共查询到20条相似文献,搜索用时 31 毫秒
1.
Ying Cai Jun Wu Jian Lu Jianhua Wang Cui Zhang 《Frontiers of Environmental Science & Engineering》2022,16(7):96
2.
Xinhua WANG Jingmei LI Xiufen LI Guocheng DU 《Frontiers of Environmental Science & Engineering》2011,5(4):615-622
Among the numerous parameters affecting the membrane bioreactor (MBR) performance, the aeration intensity is one of the most important factors. In the present investigation, an anoxic/aerobic-type (A/O-type) sequencing batch MBR system, added anoxic process as a pretreatment to improve the biodegradability of azo dye wastewater, was investigated under different aeration intensities and the impact of the aeration intensity on effluent quantity, sludge properties, extracellular polymeric substances (EPS) amount generated as well as the change of permeation flux were examined. Neither lower nor higher aeration intensities could improve A/O-type sequencing batch MBR performances. The results showed 0.15 m3·h-1 aeration intensity was promising for treatment of azo dye wastewater under the conditions examined. Under this aeration intensity, chemical oxygen demand (COD), ammonium nitrogen and color removal as well as membrane flux amounted to 97.8%, 96.5%, 98.7% and 6.21 L·m-2·h-1, respectively. The effluent quality, with 25.0 mg·L-1COD, 0.84 mg·L-1 ammonium nitrogen and 8 chroma, could directly meet the reuse standard in China. In the meantime, the sludge relative hydrophobicity, the bound EPS, soluble EPS and EPS amounts contained in the membrane fouling layer were 70.3%, 52.0 mg·g-1VSS, 38.8 mg·g-1VSS and 90.8 mg·g-1VSS, respectively, which showed close relationships to both pollutant removals and membrane flux. 相似文献
3.
Shengjie LIU Manxia ZHANG Xiang LI Xiaojia TANG Lingling ZHANG Yimin ZHU Chengyu YUAN 《Frontiers of Environmental Science & Engineering》2011,5(4):610-614
To fulfill the requirements of Guidelines for approval of ballast water management system (G8), a set of onshore ballast water treatment equipment utilizing micro-pore ceramic filtration (MPCF) and UV radiation (MPCF&UV) system was designed and set up with a maximum flow rate of 80 m3·h-1. Technical feasibilities of MPCF&UV system were evaluated in three areas: removal efficiencies of indicator organism and oceanic bacteria, perdurability of a ceramic filter, and application on native seawater. The results showed that no indicator organism (Dunaliella ) or oceanic bacteria was detected after treatment of 20 L MPCF and UV radiation at 1.3× 104 μW·s·cm-2. A 20 L ceramic filter can run continuously for 5.3 h at the flow rate of 15 m3·h-1 before its pressure drop up to 0.195 MPa. The removal percentage of total plankton amounts were 91.9% at a flow rate of 70 m3·h-1 by 80 L MPCF and UV radiation at 1.3× 104 μW·s·cm-2. 相似文献
4.
Haiguang Zhang Lei Du Jiajian Xing Gaoliang Wei Xie Quan 《Frontiers of Environmental Science & Engineering》2023,17(5):59
5.
Gefu ZHU Chaoxiang LIU Jianzheng LI Nanqi REN Lin LIU Xu HUANG 《Frontiers of Environmental Science & Engineering》2013,7(1):143-150
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. 相似文献
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7.
Zhijun Liu Xi Luo Senlin Shao Xue Xia 《Frontiers of Environmental Science & Engineering》2023,17(4):40
8.
Yanping HOU Kaiming LI Haiping LUO Guangli LIU Renduo ZHANG Bangyu QIN Shanshan CHEN 《Frontiers of Environmental Science & Engineering》2014,8(1):137-143
Separator between anode and cathode is an essential part of the microbial fuel cell (MFC) and its property could significantly influence the system perfor- mance. In this study we used polyvinyl alcohol (PVA) polymer membrane crosslinked with sulfosuccinic acid (SSA) as a new separator for the MFC. The highest power density of 7594-4 mW-m-2 was obtained when MFC using the PVA membrane crosslinked with 15% of SSA due to its desirable proton conductivity (5.16 x 10-2 S.cml). The power density significantly increased to 11064- 30 mW.m-2 with a separator-electrode-assembly config- uration, which was comparable with glass fiber (11704- 46 mW.m-2). The coulombic efficiencies of the MFCs with crosslinked PVA membranes ranged from 36.3% to 45.7% at a fix external resistance of lO00f2. The crosslinked PVA membrane could be a promising alter- native to separator materials for constructing practical MFC system. 相似文献
9.
Lihui ZHANG Guomin CAO Yulei FEI Hong DING Mei SHENG Yongdi LIU 《Frontiers of Environmental Science & Engineering》2011,5(4):604-609
A composite membrane bioreactor (CMBR) integrating the immobilized cell technique and the membrane separation technology was developed for groundwater denitrification. The CMBR had two well mixed compartments with one filled with the nitrate- containing influent and the other with a dilute ethanol solution; the compartments were separated by the composite membrane consisting of a microporous membrane facing the influent and an immobilized cell membrane facing the ethanol solution. Nitrate and ethanol molecules diffused from the respective compartments into the immobilized cell membrane where nitrate was reduced to gaseous nitrogen by the denitrifying bacteria present there with ethanol as the carbon source. The microporous membrane was attached to one side of the immobilized cell membrane for retention of the disaggregated bacteria. Relative to the single dose of external ethanol, the two-dose supplementation produced better treatment results as evidenced by the lower concentrations of N O 3 - - N and ethanol (as measured by total organic carbon) of the effluent. The batch treatment in CMBR removed most of the nitrate in the influent and attained a stable denitrification rate of 0.1 g·m-2·h-1 for most of the 96-h cycles during the 30-cycle study. The effluent was essentially free of ethanol and nitrite nitrogen. 相似文献
10.
Hong YAO Hao LIU Yongmiao HE Shujun ZHANG Peizhe SUN Chinghua HUANG 《Frontiers of Environmental Science & Engineering》2012,6(6):875-883
A pilot-scale anaerobic ammonia oxidation (ANAMMOX) reactor was used to treat mixed wastewater resulting from a chlortetracycline and starch production process. The results, collected over the course of 272 days, show that the ratio of influent ammonium to nitrite, pH, and temperature can all affect the efficiency of nitrogen removal. The ratio of influent ammonium to nitrite was maintained at about 1:1 at a concentration below 200 mg·L-1 for both influent ammonium and nitrite. The total nitrogen (TN) loading rate was 0.15–0.30 kgN·m-3·d-1, pH remained at 7.8–8.5, and temperature was recorded at 33±1°C. The rate of removal of ammonia, nitrite, and TN were over 90%, 90%, and 80%, and the effluent ammonium, nitrite and TN concentrations were below 50, 30, and 100 mg·L-1. 相似文献
11.
Dawei Yu Jianxing Wang Libin Zheng Qianwen Sui Hui Zhong Meixue Cheng Yuansong Wei 《Frontiers of Environmental Science & Engineering》2020,14(6):101
12.
Ming HUA Lili XIAO Bingcai PAN Quanxing ZHANG 《Frontiers of Environmental Science & Engineering》2013,7(3):435-441
The efficient removal of phosphorous from water is an important but challenging task. In this study, we validated the applicability of a new commercially available nanocomposite adsorbent, i.e., a polymer-based hydrated ferric oxide nanocomposite (HFO-201), for the further removal of phosphorous from the bioeffluent discharged from a municipal wastewater treatment plant, and the operating parameters such as the flow rate, temperature and composition of the regenerants were optimized. Laboratory-scale results indicate that phosphorous in real bioeffluent can be effectively removed from 0.92 mg·L-1 to<0.5 mg·L-1 (or even<0.1 mg·L-1 as desired) by the new adsorbent at a flow rate of 50 bed volume (BV) per hour and treatable volume of 3500–4000 BV per run. Phosphorous removal is independent of the ambient temperature in the range of 15°C–40°C. Moreover, the exhausted HFO-201 can be regenerated by a 2% NaOH+ 5% NaCl binary solution for repeated use without significant capacity loss. A scaled-up study further indicated that even though the initial total phosphorus (TP) was as high as 2 mg·L-1, it could be reduced to<0.5 mg·L-1, with a working capacity of 4.4–4.8 g·L-1 HFO-201. In general, HFO-201 adsorption is a choice method for the efficient removal of phosphate from biotreated waste effluent. 相似文献
13.
Chao Pang Chunhua He Zhenhu Hu Shoujun Yuan Wei Wang 《Frontiers of Environmental Science & Engineering》2019,13(4):50
14.
Xue BAI Hanchang SHI Zhengfang YE Qiujin SUN Qing WANG Zhongyou WANG 《Frontiers of Environmental Science & Engineering》2013,7(6):844-850
In this study, microorganisms (named B111) were immobilized on polyvinyl alcohol microspheres prepared by the inverse suspension crosslinked method. The biodegradation of bisphenol A (BPA) and 4-hydro- xybenzaldehyde, a degradation product of BPA, by free and immobilized B lll was investigated. The BPA degradation studies were carried out at initial BPA concentrations ranging from 25 to 150 mg·L^-1. The affinity constant Ks and maximum degradation rate Rmax were 98.3 mg·L^-1 and 19.7mg·mg^-1VSS·d^-1 for free B111, as well as 87.2mg·L^-1 and 21.1mg·mg^-1VSS·d^-1 for immobilized B 111, respectively. 16S rDNA gene sequence analyses confirmed that the dominant genera were Pseudomonas and Brevundimonas for BPA biodegradation in microorganisms B 111. 相似文献
15.
Haitao WANG 《Frontiers of Environmental Science & Engineering》2013,7(6):833-835
The outdoor smog chamber was used to thorough investigate the rate constants of gas-phase reaction between dimethyl sulfide (DMS) and ozone (O3) under conditions of relative humidity 55.0%-67.8% at (296±2)K for the first time. The rate constants were measured, at a total pressure of 1 atm, to be (10.4±0.2) × 10^-19 cm^3·molecule^-1·s^-1 at relative humidity of 67.5%±0.3% at 298K, (10.1±0.1) × 10^-19cm^3·molecule^-1·s^-1 at relative humidity of 66.5%±0.5% at 296K, (7.75±0.39) × 10^-19cm^3·molecule^-1·s^-1 at relative humidity of 64.8%± 0.1% at 294K and (3.42±0.21) × 10^-19cm^3·molecu- le^-1·s^-1at relative humidity of 55.8%±0.8% at 295K. Base on these results, it is possible to see the reaction of O3/ DMS in the presence of water vapor as an important sink for DMS in the earth atmosphere. 相似文献
16.
Zaishan Wei Meiru Tang Zhenshan Huang Huaiyong Jiao 《Frontiers of Environmental Science & Engineering》2022,16(2):20
17.
反渗透(Reverse Osmosis,RO)因出水水质好、运行成本低等优势常用于垃圾渗滤液的处理,但产生的RO浓缩液具有COD高、色度高、盐分高、难降解等特点,其处理存在效果差、能耗和成本均较高等问题.本工作采用氧化钌/氧化铱涂层电极(RuO2/IrO2-Ti)的钛网为阳极,以304不锈钢电极为阴极,设计制作了6通道的电化学反应器,通过电化学氧化处理RO浓缩液,研究考查了电流密度、循环流速、比电极面积等参数对COD去除效果的影响,分析了电化学氧化去除难降解有机物并同时脱盐的过程机理与能耗.结果表明,在电流密度32.89 mA·cm-2,循环流速0.46 cm·s-1,比电极面积65.10 m2·m-3的条件下,电化学氧化处理RO浓缩液3 h,COD去除率可达68.0%,TOC去除率可达40.6%,脱盐率可达72.1%,去除单位质量COD能耗仅为常规的板状电极电化学反应器的25.5%.本工作可为垃圾渗滤液RO浓缩液的预处理提供新思路. 相似文献
18.
Biodegradation of 2-methylisoborneol by bacteria enriched from biological activated carbon 总被引:1,自引:1,他引:0
Rongfang YUAN Beihai ZHOU Chunhong SHI Liying YU Chunlei ZHANG Junnong GU 《Frontiers of Environmental Science & Engineering》2012,6(5):701-710
One of the most common taste and odour compounds (TOCs) in drinking water is 2-methylisoborneol (2-MIB) which cannot be readily removed by conventional water treatments. Four bacterial strains for degrading 2-MIB were isolated from the surface of a biological activated carbon filter, and were characterized as Micrococcus spp., Flavobacterium spp., Brevibacterium spp. and Pseudomonas spp. based on 16S rRNA analysis. The removal efficiencies of 2-MIB with initial concentrations of 515 ng·L-1 were 98.4%, 96.3%, 95.0%, and 92.8% for Micrococcus spp., Flavobacterium spp., Brevibacterium spp. and Pseudomonas spp., respectively. These removal efficiencies were slightly higher than those with initial concentration at 4.2 mg·L-1 (86.1%, 84.4%, 86.7% and 86.0%, respectively). The kinetic model showed that biodegradation of 2-MIB at an initial dose of 4.2 mg·L-1 was a pseudo-first-order reaction, with rate constants of 0.287, 0.277, 0.281, and 0.294 d-1, respectively. These degraders decomposed 2-MIB to form 2-methylenebornane and 2-methyl-2-bornane as the products. 相似文献
19.
Taro Miyoshi Thanh Phong Nguyen Terumi Tsumuraya Hiromu Tanaka Toru Morita Hiroki Itokawa Toshikazu Hashimoto 《Frontiers of Environmental Science & Engineering》2018,12(3):1
20.
Tingwei Gao Kang Xiao Jiao Zhang Wenchao Xue Chunhai Wei Xiaoping Zhang Shuai Liang Xiaomao Wang Xia Huang 《Frontiers of Environmental Science & Engineering》2022,16(4):49