共查询到19条相似文献，搜索用时 539 毫秒
1.
两级SBR工艺除磷脱氮自动控制实验研究 总被引：4，自引：0，他引：4
聂熹 《吉林大学学报(地球科学版)》2007,37(3):611-614
为了解决混合生长系统在除磷和脱氮过程中的矛盾,采用两级SBR反应器实现磷和氮的同时去除。实验证明,根据pH、ORP和DO在除磷级和脱氮级阶段性的变化规律,利用自动控制技术,可以分别对两级反应实现自动控制。 相似文献
2.
3.
分级式除磷脱氮工艺探讨 总被引：5，自引：2，他引：3
综合考虑生物除磷与脱氮对环境条件的要求,提出了分级式除磷脱氮的工艺模式,旨在将聚磷菌与硝化菌分别控制在两级反应器中优势生长,以解决硝化菌与其他细菌混合生长系统在除磷与脱氮过程中存在的矛盾关系,达到优化除磷脱氮目的.探讨了分级式除磷脱氮的工艺流程、优化除磷脱氮的可行性及研究要点. 相似文献
4.
5.
通过对曝气系统的调节,微压流化式复合生物反应器（MP-FHBR）内可以实现好氧区和缺氧区共存,利用这一特点和MP-FHBR中同时存在的活性污泥﹑悬浮生物膜复合生物体系,进行了同步脱氮的试验研究。结果表明,MP-FHBR在好氧-缺氧条件下,实现了同步脱氮过程,TN和COD的平均去除率分别达到77.5%和98.3%。降低DO质量浓度使反应器内形成完全缺氧环境,对MP-FHBR同步脱氮效果没有显著影响,但会降低系统去除COD的效果;而提高DO质量浓度使反应器内形成完全好氧环境,MP-FHBR同步脱氮效果显著下降。在一定范围内提高进水COD/TN有利于提高MP-FHBR同步脱氮效果,COD/TN 由2升高到10,TN平均去除率由58.4%提高到78.8%,而继续提高COD/TN对系统同步脱氮效果的影响并不明显。在反应器允许的条件下,提高污泥质量浓度(MLSS)有利于提高系统反硝化脱氮效果,TN去除率随MLSS的增加而提高。 相似文献
6.
正确评估淡水环境中沉积物脱氮效应对理解淡水系统氮循环过程具有重要的科学意义,修正~(15)N同位素配对技术(revised ~(15)N isotope pairing techniques,r-IPT)可同时评估沉积物柱样中反硝化与厌氧氨氧化速率及其脱氮贡献。本文利用流动柱样培养实验,首次在淡水系统中对比了利用泥浆实验提供参数的r-IPT_(ra)与由柱样培养实验本身提供参数的r-IPT_V计算沉积物脱氮速率的差异性,并评估了秋季太湖不同沉积环境脱氮速率。研究表明:(1)泥浆实验结果表明,太湖梅梁湾与胥湖沉积物中均存在反硝化与厌氧氨氧化作用。(2)r-IPT方法的基本假设在研究区域均成立。其中,r-IPT_V得到的两湖区沉积物原位脱氮速率均与添加15NO-3浓度无关,表明r-IPT_V对沉积物脱氮速率评估具有更好的计算精度。(3)r-IPT_V计算结果表明,梅梁湾与胥湖沉积物反硝化、厌氧氨氧化、脱氮速率分别为3.09、1.47、4.56μmol/(m2·h)与0.69、0.02、0.71μmol/(m~2·h),厌氧氨氧化对两湖区沉积物脱氮贡献率(ra)分别为32.2%与3.3%。(4)对比r-IPT_(ra)与r-IPT_V在两个湖区的计算结果,当ra较低时(3.3%),r-IPT_(ra)与r-IPT_V计算的沉积物脱氮速率及厌氧氨氧化速率接近;而当ra较高时(32.2%),r-IPT_(ra)显著高估沉积物脱氮速率,低估厌氧氨氧化贡献率。 相似文献
7.
将传统SBR的曝气和沉淀过程在时间上进行分段,在不同段数厌氧、好氧、缺氧状态交替运行条件下,考查了分段式SBR工艺的运行情况,并与传统SBR进行了对比研究;通过设计正交试验确定了传统SBR、二段式SBR和三段式SBR最佳运行参数。结果表明：三段式SBR对COD、NH＋-N、总磷的去除率可以达到97．33％、96．63％、99．76％;二段式SBR对COD、NH4^＋-N、总磷的去除率可以达到96．98％、93．45％、98．63％;传统SBR对COD、NH4^＋-N、总磷的去除率可以达到95．87％、88．47％、98．15％,由此可见分段式SBR较传统SBR对有机物、NH4^＋-N和总磷有较好的去除效果。 相似文献
8.
采用内径为140 mm,高为250 mm的圆柱形SBR反应器进行试验,探讨SBR工艺对人工模拟配制味精废水的处理效果。通过实验分析了不同曝气时间、温度、进水浓度及污泥浓度与SBR处理效果之间的关系,确定了SBR法处理中浓度味精废水的最佳运行参数。实验结果表明,废水浓度在2 000~4 000 mg/L,温度为25℃时连续曝气6 h,污泥浓度在4 000~7 000 mg/L的条件下对人工味精废水中的COD具有较好的降解能力,COD cr的去除率可达80%。 相似文献
9.
10.
RTD对内循环三相生物流化床脱氨氮效率的影响 总被引：1，自引：0，他引：1
采用脉冲法刺激响应技术测定了不同流态条件下三相生物流化床的水力停留时间分布(RTD),得到反应器好氧流化区的串联级数近似为1,从而可用全混流反应器(CSTR)模型来研究其动力学特点,通过对比研究,得到在理论停留时间为1.5 h时,反应器的体积利用率达到最优。同时也对比了反应器在各种理论停留时间(HRT)下的脱氨氮效率,发现在水力停留时间为1.5 h时,反应器也具有最佳处理效率,氨氮的脱除率达到90%以上,从而验证了示踪试验的可靠性,并为生化反应器的设计放大与稳定运行提供了宝贵的资料。 相似文献
11.
A. Torabian A. H. Hassani S. Moshirvaziri 《International Journal of Environmental Science and Technology》2004,1(2):103-107
In this research, physical, chemical and biological treatability of Tehran solid waste leachate was studied. Results indicate that the amount of COD for the fresh raw leachate of Tehran is equal to 66,608 mg/l. The leachate is transferred to an equalization tank for storage and pH control process. After neutralization, leachate is introduced to an up flow and down flow anaerobic reactor. The effluent of anaerobic reactor is conducted to a sequencing batch reactor. Sequence batch reactor (SBR) effluent was pumped in to sand and activated carbon filters, after chemical coagulation and clarification. Results showed that anaerobic reactor with detention time of 3 days had a 35% COD removal and increasing the detention time to 4.5 days would improve the COD removal to 45%. Nutrient adjustment with phosphorus and nitrogen increased the initial 23% efficiency of sequence batch reactor to 44%. The effluent COD of SBR reactor was 21,309 mg/l. Recycling of aerobic reactor effluent with incoming feed to anaerobic reactor reduced the anaerobic reactor influent COD to 20,000 mg/l and this caused 53% and 57% COD removal in the anaerobic and aerobic effluent, respectively. The total systems COD performance increased to 80% and SBR effluent COD eventually reduced to 4,000 mg/l. Coagulation, flocculation and sedimentation processes were practiced to make the 4,000 mg/l effluent COD comply with environmental standards of Iran. The optimum coagulant found to be ferric chloride with the dosage of 50 mg/l at pH of 12, which reduced 10% of COD to an amount of 3,676 mg/l. The effluent was stored in a tank and then pumped in to pressure sand filter and afterwards to activated carbon filter. The COD removal was three and 90% for sand and activated carbon filters, respectively. The total process reduced the remaining COD to 36 mg/l, which is in compliance with environmental standards of Iran. 相似文献
12.
S. Govahi A. Karimi-Jashni M. Derakhshan 《International Journal of Environmental Science and Technology》2012,9(1):145-151
Continuous upflow anaerobic sludge blanket reactor performs more favorably at the higher organic loading rate than other anaerobic treatment. The treatment of municipal landfill leachate of Shiraz??s city investigated using continuous flow anaerobic reactor and subsequently aerated lagoon. Landfill leachate has chemical oxygen demand of 45,000?C90,000?mg/L and ammonia nitrogen at 1,000?C2,500 and heavy metals that can impact biological treatments. Capacity of anaerobic and aerobic reactors is 10 and 20?L that operated at detention time of 2 and 4?days, respectively. Organic loading rate of upflow anaerobic sludge blanket is between 0.5?C20?g chemical oxygen demand/L/day. Chemical oxygen demand removal efficiencies are between 57?C87, 35?C70 and 66?C94% in the anaerobic, aerobic and whole system, respectively. As the entry, leachate organic loading rate increased from 1 to 20?g/L/day, the chemical oxygen demand removal efficiency reached a maximum of 71% and 84% in the anaerobic reactor and whole system, respectively, at high organic loading rate. Ammonium removal efficiency was about 54% after the aerobic stage. 相似文献
13.
14.
在上流式好氧颗粒污泥床反应器中, 以厌氧颗粒污泥和好氧絮状活性污泥为接种泥, 采用人工配制的模拟废水, 成功培养出性能优异的好氧颗粒污泥.反应器内污泥浓度稳定在5g/L左右, 颗粒污泥粒径为0.5~2.0mm, 当进水COD为2000mg/L, 容积负荷为4.8kg/(m3·d)时, 系统对COD的去除率稳定在96%以上.通过扫描电镜观察, 好氧颗粒污泥是层状结构, 表面有大量丝状菌缠绕, 内部有短杆菌和空穴存在.逐步提高制药废水在进水中的比例, 经过47d的培养, 生物制药废水完全取代模拟废水, 系统对COD、NH3-N、TP的去除率分别稳定在90%、90%和70%以上. 相似文献
15.
Enhancement of removal efficiency of ammonia nitrogen in sequencing batch reactor using natural zeolite 总被引：2，自引：1，他引：1
Two sets of lab-scale sequencing batch reactors (SBR), i.e., control SBR and SBR using zeolite as carrier (zeo-SBR), were
applied to assess nitrogen removal efficiency. The test results revealed that zeolite powder added in SBR could improve its
performance. Due to the combination of zeolite adsorption for NH4
+–N and enhanced simultaneous nitrification and de-nitrification (SND), a higher removal ratio of ammonia nitrogen in wastewater
was observed in the test reactor, and the introduction of zeolite powder was helpful to inhabit sludge bulging comparing with
the control SBR, in other words, activated sludge immobilized by zeolite powder could remove NH4
+–N, COD, and PO4 significantly in a shorter cycle time. Applied two hydraulic retention times (HRTs) showed that the nitrogen and phosphorus
removal could be improved while adapting to load variations. 相似文献
16.
D. Chouhan R. Bello-Mendoza D. G. Wareham 《International Journal of Environmental Science and Technology》2017,14(2):365-374
This research investigated the potential for industrial-strength 2-methyl-4-chlorophenoxyacetic acid (MCPA) degradation by activated sludge microorganisms in a sequencing batch reactor (SBR) under nitrate-reducing conditions. The research was divided into four phases consisting of Phase I (a “proof-of-concept” phase); Phase II (an initial “tolerance” exploration phase); Phase III (an “effect of hydraulic retention time” phase), and Phase IV (a “limits” phase). The SBR successfully and simultaneously removed the nitrates completely and around 98 % of the MCPA up to an initial concentration of 50 mg/L MCPA in the dimethylamine salt form (DMCPA) (Phases I, II and III); however, it took approximately 28 days to observe a steady, high-level of MCPA removal. When the concentration of DMCPA was increased to 75 mg/L (Phase IV), the MCPA removal efficiency dropped to 85 %, but removal was observed only for a relatively short period of time since the biomass appeared to eventually become saturated with the herbicide, stopping conversion of DMCPA to its acid form and halting biodegradation. 相似文献
17.
Daeik Kim Yoonho Cho Kevin McKennon Greg Lowe Sungjin Jung Jinho Kim 《Environmental Earth Sciences》2017,76(16):578
A conventional sequencing batch reactor (SBR) was successfully transformed to a membrane bioreactor (MBR) at an Indian casino resort and hotel, Santa Ynez, California. The technical difficulties from the existing process at the site including a 3-mm screening unit, SBR biological tanks, and sand filtration were relieved of by new biological membrane technology. As the hotel and its vicinity expanded, the existing SBR was not able to treat an increased flow, which was major driving force for such membrane-upgraded project. In addition, as the area was in a high drought zone, without meeting the purpose of water reuse, new hotel expansion was not permitted. New membrane process was designed and built with new 2-mm screening unit, pre-anoxic, oxic (or aerobic), post-anoxic, and MBR tanks along with UV disinfection. The retrofitting work was conducted, minimizing a major revision on the existing SBR structure and its civil work. Therefore, the new packaged system has brought a number of benefits to the customer, thereby utilizing reclaimed water highly meeting the California Code of Regulations (CCR) Title 22 requirements. The reclaimed water goes to toilet water, cooling tower, and irrigation. This study details how such process transformation was technically finished and would help other similar cases in terms of retrofitting exiting biological process to a membrane application without a major civil construction. The cost analysis including capital, operation and maintenance (O&M) costs was included so that it will be practical to ones who will conduct future similar projects. 相似文献
18.
W. Bae D. Han E. Kim R. A. de Toledo K. Kwon H. Shim 《International Journal of Environmental Science and Technology》2016,13(7):1675-1684
The upflow anaerobic sludge blanket process followed by the biological aerated filter process was employed to improve the removal of color and recalcitrant compounds from real dyeing wastewater. The highest removal efficiency for color was observed in the anaerobic process, at 8-h hydraulic retention time, seeded with the sludge granule. In the subsequent aerobic process packed with the microbe-immobilized polyethylene glycol media, the removal efficiency for chemical oxygen demand increased significantly to 75 %, regardless of the empty bed contact time. The average influent non-biodegradable soluble chemical oxygen demand was 517 mg/L, and the average concentration in effluent from the anaerobic reactor was 363 mg/L, suggesting the removal of some recalcitrant matters together with the degradable ones. The average non-biodegradable soluble chemical oxygen demand in effluent from the aerobic reactor was 87, 93, and 118 mg/L, with the removal efficiency of 76, 74, and 67 %, at 24-, 12-, and 8-h empty bed contact time, respectively. The combined anaerobic sludge blanket and aerobic cell-entrapped process was effective to remove the refractory compounds from real dyeing wastewater as well as in reducing organic loading to meet the effluent discharge limits. This integrated process is considered an effective and economical treatment technology for dyeing wastewater. 相似文献
19.
探讨了SBR和PAC-SBR反应器处理盐酸林可霉素原料液生产废水过程中活性污泥特征的变化.随着废水投加量的增加,PAC-SBR反应器的污泥性能始终优于SBR反应器,但是由于盐酸林可霉素原料液生产废水对生物有较强的抑制作用,PAC-SBR反应器和SBR反应器中污泥的活性均发生恶化,COD去除率已明显下降,单独采用SBR或PAC-SBR法处理已难以达到排放标准,必须进行工艺的组合.PAC-SBR反应器较SBR反应器在污泥性质及处理效率上均有一定的改善,对处理盐酸林可霉素原料药生产废水有一定的优势. 相似文献