硫酸铵颗粒沉积作用下A3钢的大气腐蚀行为

在温度为298 K,相对湿度为(85±5)％的条件下,对硫酸铵颗粒沉积后的A3钢的大气腐蚀行为进行了研究.腐蚀动力学曲线表明,沉积硫酸铵颗粒的A3钢试样比其空白试样的腐蚀更为严重.用IR、SEM/EDAX以及XPS分析研究了不同周期试样的结构和形貌,发现腐蚀主要沿着硫酸铵颗粒沉积的地方进行,随着腐蚀时间的延长,逐渐生成碱式硫酸铁盐,这些腐蚀产物减缓了A3钢腐蚀的速度.对硫酸铵颗粒沉积条件下A3钢的腐蚀机理进行了讨论.     

老山汉墓土遗址盐分调查与分布规律探索

老山汉墓土遗址中可溶-微溶盐导致遗址表面酥碱、起甲、泛白和块状脱落等病害较为严重.利用X射线荧光光谱(XRF)、X射线衍射仪(XRD)、X射线光电子能谱(XPS)以及离子色谱(IC)等方法测定了老山汉墓遗址不同取样位置及距遗址表面不同深度处可溶盐的成分及含量,并分析了盐分对遗址破坏的可能机制.结果表明,该遗址的主要有可溶盐有Na2SO4、Na2SO4·10H2O、Na Cl、Na12Mg7(SO4)13·15H2O,微溶盐有Ca SO4、Ca SO4·2H2O,此外还含有少量的Ca Cl2、KNO3、KCl、Mg Cl2、K2SO4、Mg SO4等盐分.随着取样深度增加,各盐分的种类及含量有所减少,此分布规律可能与可溶盐的赋存环境及水分运移有关.试验结果对于老山汉墓土遗址的保护措施具有一定的参考价值.     

硫酸铵焙烧法从低品位菱镁矿提取镁及其反应动力学研究

将低品位菱镁矿经900 ℃煅烧3 h,产物轻烧镁粉按比例与硫酸铵均匀混合后焙烧,MgO转化为MgSO4,产生的氨气用水吸收得到氨水.焙烧产物经过水溶、过滤,得到硫酸镁溶液.采用TG-DTA和XRD技术分析了轻烧镁粉与硫酸铵的反应历程,计算了反应过程的动力学,采用正交实验确定了反应的最佳工艺条件.研究表明:轻烧镁粉与硫酸铵的焙烧反应分3个阶段完成,第1阶段MgO转化为(NH4)2Mg2(SO4)3;第2阶段 (NH4)2Mg2(SO4)3与MgO反应生成MgSO4;第3阶段 (NH4)2Mg2(SO4)3分解生成MgSO4;3个阶段反应的表观活化能分别为(99.10±1.50),(97.51±1.85)和(133.65±0.46) kJ*mol-1,反应速率常数为2.21,1.07和1.56,并得到每个阶段反应的速率方程.当焙烧温度为475 ℃,焙烧时间为4 h,硫酸铵与氧化镁的物质的量比为1.1∶1时,镁的转化率可达91.4%.     

硅酸盐稀土渣硫酸铵焙烧浸出研究

采用高温直接还原-磁选-(NH4)2SO4焙烧-水浴浸出的工艺流程,从低品位含稀土尾矿中提取稀土。主要考察了(NH4)2SO4配量,焙烧温度和焙烧时间等实验参数对La,Ce,Nd浸出率的影响。通过SEM-EDS,XRD和TG-DSC表征了尾矿经高温直接还原后稀土的赋存状态、不同温度(NH4)2SO4焙烧富稀土渣过程中的物相变化和浸出渣及浸出液烘干后析出晶的物相成分。结果表明:稀土尾矿经高温处理后分别得到了高品位铁精粉和富稀土渣。稀土元素主要以Ca2RE8(Si O4)6O2,CaRE2(Si O4)2硅酸盐形式存在。优化实验条件下,(NH4)2SO4与富稀土按8∶1混匀,400℃焙烧45 min,80℃热水浴浸出时间1 h,浸出液液固比10∶1,La,Ce,Nd浸出率分别为96.13%,98.88%,97.10%。经(NH4)2SO4焙烧处理后,稀土元素的最终产物变为可溶性的(NH4)RE(SO4)2和RE2(SO4)3,萤石部分转变为Ca SO4。     

含O2高温高压CO2环境中3Cr钢腐蚀产物膜特征

采用高温高压反应釜分别开展3Cr钢在CO2和O2共存、单独CO2和单独O2三种气体条件下的腐蚀实验,利用X射线衍射仪(XRD)、扫描电子显微镜(SEM)、能量色散X射线能谱(EDS)和电化学方法研究了3Cr钢在高温高压含有O2的CO2环境中的腐蚀产物膜特征.结果表明,在含有O2的CO2的条件下,3Cr钢表面腐蚀产物膜疏松多孔,主要成分为FeCO3、Fe3O4和Fe2O3,腐蚀产物中未见明显Cr元素富集,3Cr钢表现出点蚀的腐蚀形态.3Cr钢在高温高压含O2的CO2腐蚀条件下内外膜层电阻(Rf1、Rf2)和电荷传递电阻Rt均比仅含有CO2腐蚀环境的低,双电层电容(Cdl)和内外膜层电容(Cf1、Cf2)均比仅含有CO2腐蚀环境的高.含有O2的CO2条件下,其保护性显著低于单一CO2条件下形成的腐蚀产物膜.提出了在含O2的CO2气体条件下,3Cr钢表面存在由多种物质组成的腐蚀产物,这导致腐蚀产物疏松多孔,不会形成单一CO2条件下存在的显著提高腐蚀产物膜保护性的Cr(OH)3层,从而促进了3Cr钢的析氢腐蚀和酸性介质中的吸氧腐蚀的机理.     

生物膜和腐蚀产物膜对A3钢的腐蚀作用研究

应用电化学方法和表面分析技术(AFM和SEM)研究硫酸盐还原菌(SRBB)(生物环境)及其腐蚀产物(非生物环境)对A3钢腐蚀行为的影响以及A3钢在两种不同环境下的腐蚀特征.结果表明:于不同时期生成的微生物膜和腐蚀产物膜,对材料的腐蚀起着不同的作用.生成的生物膜越厚越容易剥落,而不均匀的微生物膜将引起材料的局部腐蚀.在非生物环境中生成的腐蚀产物膜比在生物环境中生成的膜更加紧密地黏附于金属的表面.     

Sn/Al2O3催化剂结构与选择性催化还原NO性能

以不同沉淀剂和铝盐与SnCl4共沉淀制备了Sn/Al2O3催化剂.考察了催化剂在富氧条件下催化丙烯选择性还原NO的性能,借助于X射线衍射(XRD)、扫描电镜(SEM)、N2吸附-脱附、吡啶吸附红外光谱(Py-IR)和程序升温还原(TPR)等方法研究了催化剂性能与结构的关系.发现以NH3.H2O和NH4HCO3为沉淀剂、NH4Al(SO4)2为铝盐制备的Sn/Al2O3催化剂催化活性最高,NO转化率达90.9%,最佳催化活性温度为350℃.该催化剂的比表面积为254 m2/g,孔体积为0.878 cm3/g,孔径分布曲线在3~8 nm出现双峰,Sn物种主要以晶态SnO2存在,且表面Lewis酸酸量增加.     

SRB和CO2共存环境中X60管线钢腐蚀电化学特征

对X60管线钢在硫酸盐还原菌(SRB)和CO2共存环境中进行浸泡实验, 对浸泡不同时间后的腐蚀形态及膜层的组成进行观察和分析, 并对膜层覆盖的X60钢的腐蚀电化学参数特征进行分析. 结果表明, SRB吸附形成的微生物膜覆盖程度加大导致X60钢电位正移, 腐蚀产物FeS和FeCO3含量增加导致X60钢电位负移. X60钢表面膜层中腐蚀产物含量较低时, 仅有一个与电极电位有关的时间常数, 当膜层中腐蚀产物的含量高时, 增加了与腐蚀产物膜有关的时间常数. 在浸泡初期, 随微生物膜覆盖程度增加, X60钢的电荷传递电阻增大; 随腐蚀产物含量增加, 电荷传递电阻先下降后增大. 随浸泡时间的延长, X60钢双电层电容和膜层电容均增大.     

NH_4Al(SO_4)_2·12H_2O的热分解动力学研究

采用热分析(TG-DTA/DTG)、X射线衍射(XRD)研究了固态物质NH4Al(SO4)2.12H2O在氩气中的热分解过程。热分析结果表明,NH4Al(SO4)2.12H2O在氩气中分5步分解,其质量变化率与理论计算相吻合。XRD结果表明,NH4Al(SO4)2.12H2O热分解的最终产物为Al2O3。用Friedman法对各步分解过程的活化能Ea进行了计算,依此为初始值,采用多元非线性回归法得到各个分解步骤可能的动力学模型和参数。     

A3钢在氧化亚铁硫杆菌、链霉菌及其混合菌体系中的腐蚀行为

采用电化学方法和表面分析技术研究了A3钢在链霉菌(Stremptomyces)和氧化亚铁硫杆菌(Thiobacillus fer-rooxidans,T.f)单独及共同作用下的腐蚀行为.结果表明,试样在不同的含菌腐蚀体系中浸泡7d后,表面生成了不均匀的生物膜层,并表现出各不相同的形貌特征;A3钢在氧化亚铁硫杆菌和链霉菌单种菌作用下发生了局部腐蚀,而混合菌体系中的试样发生均匀腐蚀;混合菌体系中A3钢的腐蚀失重速率介于两种菌单独存在时的腐蚀失重速率之间;试样浸泡14d后的电化学阻抗谱(EIS)测试结果表明,A3钢电极在氧化亚铁硫杆菌-链霉菌混合菌体系中的阻抗值介于两种单菌腐蚀体系之间.以上研究结果表明,A3钢在链霉菌体系中腐蚀最重,混合菌体系其次,氧化亚铁硫杆菌体系中腐蚀最轻.     

聚乙二醇-硫酸铵双水相萃取次甲基蓝的研究

利用分光光度法研究了次甲基蓝在聚乙二醇-硫酸铵双水相体系的萃取行为,探索了质量配比(mPEc/m(NH4)2SO4)、温度和次甲基蓝的浓度对双水相及次甲基蓝萃取率(Y)的影响.实验表明:(1)在一定的温度和浓度下,随着mPEC/m(NH4)2SO4的减小,分配系数K( cup/clow)增加,萃取率Y略有减小;(2)在一定的质量配比和浓度下,分配系数K(cup/clow)随温度的升高而增大,但萃取率Y却基本保持不变;(3)在一定的质量配比和温度下,随着次甲基蓝浓度的增加,分配系数K(cup/clow)增大;萃取率Y略有增加.在mPEG/m( NH4) 2SO4为1.50∶1,c次甲基蓝=8.915×10-5mol/L、t=30℃的实验条件下,K(cup/clow)=22.14,萃取率(y)可达95.43％.     

聚吡咯/聚苯胺复合型导电聚合物防腐蚀性能

采用循环伏安法,在含吡咯和苯胺的0.3 mol/L草酸水溶液中制备了聚吡咯/聚苯胺(PPy/Pani)的复合型导电聚合膜。采用红外光谱、极化曲线、自腐蚀电位-时间曲线、扫描电子显微镜和电化学阻抗谱研究了共聚膜的防腐蚀性能。结果表明,在1 mol/L H2SO4中,PPy、Pani与不锈钢基体发生氧化还原反应,促进不锈钢表面发生钝化;当苯胺与吡咯浓度比为1∶3时,制备得到的复合型导电聚合膜所保护的不锈钢自腐蚀电流最小,自腐蚀电位最高,保护时间最长。PPy、Pani及其共聚膜在3.5%NaCl溶液中电化学阻抗谱表明,所制备的PPy、Pani及其共聚物膜与不锈钢基体发生氧化还原反应,使其表面钝化;当Cl-到达不锈钢表面时,破坏钝化膜导致不锈钢腐蚀。     

Surface tensions of inorganic multicomponent aqueous electrolyte solutions and melts

A semiempirical model is presented that predicts surface tensions (σ) of aqueous electrolyte solutions and their mixtures, for concentrations ranging from infinitely dilute solution to molten salt. The model requires, at most, only two temperature-dependent terms to represent surface tensions of either pure aqueous solutions, or aqueous or molten mixtures, over the entire composition range. A relationship was found for the coefficients of the equation σ = c(1) + c(2)T (where T (K) is temperature) for molten salts in terms of ion valency and radius, melting temperature, and salt molar volume. Hypothetical liquid surface tensions can thus be estimated for electrolytes for which there are no data, or which do not exist in molten form. Surface tensions of molten (single) salts, when extrapolated to normal temperatures, were found to be consistent with data for aqueous solutions. This allowed surface tensions of very concentrated, supersaturated, aqueous solutions to be estimated. The model has been applied to the following single electrolytes over the entire concentration range, using data for aqueous solutions over the temperature range 233-523 K, and extrapolated surface tensions of molten salts and pure liquid electrolytes: HCl, HNO(3), H(2)SO(4), NaCl, NaNO(3), Na(2)SO(4), NaHSO(4), Na(2)CO(3), NaHCO(3), NaOH, NH(4)Cl, NH(4)NO(3), (NH(4))(2)SO(4), NH(4)HCO(3), NH(4)OH, KCl, KNO(3), K(2)SO(4), K(2)CO(3), KHCO(3), KOH, CaCl(2), Ca(NO(3))(2), MgCl(2), Mg(NO(3))(2), and MgSO(4). The average absolute percentage error between calculated and experimental surface tensions is 0.80% (for 2389 data points). The model extrapolates smoothly to temperatures as low as 150 K. Also, the model successfully predicts surface tensions of ternary aqueous mixtures; the effect of salt-salt interactions in these calculations was explored.     

O,O′-二(4-甲苯基)二硫代磷酸-N,N-二乙铵的晶体结构、热稳定性及缓蚀性

合成了O,O′-二(4-甲苯基)二硫代磷酸N,N-二乙铵（[Et2NH2][(4-MeC6H4O)2PS2],NOP）,采用元素分析、红外光谱、核磁共振谱和单晶X射线衍射测试技术对其结构进行了表征,同时研究了NOP的热稳定性和缓蚀性。 NOP晶体属单斜晶系,P21/n空间群,晶胞参数为：a=1.424 1(3) nm,b=2.008 7(4) nm,c=1.436 6(3) nm,V=3.959 9(15) nm3,Dc=1.286 Mg/m3,Z=8,F(000)=1.632,μ(MoKα)=0.360 mm-1,S=1.001,(Δ/σ)max=0.001,R1=0.077 6,wR2=0.174 9(I＞2σ(I))。 NOP的不对称结构单元中包括2个独立的子单元,2个子单元之间通过N-H…S氢键形成了一维链结构。 在H2SO4溶液中,NOP能有效抑制Q235钢的腐蚀,是一种抑制阳极反应为主的高效混合型缓蚀剂;NOP在Q235钢表面的吸附符合Langmuir吸附等温式,属自发进行的物理和化学吸附。 CCDC813309     

脱硫脱硝后V2O5/AC在含NH3气氛中的再生及硫资源化的耦合过程研究

V2O5/AC具有很好的烟气同时脱硫脱硝能力,脱硫过程包括其对烟气中SO2的吸附、吸附饱和后SO2从其上的脱附（再生）及脱附出SO2的资源化。考察了同时脱硫脱硝后的V2O5/AC在含NH3气氛中的再生和硫资源化的耦合过程。研究了NH3注入量、再生温度、再生时间和尾气循环流量对再生效率、硫回收率及二次脱硫脱硝活性的影响。结果表明,再生温度和再生时间主要影响SO2的脱附,因而影响再生效率和二次脱硫脱硝活性;NH3注入量不影响SO2的脱附,但明显影响硫回收率和二次脱硫脱硝活性;尾气循环模式是提高硫回收率的重要方法,但在研究的条件下循环流量对再生效率、硫回收率和二次脱硫脱硝活性的影响不大。     

Investigation of Glass-Like Sol-Gel Coatings for Corrosion Protection of Stainless Steel Against Liquid and Gaseous Attack

Glass-like sol-gel coatings have been investigated as corrosion protective coatings on stainless steel. Magnesium- and borosilicate coatings with thickness of about 100–700 nm and methyl-modified SiO2 coatings with a thickness of about 2 m were deposited on stainless steel plates by dip-coating. The coatings were densified between 400°C and 500°C in different atmospheres (N2, air) for 1 h. The corrosion protection against gaseous attack was investigated by accelerated corrosion tests, at 800°C in air for 1 h. A corrosion protection factor was calculated from the relation Fe/Fe2O3, determined by XRD on the surface of coated and uncoated samples. Methyl-modified SiO2 coatings showed a protection factor, which was 2 orders of magnitude higher than for the other coatings. Electrochemical investigations were performed on samples submerged in a NaCl solution for 200 h. The corrosion propagation, polarization resistance and impedance vector were measured. For accelerated corrosion tests, polarization intensity curves were determined for high potentials of up to 1 V. Again excellent results were obtained for the methyl-modified SiO2 coatings, which remained passive for 200 h. Results of the salt spray corrosion test, however, showed no corrosion protection by the sol-gel coatings. After 2000 h in the salt spray chamber the steel was corroded and the coatings peeled off. It is concluded that for the further development of these coatings an improved interfacial passivation will be required.     

XPS depth profile study of porous zirconia films deposited on stainless steel by spray pyrolysis: the problem of substrate corrosion

Zirconia (ZrO₂) films of tissue‐like structure and narrow pore size distribution have been deposited by spray pyrolysis using aqueous zirconyl chloride octahydrate (ZrOCl₂·8H₂O) precursor solutions. Stainless‐steel sheets, protected or unprotected by a ZnO barrier layer, have been used as the substrate material held at 473 K. The ZnO barrier layers have been deposited on the stainless steel held at 523 K by spray pyrolysis using a zinc acetate precursor. Their property of corrosion protection to stainless steel has been proved by electrochemical polarization measurements in 0.5 M NaCl solution. A complementary study of XPS (depth profiling, mapping) and x‐ray diffraction has shown that the unprotected steel substrates were corroded during ZrO₂ film post‐annealing in air at T ≥ 773 K, whereas steel substrates protected with a compact barrier layer of crystalline ZnO before ZrO₂ film deposition did not show surface corrosion even after annealing up to 997 K. Copyright © 2004 John Wiley & Sons, Ltd.     

Densities and apparent molar volumes of atmospherically important electrolyte solutions. 1. The solutes H2SO4, HNO3, HCl, Na2SO4, NaNO3, NaCl, (NH4)2SO4, NH4NO3, and NH4Cl from 0 to 50 °C, including extrapolations to very low temperature and to the pure liquid state, and NaHSO4, NaOH, and NH3 at 25 °C

Calculations of the size and density of atmospheric aerosols are complicated by the fact that they can exist at concentrations highly supersaturated with respect to dissolved salts and supercooled with respect to ice. Densities and apparent molar volumes of solutes in aqueous solutions containing the solutes H(2)SO(4), HNO(3), HCl, Na(2)SO(4), NaNO(3), NaCl, (NH(4))(2)SO(4), NH(4)NO(3), and NH(4)Cl have been critically evaluated and represented using fitted equations from 0 to 50 °C or greater and from infinite dilution to concentrations saturated or supersaturated with respect to the dissolved salts. Using extrapolated densities of high-temperature solutions and melts, the relationship between density and concentration is extended to the hypothetical pure liquid solutes. Above a given reference concentration of a few mol kg(-1), it is observed that density increases almost linearly with decreasing temperature, and comparisons with available data below 0 °C suggest that the fitted equations for density can be extrapolated to very low temperatures. As concentration is decreased below the reference concentration, the variation of density with temperature tends to that of water (which decreases as temperature is reduced below 3.98 °C). In this region below the reference concentration, and below 0 °C, densities are calculated using extrapolated apparent molar volumes which are constrained to agree at the reference concentrations with an equation for the directly fitted density. Calculated volume properties agree well with available data at low temperatures, for both concentrated and dilute solutions. Comparisons are made with literature data for temperatures of maximum density. Apparent molar volumes at infinite dilution are consistent, on a single ion basis, to better than ±0.1 cm(3) mol(-1) from 0 to 50 °C. Volume properties of aqueous NaHSO(4), NaOH, and NH(3) have also been evaluated, at 25 °C only. In part 2 of this work (ref 1 ) an ion interaction (Pitzer) model has been used to calculate apparent molar volumes of H(2)SO(4) in 0-3 mol kg(-1) aqueous solutions of the pure acid and to represent directly the effect of the HSO(4)(-) ? H(+) + SO(4)(2-) reaction. The results are incorporated into the treatment of aqueous H(2)SO(4) density described here. Densities and apparent molar volumes from -20 to 50 °C, and from 0 to 100 wt % of solute, are tabulated for the electrolytes listed in the title and have also been incorporated into the extended aerosol inorganics model (E-AIM, http://www.aim.env.uea.ac.uk/aim/aim.php) together with densities of the solid salts and hydrates.     

低温NH_3-SCR催化剂MnO_x-CeO_x/ACF的SO_2中毒机理(英文)

在二氧化硫(SO2)气氛下,对Fe、Cu和V改性的催化剂MnOx-CeOx/ACF(活性碳纤维)的氨选择性催化还原(NH3-SCR)一氧化氮的低温活性进行研究.实验结果表明:以Cu和V改性催化剂未提高MnOx-CeOx/ACF的低温抗SO2性能;Fe改性MnOx-CeOx/ACF在初始6h内提高了催化剂的抗SO2性能,但较长时间仍然失活.以N2吸附、X射线光电子能谱(XPS)、傅里叶变换红外(FT-IR)光谱以及热重分析(TGA)等手段对中毒催化剂进行分析.在SO2存在下,催化剂中毒归因于两个方面:一是覆盖于催化剂表面的铵盐类物质,二是SO2与催化剂中的金属氧化物反应生成的金属硫酸盐及亚硫酸盐.在中毒催化剂中硫元素主要以金属硫酸盐及亚硫酸盐的形式存在,其在中毒的MnOx-CeOx/ACF、Fe-MnOx-CeOx/ACF、Cu-MnOx-CeOx/ACF和V-MnOx-CeOx/ACF催化剂中所占比例分别为70.4%、68.9%、86.3%和71.4%(w).进一步揭示了MnOx-CeOx/ACF催化剂在低温SCR条件下的SO2中毒机理.