共查询到19条相似文献,搜索用时 234 毫秒
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文章研究了采用DNB(反硝化细菌)抑制硫酸盐还原工艺,降低石油集输系统中H2S浓度的本源微生物治理H2S模式。该工艺在实验中采用两级UASB(上流式厌氧污泥床)反应器串联来实现。实验表明:在一级反应器成功启动后,其水中的S2-浓度达到120mg/L,SO42-的浓度为200mg/L,硫酸盐转化率可达75%以上;二级UASB启动以后,出水S2-降低至20mg/L以下,去除率约83%。进一步实验表明SO42-/NO2-质量浓度比、ORP(氧化还原电位)均会对SRB产生抑制作用。研究结果对石油集输系统中H2S气体的控制具有参考价值,该技术在长庆油田现场实验,能使油井H2S浓度平均降幅达到87%,有效降低了长庆油田安全风险。 相似文献
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超声-双氧水和亚铁离子体系处理含酚废水研究 总被引:3,自引:2,他引:3
在实验装置上对超声-双氧水和亚铁离子体系联合处理含酚废水进行了实验研究。主要考察了废水初始pH值、初始双氧水浓度、超声功率、反应时间等因素对酚去除率的影响。实验结果表明:超声辐射可以在双氧水和亚铁离子体系氧化过程中起加速反应的作用,而且随着超声功率的增大,加速反应的能力增强;实验条件下废水初始pH值为4~6.8,初始双氧水浓度为140mg/L时酚去除效果最佳;超声-双氧水和亚铁离子体系处理含酚废水过程中苯酚的降解规律符合表现一级反应。 相似文献
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生物促生剂修复受污水体净化效能研究 总被引:4,自引:0,他引:4
对生物促生剂(Bio-energizer,BE)净化受污水体的效果进行了试验研究。结果表明:生物促生剂在低浓度时(小于1 ml/m^3),水体修复效果不明显;当浓度在3ml/m^3以上时,可以有效的加快水体中N、P类营养物的降解,可使NH4^+ -N和TN分别由3.6—4.4mg/L和4.4—4.9mg/L降低至0.13-0.18 mg/L和0.39—1.06 mg/L,PO4^3- -P和TP分别由0.03-0.04mg/L和0.11—0.12mg/L降低至0.004-0.008mg/L和0.025-0.04mg/L。COD在试验过程中有上升的趋势。 相似文献
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采用竖式SBR作为反应器,利用城市污水处理厂剩余污泥作为接种污泥,通过不间断运行培养出好氧颗粒污泥。实验结果表明,采用非限量曝气模式好氧颗粒污泥降解模拟污水的效果较好,其COD去除率可达98%以上。曝气量对好氧颗粒污泥的形成和稳定具有重要影响,当气速为26.5m/h时,好氧颗粒污泥的性状和处理有机废水效果最佳。同时好氧颗粒污泥对pH值的变化不明显,当pH为5—8范围内,其COD去除率都可达到85%以上。但是未经驯化的好氧颗粒污泥对对硝基苯酚和对氯苯酚两种芳香类有机物较敏感,而对硝基苯酚对其毒性更大。当对硝基苯酚和。对氯苯酚浓度为10mg/L时,其COD去除率仅为42.5%和52%。 相似文献
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以茄子秸秆为原料,ZnCl2为活化剂制备粉末状活性炭,主要研究了活性炭对染料废水的吸附性能;以活性红X-3B和酸性蓝RL为模型染料,考察了染料初始浓度、pH值、活性炭投加量和吸附时间等对染料脱色率的影响。结果表明,染料初始浓度和活性炭投加量对染料脱色率影响较大。初始浓度为300mg/L时,活性炭的最佳投加量分别为1g/L和1.4g/L;在最佳工艺条件下,脱色率分别在93%和98%以上,COD去除率分别为94.5%和86.4%,出水水质达到国家一级《纺织染整工业水污染物排放标准》(GB 4287—1992)。 相似文献
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Temperature and feed strategy effects on sulfate and organic matter removal in an AnSBB 总被引:1,自引:0,他引:1
Costabile AL Canto CS Ratusznei SM Rodrigues JA Zaiat M Foresti E 《Journal of environmental management》2011,92(7):1714-1723
The objective of this work was to analyze the interaction effects between temperature, feed strategy and COD/[SO(4)(2-)] levels, maintaining the same ratio, on sulfate and organic matter removal efficiency from a synthetic wastewater. This work is thus a continuation of Archilha et al. (2010) who studied the effect of feed strategy at 30 °C using different COD/[SO(4)(2-)] ratios and levels. A 3.7-L anaerobic sequencing batch reactor with recirculation of the liquid phase and which contained immobilized biomass on polyurethane foam (AnSBBR) was used to treat 2.0 L synthetic wastewater in 8 h cycles. The temperatures of 15, 22.5 and 30 °C with two feed strategies were assessed: (a) batch and (b) batch followed by fed-batch. In strategy (a) the reactor was fed in 10 min with 2 L wastewater containing sulfate and carbon sources. In strategy (b) 1.2 L wastewater (containing only the sulfate source) was fed during the first 10 min of the cycle and the remaining 0.8 L (containing only the carbon source) in 240 min. Based on COD/[SO(4)(2-)] = 1 and on the organic matter (0.5 and 1.5 gCOD/L) and sulfate (0.5 and 1.5 gSO(4)(2-)/L) concentrations, the sulfate and organic matter loading rates applied were 1.5 and 4.5 g/L.d, i.e., same COD/[SO(4)(2-)] ratio (=1) but different levels (1.5/1.5 and 4.5/4.5 gCOD/gSO(4)(2-)). When reactor feed was 1.5 gCOD/L.d and 1.5 gSO(4)(2-)/L.d, gradual feeding (strategy b) showed to favor sulfate and organic matter removal in the investigated temperature range, indicating improved utilization of the electron donor for sulfate reduction. Sulfate removal efficiencies were 87.9; 86.3 and 84.4%, and organic matter removal efficiencies 95.2; 86.5 and 80.8% at operation temperatures of 30; 22.5 and 15 °C, respectively. On the other hand, when feeding was 4.5 gCOD/L.d and 4.5 gSO(4)(2-)/L.d, gradual feeding did not favor sulfate removal, indicating that gradual feeding of the electron donor did not improve sulfate reduction. 相似文献
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Electrocoagulation with aluminum electrodes was used to treat the vegetable oil refinery wastewater (VORW) in a batch reactor. The effects of operating parameters such as pH, current density, PAC (poly aluminum chloride) dosage and Na(2)SO(4) dosage on the removal of organics and COD removal efficiency have been investigated. It has been shown that the removal efficiency of COD increased with the increasing applied current density and increasing PAC and Na(2)SO(4) dosage and the most effective removal capacity was achieved at the pH 7. The results indicate that electrocoagulation is very efficient and able to achieve 98.9% COD removal in 90 min at 35 mAcm(-2) with a specific electrical energy consumption of 42 kWh(kgCOD(removed))(-1). The effluent was very clear and its quality exceeded the direct discharge standard. 相似文献
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以某污水厂的高氯低COD生化出水为研究对象,探讨了硫酸汞加入量、K2Cr2O7溶液浓度、反应酸度、取水样量等参数对COD测定的影响,探讨消除该厂Cl-干扰最简单有效方法,结果表明:控制硫酸汞与氯离子比为15∶1(质量比)、K2Cr2O7浓度为0.18 mol/L、水样稀释0.75倍、Ag2SO4-H2SO4加入量为28mL,皆可有效减少氯离子的干扰。该方法相对氯气校正法,操作简单、准确可靠。 相似文献
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Biological sulfate reduction was studied in a laboratory-scale anaerobic sequential batch reactor (14 L) containing mineral coal for biomass attachment. The reactor was fed industrial wastewater with increasingly high sulfate concentrations to establish its application limits. Special attention was paid to the use of butanol in the sulfate reduction that originated from melamine resin production. This product was used as the main organic amendment to support the biological process. The reactor was operated for 65 cycles (48 h each) at sulfate loading rates ranging from 2.2 to 23.8 g SO(4)(2-)/cycle, which corresponds to sulfate concentrations of 0.25, 0.5, 1.0, 2.0 and 3.0 g SO(4)(2-) L(-1). The sulfate removal efficiency reached 99% at concentrations of 0.25, 0.5 and 1.0 g SO(4)(2-) L(-1). At higher sulfate concentrations (2.0 and 3.0 g SO(4)(2-) L(-1)), the sulfate conversion remained in the range of 71-95%. The results demonstrate the potential applicability of butanol as the carbon source for the biological treatment of sulfate in an anaerobic batch reactor. 相似文献
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MBR工艺处理粮油加工废水的研究 总被引:2,自引:0,他引:2
采用MBR(Membrane Bioreactor)工艺对粮油加工废水进行处理发现,污染物的去除是活性污泥和膜截留共同作用的结果,试验中微生物的去除作用占污染物总去除率的62.9%~88.1%,起主要作用。当系统的污泥负荷和容积负荷分别在0.4~0.54 kgCOD/kgMLSS.d之间和3.8~5.0 kgCOD/m3.d之间变化时,系统对COD的去除率在92.5%以上。本试验所用膜的临界膜通量为8~10 L/(m2.h),系统污泥浓度从1~2g/L增加到10~12g/L时,临界膜通量从10~12L/(m2.h)下降到了3~4 L/(m2.h),随着膜面流速从1.0m/s上升到1.8m/s,膜的临界通量也相应的从4~6 L/(m2.h)上升到了16~18 L/(m2.h),呈正相关。 相似文献
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用分光光度法测定水中化学需氧量CODCr,通过正交试验选择氧化的最佳选择。试验结果表明对CODCr值为50~1000mg/L的水样:氧化剂K2Cr2O7用量为0.20~0.40mol/L,催化剂Ag2SO4用量为10g/LH2SO4,消解时间10min,加热温度180℃。用CODCr为138mg/L的质控标样进行验证试验,其绝对误差为0.5~3.0mg/L。与标准方法相比用分光光度法测定CODCr具有分析误差小,省时、省力,节约药剂的特点。 相似文献
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Vijayaraghavan K Ahmad D Ezani Bin Abdul Aziz M 《Journal of environmental management》2007,82(1):24-31
In this study treatment of palm oil mill effluent (POME) was investigated using aerobic oxidation based on an activated sludge process. The effects of sludge volume index, scum index and mixed liquor suspended solids during the acclimatizing phase and biomass build-up phase were investigated in order to ascertain the reactor stability. The efficiency of the activated sludge process was evaluated by treating anaerobically digested and diluted raw POME obtained from Golden Hope Plantations, Malaysia. The treatment of POME was carried out at a fixed biomass concentration of 3900+/-200mg/L, whereas the corresponding sludge volume index was found to be around 105+/-5mL/g. The initial studies on the efficiency of the activated sludge reactor were carried out using diluted raw POME for varying the hydraulic retention time, viz: 18, 24, 30 and 36h and influent COD concentration, viz: 1000, 2000, 3000, 4000 and 5000mg/L, respectively. The results showed that at the end of 36h of hydraulic retention time for the above said influent COD, the COD removal efficiencies were found to be 83%, 72%, 64%, 54% and 42% whereas at 24h hydraulic retention time they were 57%, 45%, 38%, 30% and 27%, respectively. The effectiveness of aerobic oxidation was also compared between anaerobically digested and diluted raw POME having corresponding CODs of 3908 and 3925mg/L, for varying hydraulic retention time, viz: 18, 24, 30, 36, 42, 48, 54 and 60h. The dissolved oxygen concentration and pH in the activated sludge reactor were found to be 1.8-2.2mg/L and 7-8.5, respectively. The scum index was found to rise from 0.5% to 1.9% during the acclimatizing phase and biomass build-up phase. 相似文献