Scale-up from shake flasks to fermenters in batch and continuous mode with Corynebacterium glutamicum on lactic acid based on oxygen transfer and pH

Scale-up from shake flasks to fermenters has been hampered by the lack of knowledge concerning the influence of operating conditions on mass transfer, hydromechanics, and power input. However, in recent years the properties of shake flasks have been described with empirical models. A practical scale-up strategy for everyday use is introduced for the scale-up of aerobic cultures from shake flasks to fermenters in batch and continuous mode. The strategy is based on empirical correlations of the volumetric mass transfer coefficient (k(L) a) and the pH. The accuracy of the empirical k(L) a correlations and the assumptions required to use these correlations for an arbitrary biological medium are discussed. To determine the optimal pH of the culture medium a simple laboratory method based on titration curves of the medium and a mechanistic pH model, which is solely based on the medium composition, is applied. The effectiveness of the scale-up strategy is demonstrated by comparing the behavior of Corynebacterium glutamicum on lactic acid in shake flasks and fermenters in batch and continuous mode. The maximum growth rate (micro(max) = 0.32 h(-1)) and the oxygen substrate coefficient (Y O2 /S= 0.0174 mol/l) of C. glutamicum on lactic acid were equal for shake flask, fermenter, batch, and continuous cultures. The biomass substrate yield was independent of the scale, but was lower in batch cultures (Y(X/S) = 0.36 g/g) than in continuous cultures (Y(X/S) = 0.45 g/g). The experimental data (biomass, respiration, pH) could be described with a simple biological model combined with a mechanistic pH model.     

固定化纤维二糖酶的研究

黑曲霉 (AspergillusnigerLORRE 0 12 )的孢子中富含纤维二糖酶 ,将这些孢子用海藻酸钙凝胶包埋后 ,可以方便有效地固定纤维二糖酶。固定化后的纤维二糖酶性能稳定 ,半衰期为 38d ,耐热性和适宜的pH范围均比固定化前有所增加 ,其Km 和Vmax值分别为 6 .0 1mmol L和 7.0 6mmol (min·L)。利用固定化纤维二糖酶重复分批酶解10g L的纤维二糖 ,连续 10批的酶解得率均可保持在 97%以上 ;采用连续酶解工艺 ,当稀释率为 0 .4h- 1 ,酶解得率可达 98.5 %。玉米芯经稀酸预处理后 ,其纤维残渣用里氏木霉 (Trichodermareesei)纤维素酶降解 ,酶解得率为6 9.5 % ;通过固定化纤维二糖酶的进一步作用 ,上述水解液中因纤维二糖积累所造成的反馈抑制作用得以消除 ,酶解得率提高到 84.2 % ,还原糖中葡萄糖的比例由 5 3 .6 %升至 89.5 % ,该研究结果在纤维原料酶水解工艺中具有良好的应用前景。     

A feasible enzymatic process for D-tagatose production by an immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

To develop a feasible enzymatic process for d-tagatose production, a thermostable l-arabinose isomerase, Gali152, was immobilized in alginate, and the galactose isomerization reaction conditions were optimized. The pH and temperature for the maximal galactose isomerization reaction were pH 8.0 and 65 degrees C in the immobilized enzyme system and pH 7.5 and 60 degrees C in the free enzyme system. The presence of manganese ion enhanced galactose isomerization to tagatose in both the free and immobilized enzyme systems. The immobilized enzyme was more stable than the free enzyme at the same pH and temperature. Under stable conditions of pH 8.0 and 60 degrees C, the immobilized enzyme produced 58 g/L of tagatose from 100 g/L galactose in 90 h by batch reaction, whereas the free enzyme produced 37 g/L tagatose due to its lower stability. A packed-bed bioreactor with immobilized Gali152 in alginate beads produced 50 g/L tagatose from 100 g/L galactose in 168 h, with a productivity of 13.3 (g of tagatose)/(L-reactor.h) in continuous mode. The bioreactor produced 230 g/L tagatose from 500 g/L galactose in continuous recycling mode, with a productivity of 9.6 g/(L.h) and a conversion yield of 46%.     

Binding of Tamm-Horsfall protein to complement 1q and complement 1, including influence of hydrogen-ion concentration

The goal of this study was to further characterize the interaction between an abundant urinary glycoprotein, Tamm-Horsfall protein, and complement 1q to determine the robustness of this reaction under different environmental conditions (particularly pH) and to begin to determine the specificity of this reaction. The influence of pH coupled with ionic strength was evaluated with an ELISA that demonstrated immobilized Tamm-Horsfall protein bound complement 1q strongly with a KD in the nmol/L range from pH 9 to pH 5.5. Increasing the ionic strength from 10 mmol/L sodium chloride (NaCl) to 154 mmol/L NaCl decreased the affinity of Tamm-Horsfall protein for complement 1q slightly (2-7-fold) at pH 9 to pH 6.5. A resonant mirror biosensor was also utilized to evaluate the binding of Tamm-Horsfall protein to complement 1q at different pH values (pH 8.2-5.8). These studies indicated that, compared to at pH 8.2, Tamm-Horsfall protein bound complement 1q at pH 5.8 with an almost two-fold higher affinity (pH 8.2, KD = 5.1 nmol/L vs at pH 5.8, KD = 2.8 nmol/L) due to a faster association rate (pH 8.2 kass = 1.6 x 106 L/mol per s vs pH 5.8 kass = 2.9 x 106 L/mol per s). Surprisingly, the capacity of Tamm-Horsfall protein for complement 1q decreased significantly at pH 5.8, suggesting that a site for complement 1q binding to Tamm-Horsfall protein may be lost at the acidic pH. Biosensor studies also showed that Tamm-Horsfall protein bound the entire complement 1 complex with binding affinities and association rates similar to those obtained for complement 1q individually. This suggested that Tamm-Horsfall protein bound complement 1q at a site other than the region of its collagenous tail where C1r2 and C1s2 bind. By western blot analysis, it was demonstrated that Tamm-Horsfall protein bound preferentially to the C chain of complement 1q.     

一株乙二醇氧化酶菌株的筛选及催化特性的初步研究

利用富集培养技术从土壤中筛选获得1株高活性二醇氧化活性菌株Brevibacterium sp.CCZU12-1。以Brevibacterium sp.CCZU12-1静息细胞为催化剂,最适催化反应温度、反应pH和金属离子添加量分别为30℃、6.5和Mn2＋0.1 mmol/L。在最佳条件下,转化200 mmol/L乙二醇24 h,羟基乙酸的产率为94.6%,分批补料乙二醇5批,羟基乙酸的累积浓度为972 mmol/L。     

Continuous preparation of (S)-3-hydroxy-3-phenylpropionate by asymmetric reduction of 3-oxo-3-phenylpropionic acid ethyl ester with <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> CGMCC No.2266 in a membrane reactor

In this study, (S)-3-hydroxy-3-phenylpropionate was prepared continuously by coupling microbial transformation and membrane separation. The effect of several factors on membrane flux, reactor capacity, and reaction conversion were investigated. A kinetic model of the continuous reduction process was also developed. The appropriate molecular weight cut-off of the ultrafiltration membrane was 30 kDa. The reactor capacity reached a maximum of 0.136/h at a biomass concentration and membrane flux of 86 g/L (dry weight/reaction volume) and 20 mL/h, respectively. The (S)-3-hydroxy-3-phenylpropionate yield was 3.68 mmol/L/day after continuous reduction over seven days. The enantiometric excess of (S)-3-hydroxy-3-phenylpropionate reached above 99.5%. The kinetic constants of continuous reduction were as follows: r _m = 3.00 × 10⁻³ mol/L/h, k _cat = 3.49 × 10⁻⁴ mol/L/h, k ₁ = 3.09 × 10⁻² mol/L, and k ₂ = 5.00 × 10⁻⁷ mol/L. The kinetic model was in good agreement with the experimental data obtained during continuous reduction. Compared with batch reduction, continuous reduction can significantly improve the catalytic efficiency of microbial cells and increase the reactor capacity.     

Calcium alginate bead immobilization of cells containing tyrosine ammonia lyase activity for use in the production of p-hydroxycinnamic acid

An Escherichia coli catalyst with tyrosine ammonia lyase activity (TAL) has been stabilized for repeated use in batch conversions of high tyrosine solids to p-hydroxycinnamic acid (pHCA). The TAL biocatalyst was stabilized by controlling the reaction pH to 9.8 +/- 0.1 and immobilizing the cells within a calcium alginate matrix that was cross-linked with glutaraldehyde and polyethyleneimine (GA/PEI). We found a GA range where the bead-encapsulated TAL was not inactivated, and the resulting cross-linking provided the beads with the mechanical stability necessary for repeated use in consecutive batch reactions with catalyst recycle. The GA/PEI calcium alginate TAL catalyst was used in 41 1-L batch reactions where 50 g L(-1) tyrosine was converted to 39 +/- 4 g L(-1) pHCA in each batch. The practical usefulness and ease of this process was demonstrated by scaling up the TAL bead immobilization and using the immobilized TAL catalyst in four 125-L bioconversion reactions to produce over 12 kg of purified pHCA.     

小麦谷氨酸脱羧酶的纯化及部分性质研究

谷氨酸脱羧酶（ｇｌｕｔａｍａｔｅｄｅｃａｒｂｏｘｙｌａｓｅ,ＧＡＤ,ＥＣ４．１．１．１５）催化谷氨酸脱羧生成γ－氨基丁酸（γ－ａｍｉｎｏｂｕｔｙｒａｔｅ,ＢＡ）,植物中已从南瓜［１］、马铃薯和林生山黧豆［２］纯化了ＧＡＤ．ＧＡＤ活性在禾本科作物中作为...     

Link between primary and secondary metabolism in the biotransformation of trimethylammonium compounds by escherichia coli

The aim of this work was to understand the steps controlling the process of biotransformation of trimethylamonium compounds into L(-)-carnitine by Escherichia coli and the link between the central carbon or primary and the secondary metabolism expressed. Thus, the enzyme activities involved in the biotransformation process of crotonobetaine into L(-)-carnitine (crotonobetaine hydration reaction and crotonobetaine reduction reaction), in the synthesis of acetyl-CoA (pyruvate dehydrogenase, acetyl-CoA synthetase, and ATP:acetate phosphotransferase) and in the distribution of metabolites for the tricarboxylic acid (isocitrate dehydrogenase) and glyoxylate (isocitrate lyase) cycles, were followed in batch with both growing and resting cells and during continuous cell growth in stirred-tank and high-cell-density membrane reactors. In addition, the levels of carnitine, crotonobetaine, gamma-butyrobetaine, ATP, NADH/NAD(+), and acetyl-CoA/CoA ratios were measured to determine how metabolic fluxes were distributed in the catabolic system. The results provide the first experimental evidence demonstrating the important role of the glyoxylate shunt during biotransformation of resting cells and the need for high levels of ATP to maintain metabolite transport and biotransformation (2.1 to 16.0 mmol L cellular/mmol ATP L reactor h). Moreover, the results obtained for the pool of acetyl-CoA/CoA indicate that it also correlated with the biotransformation process. The main metabolic pathway operating during cell growth in the high cell-density membrane reactor was that related to isocitrate dehydrogenase (during start-up) and isocitrate lyase (during steady-state operation), together with phosphotransacetylase and acetyl-CoA synthetase. More importantly, the link between central carbon and L(-)-carnitine metabolism at the level of the ATP pool was also confirmed.     

抗坏血酸对酵母蔗糖酶的激活动力学研究

采用甲苯自溶法从鲜酵母中提取了蔗糖酶,并用乙醇分级及ＤＥＡＥ－纤维素柱层析进行了纯化,用ＰＡＧ凝胶电泳作了纯度鉴定,在ｐＨ５．０,３０℃条件下进行了酶反应,用双倒数作图法测出其Ｋｍ＝２．１×１０－２ｍｏｌ／Ｌ,Ｖｍａｘ＝０．２６（每分钟的光密度值）．在此系统中,加入不同浓度的抗坏血酸（Ｖｉｔ．Ｃ）,发现其具有激活作用并存在量效关系．双倒数作图显示：酶的表观Ｖｍａｘ（Ｖｐ）随抗坏血酸浓度的增加而增大,但其表观Ｋｍ（Ｋｐ）不变（Ｋｐ＝Ｋｍ）．经实验结果分析,推论出抗坏血酸激活作用的酶促反应方程式,并推导出反应速度公式     

金属螯合载体固定重组腈水解酶

以琼脂粉为基质制备金属螯合载体,并用于固定重组腈水解酶。研究发现:制备金属螯合载体最合适的金属离子为Zn2+。当Zn2+离子浓度0.3 mol/L、给酶量15.6 mg/g、固定化pH 8.0、固定化温度40℃时,制得的固定化酶活性最高。固定化酶最适反应温度为50℃、最适反应pH为7.0。当扁桃腈浓度为10 mmol/L、反应1 h时,固定化酶最大产率为0.041 mmol/(g·h);在反应12 h时,产物e.e.值可达到99%以上。固定化酶重复使用8次以后,酶活力仍保持在45%。     

Determination of MDMA and MDA in rat urine by semi-micro column HPLC-fluorescence detection with DBD-F and their monitoring after MDMA administration to rat.

A simultaneous semi-micro column HPLC method with fluorescence detection of abused drugs, such as 3,4-methylenedioxymethamphetamine (MDMA), 3,4-methylenedioxyamphetamine (MDA), amphetamine (AP) and methamphetamine (MP) in rat urine was examined by using 4-(N,N-dimethylaminosulphonyl)-7-fluoro-1,2,3-benzoxadiazole (DBD-F) as a labelling reagent and alpha-phenylethylamine as an internal standard (IS). A sample (50 microL) of rat urine was added to 5 microL IS and 100 microL 100 mmol/L borate buffer (pH 12) and extracted with 1.5 mL n-hexane. After evaporation, 50 microL 75 mmol/L borate buffer (pH 8.5) and 50 microL 20 mmol/L DBD-F in CH3CN were added to the residue and mixed well. The resultant solution was heated for 20 min at 80 degrees C and then cooled in an ice bath. A good separation of DBD-derivatives could be achieved within 45 min using a semi-micro ODS column with an eluent of CH3CN/CH3OH/10 mmol/L imidazole-HNO3 buffer (pH 7.0) (= 45:5:50, v/v/v %). The DBD derivatives were monitored at 565 nm with an excitation at 470 nm. The calibration curves showed good linearity (r = 0.997) with 0.5-15 ng/mL detection limits at a S/N ratio of 3. MDMA and MDA in rat urine could be monitored for 15 h after a single administration of MDMA to rat (2.0 mg/kg, i.p.). The concentrations for MDMA and MDA (n = 3) were 0.13-160.1 and 0.17-10.9 microg/mL, respectively.     

RP-HPLC测定红丝线提取物中紫蓝素的含量

建立了红丝线提取物中紫蓝素的测定方法。采用反相高效液相色谱法,色谱柱为ZORBAXXDB-C18(4.6mm×150mm,5μm);流动相:V(乙腈):V[75mmol/L乙酸铵+0.5mmol/LEGTA(pH7.0)]=8∶92;流速:1mL/min;检测波长590nm。紫蓝素的线性范围为2.5～50mg/L(r=0.9999),回收率97.9%～101.5%。该法简便、准确,重复性好,适用于测定红丝线提取物中紫蓝素的含量。     

Effect of hydraulic retention time on anaerobic hydrogenesis in CSTR

The objective of this work was to evaluate the production of hydrogen in a continuous system as a function of hydraulic retention time (HRT). The intermediates accumulated and other parameters of pH, oxidation-reduction potential were quantified. The heat treatment (103 degrees C for 24 h) of the compost from a cattle dung composting facility was able to select H2-producing spores; this product was used as a seed for continuous systems. The brewery waste was used as substrate. For the eight runs with combinations of five HRTs and four pHs, the results indicate that at pH=5.5, a maximum H2 production of 47% H2 concentration, 43 ml H2/g COD(added), and 3.1 l H2/l reactor d was achieved at HRT=18 h. Nevertheless, at HRT=18 h, pH 5.5 was also the optimum pH for the maximum H2 production among four pHs evaluated from 5 to 6.5. There was a significant accumulation of volatile acid and alcohols during the entire study.     

Estimating optimal profiles of genetic alterations using constraint-based models

Metabolic engineering involves application of recombinant DNA methods to manipulate metabolic networks to improve cellular properties. It is critical that the genetic alterations be performed in an optimal manner to maximize profit. In addition to the product yield, productivity consideration is also critical, especially for the production of bulk chemicals such as 1,3-propanediol. In this work, we demonstrate that it is suboptimal from the standpoint of productivity to induce genetic alteration at the start of the production process. A bi-level optimization scheme is formulated to determine the optimal temporal flux profile for the manipulated reaction. In the first case study, an optimal flux in the reaction catalyzed by glycerol kinase is determined to maximize the glycerol production at the end of a 6-h batch cultivation of Escherichia coli under aerobic conditions. The final glycerol concentration is 30% higher for the optimal flux profile compared with having an active flux during the entire batch. The effect of the mass transfer coefficient on the optimal profile and the glycerol concentration is also determined. In the second case study, the anaerobic batch fermentation of the ldh(-) strain of Escherichia coli is considered. The optimal flux in the acetate pathway is determined to maximize the final ethanol concentration. The optimal flux results in higher ethanol concentration (11.92 mmol L(-1)) compared to strains with no acetate flux (8.36 mmol L(-1)) and fully active acetate flux (6.22 mmol L(-1)). We also examine the effects of growth inhibition due to high ethanol concentrations and variations in final batch time on ethanol production.     

Morphology and physiology of an alpha-amylase producing strain of Aspergillus oryzae during batch cultivations

The microscopic morphology, that is, total hyphal length and total number of tips, has been characterized during batch cultivations of Aspergillus oryzae. The specific growth rate estimated by measuring the total hyphal length (mu(h)) corresponds well with the specific growth rate estimated from dry weight measurements during cultures grown as free hyphal elements. The average tip extension rate can be described with a saturation type kinetics with respect to the average total hyphal length, and the branching frequency is closely related to the total hyphal length. For the applied strain of A. oryzae, pellet formation occurs by coagulation of spores. The agglomeration process is pH dependent and pellets are formed at pH values higher than 5, whereas low pH (<3.5) results in growth as freely dispersed hyphal elements. The maximum specific growth rate has a broad pH optimum between 3 and 7, whereas the alpha-amylase production has a sharper maximum at about pH 6. During batch cultivation with pellets the growth is described well by the cube-root law when pellet fragmentation can be neglected. The kinetic parameter k in the cube-root law is derived from the growth kinetics with no mass transfer limitation, k = mu(h)/3. Based on an oxygen balance, the active growth layer in the pellet is estimated to be 200 to 325 mum and, consequently, up to 50% of the biomass is limited by oxygen for large pellets. Ethanol production (up to 1 g L(-1)) was observed during batch cultivations with pellets, suggesting that ethanol is produced in the oxygen limited part of the biomass. A constitutive, low alpha-amylase production was observed at high glucose concentration. The specific alpha-amylase production was significantly higher for filamentous growth than for pellets and oxygen appears to be necessary for production of alpha-amylase. (c) 1996 John Wiley & Sons, Inc.     

Continuous hydrogen production during fermentation of alpha-cellulose by the thermophillic bacterium Clostridium thermocellum

Continuous hydrogen (H2) production during fermentation of alpha-cellulose was established using the thermophillic, anaerobic bacterium Clostridium thermocellum ATCC 27405. The objectives of this work were to characterize growth of C. thermocellum, quantify H2 production and determine soluble end-product synthesis patterns during fermentation of a cellulosic substrate under continuous culture conditions. A 5 L working volume fermentor was established and growth experiments were maintained for over 3,000 h. Substrate concentrations were varied from 1 to 4 g/L and the feed was introduced with continuous nitrogen gas sparging to prevent clogging of the feed-line. The pH and temperature of the reactor were maintained at 7.0 and 600 degrees C, respectively, throughout the study. At concentrations above 4 g/L, the delivery of alpha-cellulose was impaired due to feed-line clogging and it became difficult to maintain a homogenous suspension. The highest total gas (H2 plus CO2) production rate, 56.6 mL L(-1) h(-1), was observed at a dilution rate of 0.042 h(-1) and substrate concentration of 4 g/L. Under these conditions, the H2 production rate was 5.06 mmol h(-1). Acetate and ethanol were the major soluble end-products, while lactate and formate were greatly reduced compared to production in batch cultures. Concentrations of all metabolites increased with increasing substrate concentration, with the exception of lactate. Despite a number of short-term electrical and mechanical failures during the testing period, the system recovered quickly, exhibiting substantial robustness. A carbon balance was completed to ensure that all end-products were accounted for, with final results indicating near 100% carbon recovery. This study shows that long-term, stable H2 production can be achieved during direct fermentation of an insoluble cellulosic substrate under continuous culture conditions.     

Sporulation of Clostridium cellulolyticum while grown in cellulose-batch and cellulose-fed continuous cultures on a mineral-salt based medium

Clostridium cellulolyticum sporulation was investigated during growth on cellulose fibers in a mineral-salt based medium which corresponds to conditions linked to its natural ecological niche. At steady state of the continuous cultures under limitation and with an excess of cellulose and/or ammonium, bacterial cells mainly sporulated at low dilution rates (D), at least 10% sporulation being observed at the lowest D tested. Increasing the cellulose concentration in the feed-medium reservoir increased the percentage of spores in the bioreactor. It appeared that the remaining undigested cellulose could serve as an exogenous carbon source supply at a continuous but limited rate throughout the sporulation process. In addition to the proportion of carbon and nitrogen, the influence of the environmental pH on spore formation was studied. In cellulose-fed continuous cultures at a constant D and a pH decreasing from 7.2 to 6.4, the percentage of spores increased to 14% at the lowest pH tested. When C. cellulolyticum was grown in batch culture, the level of sporulation was dramatically higher in unregulated-pH fermentation compared to pH-controlled growth conditions at pH 7.2 since in the former it reached 45% within 5 days of cultivation. It then appeared that a low specific growth rate and a low environmental pH in the presence of an insoluble carbon substrate were the major factors inducing sporulation in C. cellulolyticum. Furthermore, since the spores adhere to the carbon substrate (the cellulose) the bacteria gain advantages when the environment allows germination thanks to the recovery of suitable growth conditions. By allowing the maintenance and the integrity of the bacteria in the microbiota, spore formation could then explain the successful survival of C. cellulolyticum in cellulosic anaerobic habitats where low environmental pH conditions are often found.     

L-抗坏血酸洛芬酯非水相酶促合成的动力学与热力学

对酶法合成L-抗坏血酸洛芬酯(芬维C酯)的反应动力学与热力学进行研究,确定了最有效的酶促反应环境。合成布洛芬维C酯的最优条件:转速200r/min,温度65℃,加酶量5%(以底物的质量分数计),底物浓度1mol/L,平衡所需时间66h,平衡时产物质量分数为19.07%;合成酮洛芬维C酯的最优条件:200r/min,60℃,加酶量7.5%,底物浓度600mmol/L,平衡时间132h,产物质量分数为10.63%;合成氟比洛芬维C酯的最优条件:200r/min,65℃,加酶量5%,底物浓度400mmol/L,平衡时间144h,产物质量分数为6.76%。对底物进行了比较,得到了各自的动力学与热力学参数。布洛芬米氏常数为0.101μmol/L,vmax=32.68μmol/(min.g),热力学平衡常数为0.166;酮洛芬的分别为0.144μmol/L,12.97μmol/(min.g),0.091;氟比洛芬的分别为0.185μmol/L,9.35μmol/(min.g),0.055。     

Changes in Acid-base balance during simulated soccer match play

This study evaluated changes in markers of acid-base balance that occurred during simulated soccer match play. Sixteen academy soccer players participated in a soccer match simulation that consisted of 90 minutes of soccer-specific exercise with skills throughout. Blood samples were obtained before exercise (preexercise), every 15 minutes during the simulation (15, 30, 45, 60, 75, and 90 minutes), and 10 minutes into the half-time break (half time). Blood lactate concentrations were elevated throughout exercise (preexercise: 1.5 ± 0.12 mmol·L; 90 minutes: 6.1 ± 0.7 mmol·L, time effect: p < 0.01, partial-eta = 0.740). Relative to preexercise values, actual blood bicarbonate (preexercise: 28.02 ± 0.92 mmol·L; 90 minutes: 21.73 ± 0.65 mmol·L, time effect = p < 0.01, partial-eta = 0.680), standard blood bicarbonate (preexercise: 25.97 ± 0.43 mmol·L; 90 minutes: 22.87 ± 0.31 mmol·L, time effect = p < 0.01, partial-eta = 0.667), base excess (preexercise: 2.40 ± 0.54 mmol·L, 90 minutes: -1.57 ± 0.39 mmol·L, time effect = p < 0.01, partial-eta = 0.664), and pH (preexercise: 7.44 ± 0.01 units; 90 minutes: 7.39 ± 0.01 units, time effect = p < 0.01, partial-eta = 0.542) were depressed throughout the exercise. Interestingly, blood bicarbonate, base excess, and pH recovered at half time (p > 0.05). This is the first study to provide data concerning the acid-base balance of familiarized soccer players during exercise that simulates soccer match play. These findings suggest that (a) blood pH is reduced during soccer-specific exercise and (b) although buffering capacity is reduced throughout exercise, it returns to normal during half time. Further research is warranted to develop interventions that can maintain acid-base balance throughout the full duration of a soccer match.