嗜酸氧化亚铁硫杆菌生长动力学

在确定二价铁离子为A.f生长过程中惟一限制性底物条件下,通过考察初始亚铁离子浓度、初始pH值两种影响亚铁离子氧化代谢的主要因素来研究细菌的生长特性,得到以限制性底物亚铁离子浓度为表征的细菌生长曲线。利用基于Monod方程建立的细菌生长动力学方程模型,采用Matlab软件中的Gauss-Newton算法确定了在不同条件下细菌生长动力学参数,包括最大比生长速率μm、Monod常数K及Ro,推导出了不同条件下A.f对数期以底物Fe(Ⅱ)浓度为表征的生长动力学方程。     

沼泽红假单胞菌乙酸光合放氢研究

依据光合细菌生长代谢特性和有机废水降解主要产物类型,11种有机物被用于沼泽红假单胞菌（Rhodopseudomonas palustris）Z菌株的光合产氢研究,其中,乙酸反应体系产氢活性最高。在此基础上,研究了该菌株的生长与产氢动力学行为,探求了影响该菌株光合放氢的主要限制性影响因素。结果表明,该菌株产氢与生长部分相关。种子培养基和菌龄对产氢活性有明显影响。细胞最适产氢和生长所需要的光照强度和温度基本一致。当种子来源于硫酸铵高菌龄预培养物或谷氨酸钠对数期预培养物时,该菌株产氢活性显著增加,产氢延滞期明显缩短。氧浓度和接种量对产氢活性也有显著影响。供氢体和氮源浓度直接决定细胞的生长与光放氢活性。在低于70 mmol/L乙酸钠和15 mmol/L谷氨酸钠时,产氢活性随底物浓度的增加而增强。谷氨酸钠浓度高于15mmol/L时,由于游离NH₄⁺的出现,产氢活性受到抑制,但却明显刺激细胞的生长。在标准状况下,该菌株的最大产氢速率可达19.4 mL·L^-1·h^-1。     

氮源NH4Cl浓度对粪产碱杆菌发酵生产热凝胶的影响

研究了利用粪产碱杆菌(Alcaligenes faecalis)发酵生产热凝胶的发酵条件,氮源是菌体生长的限制性底物,单纯地提高初始底物(氮源)浓度并不一定能促进细菌的生长和产物的合成.在分批发酵过程中,底物消耗导致培养环境pH的改变也是影响细菌进一步生长和产物合成的重要因素.通过增加培养基中初始氯化铵的浓度并同时控制发酵过程的pH条件,得到了较高的菌体浓度,热凝胶的合成水平也得到了显提高.当培养基中NH4Cl浓度提高到3.6g/L时,菌体浓度达到7.2g/L,热凝胶合成的产量可达30.5g/L,比原来NH4Cl浓度为1.1g/L时提高了51.7%.提高菌体浓度意味着需要提高溶氧水平来满足细菌的生长和代谢.初始氮源NH4Cl浓度的增加虽然能使菌体浓度得到提高,但发酵过程对溶氧的需求也相应增加,需要提高搅拌转速和通风以增加供氧水平.但高搅拌速率产生的高剪切力对热凝胶的凝胶性能将产生破坏作用,因此在发酵过程中需要综合考虑细菌培养密度对合成热凝胶产量和质量的影响.     

初始底物浓度及pH对丁酸梭菌T4发酵木糖产氢的影响

本研究采用间歇培养方式对丁酸梭菌T4发酵木糖进行产氢研究,考察初始pH和初始底物浓度对其产氢特性的影响。结果表明,菌株T4在初始pH5.0～8.5及初始底物浓度5～40g/L时均可以产氢,其累积产氢量和最大比产氢速率随着pH及底物浓度的增加均呈现先增加后减少的趋势。在pH6.5和底物浓度20g/L时,比产氢速率和累积产氢量达到最大,分别为4.26L/L和18.86mmol-H2/hg-DCW,而后随着pH或者底物浓度的增加二者均呈现减少的趋势;在pH6.5和底物浓度15g/L时,得到最大值比产氢量为2.17mol/mol-木糖。而在不同的pH下,发酵产生的液态产物主要是乙酸和丁酸,其中在pH小于6.0时,有少量的丙酸生成,而在pH大于6.0时,则有乙醇生成。     

嗜酸氧化亚铁硫杆菌生长动力学方程的应用

基于Monod模型推导出了A．f的生长动力学方程模型,采用Gauss-Newton算法确定了在不同初始条件下细菌生长的动力学参数,即最大比生长速率‰、Monod常数K及R0。通过在不同初始条件下细菌生长特性的研究,得到了相应初始生长条件下以限制性底物亚铁离子浓度为表征的生长动力学方程,理论上揭示了动力学参数变化对细菌生长的影响规律,其中生长动力学方程的数值模拟与实验数据相吻合。     

氮源NH4Cl浓度对粪产碱杆菌发酵生产热凝胶的影响

研究了利用粪产碱杆菌 (Alcaligenesfaecalis)发酵生产热凝胶的发酵条件 ,氮源是菌体生长的限制性底物 ,单纯地提高初始底物 (氮源 )浓度并不一定能促进细菌的生长和产物的合成。在分批发酵过程中 ,底物消耗导致培养环境pH的改变也是影响细菌进一步生长和产物合成的重要因素。通过增加培养基中初始氯化铵的浓度并同时控制发酵过程的pH条件 ,得到了较高的菌体浓度 ,热凝胶的合成水平也得到了显著提高。当培养基中NH₄Cl浓度提高到3.6g/L时 ,菌体浓度达到72g/L ,热凝胶合成的产量可达 30.5g L ,比原来NH₄Cl浓度为11g L时提高了51.7%。提高菌体浓度意味着需要提高溶氧水平来满足细菌的生长和代谢。初始氮源NH₄Cl浓度的增加虽然能使菌体浓度得到提高 ,但发酵过程对溶氧的需求也相应增加 ,需要提高搅拌转速和通风以增加供氧水平。但高搅拌速率产生的高剪切力对热凝胶的凝胶性能将产生破坏作用 ,因此在发酵过程中需要综合考虑细菌培养密度对合成热凝胶产量和质量的影响。     

玉米芯发酵法生物制氢

在批式培养试验中, 以牛粪堆肥为天然产氢菌源, 玉米芯为底物, 通过厌氧发酵生产氢气。系统考察了底物预处理条件、初始pH值和底物浓度对玉米芯产氢能力的影响。在初始pH 8.0, 1.0%盐酸预处理底物30 min, 底物浓度10 g/L的最佳产氢条件下, 玉米芯最大产氢能力〔每克TVS（总挥发性固体物）产氢量〕和最大产氢速率（每克TVS每小时产氢量）分别为107.9 mL /g、4.20 mL/g·h-1。玉米芯经酸预处理后半纤维素含量由42.2%下降至3.0%, 而酸预处理的玉米芯产氢前后纤维素、半纤维素和木质素含量只有少量变化。产氢菌主要用酸预处理产生的可溶性糖产氢, 故底物的酸预处理对玉米芯的发酵产氢非常重要。用傅里叶变换红外光谱(FTIR)分析显示酸预处理和产氢过程中玉米芯的特征峰发生变化, 酸预处理过程降解了底物纤维素的无定形区和半纤维素, 产氢微生物对纤维素的结晶区有破坏作用。     

玉米芯发酵法生物制氢

在批式培养试验中, 以牛粪堆肥为天然产氢菌源, 玉米芯为底物, 通过厌氧发酵生产氢气。系统考察了底物预处理条件、初始pH值和底物浓度对玉米芯产氢能力的影响。在初始pH 8.0, 1.0%盐酸预处理底物30 min, 底物浓度10 g/L的最佳产氢条件下, 玉米芯最大产氢能力〔每克TVS（总挥发性固体物）产氢量〕和最大产氢速率（每克TVS每小时产氢量）分别为107.9 mL /g、4.20 mL/g·h-1。玉米芯经酸预处理后半纤维素含量由42.2%下降至3.0%, 而酸预处理的玉米芯产氢前后纤维素、半纤维素和木质素含量只有少量变化。产氢菌主要用酸预处理产生的可溶性糖产氢, 故底物的酸预处理对玉米芯的发酵产氢非常重要。用傅里叶变换红外光谱(FTIR)分析显示酸预处理和产氢过程中玉米芯的特征峰发生变化, 酸预处理过程降解了底物纤维素的无定形区和半纤维素, 产氢微生物对纤维素的结晶区有破坏作用。     

营养及水力条件影响光合细菌生物膜生长特性实验

对平板式生物膜反应器内,流量及底物浓度范围分别为37.8~1080ml/h、0.05~10g/L的不同生长条件下光合产氢细菌生物膜生长特性进行了实验研究,讨论了不同水力及营养条件对沼泽红假单胞菌生物膜表面覆盖率、膜厚、干重和密度的影响。实验结果表明,不同水力及营养条件对生物膜生长速率及结构具有重要影响。在相同的时间间隔内,在高流速条件下光合细菌菌落生长较快,但过高的液体流速会导致部分生物膜脱落;高流速条件易使生物膜形成薄而致密的结构。光合细菌生物膜在循环液底物浓度较高时生长较快,密度也最高;而贫营养条件可以促成结构疏松生物膜在固液界面的形成,这种生物膜结构有利于微生物在低底物浓度条件下底物在生物膜内的传输。     

啤酒废水的厌氧发酵产氢

对经热处理后的厌氧污泥利用啤酒废水厌氧产氢的影响因素（温度、初始pH值和有机物浓度）进行了研究。结果表明,温度与初始pH值对厌氧产氢过程均有显著影响。最佳温度为35℃,此时,比产氢速率、氢气产率、VFA含量与总糖降解率均达到最大,分别为10.16mL/g-VSS.h、0.1673mL/mg.COD、4640.0mg/L和95.20%。最适初始pH值为6.0～7.0,在此范围内氢气产率、VFA含量、总糖降解率均可获得最大值。一个半经验模型适用于描述初始pH值与氢气产率之间的相互关系。在35℃、初始pH值6.5的条件下,有机物浓度COD1000mg/L～2000mg/L时,总糖降解率与VFA产率均获得最大值。底物抑制模型分析结果显示COD1587mg/L时,氢气产率（0.1935mL/mg.COD）达到最大。     

谷氨酰胺对微囊化重组CHO细胞生长代谢及内皮抑素表达的影响

微囊化技术是一种有发展潜力的生物技术,在细胞移植和药物控释等方面具有广泛的应用。然而由于目前微囊化细胞规模化培养技术还不成熟,阻碍了其在临床治疗中的推广与应用。为了了解微囊化重组CHO细胞的生长代谢特性为今后规模化培养优化提供技术参考,考察了主要氮源物质谷氨酰胺对微囊化重组CHO细胞生长代谢及内皮抑素表达的影响。结果显示:当谷氨酰胺起始浓度从2.69mmolL增加到9.05mmolL时最大活细胞密度并没有增高,细胞增殖没有显著差异。当谷氨酰胺起始浓度较低(2.69mmolL)时,葡萄糖的比消耗速率较大;当谷氨酰胺起始浓度增高时(7.91mmolL～9.05mmolL)葡萄糖和谷氨酰胺的比消耗速率增大,但细胞对葡萄糖和谷氨酰胺的利用率降低。谷氨酰胺对产物表达有显著影响,起始浓度为4.97mmolL时的内皮抑素累积浓度最高,达546.36ngmL,过低和过高谷氨酰胺起始浓度下内皮抑素的累积浓度均较低。     

Effects of flow rate and substrate concentration on the formation and H2 production of photosynthetic bacterial biofilms

Photosynthetic bacteria (PSB), Rhodopseudomonas palustris CQK 01, were immobilized on the surface of a thin glass slide in a lab-scale flat panel photobioreactor under different flow rates and substrate concentrations. The morphology, dry weight and thickness of the mature PSB biofilms were determined to reveal the relationship between biofilm formation and hydrogen production performance. The mature biofilm formed at a low flow rate and a high substrate concentration showed a looser structure, these structures of the mature biofilm then affected the H₂ production performance of the bioreactor during mature stage. The biofilm formed at a flow rate of 228 ml/h and a substrate concentration of 60 mmol/l exhibited the highest dry weight and optimally porous structure, which is beneficial not only for hydrogen removal from the biofilm but also glucose diffusion into the biofilm, thus significantly boosting the photo-hydrogen production performance.     

Effect of some environmental parameters on fermentative hydrogen production by Enterobacter cloacae DM11

Fermentative hydrogen production was carried out by Enterobacter cloacae DM11, using glucose as the substrate. The effects of initial substrate concentration, initial medium pH, and temperature were investigated. Results showed that at an initial glucose concentration of 1.0% (m/v), the molar yield of hydrogen was 3.31 mol (mol glucose)(-1). However, at higher initial glucose concentration, both the rate and cumulative volume of hydrogen production decreased. The pH of 6.5 +/- 0.2 at a temperature of 37 degrees C was found most suitable with respect to maximum rate of production of hydrogen in batch fermentation. Activation enthalpies of fermentation and that of thermal deactivation of the present process were estimated following a modified Arrhenius equation. The values were 47.34 and 118.67 kJ mol(-1) K(-1), respectively. The effect of the addition of Fe(2+) on hydrogen production was also studied. It revealed that the presence of iron (Fe(2+)) in the media up to a concentration of 20 mg L(-1) had a marginal enhancing effect on total hydrogen production. A simple model developed from the modified Gompertz equation was applied to estimate the hydrogen production potential, production rate, and lag-phase time in a batch process, based on the cumulative hydrogen production curves, using the software program Curve Expert 1.3.     

甲醇抑制时重组毕赤酵母发酵的特性研究

本文对毕赤酵母进行了恒化培养研究。以甲醇为唯一碳源时,在稀释率较低时(D<0.048 h^-1),连续培养系统操作很稳定。但在稀释率高时(D>0.048h^-1),连续培养系统的定态点不止一个,实验不能维持,故采用比生长速率恒定的分批流加培养进行研究。结果表明,毕赤酵母的生长符合Andrew普遍化底物抑制模型。综合考虑水蛭素的生成、底物的消耗,在生产中维持甲醇浓度为限制性浓度(0.5 g/L),且维持比生长速率为0.02 h^-1时,水蛭素Hir65的比生成速率达到最大值0.2 mg/(g·h)且甲醇的比消耗速率为0.04 g/(g·h)。     

Influence of Ni(2+) concentration on biohydrogen production

In this paper, the effect of Ni(2+) concentration ranging from 0 to 50mg/L on fermentative hydrogen production by mixed cultures was investigated in batch test. The results showed that at 35 degrees C and initial pH 7.0, Ni(2+) was able to enhance the hydrogen production rate with increasing Ni(2+) concentration from 0 to 0.2mg/L, and enhance the hydrogen production potential and hydrogen yield with increasing Ni(2+) concentration from 0 to 0.1mg/L. The maximum hydrogen production potential of 288.6mL and the maximum hydrogen yield of 296.1mL/g glucose were obtained at the Ni(2+) concentration of 0.1mg/L. In all tests, the major soluble metabolites produced by mixed cultures were ethanol, acetic acid and butyric acid, without propionic acid. Ni(2+) had little effect on the substrate degradation efficiency with increasing concentration from 0 to 50mg/L. Ni(2+) was able to enhance the biomass production yield with increasing Ni(2+) concentration from 0 to 0.1mg/L. The maximum biomass production yield of 232.5mg/g glucose was obtained at the Ni(2+) concentration of 0.1mg/L. In all tests, the final pH after fermentative hydrogen production was lower than the initial pH.     

Fedbatch operation using Clostridium acetobutylicum suspension culture as biocatalyst for enhancing hydrogen production

We demonstrated the feasibility of fedbatch operation using Clostridium acetobutylicum suspension culture as a biocatalyst for the continuous production of hydrogen. The optimum operating pH and temperature of the current cultivation system for hydrogen production were pH 6.0 and 37 degrees C, respectively. The volumetric loading of the bioreactor for hydrogen production can be as high as 650 mmol hydrogen/L culture with a yield at approximately 2.0 mol hydrogen/mol glucose. Acetate and butyrate made up approximately 80% of the total metabolites. The inhibitory effect from the two metabolites on the hydrogen production process was investigated. Butyrate at a concentration higher than 13 g/L significantly inhibited not only cell growth but also hydrogen production (i.e., specific hydrogen production rate). Acetate appears to be less toxic than butyrate to the hydrogen production process. While significantly inhibiting cell growth, acetate hardly affected hydrogen production. Finally, the factors limiting cultivation performance were discussed and possible strategies for enhancing the production of hydrogen were proposed.     

Effect of ammonia concentration on fermentative hydrogen production by mixed cultures

The effect of ammonia concentration ranging from 0 to 10 g N/L on fermentative hydrogen production by mixed cultures was investigated in batch tests using glucose as substrate at 35 degrees C and initial pH 7.0. The experimental results showed that during the fermentative hydrogen production, the substrate degradation efficiency increased with increasing ammonia concentration from 0 to 0.01 g N/L. The hydrogen production potential, hydrogen yield and average hydrogen production rate increased with increasing ammonia concentration from 0 to 0.1g N/L. The maximum hydrogen production potential of 291.4 mL, maximum hydrogen yield of 298.8 mL/g glucose and maximum average hydrogen production rate of 8.5 mL/h were all obtained at the ammonia concentration of 0.1g N/L.     

耐铵型产琥珀酸放线杆菌的选育及铵离子对其生长代谢的影响

经硫酸二乙酯(DES)诱变,在含61～242mmol/LNH4+梯度平板中,筛选到一株耐铵型突变株YZ25,该菌株在含121mmol/LNH4+发酵培养基中,琥珀酸产量达32.68g/L,转化率为65.4%,比出发菌提高了180.5%。进一步考察了不同形态铵盐对YZ25生长的影响,结果表明添加少量铵盐能够提高突变菌的生长速率,但当超过一定量后菌株生长受到抑制,不同铵盐对菌株的抑制程度不同,硫酸铵、碳酸氢铵、氯化铵和硝酸铵对突变株YZ25的半抑制浓度分别为:215mmol/L、265mmol/L、235mmol/L、210mmol/L。为了考察铵离子对YZ25发酵产琥珀酸的影响过程,在3.0L发酵罐以氨水作为pH的调控剂发酵,结果表明在稳定期前菌株生长基本不受铵离子抑制,生物量能够达到正常水平,但是进入稳定期后铵离子抑制作用越来越明显,导致菌株生长提前结束,耗糖不完全,产酸受阻。最后结合产琥珀酸放线杆菌Actinobacillus succinogenes代谢途径分析了铵离子对菌株抑制作用的机理。