Succinic acid production from wheat using a biorefining strategy

The biosynthesis of succinic acid from wheat flour was investigated in a two-stage bio-process. In the first stage, wheat flour was converted into a generic microbial feedstock either by fungal fermentation alone or by combining fungal fermentation for enzyme and fungal bio-mass production with subsequent flour hydrolysis and fungal autolysis. In the second stage, the generic feedstock was converted into succinic acid by bacterial fermentation by Actinobacillus succinogenes. Direct fermentation of the generic feedstock produced by fungal fermentation alone resulted in a lower succinic acid production, probably due to the low glucose and nitrogen concentrations in the fungal broth filtrate. In the second feedstock production strategy, flour hydrolysis conducted by mixing fungal broth filtrate with wheat flour generated a glucose-rich stream, while the fungal bio-mass was subjected to autolysis for the production of a nutrient-rich stream. The possibility of replacing a commercial semi-defined medium by these two streams was investigated sequentially. A. succinogenes fermentation using only the wheat-derived feedstock resulted in a succinic acid concentration of almost 16 g l^–1 with an overall yield of 0.19 g succinic acid per g wheat flour. These results show that a wheat-based bio-refinery employing coupled fungal fermentation and subsequent flour hydrolysis and fungal autolysis can lead to a bacterial feedstock for the efficient production of succinic acid.     

稀酸水解玉米芯制备丁二酸

利用正交设计得到稀H2SO4水解玉米芯制备混合糖液的优化工艺:玉米芯料液比1∶5(质量体积比),物料粒径250~380μm、H2SO4用量3%(体积分数)、水解温度126℃、反应时间2.5 h。此工艺条件下的总糖收率达90%,总糖质量浓度为60 g/L,发酵抑制物糠醛含量为0.87 g/L,5-羟甲基糠醛含量为0.68 g/L。在此基础上利用活性炭吸附和Ca(OH)2中和对玉米芯混合糖液进行脱毒及脱盐处理,SO42-脱除率达96%,色素脱除率为96%,糠醛、5-羟甲基糠醛及多酚类物质脱除率均高于50%。处理后的玉米芯多组分糖液作为产琥珀酸放线杆菌(Actinobacillus succino-genes)NJ113的发酵C源,当培养基中初始总糖质量浓度为50 g/L时,丁二酸收率为61.68%,丁二酸质量浓度为30.8 g/L;初始总糖质量浓度为70 g/L时,丁二酸收率仍可达50%以上,丁二酸质量浓度为35.2 g/L。发酵实验表明,将经过脱毒脱盐处理的玉米芯多组分糖液替代葡萄糖作为C源发酵制备丁二酸具有可行性。     

发酵产丁二酸过程中废弃细胞的循环利用

对厌氧发酵产丁二酸后的废弃细胞进行破壁处理,考察了以细胞水解液作为有机氮源重新用于丁二酸发酵的可行性。比较了超声破碎、盐溶、酶解3种方法破碎细胞获得的水解液作为氮源发酵产丁二酸的效果,结果表明酶解制得的细胞水解液效果最佳。以总氮含量为1.11g/L的酶解液(相当于10g/L酵母膏)作为氮源发酵,丁二酸产量可达42.0g/L,继续增大酶解液用量对耗糖、产酸能力没有显著提高。将细胞酶解液与5g/L酵母膏联用发酵36h后,丁二酸产量达75.5g/L,且丁二酸生产强度为2.10g/(L·h),比使用10g/L酵母膏时提高了66.7%。因此,厌氧发酵产丁二酸结束后的废弃细胞酶解液可以替代原培养基中50%的酵母膏用于发酵。     

木薯粉同步糖化发酵(SSF)产丁二酸

【目的】通过优化产琥珀酸放线杆菌GXAS137同步糖化发酵木薯粉产丁二酸的发酵培养基,提高丁二酸产量,降低生产成本。【方法】在单因素试验的基础上,先利用Plackett-Burman试验设计筛选出影响丁二酸发酵的重要参数,再采用正交试验确定重要参数的最佳水平。【结果】价格低廉玉米浆可用作氮源,影响丁二酸产量的重要参数是木薯粉、玉米浆、碱式碳酸镁和糖化酶浓度。最佳条件为(g/L):木薯粉100,玉米浆14,糖化酶2.0 AGU/g底物,碱式碳酸镁75。优化后丁二酸产量达到69.31 g/L,丁二酸得率为90.01%,生产强度为1.44 g/(L·h)。与初始条件(52.34 g/L)相比,丁二酸浓度提高了32.42%。并利用1.3 L发酵罐对SSF与SHF两种发酵工艺进行了比较,SSF丁二酸产量(72.21 g/L)远高于SHF(56.86 g/L)。【结论】产琥珀酸放线杆菌同步糖化发酵木薯粉丁二酸产量高,生产成本低,具有较好的工业化应用前景。     

Optimization of organic acid pretreatment of wheat straw

The objective of this study was to determine the effectiveness of different organic acids (maleic, succinic, and oxalic acid) on enzymatic hydrolysis and fermentation yields of wheat straw. It was also aimed to optimize the process conditions (temperature, acid concentration, and pretreatment time) by using response surface methodology (RSM). In line with this objective, the wheat straw samples were pretreated at three different temperatures (170, 190, and 210°C), acid concentrations (1%, 3%, and 5%) and pretreatment time (10, 20, and 30 min). The findings show that at extreme pretreatment conditions, xylose was solubilized in liquid phase, causing an increase in cellulose and lignin content of biomass. Enzymatic hydrolysis experiments revealed that maleic and oxalic acids were quite effective at achieving high sugar yields (>90%) from wheat straw. In contrast, the highest sugar yields were 50–60%, when the samples were pretreated with succinic acid, indicating that succinic acid was not as effective. The optimum process conditions for maleic acid were, 210°C, 1.08% acid concentration, and 19.8 min; for succinic acid 210°C, 5% acid concentration, and 30 min; for oxalic acid 210°C, 3.6% acid concentration, and 16.3 min. The ethanol yields obtained at optimum conditions were 80, 79, and 59% for maleic, oxalic and succinic acid, respectively. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1487–1493, 2016     

Simultaneous saccharification and fermentation of acid-pretreated rapeseed meal for succinic acid production using Actinobacillus succinogenes

Rapeseed meal was evaluated for succinic acid production by simultaneous saccharification and fermentation using Actinobacillus succinogenes ATCC 55618. Diluted sulfuric acid pretreatment and subsequent hydrolysis with pectinase was used to release sugars from rapeseed meal. The effects of culture pH, pectinase loading and yeast extract concentration on succinic acid production were investigated. When simultaneous saccharification and fermentation of diluted acid pretreated rapeseed meal with a dry matter content of 12.5% (w/v) was performed at pH 6.4 and a pectinase loading of 2% (w/w, on dry matter) without supplementation of yeast extract, a succinic acid concentration of 15.5 g/L was obtained at a yield of 12.4 g/100g dry matter. Fed-batch simultaneous saccharification and fermentation was carried out with supplementation of concentrated pretreated rapeseed meal and pectinase at 18 and 28 h to yield a final dry matter content of 20.5% and pectinase loading of 2%, with the succinic acid concentration enhanced to 23.4 g/L at a yield of 11.5 g/100g dry matter and a productivity of 0.33 g/(Lh). This study suggests that rapeseed meal may be an alternative substrate for the efficient production of succinic acid by A. succinogenes without requiring nitrogen source supplementation.     

A wheat biorefining strategy based on solid-state fermentation for fermentative production of succinic acid

In this study, a novel generic feedstock production strategy based on solid-state fermentation (SSF) has been developed and applied to the fermentative production of succinic acid. Wheat was fractionated into bran, gluten and gluten-free flour by milling and gluten extraction processes. The bran, which would normally be a waste product of the wheat milling industry, was used to produce glucoamylase and protease enzymes via SSF using Aspergillus awamori and Aspergillus oryzae, respectively. The resulting solutions were separately utilised for the hydrolysis of gluten-free flour and gluten to generate a glucose-rich stream of over 140gl(-1) glucose and a nitrogen-rich stream of more than 3.5gl(-1) free amino nitrogen. A microbial feedstock consisting of these two streams contained all the essential nutrients required for succinic acid fermentations using Actinobacillus succinogenes. In a fermentation using only the combined hydrolysate streams, around 22gl(-1) succinic acid was produced. The addition of MgCO(3) into the wheat-derived medium improved the succinic acid production further to more than 64gl(-1). These results demonstrate the SSF-based strategy is a successful approach for the production of a generic feedstock from wheat, and that this feedstock can be efficiently utilised for succinic acid production.     

Succinate production from different carbon sources under anaerobic conditions by metabolic engineered Escherichia coli strains

Succinic acid has drawn much interest as a precursor of many industrially important chemicals. Using a variety of feedstocks for the bio-production of succinic acid would be economically beneficial to future industrial processes. Escherichia coli SBS550MG is able to grow on both glucose and fructose, but not on sucrose. Therefore, we derived a SBS550MG strain bearing both the pHL413 plasmid, which contains Lactococcus lactis pycA gene, and the pUR400 plasmid, which contains the scrK, Y, A, B, and R genes for sucrose uptake and catalyzation. Succinic acid production by this modified strain and the SBS550pHL413 strain was tested on fructose, sucrose, a mixture of glucose and fructose, a mixture of glucose, fructose and sucrose, and sucrose hydrolysis solution. The modified strain can produce succinic acid efficiently from all combinations of different carbon sources tested with minimal byproduct formation and with high molar succinate yields close to that of the maximum theoretic values. The molar succinic acid yield from fructose was the highest among the carbon sources tested. Using the mixture of glucose and fructose as the carbon source resulted in slightly lower yields and much higher productivity than using fructose alone. Fermenting sucrose mixed with fructose and glucose gave a 1.76-fold higher productivity than that when sucrose was used as the sole carbon source. Using sucrose pretreated with sulfuric acid as carbon source resulted in a similar succinic acid yield and productivity as that when using the mixture of sucrose, fructose, and glucose. The results of the effect of agitation rate in aerobic phase on succinate production showed that supplying large amount of oxygen in aerobic phase resulted in higher productions of formate and acetate, and therefore lower succinate yield. This study suggests that fructose, sucrose, mixture of glucose and fructose, mixture of glucose, fructose and sucrose, or sucrose hydrolysis solution could be used for the economical and efficient production of succinic acid by our metabolic engineered E. coli strain.     

Ultrasonic pretreatment and acid hydrolysis of sugarcane bagasse for succinic acid production using Actinobacillus succinogenes

Immense interest has been devoted to the production of bulk chemicals from lignocellulose biomass. Diluted sulfuric acid treatment is currently one of the main pretreatment methods. However, the low total sugar concentration obtained via such pretreatment limits industrial fermentation systems that use lignocellulosic hydrolysate. Sugarcane bagasse hemicellulose hydrolysate is used as the carbon and nitrogen sources to achieve a green and economical production of succinic acid in this study. Sugarcane bagasse was ultrasonically pretreated for 40 min, with 43.9 g/L total sugar obtained after dilute acid hydrolysis. The total sugar concentration increased by 29.5 %. In a 3-L fermentor, using 30 g/L non-detoxified total sugar as the carbon source, succinic acid production increased to 23.7 g/L with a succinic acid yield of 79.0 % and a productivity of 0.99 g/L/h, and 60 % yeast extract in the medium could be reduced. Compared with the detoxified sugar preparation method, succinic acid production and yield were improved by 20.9 and 20.2 %, respectively.     

Occurrence of a nucleoprotein bound RNase in rat brain and liver

An RNase activity was found to be present in rat brain and liver and was strongly bound to the nucleoprotein fractions of these tissues. It could not be solubilized by treatment with acid or by lipid solvents. The pattern of oligonucleotides produced during hydrolysis by this enzyme indicated that it was probably an endonuclease with restricted specificity. It was inhibited by zinc ions and by low pH.     

Occurrence of 2-keto-deoxyoctonic acid 5-phosphate in lipopolysaccharides of Vibrio cholerae Ogawa and Inaba.

A phosphorylated 2-keto-3-deoxyoctonic acid (KDO) was released from the lipopolysaccharides of Vibrio cholerae Ogawa and Inaba after strong acid hydrolysis. The phosphorylated KDO was identified by gas-liquid chromatography and mass spectrometry after reduction and permethylation as KDO-5-phosphate and an isomer of it being phosphorylated at position 7 or 8. After treatment with alkaline phosphatase, KDO was detected by gas-liquid chromatography and mass spectrometry. It was indistinguishable from authentic 2-keto-3-deoxy-D-manno-octonic acid.     

Identification of phosphorylated 3-deoxy-manno-octulosonic acid as a component of Haemophilus influenzae lipopolysaccharide.

A phosphorylated 3-deoxy-manno-octulosonic acid (KDO) was released from the lipopolysaccharide (LPS) of the deep rough mutant (Rb+169) of Haemophilus influenzae by acid hydrolysis. Both phosphorylated and dephosphorylated KDO, produced by treatment with alkaline phosphatase, were identified by gas chromatography-mass spectrometry after trimethylsilylation. This technique provides a rapid and reliable method for the identification of phosphorylated KDO in LPS.     

Selective chemical modification of cytochrome P-450SCC lysine residues. Identification of lysines involved in the interaction with adrenodoxin

Selective chemical modification of cytochrome P-450SCC has been carried out with lysine-modifying reagents. Modification of cytochrome P-450SCC with succinic anhydride was shown to result in loss of its ability to interact with intermediate electron transfer protein - adrenodoxin. To identify amino acid residues involved in charge-ion pairing with complementary carboxyl groups of adrenodoxin, cytochrome P-450SCC complex with adrenodoxin was modified with succinic anhydride. Adrenodoxin was then removed and cytochrome P-450 was additionally modified with isotopically labelled reagent. Subsequent chymotryptic hydrolysis of [14C]succinylated cytochrome P-450SCC and separation of digest obtained by combining various types of HPLC resulted in seven major radioactive peptides. The amino acid sequence of the peptides was determined by microsequencing. The major amino groups modified with radioactive succinic anhydride were found to be at Lys-73, -109, -110, -126, -145, -148 and -154 in the N-terminal sequence of cytochrome P-450SCC molecule and at Lys-267, -270, -338 and -342 in the C-terminal sequence. The role of electrostatic interactions in fixation of cytochrome P-450SCC complex with adrenodoxin is discussed.     

Recent advances in production of succinic acid from lignocellulosic biomass

Production of succinic acid via separate enzymatic hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF) are alternatives and are environmentally friendly processes. These processes have attained considerable positions in the industry with their own share of challenges and problems. The high-value succinic acid is extensively used in chemical, food, pharmaceutical, leather and textile industries and can be efficiently produced via several methods. Previously, succinic acid production via chemical synthesis from petrochemical or refined sugar has been the focus of interest of most reviewers. However, these expensive substrates have been recently replaced by alternative sustainable raw materials such as lignocellulosic biomass, which is cheap and abundantly available. Thus, this review focuses on succinic acid production utilizing lignocellulosic material as a potential substrate for SSF and SHF. SSF is an economical single-step process which can be a substitute for SHF — a two-step process where biomass is hydrolyzed in the first step and fermented in the second step. SSF of lignocellulosic biomass under optimum temperature and pH conditions results in the controlled release of sugar and simultaneous conversion into succinic acid by specific microorganisms, reducing reaction time and costs and increasing productivity. In addition, main process parameters which influence SHF and SSF processes such as batch and fed-batch fermentation conditions using different microbial strains are discussed in detail.     

Study of the role of lysine residues of the cholesterol hydroxylating cytochrome P-450 by a method of chemical modification

Chemical modification of cytochrome P-450scc by lysine-specific reagents has been performed. Modification of the hemoprotein was shown to result in the loss of its ability to interact with adrenodoxin. With a view of identifying lysine residues involved in the interaction with adrenodoxin, cytochrome P-450scc was modified by succinic anhydride in the presence of adrenodoxin. After the removal of ferredoxin, the modification was performed with the use of a radioactively labeled reagent. Subsequent hydrolysis of the succinic hemoprotein by chymotrypsin and separation of the peptides obtained by high pressure liquid chromatography resulted in the isolation of seven chymotryptic peptides containing labeled lysine residues. These amino acid sequences were identified. The role of lysine residues of cytochrome P-450scc in complex formation with adrenodoxin is discussed.     

Factors affecting the course of DNA acid hydrolysis in carrying out the Feulgen reaction]

Literature data concerning acid hydrolysis of DNA during the Feulgen procedure are reviewed, with emphasis being made on the dependence of Schiff-apurinic acid binding on the fixation technique, the temperature of hydrolysis and acid concentration, the rate of extraction of depolymerized DNA fragments, the nucleotide composition of DNA, the chromatin state, and on the composition of nucleoprotein. Some practical considerations for optimization of the Feulgen procedure for a precise quantitative determination of DNA amount are given.     

Activation of carboxyl group with cyanate: peptide bond formation from dicarboxylic acids

The reaction of cyanate with C-terminal carboxyl groups of peptides in aqueous solution was considered as a potential pathway for the abiotic formation of peptide bonds under the condition of the primitive Earth. The catalytic effect of dicarboxylic acids on cyanate hydrolysis was definitely attributed to intramolecular nucleophilic catalysis by the observation of the ¹H-NMR signal of succinic anhydride when reacting succinic acid with KOCN in aqueous solution (pH 2.2–5.5). The formation of amide bonds was noticed when adding amino acids or amino acid derivatives into the solution. The reaction of N-acyl aspartic acid derivatives was observed to proceed similarly and the scope of the cyanate-promoted reaction was analyzed from the standpoint of prebiotic peptide formation. The role of cyanate in activating peptide C-terminus constitutes a proof of principle that intramolecular reactions of adducts of peptides C-terminal carboxyl groups with activating agents represent a pathway for peptide activation in aqueous solution, the relevance of which is discussed in connexion with the issue of the emergence of homochirality.     

Acid-catalyzed hydrolysis of α-ketoglutaramic acid : A proposed mechanism involving decarboxylation and amide hydrolysis of the γ-lactam, 2-pyrrolidone-5-hydroxy-5-carboxylic acid

The rates of the acid-catalyzed decarboxylation and amide hydrolysis of α-ketoglutaramic acid, the keto analog of glutamine, were investigated and the products of the reactions were characterized. In strong acid at 100°C, amide hydrolysis and decarboxylation occur with about equal facility, yielding α-ketoglutaric acid and 5-hydroxy-2-pyrrolidone, respectively. 5-Hydroxy-2-pyrrolidone undergoes further amide hydrolysis so that the products of complete acid hydrolysis of α-ketoglutaramic acid are ammonia (100%), carbon dioxide (50%), and approximately equal yields (50%) of α-ketoglutaric acid and succinic semialdehyde (β-formylpropionic acid). At increasing pH values, the relative rate of decarboxylation to amide hydrolysis of α-ketoglutaramic acid increases, such that, at pH values of 2 or greater, decarboxylation occurs almost exclusively. The decarboxylation product 5-hydroxy-2-pyrrolidone, was characterized chromatographically and by its infrared and pmr spectra; the compound may be regarded as the cyclized form of succinamic semialdehyde. A mechanism for the competing amide hydrolysis and decarboxylation reactions is proposed, and the potential biological significance of the decarboxylation pathway is discussed.     

Uptake and efflux of succinic acid by uninduced mycelium of Claviceps purpurea.

Claviceps purpurea PRL 1980 grew on partially dissociated succinic acid (pH 4) but not on fully dissociated succinic acid (pH 7.2). Myeclium suspended in 42 mM solution of partially ionized succinic acid (pH 4; 60.1% nonionized, 39% monoanion, and 0.9% dianion, K+ salt) over a period of 25 min accumulated more succinic acid carbon than mycelium suspended in highly ionized solution (pH 6.8; 0.01% nonionized, 4.8% monoanion, and 95% dianion). The greater accumulation from partially ionized solution was not attributable solely to metabolism of succinic acid nor to the lower external concentration of potassium ion. Rate of uptake by sodium azide and iodoacetate-treated mycelium was proportional to external concentration at least up to 200 mumol/ml. External potassium or sodium ion was not required for uptake by inhibited or uninhibited mycelium and external sodium ion and glucose did not allow concentration of succinic acid. The internal concentrations of succinic acid carbon expressed as succinic acid in cell water were about the same as the external concentrations. Uptake was not appreciably affected by extent of ionization of external succinic acid but accumulation was markedly affected. A plot of accumulated succinic acid carbon against external pH produced a bimodal curve with the two maxima corresponding to the maximal concentrations of nonionized and monoanion succinic acid. The bimodal curve probably results from overlapping of two separate curves; the nonionized form accumulating efficiently because of one interaction with the cell and the monoanion form accumulating efficiently because of another interaction. Uptake from concentrated solution is by diffusion and efflux is rapid but not complete. Efflux is not retarded by presence of phosphate in the external solution.     

Selective extraction of succinic acid from binary mixture of succinic acid and acetic acid

In production of succinic acid by fermentation, succinic acid and acetic acid are co-produced. To purify the succinic acid from binary-acid mixture of succinic acid and acetic acid, the tertiary amine-based extraction was used. In 1-octanol, the selectivity for succinic acid was proportional to the chain length of tertiary amine. But, the distribution of acids into organic phase was low in n-heptane. These results are due to the different degree of intramolecular hydrogen bonding of succinic acid and hydrophobicity of each acid.