Model-based temperature control for improving lactic acid production from glycerol.

To maximize the final lactic acid productivity and concentration, temperature control was optimized using a mathematical modelling approach. A kinetic model, including cell growth, product formation and substrate consumption equations, was proposed to describe the lactic acid production process by Escherichia coli AC-521 with glycerol as the substrate. By constructing four functions, the temperature effect was introduced on the fermentation process, where four parameters (X max, µ max, Y ps and ß) were observed to be significantly affected by the temperature. For the convenience of application, the temperature control strategies were simplified by dividing the whole fermentation process into several units. In each unit, the temperature was controlled constantly. Based on the model, the optimal temperature for each unit was determined to maximize the final lactate productivity. This temperature control strategy can be effectively applied in batch and fed-batch cultures, and the verified experimental evaluation showed a good correlation with the model data. Under improved temperature control conditions, a maximal lactic acid concentration of 90.4 g L-1 was obtained after 80 h of fed-batch fermentation, giving a productivity of 1.13 g L-1 h-1, which is 1.2 times more than that in the conventional constant temperature during the cultivation course.

In vivo anti-inflammatory activities of novel cytokine IL-38 in Murphy Roths Large (MRL)/lpr mice.

The newly named interleukin (IL)-36 subfamily member IL-38 has been shown to exert anti-inflammatory activity. However, the in vivo immunomodulatory activity of IL-38 was poorly investigated in systemic lupus erythematosus (SLE). We have investigated the expression of CD4+IL-17+ Th17, CD4+IFN-γ+ Th1 and CD3+CD4-CD8- double negative (DN) T cells and the related immunopathological mechanisms in female MRL/lpr mice model of spontaneous lupus-like disease, with or without IL-38 treatment. Intravenous administration of murine recombinant IL-38 into MRL/lpr mice can ameliorate the lupus-like clinical symptoms including proteinuria, leukocyteuria and skin lesions. A remission of histopathology characteristics of skin and nephritis was also observed upon IL-38 treatment. Accordingly, IL-38 receptor was expressed on the cell surface of both CD4+ Th and CD19+ B lymphocytes. The splenic Th17 and DN T lymphocytes, the average mRNA level of epigenetically regulated gene expression of Th17 cells, and serum concentrations of IL-17 and IL-22 were significantly decreased upon the treatment of IL-38 (all p<0.05). The in vivo results suggest that IL-38 can ameliorate skin inflammation and nephritis in SLE mice probably via suppressing the formation of inflammatory cytokines such as IL-17 and IL-22, and pathogenic DN T cells. These findings may provide a biochemical basis for further investigation of the therapeutic mechanisms of IL-38 for the treatment of autoimmune-mediated inflammation.

The implementation of high fermentative 2,3-butanediol production from xylose by simultaneous additions of yeast extract, Na2EDTA, and acetic acid.

The effective use of xylose may significantly enhance the feasibility of using lignocellulosic hydrolysate to produce 2,3-butanediol (2,3-BD). Previous difficulties in 2,3-BD production include that the high-concentration xylose cannot be converted completely and the fermentation rate is slow. This study investigated the effects of yeast extract, ethylenediaminetetraacetic acid disodium salt (Na2EDTA), and acetic acid on 2,3-BD production from xylose. The central composite design approach was used to optimize the concentrations of these components. It was found that simultaneous addition of yeast extract, Na2EDTA, and acetic acid could significantly improve 2,3-BD production. The optimal concentrations of yeast extract, Na2EDTA, and acetic acid were 35.2, 1.2, and 4.5 g/L, respectively. The 2,3-BD concentration in the optimized medium reached 39.7 g/L after 48 hours of shake flask fermentation, the highest value ever reported in such a short period. The xylose utilization ratio and the 2,3-BD concentration increased to 99.0% and 42.7 g/L, respectively, after 48 hours of stirred batch fermentation. Furthermore, the 2,3-BD yield was 0.475 g/g, 95.0% of the theoretical maximum value. As the major components of lignocellulosic hydrolysate are glucose, xylose, and acetic acid, the results of this study indicate the possibility of directly using the hydrolysate to effectively produce 2,3-BD.

[Detection of Hawthorn Fruit Defects Using Hyperspectral Imaging].

Hyperspectral imaging technology covered the range of 380-1000 nm was employed to detect defects (bruise and insect damage) of hawthorn fruit. A total of 134 samples were collected, which included damage fruit of 46, pest fruit of 30, injure and pest fruit of 10 and intact fruit of 48. Because calyx · s⁻¹ tem-end and bruise/insect damage regions offered a similar appearance characteristic in RGB images, which could produce easily confusion between them. Hence, five types of defects including bruise, insect damage, sound, calyx, and stem-end were collected from 230 hawthorn fruits. After acquiring hyperspectral images of hawthorn fruits, the spectral data were extracted from region of interest (ROI). Then, several pretreatment methods of standard normalized variate (SNV), savitzky golay (SG), median filter (MF) and multiplicative scatter correction (MSC) were used and partial least squares method(PLS) model was carried out to obtain the better performance. Accordingly to their results, SNV pretreatment methods assessed by PLS was viewed as best pretreatment method. Lastly, SNV was chosen as the pretreatment method. Spectral features of five different regions were combined with Regression coefficients(RCs) of partial least squares-discriminant analysis (PLS-DA) model was used to identify the important wavelengths and ten wavebands at 483, 563, 645, 671, 686, 722, 777, 819, 837 and 942 nm were selected from all of the wavebands. Using Kennard-Stone algorithm, all kinds of samples were randomly divided into training set (173) and test set (57) according to the proportion of 3:1. And then, least squares-support vector machine (LS-SVM) discriminate model was established by using the selected wavebands. The results showed that the discriminate accuracy of the method was 91.23%. In the other hand, images at ten important wavebands were executed to Principal component analysis (PCA). Using "Sobel" operator and region growing algrorithm "Regiongrow", the edge and defect feature of 86 Hawthorn could be recognized. Lastly, the detect precision of bruised, insect damage and two-defect samples is 95.65%, 86.67% and 100%, respectively. This investigation demonstrated that hyperspectral imaging technology could detect the defects of bruise, insect damage, calyx, and stem-end in hawthorn fruit in qualitative analysis and feature detection which provided a theoretical reference for the defects nondestructive detection of hawthorn fruit.

Calpain, Atg5 and Bak play important roles in the crosstalk between apoptosis and autophagy induced by influx of extracellular calcium.

Calcium (Ca(2+)) signals are involved in important checkpoints in cell death pathways and promote both apoptosis and autophagy. However, the relationship between autophagy and apoptosis in response to Ca(2+) level elevation is poorly understood. Here, we provided evidence that the influx of extracellular Ca(2+) triggered by Trichokonin VI (TK VI), an antimicrobial peptide, induced calpain-dependent apoptosis and autophagy in hepatocellular carcinoma (HCC) cells. Remarkably, TK VI preferentially induced apoptosis that was associated with calpain-mediated Bax and Atg5 cleavage, which resulted in the collapse of the mitochondrial membrane potential and cytochrome c release. Interestingly, truncated, but not full-length Atg5, associated with Bcl-xL and promoted the intrinsic pathway. Moreover, TK VI treatment induced reactive oxygen species (ROS) accumulation, an effect in which Bak might play a major role. This accumulation of ROS resulted in the subsequent disposal of damaged mitochondria within autophagosomes via Atg5-mediated and mitochondria-selective autophagy. Both the inhibition of calpain activity and Bax deficiency activated a switch that promoted an enhancement of autophagy. The inhibition of both apoptosis and autophagy significantly attenuated the TK VI cytotoxicity, indicating that the two processes had stimulatory effects during TK VI-meditated cell death. These results suggested that calpain, Bak and Atg5 were molecular links between autophagy and apoptosis and revealed novel aspects of the crosstalk between these two processes. The potential of TK VI is proposed as a promising anticancer agent for its well-characterized activity of Ca(2+) agonist and as a possible novel therapeutic strategy that acts on cancer cell mitochondria.

Downstream processing of biotechnological produced succinic acid.

Succinic acid is a promising chemical which has a wide range of applications and can be biologically produced. The separation of succinic acid from fermentation broth makes more than 50 % of the total costs in their microbial production. This review summarizes the present state of methods studied for the recovery and purification of biologically produced succinate. Previous studies on the separation of succinic acid primarily include direct crystallization, precipitation, membrane separation, extraction, chromatography, and in situ separation. No single method has proved to be simple and efficient, and improvements are especially needed with regard to yield, purity, and energy consumption. It is argued that separation technologies coupled with upstream technology, in situ product removal, and biorefining strategy deserve more attentions in the future.

Rational synthesis of 1,3-diolein by enzymatic esterification.

t-Butanol was an excellent reaction medium for enzyme-mediated esterification of oleic acid with glycerol for 1,3-diolein preparation which has been proved by our group. Herein, to achieve the rational synthesis of 1,3-diolien, response surface methodology was applied to examine the effects of the significant variables and their reciprocal effects on the product synthesis. Under the optimal conditions (62.4°C, 0.75g Novozym 435, substrate molar ratio (oleic acid/glycerol) 2.4 and 4.8g t-butanol), the diolein yield of 87.4% could be achieved, and the value of 1,3-diolien/diolein was as high as 87.8%, which were quite close to the predicted values. Compared with the results of our previous single factor experiment, although the values of diolein yield and 1,3-diolien/diolein could not be improved markedly, the enzyme dosage and the reaction medium were spared by 25% and 20%, respectively, which was a remarkable improvement of the enzymatic process.

Biodiesel from conventional feedstocks.

At present, traditional fossil fuels are used predominantly in China, presenting the country with challenges that include sustainable energy supply, energy efficiency improvement, and reduction of greenhouse gas emissions. In 2007, China issued The Strategic Plan of the Mid-and-Long Term Development of Renewable Energy, which aims to increase the share of clean energy in the country's energy consumption to 15% by 2020 from only 7.5% in 2005. Biodiesel, an important renewable fuel with significant advantages over fossil diesel, has attracted great attention in the USA and European countries. However, biodiesel is still in its infancy in China, although its future is promising. This chapter reviews biodiesel production from conventional feedstocks in the country, including feedstock supply and state of the art technologies for the transesterification reaction through which biodiesel is made, particularly the enzymatic catalytic process developed by Chinese scientists. Finally, the constraints and perspectives for China's biodiesel development are highlighted.

The mechanism of solvent effect on the positional selectivity of Candida antarctica lipase B during 1,3-diolein synthesis by esterification.

We investigated the influence of solvent on the positional selectivity of Novozym 435 which was the immobilized Candida antarctica lipase B (CALB) during the esterification of oleic acid with glycerol for 1,3-diolein preparation previously. Herein, molecular modeling was used to elucidate the underlying mechanism of the solvent effect on the positional selectivity of the enzyme. The results showed that the binding energy of sn-1 hydroxyl of glycerol molecular with CALB became higher, and the binding energy of sn-2 hydroxyl of glycerol molecular with CALB became lower along with the increase of the solvent log P. It was demonstrated that, increasing log P of the solvent, the enzyme selectivity to sn-1 hydroxyl of glycerol molecular grew weaker, and the selectivity to sn-2 hydroxyl of glycerol molecular grew stronger.

Influence of dhaT mutation of K. pneumoniae on 1,3-propanediol fermentation.

Metabolic role of 1,3-propanediol oxidoreductase (PDOR) in the production of 1,3-propanediol (1,3-PDO) with K. pneumonia was investigated by knocking out the coded gene dhaT. Fermentation with both the wide-type and mutant were studied in 5 l fermentor. A PDOR-deficient mutant K. pneumonia T1.9131 with 19% PDOR activity of the wild type was constructed. The cultures of the mutant indicated that PDOR inactivation had great effect on the other dha regulon enzymes: activity of glycerol dehydratase decreased by 70% while activity of glycerol dehydrogenase increased by 68%. Fed-batch fermentation showed that more metabolic flux of glycerol was directed to lactate and ethanol in the mutant. Lactate was identified as major metabolite and received an increase in the final concentration from 45 to 91 g l(-1), while the concentration of 1,3-PDO production dropped from 94 to 36 g l(-1). The results demonstrated PDOR was not indispensable in glycerol metabolism but was crucial in high 1,3-PDO productivity. It is postulated that a hypothetical oxidoreductase was expressed and replaced the function of PDOR. Blocking the pathway towards lactate and ethanol could be a plausible scheme to enhance 1,3-PDO productivity.

Two subtypes of meningiomas with different imaging co-existed at sphenoid ridge.

Intracranial multiple meningiomas are not uncommon, but multiple meningiomas consisting of different subtypes are rare. Here, we describe an adult male patient with two meningiomas located at sphenoid ridge, with different features on MRI and CTA. Histological examination revealed that one was fibrous meningioma and the other was psammomatous meningioma.

Consequences of cps mutation of Klebsiella pneumoniae on 1,3-propanediol fermentation.

The filtration in 1,3-propanediol (1,3-PD) downstream process is influenced by the large amounts of capsular polysaccharides (CPS) produced by Klebsiella pneumoniae CGMCC 1.6366. The morphological and fermentation properties were investigated with the CPS-deficient mutant K. pneumoniae CGMCC 1.6366 CPS. Similar biomass was obtained with CGMCC 1.6366, and the mutant strain in batch cultures indicating the cell growth was slightly inhibited by CPS defection. The viscosity of fermentation broth by mutant strain decreased by 27.45%. The flux with ceramic membrane filter was enhanced from 168.12 to 303.6 l h(-1) m(-2), exhibiting the great importance for downstream processing of 1,3-PD fermentation. The products spectrum of mutant isolate changed remarkably regarding to the concentration of fermentation products. The synthesis of important 1,3-PD and 2,3-butanediol was enhanced from 9.73 and 4.06 g l(-1) to 10.37 and 4.77 g l(-1) in batch cultures. The noncapsuled K. pneumoniae provided higher 1,3-PD yield of 0.54 mol mol(-1) than that of encapsuled wild parent in batch cultures. The fed-batch fermentation of mutant strain resulted in 1,3-PD concentration, yield, and productivity of 78.13 g l(-1), 0.53 mol mol(-1), and 1.95 g l(-1) h(-1), respectively.

Ammonium and phosphate limitation in 1,3-propanediol production by Klebsiella pneumoniae.

Excretion of 1,3-propanediol (1,3-PD) by K. pneumoniae was compared in ammonium- and phosphate-limited chemostat cultures running with an excess of glycerol. 59 and 43% catabolic flux were directed to 1,3-PD in ammonia-limited cultures and phosphate-limited cultures at dilution rate of 0.1 h(-1), respectively. Ammonia-limited fed-batch cultures produced 61 g 1,3-PD l(-1) and a total of 15 g l(-1) organic acid in 36 h. However, phosphate-limited fed-batch cultures excreted 61 g lactate l(-1) and 44 g 1,3-PD l(-1).

The solvent influence on the positional selectivity of Novozym 435 during 1,3-diolein synthesis by esterification.

The influence of solvents with a wide range of log P (from -0.23 to 4.5) on the positional selectivity of the immobilized lipase Novozym 435 during the esterification of oleic acid with glycerol for 1,3-diolein preparation was investigated. Analysis was performed on the basis of a simplified kinetic model of 1,3-diolein synthesis. The results showed that the preferential selectivity of Novozym 435 to 1-position over 2-position of the glycerol molecular became weaker and weaker with the increasing log P of the solvent. But after one 1-position was acylated, the preferential selectivity to the other 1-position over 2-position would be enhanced strongly for each solvent. The study also revealed that relatively hydrophilic solvent such as t-butanol was an ideal solvent for Novozym 435 catalyzed 1,3-diolein synthesis through esterification of oleic acid with glycerol.

Metabolism in 1,3-propanediol fed-batch fermentation by a D-lactate deficient mutant of Klebsiella pneumoniae.

Klebsiella pneumoniae HR526, a new isolated 1,3-propanediol (1,3-PD) producer, exhibited great productivity. However, the accumulation of lactate in the late-exponential phase remained an obstacle of 1,3-PD industrial scale production. Hereby, mutants lacking D-lactate pathway were constructed by knocking out the ldhA gene encoding fermentative D-lactate dehydrogenase (LDH) of HR526. The mutant K. pneumoniae LDH526 with the lowest LDH activity was studied in aerobic fed-batch fermentation. In experiments using pure glycerol as feedstock, the 1,3-PD concentrations, conversion, and productivity increased from 95.39 g L(-1), 0.48 and 1.98 g L(-1) h(-1) to 102. 06 g L(-1), 0.52 mol mol(-1) and 2.13 g L(-1) h(-1), respectively. The diol (1,3-PD and 2,3-butanediol) conversion increased from 0.55 mol mol(-1) to a maximum of 0.65 mol mol(-1). Lactate would not accumulate until 1,3-PD exceeded 84 g L(-1), and the final lactate concentration decreased dramatically from more than 40 g L(-1) to <3 g L(-1). Enzymic measurements showed LDH activity decreased by 89-98% during fed-batch fermentation, and other related enzyme activities were not affected. NADH/NAD(+) enhanced more than 50% in the late-exponential phase as the D-lactate pathway was cut off, which might be the main reason for the change of final metabolites concentrations. The ability to utilize crude glycerol from biodiesel process and great genetic stability demonstrated that K. pnemoniae LDH526 was valuable for 1,3-PD industrial production.

Physiologic mechanisms of sequential products synthesis in 1,3-propanediol fed-batch fermentation by Klebsiella pneumoniae.

The glycerol fed-batch fermentation by Klebsiella pneumoniae CGMCC 1.6366 exhibited the sequential synthesis of products, including acetate, 1,3-propanediol (1,3-PD), 2,3-butanediol, ethanol, succinate, and lactate. The dominant flux distribution was shifted from acetate formation to 1,3-PD formation in early- exponential growth phase and then to lactate synthesis in late-exponential growth phase. The underlying physiological mechanism of the above observations has been investigated via the related enzymes, nucleotide, and intermediary metabolites analysis. The carbon flow shift is dictated by the intrinsic physiological state and enzymatic activity regulation. Especially, the internal redox state could serve as a rate-controlling factor for 1,3-PD production. The q(1,3-PD) formation was the combined outcomes of regulations of glycerol dehydratase activity and internal redox balancing. The q(ethanol)/q(acetate) ratios demonstrated the flexible adaptation mechanism of K. pneumoniae preferring ATP generation in early-exponential growth phase. A low PEP to pyruvate ratio corresponded LDH activity increase, leading to lactate accumulation in stationary phase.

Statistical optimization of culture conditions for 1,3-propanediol by Klebsiella pneumoniae AC 15 via central composite design.

A central composite design was used to study the effect of glycerol, rate of stirring, air aeration and pH on the synthesis of 1,3-propanediol (1,3-PD) by Klebsiella pneumoniae AC 15. Among the four variables, glycerol and rate of stirring significantly affected 1,3-PD productivity, whereas air aeration and pH were not effective. A quadratic polynomial equation was obtained for 1,3-PD productivity by multiple regression analysis using response surface methodology. The validation experimental confirmed with the predicted model. The optimum combinations for 1,3-PD productivity was glycerol, rate of stirring, air aeration, and pH of 50 g/l, 318 rpm, 0.6 vvm, 6.48, respectively. The subsequent fed batch experiments produced 1,3-PD of 70 g/l at a fermentation of 30 h.

Production of 1,3-propanediol by Klebsiella pneumoniae from glycerol broth.

Broth containing 152 g glycerol l(-1) from Candida krusei culture was converted to 1,3-propanediol by Klebsiella pneumoniae. Residual glucose in the broth promoted growth of K. pneumoniae while acetate was inhibitory. After desalination treatment of glycerol broth by electrodialysis, the acetate in the broth was removed. A fed-batch culture with electrodialytically pretreated broth as substrate was developed giving 53 g 1,3-propanediol l(-1) with a yield of 0.41 g g(-1) glycerol and a productivity of 0.94 g l(-1) h(-1).

Multiple growth inhibition of Klebsiella pneumoniae in 1,3-propanediol fermentation.

The inhibition of substrate and product on the growth of Klebsiella pneumoniae in anaerobic and aerobic batch fermentation for the production of 1,3-propanediol was studied. The cells under anaerobic conditions had a higher maximum specific growth rate of 0.19 h(-1) and lower tolerance to 110 g glycerol l(-1), compared to the maximum specific growth rate of 0.17 h(-1) and tolerance to 133 g glycerol l(-1) under aerobic conditions. Acetate was the main inhibitory metabolite during the fermentation under anaerobic conditions, with lactate and ethanol the next most inhibitory. The critical concentrations of acetate, lactate and ethanol were assessed to be 15, 19, 26 g l(-1), respectively. However, cells grown under aerobic conditions were more resistant to acetate and lactate but less resistant to ethanol. The critical concentrations of acetate, lactate and ethanol were assessed to be 24, 26, and 17 g l(-1), respectively.

1,3-Propanediol production by Klebsiella pneumoniae under different aeration strategies.

1,3-Propanediol production by Klebsiella pneumoniae was studied in batch cultures under N2 flow and four airflow systems. Different byproducts were formed under different aeration conditions. An anaerobic/aerobic combined fed-batch culture was developed giving 70 g 1,3-propanediol l(-1) and 16 g 2,3-butanediol l(-1) with total diol yield of 0.6 mol(-1) glycerol.