地衣芽孢杆菌产生碱性蛋白酶的动力学研究

应用自动控制发酵设备,首先进行分批发酵试验摸索了地衣芽孢杆菌2709生长与代谢的基本规律。然后采用补料分批发酵方法限制生长基质浓度,测定了一系列(S_I,μ_I)、(μ_j,q_pj)数据,获得K_S、μ_max、α、β等参数的值,并且推导出了细胞生长与产物合成的动力学公式,从而证明了用Monod方程描述地衣芽孢杆菌2709生长速率与基质浓度关系的合理性和合成碱性蛋白酶的发酵属于生长部分关联型。     

蜜环菌胞外漆酶的合成、纯化及性质研究

研究了蜜环菌胞外漆酶合成条件和酶学性质。实验表明,培养基初始pH5.5、培养温度25℃有利于菌株产酶;与麦芽糖、山梨糖和半乳糖相比,纤维二糖和棉子糖作为碳源时漆酶产量更高;有机氮源比无机氮源有利于漆酶合成。泥炭提取液可显著诱导漆酶生成,当其含量为50%时,菌株漆酶最高产量是对照组的7倍。在蜜环菌发酵上清液中检测到3个漆酶同功酶组分,其主要活性（约占75%）组份漆酶A经 (NH₄)₂SO₄沉淀、制备级PAGE电泳和阴离子交换柱层析被分离纯化至电泳均一,SDSPAGE法测得酶亚基分子量59kD,凝胶过滤色谱法测定活性酶分子量58kD。纯化的漆酶A等电点pI为4.0,氧化愈创木酚的最适反应pH为5.6,最适温度为60℃,在60℃和65℃时半衰期分别为45min和36.8min,在pH5.2～7.2范围内稳定性较好。100mmol/L Cl^-对该酶有显著抑制作用,1mmol/L SO^2-₄ 对漆酶有激活作用,1mmol/L NaN₃可完全抑制酶活性,10 mmol/L EDTA对漆酶活没有明显影响,1mmol/L Cu²⁺对漆酶有激活作用。以愈创木酚为底物时,测得酶的K_m=1.026mmol/L,V_max=5μmol/(min·mg);以ABTS为底物时,测得其K_m=0.22mmol/L,V_max=69μmol/(min·mg)。     

分批发酵动力学模型参数的估算

本文基于通用的发酵动力学数学模型,导出了用于描述分批发酵特征的解析解。藉助于由FORTRAN－77编写的POWELL优化算法,以赖氨酸分批发酵为倒^［5］,一举估算出该解析解中所有的发酵动力学参数;μ_max、K_s、α、β、Y_G、Y_p,及m。结果表明t(1)用模型所得到的计算值与实测值具有较好的一致性,(2)赖氨酸合成速度取决于微生物的生长速度及浓度。     

热带假丝酵母细胞内pH的测定及其与生长代谢活性的关系

应用荧光探针5(6)-双醋酸羧基荧光素 (Carboxyfluorescein diacetate) 测定了产长链二元酸热带假丝酵母 (Candida tropicalis) 细胞内pH (pHi) 值,确定了该探针载入C. tropicalis细胞的适宜条件。用摇瓶培养C. tropicalis细胞,考察了细胞外pH和生长碳源对pH_I的影响,实验结果表明：细胞外pH对pH_I略有影响,而生长碳源对pH_I的影响略为明显。利用5L发酵罐进一步研究了细胞生长代谢活性与pHi的关系,结果表明：细胞比生长速率、CO₂比生产速率和葡萄糖比消耗速率与pHi变化密切相关,pH_I的增加伴随着细胞生长活力的增加,反之亦然。在pH6.0条件下用葡萄糖和醋酸钠共作碳源培养C. tropicalis细胞时,测得的pH_I值维持在5.72～6.15范围内。     

固定化纤维二糖酶的研究

黑曲霉（Aspergillus niger LORRE 012）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38 d,耐热性和适宜的pH范围均比固定化前有所增加,其K_m和V_max值分别为6.01 mmol/L和7.06 mmol/(min·L)。利用固定化纤维二糖酶重复分批酶解10 g/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0.4 h^-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（Trichoderma reesei）纤维素酶降解,酶解得率为69.5%;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53.6%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。     

聚球藻7002在光生物反应器中的光自养培养

通过对聚球藻7002在光生物反应器中的培养,研究了光强在聚球藻7002培养液中的衰减规律,得到了培养过程光强随藻细胞浓度和光程距离变化的关系式,即I=I₀exp［-(-0.0239+0.0777OD₇₅₀)·L］。并对培养过程特性及培养温度、外加CO₂浓度和光照强度对藻细胞生长的影响进行了较为详细的研究,得到了反应器中较为适宜的聚球藻7002的培养条件,藻细胞培养密度达到3.4g/L(干重),体积产率达到0.57g/(L·d)的较高水平。     

蜗牛酶中一种人参皂苷Rb1水解酶的分离纯化

通过DEAE-Sepharose离子交换分段层析,DEAE-Sepharose离子交换梯度层析和Sephadex G100凝胶过滤层析三种方法的联用从中华白玉蜗牛消化酶中分离出一种人参皂苷Rb1水解酶。分离后该酶在SDS-PAGE上呈单一蛋白质条带。应用SDS-PAGE和凝胶过滤层析对分子量的测定,提示该酶是由4个分子量为110～115 kD的相同亚基组成的同源四聚体。Rb1为底物的动力学参数K_m和V_max分别为0.790 mmol/L和10.192 μmol/min/mg。该酶对人参皂苷Rb₁糖键进行有选择的水解,可水解人参皂苷Rb₁C₂₀位的一个糖苷键生成人参皂苷Rd。     

纤维载体固定化红螺菌反应器处理发酵废液及其动力学模型

在充填软性纤维材料的玻璃柱式反应器中,利用Rhodopseudomonas palustris Y6光合细菌(PSB)连续处理发酵废液。建立了该处理系统动力学模型。计算出模型参数t K_s=45．56mg／m1,μm=0．224h^-1。模型理论曲线与实验值较吻合。研究得出较适合的稀释率Dopt为o．129^-1’,此时COD去除能力最大为1686．Oppm COD／h。本文为纤维载体固定化PSB处理有机废水提供了一些放大操作依据。     

苯酚降解菌的筛选及其降解特性的初步研究

从某印染厂下水道的污泥中分离到一株能高效降解苯酚的菌株ph₁₆,经初步鉴定为微球菌属 (Micrococcussp )。该菌株最高可耐受 1.5g L左右的苯酚 ,对苯酚降解最适条件为pH7.0 ,温度 35℃ ,苯酚浓度为1.0g/L ,时间为 36h,降解率可达 99.6 %。试验还表明Hg⁺ 、Co²⁺ 、Ag²⁺ 等重金属离子对该菌株降解苯酚能力有不同程度的抑制作用。并对其降解动力学作了初步探讨。     

马肝醇脱氢酶催化有机硅酮不对称还原反应动力学

探讨了马肝醇脱氢酶(HLADH)催化三甲基硅乙酮及其碳结构类似物不对称还原反应动力学.结果表明,在酶浓度低于150 mg/L时,底物浓度与反应初速度的关系符合米氏动力学方程;HLADH催化三甲基硅乙酮不对称还原反应的K_m、v_max和E_a分别为2.67 mmol/L、0.118 mmol/(L·min·mg)和37 kJ/mol, 其碳结构类似物的相应值分别为3.56 mmol/L、0.084 mmol/(L·min·mg)和61 kJ/mol.     

Is the naphthalene sulfonate H-acid biodegradable in mixed microbial cultures under aerobic conditions?

Synthetically prepared wastewater originating from the H-acid (4-Amino-5-hydroxy-2,7-naphthalene disulfonic acid) manufacturing process was subjected to respirometric analysis for evaluating the level of achievable biodegradation in the presence of this commercially important azo dye precursor. For this purpose, H-acid was mixed with synthetic substrate having the same characteristics as sewage at a concentration and composition being typical for H-acid manufacturing wastewater. Experimental results indicated that H-acid was not biodegradable under activated sludge treatment conditions even after prolonged acclimation periods. The results were also confirmed by model evaluation of oxygen uptake rate profiles. H-acid also did not inhibit the biodegradation of synthetic sewage but accumulated as soluble inert COD in the treated wastewater.     

Continuous anaerobic treatment of autoxidized bark extracts in laboratory-scale columns

Debarking wastewaters of the forest industry contain high concentrations of tannins that are inhibitory to methane bacteria. The tannins can be polymerized to nontoxic colored compounds by the applications of an autoxidation pretreatment, enabling the anaerobic treatment of easily biodegradable components in the wastewater. The continuous anaerobic treatment of untreated and autoxidized pine bark extract was studied in laboratory-scale columns packed with a granular sludge bed. The autoxidation doubled the conversion efficiency of bark extract COD to methane (from 19 to 40%). After 5 months of operation, anaerobic treatment of the autoxidized extracts was feasible at high influent concentrations (14 g COD/L) and loading rates (26 g biodegradable COD/L . d) with 98% elimination of the biodegradable fraction. The detoxification pretreatment polymerized the toxic tannins to poorly biodegradable high molecular weight tannins and humic compounds which were not eliminated during anaerobic treatment. Although the original tannins of the untreated extract were eliminated by 60%, they were not biodegraded to volatile fatty acids and methane but instead were transformed to phenolic degradation intermediates (phenol, p-cresol, 3-phenyl-propionate, and carboxycyclohexane). Therefore, the autoxidation pretreatment did not decrease the content of readily biodegradable substrates which accounted for 53% of the extract COD. The recalcitrant COD expected in the effluents of reactors treating autoxidized debarking waste-water can be effectively separated by calcium precipitation prior to anaerobic treatment.     

Biodegradation kinetics of stored wastewater substrates by a mixed microbial culture

The anaerobic accumulation of several organic pollutants from industrial wastewaters, as storage substrates, and their subsequent aerobic biodegradation using a wastewater treatment mixed microbial culture for biological nutrient removal has been studied. The amount and the kinetics of substrate accumulation in the anaerobic stage depended on the characteristics of the wastewater fed to the anaerobic stage. Depending on the substrate used, levels of between 27 and 86% of storage polymers were accumulated with respect to the level obtained on feeding with acetate. The biodegradation kinetics were studied by modelling respirometry results. During the aerobic stage, oxygen-consumption data obtained in the respirometric tests were fitted to a model using a non-linear fitting estimation method. The simulation data obtained correlated well with the experimental oxygen-consumption data. The estimated kinetic parameters obtained indicate that each storage polymer was degraded at a different rate. However, the values obtained for the storage polymer half-saturation coefficient, K_S: 16 mg COD l⁻¹, and for the coefficient for endogenous respiration, b: 0.008 h⁻¹, were similar in all the experiments. The results indicate that each substrate produces the synthesis of a specific storage polymer that is degraded at a different rate.     

Kinetics and modeling of autotrophic thiocyanate biodegradation

The biokinetic parameters for autotrophic systems are difficult to obtain and are often mistakenly determined because the size of the autotrophic population in mixed (i.e., heterotrophic and autotrophic) cultures cannot be accurately estimated. This article presents a systematic approach, combining bioenergetic calculations and experimental data, to obtain values of the biokinetic parameters pertinent to the aerobic, autotrophic biodegradation of thiocyanate. Nonlinear regression techniques were employed using both initial thiocyanate utilization rate data and single thiocyanate depletion curves. Both types of data were necessary to overcome the problems arising from the linear nature of the substrate depletion curves and the high correlation of the biokinetic model parameters inherent in nonlinear regression analysis. The aerobic biodegradation of thiocyanate followed a substrate inhibition pattern that was successfully described by the Haldane-Andrews model. Although regression analysis did not yield unique biokinetic parameter estimates, the following parameter value ranges were obtained: maximum specific substrate utilization rate (k), 0.26 to 0.44 mg SCN-/mg biomass h; half-saturation coefficient (Ks), 2.3 to 7.1 mg SCN-/L; and inhibition coefficient (Ki), 28 to 109 mg SCN-/L. Based on the estimated biokinetic parameter values, a design and operation diagram was constructed that depicts the steady-state thiocyanate concentration as a function of solids retention time for a completely mixed, continuous-flow reactor.     

Fundamental Mechanisms of Phosphate Removal by Anaerobic/Aerobic Activated Sludge in Treating Municipal Wastewater

Acetate is thought to be an important substrate for phosphate removal in anaerobic/aerobic activated sludge (AS) processes. The acetate content in municipal wastewater is low, and the main organic compounds in such wastewater are particulate organic matters (POMs) that are converted to endogenous substrates in AS processes when municipal wastewater is introduced into AS reactors. The question which then arises is which substrate, acetate or POM, is important for phosphate removal in full‐scale AS plants. The rates of phosphate release and substrate uptake were determined using AS harvested from a full‐scale anaerobic/aerobic AS plant and also AS acclimated to peptone under alternate anaerobic and aerobic conditions for 26 months. The rate of phosphate release upon POM addition per AS concentration per unit of time was about 0.84 mg PO₄‐P/(g MLSS·h) irrespective of the wastewater quality. This value was about 0.05 in the case of AS acclimated to peptone for 26 months. When the AS concentration is 2.5 g/L and the mixed liquor retention time is 2 h in the anaerobic zone, about 4.2 mg/L PO₄‐P is released upon POM addition. Hence, phosphate can be removed from municipal wastewater using full‐scale AS plants running under these conditions.     

Dual substrate biodegradation of a nonionic surfactant and pentachlorophenol by Sphingomonas chlorophenolica RA2

The simultaneous biodegradation of the nonionic surfactant Tween 20 (Tw20) and pentachlorophenol (PCP) by Sphingomonas chlorophenolica sp. Strain RA2 (RA2) was measured. As a sole substrate, Tw20 biodegradation was best described by the Contois kinetic model. During concurrent biodegradation of Tw20 and PCP, the biodegradation rates of Tw20 were not significantly affected by 50 or 100 mg/L PCP, but were significantly inhibited by 500 mg/L PCP. Decreases in cell yield in the presence of PCP suggest that PCP was acting as an uncoupler. Cultures were pre-grown on PCP or Tw20 before degradation of PCP to evaluate enzyme induction effects, and long lags before PCP biodegradation after growth on Tw20 occurred. Although biokinetic models could accurately describe some of the data sets of RA2 growth and Tw20 and PCP degradation, finding a single set of kinetic parameters that predicted all dual substrate tests was not achieved. The complicating factors to modeling PCP and Tw20 interactions are described and may be more widely applicable to the biodegradation of toxic organic compounds in the presence of a biodegradable surfactant.     

Kinetic modeling of aerobic biodegradation of high oil and grease rendering wastewater

Batch scale activated sludge kinetic studies were undertaken for the treatment of pet food wastewater characterized by oil and grease concentrations of up to 21,500 mg/L, COD and BOD concentrations of 75,000 and 60,000 mg/L, respectively as well as effluent from the batch dissolved air flotation (DAF) system. The conducted kinetics studies showed that Haldane Model fit the substrates and biomass data better than Monod model in DAF-pretreated wastewater, while the modified hydrolysis Monod model better fit the raw wastewater kinetic data. For the DAF pretreated batches, Haldane Model kinetic coefficients k, K(S), Y and Ki values of 1.28-5.35 g COD/g VSS-d, 17,833-23,477 mg/L, 0.13-0.41 mg VSS/mg COD and 48,168 mg/L, respectively were obtained reflecting the slow biodegradation rate. Modified hydrolysis Monod model kinetic constants for the raw wastewater i.e., k, K(S), Y, and K(H) varied from 1-1.3 g COD/g VSS-d, 5580-5600 mg COD/l, 0.08-0.85 mg VSS/mg COD, and 0.21-0.66 d(-1), respectively.     

Saponification of fatty slaughterhouse wastes for enhancing anaerobic biodegradability

The thermochemical pretreatment by saponification of two kinds of fatty slaughterhouse waste – aeroflotation fats and flesh fats from animal carcasses – was studied in order to improve the waste’s anaerobic degradation. The effect of an easily biodegradable compound, ethanol, on raw waste biodegradation was also examined. The aims of the study were to enhance the methanisation of fatty waste and also to show a link between biodegradability and bio-availability. The anaerobic digestion of raw waste, saponified waste and waste with a co-substrate was carried out in batch mode under mesophilic and thermophilic conditions.     

Mesophilic and thermophilic activated sludge post treatment of anaerobic effluent. Sludge and wastewater characterisation using batch experiments

Anaerobic pretreated paper process water was characterized interms of readily biodegradable, slowly biodegradable, very slowly biodegradable and inert wastewaterfractions under mesophilic and thermophilic conditions. The anaerobic pretreated paper process water containeda relatively high amount of slowly biodegradable components and few easily biodegradable componentsas indicated by the ratio of short term BOD over the BOD5. Wastewater readily biodegradable COD, determinedas short term BOD, was almost similar when measured under both temperature conditions. Fractions ofslowly biodegradable COD and inert COD of the same wastewater were found to depend on the type of biomassinvolved in the test. Thermophilic aerobic biomass was not able to degrade the wastewater to the sameextent as the mesophilic biomass resulting in higher apparent inert COD levels. Furthermore, wastewater colloidalCOD did not flocculate under thermophilic conditions and was thus not removed from the liquid phase.     

Thermophilic anaerobic digestion of Lurgi coal gasification wastewater in a UASB reactor

Lurgi coal gasification wastewater (LCGW) is a refractory wastewater, whose anaerobic treatment has been a severe problem due to its toxicity and poor biodegradability. Using a mesophilic (35 ± 2 °C) reactor as a control, thermophilic anaerobic digestion (55 ± 2 °C) of LCGW was investigated in a UASB reactor. After 120 days of operation, the removal of COD and total phenols by the thermophilic reactor could reach 50-55% and 50-60% respectively, at an organic loading rate of 2.5 kg COD/(m³ d) and HRT of 24 h; the corresponding efficiencies were both only 20-30% in the mesophilic reactor. After thermophilic digestion, the wastewater concentrations of the aerobic effluent COD could reach below 200 mg/L compared with around 294 mg/L if mesophilic digestion was done and around 375 mg/L if sole aerobic pretreatment was done. The results suggested that thermophilic anaerobic digestion improved significantly both anaerobic and aerobic biodegradation of LCGW.