模拟冷却水中304不锈钢的耐蚀性影响因素研究

用电化学方法研究了Cl^-、S^2-、NO3^-、温度以及某电厂水质稳定剂对304不锈钢耐蚀性的影响。极化曲线表明：在[Cl-]／[SO4^2-]约为0．56时，点蚀电位开始下降，并随着Cl-浓度的增大逐渐降低；S2-的加入使钝化电流显著增大；NO3-浓度增加使点蚀电位逐渐升高；溶液温度的提高使点蚀电位降低，钝化电流也有所增大，钝化膜的耐蚀性降低;实验表明采用的某厂水质稳定剂可引起304不锈钢点蚀电位的下降。Mott-Schottky图显示S2-浓度的增加使体现p-型半导体(氧化铬)性质的直线段发生较大变化，说明硫离子影响了铬氧化物的性质。     

火电厂循环冷却水对铜合金的点蚀

以北方某电厂循环冷却水为例,用电化学方法研究了Cl-、SO2-4、S2-和pH值等因素对HSn701-B铜合金管材点蚀的影响.极化曲线表明:在该电厂冷却水水质条件下,该管材的点蚀电位随水样中Cl-浓度的增大而下降,腐蚀电位也随之下降,但钝化电流变化不大,点蚀电位与Cl-浓度关系的表达式为:Eb=61.19-14.83lg[Cl-];少量SO2-4的加入对铜管的腐蚀有阻碍作用,当溶液中[HCO-3]/[SO2-4]<0.47时,又有促进作用;S2-的加入使铜管的点蚀电位负移、钝化电流增大;pH值的降低会使管材的点蚀电位负移.     

316L不锈钢在氯离子环境中的腐蚀行为

为了研究316L不锈钢在含Cl-环境中的腐蚀行为,采用浸泡和电化学相结合的方法,研究了其在不同Cl-浓度溶液中不同浸泡时间的腐蚀行为,采用扫描电镜(SEM)观察了腐蚀形貌.结果表明:316L不锈钢在含Cl-环境中的点蚀程度与Cl-浓度密切相关,随着Cl-浓度的增加,点蚀程度先增大后减弱,当Cl-浓度为3％时,点蚀最严重,当Cl-浓度超过3％时,点蚀减缓;316L不锈钢在NaCl溶液中钝化膜的形成是缓慢的,膜结构具有不完整性,为点蚀的孕育、萌生提供了结构条件,而点蚀一旦形成,在自催化作用下继续发展;316L不锈钢在含Cl-体系中的腐蚀行为是Cl-浓度与溶解氧含量两因素共同作用的结果,溶液中Cl-含量的增加一方面为加速腐蚀提供了物质条件,促进腐蚀;另一方面减少了介质中溶解氧的含量,抑制了腐蚀,两者的综合作用使腐蚀得以控制.     

基于点蚀的316L不锈钢在酸性气田环境中的适应性评价

国内外酸性气田的开发使腐蚀环境越来越苛刻,为满足气液混输的工艺要求,发展了耐蚀合金/碳钢的双金属复合管技术。316L不锈钢被广泛用于双金属管的内衬,在含H_2S和CO_2环境中腐蚀速率很低,然而在高含Cl-的溶液中,316L不锈钢容易出现点蚀而诱发集输管线失效,为此,就316L不锈钢在酸性气田集输环境中的点蚀进行评述。讨论了影响316L不锈钢点蚀的材质因素,Mn和Fe的硫化物及Mg、Al、Ca的氧化物等两种夹杂物均能促进钝化膜的溶解而引起点蚀;分析了316L不锈钢点蚀的H_2S、CO_2、温度、Cl-浓度和pH值等环境的适应性条件,发现H_2S环境比CO_2环境更容易发生点蚀,H_2S和CO_2对点蚀发生存在协同机制,温度升高、Cl-浓度增加和酸性介质均会增加316L不锈钢点蚀的敏感性。为进一步优化选材原则,需重点加强环境因素的协同机制、环境适应性的边界条件、点蚀发展的动力学以及新的标准研究。     

等离子体钝化316L不锈钢抗点蚀性能研究

本文运用冷弧空气等离子体射流技术处理316L不锈钢表面,分别采用俄歇能谱、阳极极化和FeCl3加速腐蚀实验等研究316L不锈钢表面所形成钝化膜的成分、结构和抗点蚀性能。研究表明:316L不锈钢表面经空气等离子体射流氧化处理后,点蚀电位和开路电位与未经处理的样品相比提高400mV;点蚀坑的数量、直径和深度明显降低;316L不锈钢表面钝化膜的厚度大幅提高,从而提高基体的耐点蚀能力。     

2205双相不锈钢在CO_2-H_2S-Cl~--H_2O环境中的电化学腐蚀行为

为充分了解2205双相不锈钢在CO2-H2S-Cl--H2O环境下的耐蚀性能,尤其是其抗点蚀特性,借助计时电流和动电位循环极化测试等手段研究了其钝化动力学特征以及腐蚀特征参数如Ecorr、Epit、Epp、ΔE和Jpass的变化,分析了2205双相不锈钢在含CO2和CO2/H2S的Na Cl溶液中的点蚀差异,并对其点蚀和钝化机理进行了讨论。结果表明,2205双相不锈钢具有优越的抗CO2腐蚀性能,随Cl-浓度增大,发生点腐蚀敏感性提高;随H2S浓度增大,点蚀电位Epit和保护电位Epp均降低,钝化区域稳定性下降,点蚀敏感性进一步提高。     

316L不锈钢在不同环境中点蚀形核研究

通过人工海水中长期浸泡实验和循环伏安极化曲线测试,研究了温度、Cl-浓度、溶解氧浓度对抛光后的316L不锈钢点蚀形核的影响,确定了不锈钢在不同环境的人工海水中点蚀的萌生时间和位置。结果表明:与温度和Cl-浓度的影响不同,溶解氧浓度的增加对不锈钢点蚀形核具有抑制作用。316L不锈钢在4℃,8×10-6溶解氧浓度,10%(质量分数)NaCl溶液中浸泡后表面出现钝化膜局部破坏,点蚀形核时间为60~70天,形核位置存在MgO-Al2O3系和CaO-SiO2系非金属夹杂物。不锈钢在4℃人工海水和0.02×10-6溶氧量浓度下浸泡后,表面出现点蚀的时间为70~80天。     

高氮奥氏体不锈钢耐点蚀性能研究

目前产于高氮不锈钢的研究多集中于理论基础、制造工艺和力学性能等方面,有关耐蚀性方面的研究有限。通过循环极化、Mott-Schottky曲线以及电化学阻抗(EIS)等方法,研究了Cr23Mo1N奥氏体不锈钢(高氮钢,HNSS)和316L不锈钢在Cl-溶液中的耐点蚀性能。结果表明:与316L不锈钢相比,高氮钢具有更正的自腐蚀电位,更小的维钝电流密度。阻抗谱表明高氮钢的钝化膜比316L更加稳定,且电荷转移电阻更大。Mott-Schottky曲线表明高氮钢的点缺陷施主浓度比316L不锈钢低一个数量级,钝化膜的绝缘性更好。循环极化曲线表明高氮钢的点蚀敏感性更小,钝化膜的自修复能力更强,耐蚀性能更加优越。     

模拟不同浓度Cl-对14Cr12Ni3WMoV不锈钢电化学腐蚀行为的影响

为了探明Cl-浓度对汽轮机末级叶片常用钢腐蚀的影响,通过动电位极化法、电化学阻抗谱、Mott-Schottky曲线、激光共聚焦显微镜、扫描电镜等方法分析了在不同Cl-浓度模拟溶液中14Cr12Ni3WMoV马氏体不锈钢的电化学腐蚀行为.结果表明:随着Cl-浓度的不断增大,不锈钢钝化膜点缺陷增加,稳定性下降,点蚀敏感性增...     

酸性溶液中Cl-含量和温度对PH13-8Mo腐蚀行为的影响

为了解决在深海油气钻采中出现的酸性环境中对钻采设备的腐蚀问题,结合海洋中油气田的实际环境,在pH值为3的Na2SO4+H2SO4溶液中,采用电化学极化曲线、循环极化曲线、电化学阻抗谱(EIS)结合静态浸泡实验,分别研究了Cl-质量分数(1%、3.5%和7%)和溶液温度(4、25、50和80℃)对马氏体沉淀硬化不锈钢PH13-8Mo电化学腐蚀行为的影响,并采用点缺陷PDM模型结合闭塞电池理论对其腐蚀机理进行了分析.结果表明,随着溶液中Cl-浓度的升高,PH13-8Mo极化曲线中二次钝化的特性消失.溶液中Cl-浓度和温度的升高均使得PH13-8Mo的点蚀电位降低、点蚀保护电位降低,抗点蚀能力下降,腐蚀电流密度增大,钝化电位区间缩短,电荷转移电阻呈指数关系下降,样品表面腐蚀形貌由点蚀发展为全面腐蚀.     

Physico-chemical treatments for removal of recalcitrant contaminants from landfill leachate

In this paper, the technical applicability and treatment performance of physico-chemical techniques (individual and/or combined) for landfill leachate are reviewed. A particular focus is given to coagulation-flocculation, chemical precipitation, ammonium stripping, membrane filtration and adsorption. The advantages and limitations of various techniques are evaluated. Their operating conditions such as pH, dose required, characteristics of leachate in terms of chemical oxygen demand (COD) and NH3-N concentration and treatment efficiency are compared. It is evident from the survey of 118 papers (1983-2005) that none of the individual physico-chemical techniques is universally applicable or highly effective for the removal of recalcitrant compounds from stabilized leachate. Among the treatments reviewed in this article, adsorption, membrane filtration and chemical precipitation are the most frequently applied and studied worldwide. Both activated carbon adsorption and nanofiltration are effective for over 95% COD removal with COD concentrations ranging from 5690 to 17,000 mg/L. About 98% removal of NH3-N with an initial concentration ranging from 3260 to 5618 mg/L has been achieved using struvite precipitation. A combination of physico-chemical and biological treatments has demonstrated its effectiveness for the treatment of stabilized leachate. Almost complete removal of COD and NH3-N has been accomplished by a combination of reverse osmosis (RO) and an upflow anaerobic sludge blanket (UASB) with an initial COD concentration of 35,000 mg/L and NH3-N concentration of 1600 mg/L and/or RO and activated sludge with an initial COD concentration of 6440 mg/L and NH3-N concentration of 1153 mg/L. It is important to note that the selection of the most suitable treatment method for landfill leachate depends on the characteristics of landfill leachate, technical applicability and constraints, effluent discharge alternatives, cost-effectiveness, regulatory requirements and environmental impact.     

Tertiary treatment of textile wastewater with combined media biological aerated filter (CMBAF) at different hydraulic loadings and dissolved oxygen concentrations

An up-flow biological aerated filter packed with two layers media was employed for tertiary treatment of textile wastewater secondary effluent. Under steady state conditions, good performance of the reactor was achieved and the average COD, NH(4)(+)-N and total nitrogen (TN) in the effluent were 31, 2 and 8mg/L, respectively. For a fixed dissolved oxygen (DO) concentration, an increase of hydraulic loading resulted in a decrease in substrate removal. With the increase of hydraulic loadings from 0.13 to 0.78m(3)/(m(2)h), the removal efficiencies of COD, NH(4)(+)-N and TN all decreased, which dropped from 52 to 38%, from 90 to 68% and from 45 to 33%, respectively. In addition, the results also confirmed that the increase of COD and NH(4)(+)-N removal efficiencies resulted from the increase of DO concentrations, but this variation trend was not observed for TN removal. With the increase of DO concentrations from 2.4 to 6.1mg/L, the removal efficiencies of COD and NH(4)(+)-N were 39-53% and 64-88%, whenas TN removal efficiencies increased from 39 to 42% and then dropped to 35%.     

新型生态膜＋活性炭深度处理深圳某小区生活污水的研究

通过对新型生态膜反应器处理生活污水的试验研究,考察了不同水力停留时间（HRT）对反应器中去除CODer、NH,-N、TP污染物效果的影响。通过实验表明,在实际工况下,控制HRT为最佳工况状态,CODcr、NH3-N、TP的去除率分别达到80％、78％、65％以上,出水浓度可达到30mg／L、5mg／L、1mg／以下。出水水质达到国家标准《城镇污水处理厂污染物排放标准》（GB18918—2002）一级A标准要求。     

TiO2纳米管阵列膜的制备及对304不锈钢的光生阴极保护效应

应用电化学阳极氧化法在Ti表面构筑不同的TiO2纳米管阵列膜。采用XRD、SEM、XPS表征薄膜的结构、形貌和组成。通过电化学阻抗谱及电位随时间变化的测试,考察TiO2薄膜的光生阴极保护效应。结果表明薄膜主要由锐钛矿型的TiO2纳米管阵列组成,当304不锈钢耦连于紫外光照下的TiO2薄膜电极时,其界面反应电阻变小,电极电位显著降低,说明TiO2纳米管薄膜能够对不锈钢产生良好光生阴极保护效应,特别是掺Fe的TiO2薄膜在光照时可使不锈钢电位降低约450mV,而且在暗态时也能较长时间保持对不锈钢的阴极保护作用。     

Degradation of recalcitrant compounds from stabilized landfill leachate using a combination of ozone-GAC adsorption treatment

Laboratory experiments were undertaken to investigate the treatment performances of ozonation alone and/or its combination with granular activated carbon (GAC) adsorption for raw leachate from the NENT landfill (in Hong Kong). To improve its removal of recalcitrant contaminants from the leachate, the surface of GAC was oxidized with ozone prior to treatment. With respect to ozone dose and pH, the removal of COD and/or NH(3)-N from ozonation alone and combined ozone-GAC adsorption were evaluated and compared to those of other physico-chemical treatments in some reported studies. The removal mechanism of recalcitrant compounds by ozone-GAC adsorption treatment was presented. Among the various treatments studied, the combination of ozone-GAC adsorption using ozone-modified GAC had the highest removal for COD (86%) and/or NH(3)-N (92%) compared to ozonation alone (COD: 35%; NH(3)-N: 50%) at the same initial COD and/or NH(3)-N concentrations of 8000 and 2620 mg/L, respectively. Although the integrated treatment was more effective than ozonation alone for treating stabilized leachate, the results suggested that it could not generate treated effluent that complied with the COD limit of lower than 200 mg/L and the NH(3)-N discharge standard of less than 5 mg/L. Therefore, further biological treatments to complement the degradation of the leachate are still required to meet the environmental legislation.     

Cl~-和H_2S对不锈钢电化学行为的协同影响

目前,对Cl~-和H_2S共存条件下不锈钢的腐蚀尤其是点蚀行为鲜有研究。采用动电位扫描和交流阻抗测试研究了304,316L和2205 3种不锈钢在含有不同浓度Cl~-和H_2S的溶液中的电化学行为。结果表明:在含有1 200 mg/L Cl~-的溶液中,随H_2S浓度增大,304和316L的点蚀敏感性均增大,但此条件下的H_2S浓度并未对2205双相不锈钢产生影响。当Cl~-浓度增大到1 500 mg/L时,2205产生了点蚀现象,说明虽然H_2S促进了不锈钢点蚀的发生,但Cl~-是诱导不锈钢产生点蚀的关键因素。     

模拟2倍浓缩海水中聚环氧琥珀酸和Na2MoO4对304不锈钢的缓蚀作用

为开发适用于循环冷却海水／不锈钢体系的绿色缓蚀剂,采用电化学阻抗谱、极化曲线及表面腐蚀形貌分析,研究了聚环氧琥珀酸（PESA）、Na2MoO4在模拟2倍浓缩海水中对304不锈钢的缓蚀作用。结果表明：在模拟2倍浓缩海水中,PESA与Na2MoO4均能在304不锈钢表面形成保护膜,产生缓蚀作用;PESA为阳极吸附型缓蚀剂,...     

Selective inhibition of nitrite oxidation by chlorate dosing in aerobic granules

Partial nitrification was successfully achieved with addition of 5mM KClO(3) in the aerobic granules system. Batch tests demonstrated that KClO(3) selectively inhibited nitrite-oxidizing bacteria (NOB) but not ammonia-oxidizing bacteria (AOB). During stable partial nitrification, the influent pH was kept at 7.8-8.2, while the DO and temperature were not controlled in the SBR. When the NH(4)-N and COD levels were kept at 100mg/l and 400mg/l in the influent, the NH(4)-N and COD removal efficiencies reached 98.93% and 78.65%, respectively. The NO(2)-N accounted for 92.95% of the NO(χ)-N (NO(2)-N+NO(3)-N) in the effluent. Furthermore, about 90% of the chlorate was reduced to nontoxic chloride, thus it would not cause environmental problem. SEM showed that the main composition of the aerobic granules was bacilli and coccus bacteria. FISH analysis revealed that AOB became the dominant nitrifying bacteria, whereas NOB were detected only in low abundance. Chlorate could be used to control the development and maintenance of aerobic granules sludge for partial nitrification.     

Electrolytic treatment of Standard Malaysian Rubber process wastewater

A new method of Standard Malaysian Rubber (SMR) process wastewater treatment was developed based on in situ hypochlorous acid generation. The hypochlorous acid was generated in an undivided electrolytic cell consisting of two sets of graphite as anode and stainless sheets as cathode. The generated hypochlorous acid served as an oxidizing agent to destroy the organic matter present in the SMR wastewater. For an influent COD concentration of 2960 mg/L at an initial pH 4.5+/-0.1, current density 74.5 mA/cm(2), sodium chloride content 3% and electrolysis period of 75 min, resulted in the following residual values pH 7.5, COD 87 mg/L, BOD(5) 60 mg/L, TOC 65 mg/L, total chlorine 146 mg/L, turbidity 7 NTU and temperature 48 degrees C, respectively. In the case of 2% sodium chloride as an electrolyte for the above said operating condition resulted in the following values namely: pH 7.2, COD 165 mg/L, BOD(5) 105 mg/L, TOC 120 mg/L, total chlorine 120 mg/L, turbidity 27 NTU and temperature 53 degrees C, respectively. The energy requirement were found to be 30 and 46 Wh/L, while treating 24 L of SMR wastewater at 2 and 3% sodium chloride concentration at a current density 74.5 mA/cm(2). The observed energy difference was due to the improved conductivity at high sodium chloride content.