

Laboratory evaluation of ensiled mixtures of alkali-treated cattle excreta and whole-crop maize

Faeces or manure (faeces + urine + straw bedding) from beef cattle given maize silage diets were ensiled with whole-crop maize (27% dry matter), after treatment with NaOH at 0, 7.5 or 15 g per 100 g excreta DM, so that excreta DM comprised 25, 50 or 100% of the total DM, in a factorial design. A control treatment consisted of maize forage ensiled alone. The ensiled products were analysed for the content of fermentation acids, pH, nitrogenous compounds, structural carbohydrates, starch, water-soluble carbohydrates, ash, sodium and digestibility in vitro. Mixtures which contained 25% excreta DM were well preserved with relatively low values for pH, butyric acid and ammonia-N, and a high proportion of fermentation acids as lactic acid. Mixtures which contained 50% excreta DM were generally poorly preserved. Addition of NaOH to excreta prior to ensiling was reflected in a decrease in the content of neutral detergent fibre and increased digestibility of organic matter in vitro in the ensiled products. Mixtures of 25% excreta treated with 15 g NaOH/100 g excreta DM gave values for digestibility in vitro similar to that of the maize ensiled alone.     

Recovery of native protein from potato root water by expanded bed adsorption with amberlite XAD7HP

Potato root water (PRW) contains ～1.5% protein. In this study, expanded bed adsorption (EBA) chromatography with Amberlite XAD7HP resin adsorbent was used to isolate native protein from crude PRW. The optimal pH and ionic strength for potato protein binding onto Amberlite XAD7HP were 5.0 and 20 mmol/L. The EBA-refined proteins were dried by vacuum freeze drying and spray drying at varying outlet temperatures. Results indicated that low temperature spray drying was the most cost effective method with respect to retaining protease inhibitor activities. The dried protein concentrates appeared bright yellow or dark reddish brown, with a total glycoalkaloid content of ～170 μg/g. The protease inhibitor activity was ～400 mg/g and 11 ～ 12 mg/g for trypsin inhibition and chymotrypsin inhibition, respectively. The results presented here suggest that EBA using Amberlite XAD7HP as the adsorbent is a feasible strategy for the direct adsorption of native protein from crude PRW.     

吸附层析分离麻黄生物碱的过程优化

研究了用吸附层析取代现有的二甲苯萃取麻黄生物碱的工艺,重点考察了洗脱剂和操作条件对产品纯度和回收率的影响,发现在树脂吸附后的洗脱中,0．08M草酸的洗脱率最高,达99．3％,纯化倍数大于20;在操作条件中,进料量、pH和料液在层析柱中的停留时间影响最大：进料量增大导致纯度和收率的下降,树脂的动态吸附容量为27．5mg／mL树脂;停留时间在20rain时纯度较高,而洗脱率随停留时间减少却略有下降;pH=10时吸附性能较好。     

Synthesis of 3-tert-butylcatechol by an engineered monooxygenase

Recombinant Escherichia coli JM101 was used for the in vivo biocatalytic synthesis of 3-tert-butyl- catechol. The bacterial strain synthesized the laboratory-evolved variant HbpA(T2) of 2-hydroxybiphenyl 3-monooxygenase (HbpA, EC 1.14.13.44) from Pseudomonas azelaica HBP1. The mutant enzyme HbpA(T2) is able to hydroxylate 2-tert-butylphenol to the corresponding catechol, a reaction that is not catalyzed by the wild-type enzyme. The biotransformation was performed in a 3-L bioreactor for 24 h. To mitigate the toxicity of the 2-tert-butylphenol starting material, we applied a limited substrate feed. Continuous in situ product removal with the hydrophobic resin Amberlite XAD-4 was used to separate the product from culture broth. In addition, binding to the resin stabilized the product, which was important because 3-tert-butylcatechol is very labile in aqueous solution. The productivity of the process was 63 mg L(-1) h(-1) so that after 24 h, 3.0 g of 3-tert-butylcatechol were isolated. Down-stream processing consisted of two steps. First, bound 2-tert-butylphenol and 3-tert-butylcatechol were eluted from Amberlite XAD-4 with methanol. Second, the two compounds were separated over neutral aluminum oxide, which selectively binds the produced catechol but not the phenol substrate. The final purity of 3-tert-butylcatechol was greater than 98%.     

Metabolic profile of ginkgo kernel juice fermented with lactic aicd bacteria: A potential way to degrade ginkgolic acids and enrich terpene lactones and phenolics

In this paper, the influence of lactic acid fermentation on the metabolic profile of ginkgo kernel juice was studied. For this purpose, three lactic acid bacteria (LAB), Lactobacillus acidophilus, Lactobacillus plantarum and Lactobacillus casei, were selected. The results showed that all the lactobacilli grew well in ginkgo kernel juice with viable cell counts exceeding 8.0 Log CFU/mL. The organic acid contents underwent dynamic changes, and the lactic acid production reached more than 3 g/L. The consumption of sugars and free amino acids by LAB was evident. Meanwhile, more than 70% of the ginkgolic acids were degraded by LAB, and the final concentrations in ginkgo kernel juice were below 1 mg/L after 48 h of fermentation. In contrast, the terpene lactones contents in fermented ginkgo kernel juice exceed 20 mg/L, which was 1.6-fold higher than that in the unfermented juice. Certain phenolics were significantly enriched, and the total phenolic content increased by approximately 9% through fermentation. In addition, lactic acid fermentation significantly enhanced the antioxidant and antimicrobial activities of ginkgo kernel juice. Overall, the results indicated that lactic acid fermentation can effectively improve the nutritional value and safety of ginkgo kernel juice.     

Hydrothermal conversion of municipal organic waste into resources

Sub- and supercritical water have been focused on as an environmentally attractive reaction media where organic materials can be decomposed into smaller molecules. We applied a hydrothermal reaction in subcritical water to the treatment of rabbit food as a model municipal solid waste. The reaction was carried out in a batch reactor at the temperature range of 473-623 K or in a semi-continuous reactor with the temperature profile from 473 to 573 K. The liquid reaction products were separated into water-soluble and water-insoluble parts. The water-soluble part was analyzed in terms of glucose and organic acids. For the batch reactor, the largest amount of water-soluble component was approximately 50%. Major organic acids detected were acetic acid and lactic acid. The largest yields were 2.6% for acetic acid and 3.2% for lactic acid. The largest yield of glucose was 33% at 523 K. For the semi-continuous reactor, the glucose yields were 11.5%, 3.9% and 8.7% in each fraction obtained at 473, 523, and 573 K, respectively.     

Separation of lactic acid from acetic acid using a four-zone SMB

A simulated moving bed (SMB) process has been developed to separate l-(+)-lactic acid from acetic acid, a major impurity in the fermentation broth of Lactobacillus rhamnosus. Poly(4-vinylpyridine) resin (PVP) was selected as the adsorbent. Adsorption isotherms and mass transfer parameters of the organic acids were estimated from single-column frontal tests. Experimental results show that the Langmuir isotherms obtained from the frontal tests can be used in the design of an SMB process to achieve 99.9% purity and over 93% yield of lactic acid. The column profiles and effluent histories, however, deviate from rate model predictions based on the Langmuir isotherms. They agree more closely with the predictions based on a modified Langmuir isotherm for lactic acid. The standing wave design method for systems with modified Langmuir isotherms is developed in this study. Rate model simulations show that the process based on the modified design method can achieve high purity (>99.9%) and high yield (>99.9%). For this nonlinear system, accurate isotherm model and model parameters are needed in the design, and the zone flow rates must be closely monitored and controlled in order to ensure high purity and high yield in the SMB process.     

Purification of l-(+)-lactic acid from pre-treated fermentation broth using vapor permeation-assisted esterification

The vapor permeation-assisted esterification of l-(+)-lactic acid and ethanol was investigated using a zeolite membrane. Pervaporation and vapor permeation were initially investigated for dehydration performances, and the latter showed much better results. The molecular sieve property of the membrane resulted in a high separation factor of over 1000 for all conditions. The maximum flux was 10.24 kg/(m² h) at a feed temperature of 145 °C, a water feed concentration of 10 wt%, and a feed pressure of 4.0 bars, respectively. For vapor permeation-assisted esterification using synthetic solutions, the productivity and ethyl lactate yield strongly depended on the dehydration rate. Realistic purifications were performed with fermentation broths of Pediococcus pentosaceus as the lactic acid producer. Experimental results revealed that most of the lactic acid was converted into ethyl lactate at the final stage of the reaction. After distillation and hydrolysis, high purity l-(+)-lactic acid was obtained with more than 95% recovery yields.     

In situ separation of lactic acid from fermentation broth using ion exchange resins

Lactic acid fermentation is an end product inhibited reaction. In situ separation of lactic acid from fermentation broth using ion exchange resins was investigated and compared with conventional fermentation system. Amberlite resin (IRA-400, Cl⁻) was used to separate lactic acid from fermentation broth and pH was controlled online with an automatic pH controller. The effect of process variables on lactic acid production by Lactobacillus casei in whey permeate was studied. The maximum productivity was obtained at pH = 6.1, T = 37 °C and impeller speed = 200 rpm. The maximum concentration of lactic acid at optimum condition was found to be 37.4 g/L after 38 h of fermentation using in situ separation system. The productivity of in situ separation system was five times increased in comparison with conventional system.     

A novel and environment-friendly bioprocess of 1,3-propanediol fermentation integrated with aqueous two-phase extraction by ethanol/sodium carbonate system

An integrated fermentation–separation process for the production of 1,3-propanediol (1,3-PD) was investigated. Aqueous two-phase system (ATPS) not only recovered 97.9% of 1,3-PD, but simultaneously also removed 99.1% cells, 81.9% proteins, 75.5% organic acids, and 78.7% water. Furthermore, after extraction the bottom phase of ATPS was used to adjust the pH of the culture during fermentation, leading to 16% and 126% increases in the concentrations of 1,3-PD and lactic acid, and dramatic decreases in the concentration of acetic acid and formic acid. The total mass conversion yield of three main products (1,3-PD, 2,3-butanediol, and lactic acid) from glycerol reached 81.6%. The salt-enriched phase could also be used to absorb carbon dioxide (CO₂), resulting in 94% recovery for carbonate. Finally, process simulation using the program PRO/II showed the use of ATPS reduced 75.1% of the energy expenditure and 89.0% of CO₂ emissions.     

Characterization of biotechnological processes and products using high-performance liquid chromatography (HPLC). III. Quantitative analysis of organic acids in the α-ketoglutaric acid synthesis

A HPLC technique for the analysis of organic acids in the production of α-ketoglutaric acid was developed. The method was applied and optimized for the quantitative determination of citric acid, pyruvic acid, isocitric acid and α-ketoglutaric acid in fermentation solutions. As microorganism the yeast Yarrowia lipolytica and as substrates glucose or paraffins were used. The chromatographic separations were carried out by means of 50 and 100 × 8 mm i.d. glass columns packed with an anion-exchange resin based on an 8% cross-linked polystyrene-divinylbenzene copolymer. The relative errors ranged from 2.1% (α-ketoglutaric acid) to 5.2% (isocitric acid). The percent recovery values varied between 94.4% (isocitric acid) and 107.7% (pyruvic acid). The contents of organic acids in fermentation solutions after the microbial synthesis based on paraffins or glucose were compared.