利用三七渣固态发酵灵芝菌的研究

以川芝6号为发酵菌种,对三七渣固态发酵灵芝菌的培养基制备条件进行了研究和优化。结果表明,优化的培养基制备条件为采用过60目筛的三七渣,酵母粉添加量5%(质量分数,下同),磷酸二氢钾添加量0.025%,培养基含水量70%,不调节初始pH。在此条件下进行灵芝发酵,发酵培养物中灵芝菌丝体的质量分数最高可达31.27%。     

调节细胞通透性促进天蓝色链霉菌蓝色素生物合成

在天蓝色链霉菌分批发酵中，36h时一次加入20mg/L的青霉素，色素浓度和分泌率分别提高了26．2％和39．2％；与一次性添加青霉素相比，分多次添加可使色素浓度再提高9％，但分泌率没有明显变化。DMSO浓度为6g/L时，色素浓工和分泌率较对照分别提高了20．5％和50％；2－50g/L的DMSO对菌体生长没有影响。36h时lg/L的吐温80，色素浓度和分泌率分别提高了16．9％和37．5％，60h时加入0.2g/L浓度的SDS，色素浓度较对照基本相当，但分泌率却提高了16．1％。图4表1参7     

高温制备土霉素菌渣生物炭对铀尾矿库渗排水中铀的吸附效果与机理

以土霉素菌渣（oxytetracycline fermentation residue,OFR）为原料,在300~900 ℃（间隔100 ℃）条件下制备生物炭,研究高温（800~900 ℃）制备OFR生物炭对废水中铀的吸附效果与机理。结果表明：对于不同温度下制备的生物炭,随着温度的升高,OFR生物炭表面功能基团逐渐减少,Ca晶体形态由CaC₂O₄（300~400 ℃）转变为CaCO₃（500~700 ℃）、CaO（800~900 ℃）,而这也导致了吸附效果的变化。当制备温度升至800~900 ℃时,OFR生物炭10 min吸附即可对南方某铀尾矿库渗排水中的铀达到98%以上去除率,且高温制备的OFR生物炭在较宽的pH范围（4.0~9.0）与铀初始浓度（0.8~3.0 mg/L）下,均能稳定达到大于98%的去除率,处理后上清液中铀浓度远低于铀矿冶辐射防护和辐射环境保护规定的排放标准。因此,高温制备OFR生物炭在铀尾矿库渗排水原位处理方面,展示了较好的应用前景。

     

培养基特性对三七渣发酵产红曲色素的影响

考察了蛋白胨添加量、磷酸二氢钾添加量、含水率、培养基初始pH值、基质粒径对紫色红曲霉固态发酵三七渣产红曲色素的影响。结果表明：三七渣固态发酵生产的红曲色素中黄色素的色价显著高于红色素;培养基特性对红色素和黄色素产量的影响规律相似;适宜的发酵培养基特性为：采用过60或80 目筛的三七渣,蛋白胨添加量5%~6%,磷酸二氢钾添加量1%,培养基含水率60%~70%,初始pH=5。     

厌氧发酵方式对乳渣废水产酸性能的影响

为了研究厌氧发酵方式对乳渣废水发酵产酸效果的影响,分别对乳渣废水采用自然型发酵、填料型发酵及中性型发酵（pH=7.0±0.2）,并进行连续2个周期的厌氧反应。分析乳渣废水中可溶性化学需氧量（SCOD）、蛋白质、多糖、挥发性短链脂肪酸（SCFAs）、水解酶（蛋白酶、α-葡萄苷酶）和辅酶420、NH4+-N及PO43--P指标的变化。研究发现,中性产酸系统中水解酶活性较高,蛋白质和多糖等物质水解性能较好,使乳渣废水产酸性能最佳,最大SCFAs积累量为12 328.37 mg-COD·L-1。自然发酵产酸系统中水解酶活性最低,系统中残留大量的蛋白质和多糖等物质,最低SCFAs积累量为4 322.61 mg COD·L-1。同时发现,3个发酵系统中挥发性短链脂肪酸酸成分具有显著差别,其中自然型发酵系统乙酸积累率最大,可达69.70%,中性发酵系统丙酸积累率最大可达49.27%,填料型发酵系统正丁酸积累率最大可达38.85%。     

Fermentative hydrogen production from beet sugar factory wastewater treatment in a continuous stirred tank reactor using anaerobic mixed consortia

A low pH, ethanol-type fermentation process was evaluated for wastewater treatment and bio-hydrogen production from acidic beet sugar factory wastewater in a continuous stirred tank reactor (CSTR) with an effective volume of 9.6 L by anaerobic mixed cultures in this present study. After inoculating with aerobic activated sludge and operating at organic loading rate (OLR) of 12 kgCOD?m^-3·d^-1, HRT of 8h, and temperature of 35°C for 28 days, the CSTR achieved stable ethanol-type fermentation. When OLR was further increased to 18 kgCOD?m^-3·d^-1 on the 53rd day, ethanol-type fermentation dominant microflora was enhanced. The liquid fermentation products, including volatile fatty acids (VFAs) and ethanol, stabilized at 1493 mg·L^-1 in the bioreactor. Effluent pH, oxidation-reduction potential (ORP), and alkalinity ranged at 4.1–4.5, -250–(-290) mV, and 230–260 mgCaCO₃?L^-1. The specific hydrogen production rate of anaerobic activated sludge was 0.1 L?gMLVSS^-1·d^-1 and the COD removal efficiency was 45%. The experimental results showed that the CSTR system had good operation stability and microbial activity, which led to high substrate conversion rate and hydrogen production ability.     

牛粪厌氧发酵的载体筛选试验研究

为了提高厌氧发酵装置的效率,人们研究了各种各样的方法和措施,其中应用填料或载体使生物菌能够延长驻留期是其中的方法之一,开展载体筛选及其结构设计在厌氧发酵装置中的试验,有助于对此问题的深入研究以及将其成果应用于生产实践。通过静态载体筛选试验选择了玻璃纤维作为载体、PVC塑料管作为载体骨架制成的装置在动态序批式厌氧发酵装置中进行了试验。结果表明：此载体骨架结构对于牛粪动态厌氧发酵具有明显的提高产气效率、改变产气质量和促进有机物转化为挥发性脂肪酸的作用。     

耐热乳杆菌的分离及在食物垃圾乳酸发酵中的应用

食物垃圾在我国城市生活垃圾中占有较大比重.发酵食物垃圾生产乳酸是实现其资源化的有效方法.从厌氧发酵的食物垃圾中分离到一株耐热乳酸菌TY50,根据形态、生理生化特征和16S rDNA序列,确定该菌株属于乳杆菌属的干酪乳杆菌组群(Lactobacillus casei group),其最高生长温度为52℃.TY50发酵食物垃圾生产乳酸的最佳同液比为1:12,最适温度为45 ℃.在pH 5.5～6.0条件下,发酵食物垃圾产生36.29 g/L的乳酸,乳酸体积产牢和转化率(乳峻/垃圾干重)分别达到1.01 g/(L·h)和0.44.     

Vacuum promotes metabolic shifts and increases biogenic hydrogen production in dark fermentation systems

The successful operation of any type of hydrogen-producing bioreactor depends on the performance of the microorganisms present in the system. Both substrate and partial gas pressures are crucial factors affecting dark fermentation metabolic pathways. The main objective of this study was to evaluate the impact of both factors on hydrogen production using anaerobic granular sludge as inoculum and, secondly, to study the metabolic shifts of an anaerobic community subjected to low partial gas pressures. With this goal in mind, seven different wastewater (four synthetic media, two industrial wastewater, and one domestic effluent) and the effect of applying vacuum on the systems were analyzed. The application of vacuum promoted an increase in the diversity of hydrogenproducing bacteria, such as Clostridium, and promoted the dominance of acetoclastic- over hydrogenotrophic methanogens. The application of different media promoted a wide variety of metabolic pathways. Nevertheless, reduction of the hydrogen partial pressure by application of vacuum lead to further oxidation of reaction intermediates irrespective of the medium used, which resulted in higher hydrogen and methane production, and improved the COD removal. Interestingly, vacuum greatly promoted biogenic hydrogen production from a real wastewater, which opens possibilities for future application of dark fermentation systems to enhance biohydrogen yields.     

Abating whey organic load through ethanol and lactic acid production by kefir

Abstract

The extent to which selected ethanol and lactic acid production bioprocesses contribute to whey waste abatement was examined. Alcoholic fermentation of whey was carried out by kefir cells immobilized on grape stalks, delignified cellulosic materials, or brewer's spent grains. Lactic acid fermentation was also performed by free kefir cells with or without addition of brewer's spent grains as promoting material. Since whey fermentation rate is affected by the lactose uptake rate, ¹⁴C-labeled lactose was used to study the fermentation ability of kefir. The highest reductions in biochemical oxygen demand and chemical oxygen demand of whey, about 68% and 52%, respectively, were achieved by lactic acid fermentation in 6 h at 37 °C and pH 5.5, in the presence of 120 g brewer's spent grains. Additionally, at the same conditions, the highest ¹⁴C-labeled lactose uptake rate by kefir and consequently the highest alcoholic fermentation rate were also recorded. However, greater reductions in biochemical oxygen demand and chemical oxygen demand of whey are required prior to final disposal.