研究了氧气和震荡条件对酿酒酵母高浓度乙醇发酵的影响.结果表明,震荡是提高发酵液乙醇浓度和产率的最重要因素.与静止培养相比,在不通气情况下震荡培养使乙醇浓度提高了69%(从75.8 g L-1提高到128.1 g L-1),在通气条件下乙醇浓度提高了68.7%(从85.2 g L-1提高到to 143.8 g L-1).在最优条件下,两次补料,经54 h发酵,发酵液中乙醇浓度达到143.8 g L-1,乙醇产率与理论产率的比值为0.471 g/g(即92.20%).经分析,通气和震荡条件提高了发酵液中酿酒酵母的生物量和细胞活力.图5表1参12 相似文献
为提高重组大肠杆菌中顺丁烯二酸异构酶表达量,通过正交试验设计,对工程菌的生长条件和目的蛋白可溶表达条件进行优化.采用250 mL三角瓶中装有50 mL(Amp 100 mg L-1)的培养基,分别研究培养基中葡萄糖、蛋白胨、酵母浸粉的浓度,培养基pH值以及摇床转速、装液量、接种量等对蛋白可溶表达量的影响.确定顺丁烯二酸异构酶工程菌最优化培养基为:蛋白胨20 g L-1、酵母浸粉2.5 g L-1、K2HPO4·3H2O 3.0 g L-1、KH2PO4 1.5 g L-1、NaCl 6 g L-1、MgSO43 g L-1,培养基pH调至6.5.确定顺丁烯二酸异构酶工程菌可溶性表达最优条件为:37℃下培养至D600 nm值为1.0时,添加终浓度为0.05 mmol L-1的IPTG进行诱导,诱导温度37℃,摇床转速220 r min-1,装液量20%,接种量5%,诱导时长为6 h.利用BioFlo 415发酵罐以最优化的培养基和发酵条件对该工程菌进行了3批发酵实验,与摇瓶实验相比,顺丁烯二酸异构酶的表达量提高了近1.5倍,单位发酵液的酶活力由46 U mL-1发酵液提高到78 U mL-1发酵液.以上数据为顺丁烯二酸异构酶重组工程菌的中试发酵奠定了基础.图7表2参17 相似文献
The effect of dissolved oxygen (DO) concentration on nitrite accumulation was investigated in a pilot-scale pre-denitrification process at room temperature for 100 days. In the first 10 days, due to the instability of the system, the DO concentration fluctuated between 1.0 and 2.0 mg/L. In the next 14 days, the DO concentration was kept at 0.5 mg/L and nitrite accumulation occurred, with the average nitrite accumulation rate at 91%. From the 25th day, the DO concentration was increased to 2.0 mg/L to destroy the nitrite accumulation, but nitrite accumulation rate was still as high as 90%. From the 38th day the nitrite accumulation rate decreased to 15%–30% linearly. From the 50th day, DO concentration was decreased to 0.5 mg/L to resume nitrite accumulation. Until the 83rd day the nitrite accumulation rate began to increase to 80%. Dissolved oxygen was the main cause of nitrite accumulation, taking into account other factors such as pH, free ammonia concentration, temperature, and sludge retention time. Because of the different affinity for oxygen between nitrite oxidizing bacteria and ammonia oxidizing bacteria when DO concentration was kept at 0.5 mg/L, nitrite accumulation occurred. 相似文献
Polymerase chain reaction-denaturing gradient gel electrophoresis (PCR-DGGE) and microelectrode technology were employed to evaluate the Nitrous oxide (N2O) production in biological aerated filters (BAFs) under varied dissolved oxygen (DO) concentrations during treating wastewater under laboratory scale. The average yield of gasous N2O showed more than 4-fold increase when the DO levels were reduced from 6.0 to 2.0 mg?L–1, indicating that low DO may drive N2O generation. PCR-DGGE results revealed that Nitratifractor salsuginis were dominant and may be responsible for N2O emission from the BAFs system. While at a low DO concentration (2.0 mg?L–1), Flavobacterium urocaniciphilum might play a role. When DO concentration was the limiting factor (reduced from 6.0 to 2.0 mg?L–1) for nitrification, it reduced NO2--N oxidation as well as the total nitrification. The data from this study contribute to explain how N2O production changes in response to DO concentration, and may be helpful for reduction of N2O through regulation of DO levels.
● Dolomite-doped biochar/bentonite was synthesized for phosphate removal.● DO/BB exhibited a high phosphate adsorption capacity in complex water environments.● PVC membrane incorporated with DO/BB can capture low concentration phosphate.● Electrostatic interaction, complexation and precipitation are main mechanisms. The removal of phosphate from wastewater using traditional biological or precipitation methods is a huge challenge. The use of high-performance adsorbents has been shown to address this problem. In this study, a novel composite adsorbent, composed of dolomite-doped biochar and bentonite (DO/BB), was first synthesized via co-pyrolysis. The combination of initial phosphate concentration of 100 mg/L and 1.6 g/L of DO/BB exhibited a high phosphate-adsorption capacity of 62 mg/g with a removal efficiency of 99.8%. It was also stable in complex water environments with various levels of solution pH, coexisting anions, high salinity, and humic acid. With this new composite, the phosphate concentration of the actual domestic sewage decreased from 9 mg/L to less than 1 mg/L, and the total nitrogen and chemical oxygen demand also decreased effectively. Further, the cross-flow treatment using a PVC membrane loaded with DO/BB (PVC-DO/BB), decreased the phosphate concentration from 1 to 0.08 mg/L, suggesting outstanding separation of phosphate pollutants via a combination of adsorption and separation. In addition, the removal of phosphate by the PVC-DO/BB membrane using NaOH solution as an eluent was almost 90% after 5 cycles. The kinetic, isotherm and XPS analysis before and after adsorption suggested that adsorption via a combination of electrostatic interaction, complexation and precipitation contributed to the excellent separation by the as-obtained membranes. 相似文献
To investigate the nitrogen transport and conversion inside activated sludge flocs, micro-profiles of O2, NH4+, NO2–, NO3–, and pH were measured under different operating conditions. The flocs were obtained from a laboratory-scale sequencing batch reactor. Nitrification, as observed from interfacial ammonium and nitrate fluxes, was higher at pH 8.5, than at pH 6.5 and 7.5. At pH 8.5, heterotrophic bacteria used less oxygen than nitrifying bacteria, whereas at lower pH heterotrophic activity dominated. When the ratio of C to N was decreased from 20 to 10, the ammonium uptake increased. When dissolved oxygen (DO) concentration in the bulk liquid was decreased from 4 to 2 mg·L-1, nitrification decreased, and only 25% of the DO influx into the flocs was used for nitrification. This study indicated that nitrifying bacteria became more competitive at a higher DO concentration, a higher pH value (approximately 8.5) and a lower C/N. 相似文献
In this study, three sequential batch biofilm reactors (SBBRs) were operated for 155 days to evaluate the performance of completely autotrophic nitrogen removal over nitrite (CANON) process under different aeration modes and dissolved oxygen (DO). Synthetic wastewater with 160-mg NH4+-N/L was fed into the reactors. In the continuously-aerated reactor, the efficiency of the ammonium nitrogen conversion and total nitrogen (TN) removal reached 80% and 70%, respectively, with DO between 0.8–1.0 mg/L. Whereas in the intermittently-aerated reactor, at the aeration/non-aeration ratio of 1.0, ammonium was always under the detection limit and 86% of TN was removed with DO between 2.0–2.5 mg/L during the aeration time. Results show that CANON could be achieved in both continuous and intermittent aeration pattern. However, to achieve the same nitrogen removal efficiency, the DO needed in the intermittently-aerated sequential batch biofilm reactor (SBBR) during the aeration period was higher than that in the continuously-aerated SBBR. In addition, the DO in the CANON system should be adjusted to the aeration mode, and low DO was not a prerequisite to CANON process. 相似文献
Since the ammonia in the effluent of the traditional water purification process could not meet the supply demand, the advanced treatment of a high concentration of NH4+-N micro-polluted source water by biological activated carbon filter (BACF) was tested. The filter was operated in the downflow manner and the results showed that the removing rate of NH4+-N was related to the influent concentration of NH4+-N. Its removing rate could be higher than 95% when influent concentration was under 1.0 mg/L. It could also decrease with the increasing influent concentration when the NH4+-N concentration was in the range from 1.5 to 4.9 mg/L and the dissolved oxygen (DO) in the influent was under 10 mg/L, and the minimum removing rate could be 30%. The key factor of restricting nitrification in BACF was the influent DO. When the influent NH4+-N concentration was high, the DO in water was almost depleted entirely by the nitrifying and hetetrophic bacteria in the depth of 0.4 m filter and the filter layer was divided into aerobic and anoxic zones. The nitrification and degradation of organic matters existed in the aerobic zone, while the denitrification occurred in the anoxic zone. Due to the limited carbon source, the denitrification could not be carried out properly, which led to the accumulation of the denitrification intermediates such as NO2?. In addition to the denitrification bacteria, the nitrification and the heterotrophic bacteria existed in the anoxic zone. 相似文献