纳米TiO2/SiO2对甲苯-SO2体系气相光催化作用的影响因素

以纳米TiO₂/SiO₂为光催化剂、C₇H₈(toluene)-SO₂-O₂-TiO₂/SiO₂为重点研究体系,研究了甲苯的初始浓度、氧气含量、水蒸气含量和光强对甲苯光催化降解的影响。结果发现,甲苯的初始反应速率随其初始浓度的增加而增大,并最终趋于稳定;随着含氧量增加而不断增大,体积分数为25％时达到最大,之后逐渐减小;水蒸气的体积分数为0.4%时,甲苯降解速率最大;光强增加,甲苯增大反应速率, 3.0 mW/cm²时反应速率趋于定值。体系中引入SO₂促进了甲苯的初步降解,却抑制反应中间产物的进一步降解;同时甲苯的存在也抑制了SO₂的降解。     

高盐强酸性地下水中复合苯系污染物原位芬顿氧化实验研究

在原位氧化过程中,实际场地地下水和含水介质的物化特征是影响氧化效果的重要因素,而目前对此影响的研究较少。以某场地实际高盐强酸性复合苯系污染地下水为研究对象,以地下水中2-硝基-4-甲氧基苯胺(2-nitro-4-methoxyaniline,2-N)和3-硝基-4-甲氧基苯胺(3-nitro-4-methoxyaniline,3-N)为特征污染物,探究芬顿(Fenton)试剂原位氧化特征,并研究液相环境因素(初始H2O2浓度、初始Fe2+浓度、初始pH值、初始醋酸(Acetic acid,HAc)浓度、初始SO4^2-浓度)以及含水层介质对Fenton法去除2-N和3-N的影响。结果显示:(1)Fenton法去除2-N和3-N效果显著,且在初始液相条件为c(H2O2)=7 mmol/L、c(Fe²⁺)=4 mmol/L、pH=4、c(HAc)=0 mg/L和c(SO4^2-)=0 mmol/L时去除效果最佳;(2)各因素对Fenton法氧化2-N和3-N的影响不同,加入H₂O₂和Fe²⁺使2-N和3-N去除率上升,增大HAc浓度使2-N和3-N去除率下降;(3)含水层介质对2-N和3-N具有一定吸附性,且对3-N的吸附性强于2-N,二者在本实验中最大吸附态占比分别为29%和42%,而吸附态的存在会抑制Fenton法对2-N和3-N的去除;(4)矿物分析结果显示介质含有少量黄铁矿,在硫酸环境下,介质腐蚀溶解释放Fe²⁺,在达到一定浓度后,无需额外添加Fe²⁺即可完成Fenton反应进而去除2-N和3-N。     

离子色谱法测定环境水中阴离子

建立了测定环境水中阴离子的方法.以1.8 mmol/L Na₂CO₃和1.7 mmol/L NaHCO₃为淋洗液,36 mmol/L的H₂SO₄为微膜抑制器的再生液,用Pac AS-14A阴离子分离柱,一次进样10 μL,8 min内检测出7种阴离子.详细讨论了色谱的工作条件及其影响因素.该方法简便、快速、准确度高,能够满足环境水样中阴离子的分析要求.     

装涂油漆废水的处理工艺研究

在对微电解、H₂O₂氧化机理研究的基础上,对装涂油漆废水提出利用微电解-化学氧化法处理的方案,通过实验确定出最佳的微电解反应条件及氧化条件。实验结果表明,该方法可使原水的ρ(COD_cr)从4 000 mg/L降至100 mg/L,废水的COD_cr去除率>95%,出水达到排放标准。本研究对微电解方案存在的问题进行了分析,并提出部分解决措施。     

铁盐淋洗剂对稀土污染土壤的淋洗修复研究

稀土矿的大量开采,加剧了土壤污染,危害居民健康。本研究采用不同三价铁盐(Fe₂(SO₄)₃、Fe(NO₃)₃和FeCl₃)对稀土污染的农田土壤进行淋洗修复,同时对比其他无机盐(亚铁盐、镁盐、铵盐和钠盐)的淋洗效果;并研究三价铁盐淋洗剂浓度、液固比和淋洗时间对稀土元素(REE)去除效果的影响。结果表明,三价铁盐对REE的淋洗率高达41.7%～54.3%,显著高于其他无机盐(0.2%～26.8%);三价铁盐的最佳淋洗时间为1440 min,当淋洗剂浓度从5 mmol/L增加到50 mmol/L的过程中,土壤中REE淋洗率显著增加,淋洗率随淋洗液固比(1∶1～5∶1)的升高而增加,其中,淋洗剂浓度对REE去除率的促进作用显著大于液固比。在优化淋洗条件下,Fe₂(SO₄)₃对REE的淋洗率为54.3%,显著高于Fe(NO₃)₃(46.1%)和FeCl     

Fe/Ag催化臭氧氧化降解苯酚的研究

为研究双金属催化剂去除有机污染物的效果,采用自制Fe/Ag催化剂对模拟苯酚废水进行了臭氧催化氧化处理。通过扫描电子显微镜(SEM)、比表面积分析仪(BET)和X射线衍射(XRD)对催化剂进行表征,并考察了催化剂类型、催化剂投加量和溶液初始pH值对降解效果的影响规律。结果表明:与Fe相比,Fe/Ag比表面积减少了22.8%,在Fe/Ag/O₃与含苯酚废水的反应体系中,反应遵循臭氧直接作用和活性自由基(·OH、·O₂、H₂O₂)共同作用的机理;Fe/Ag在反应过程中体现出良好的协同作用;300 mg/L的苯酚模拟废水在pH=6.3、Fe/Ag投加量为1.00 g的最优反应条件下经60 min反应,苯酚与化学需氧量(COD)去除率比单独臭氧氧化分别提高了18.4%和29.4%。     

H_2O_2增效TiO_2/凹凸棒石光催化体系降解亚甲基蓝

以钛酸四丁酯为前驱体,天然凹凸棒石为载体,采用溶胶凝胶法制备了TiO_2/凹凸棒石复合光催化剂,并用XRD、TEM对其进行表征.以亚甲基蓝染料为模拟污染物,采用300 W汞灯为紫外光源,以光催化实验来评价该催化剂的活性,并研究了H_2O_2的引入对光催化活性的影响.实验结果表明,H_2O_2能显著提高染料的脱色效率:亚甲基蓝的初始浓度为50 mg/L,催化体系为2 mmol/L H_2O_2+0.5 g/L TiO_2/凹凸棒石+UV(紫外线),光催化10 min后其脱色率为95%,相对于单独的0.5 g/L TiO_2/凹凸棒石+UV催化体系,其脱色率提高了约50%.全波段扫描显示,加入H_2O_2后,亚甲基蓝在290 nm对应的苯环吸收蜂急剧下降,665 nm对应的最大吸收峰则近乎消失,且没有新的吸收峰产生.     

二价铁活化过硫酸盐去除水中苯胺

零价铁和硝基苯反应后生成二价铁和苯胺,而苯胺也是地下水污染物。硫酸根自由基具有强氧化性,可以降解苯胺。而二价铁可以活化过硫酸盐产生硫酸根自由基,进而去除苯胺。本文研究了二价铁浓度、过硫酸盐浓度、苯胺初始浓度、体系初始pH、反应温度等因素对二价铁活化过硫酸盐去除水中苯胺处理效率的影响。结果表明:1)Fe2+活化过硫酸盐生成SO-4·能快速并有效氧化降解苯胺,对于目标浓度为1 000 mg/L的苯胺而言,Fe2+浓度为3.3 mmol/L,Na2S2O8浓度为4.4 mmol/L时,对苯胺有较佳降解效果,苯胺的降解率为86.33%。2体系对较低浓度的苯胺降解效果较好,当污染物初始浓度由1 000 mg/L降低到500 mg/L和100 mg/L时,苯胺降解率由86.33%升高为90.27%和97.16%。3初始pH对苯胺的降解率影响较大,中性条件下(pH=7左右)降解率较好,高初始pH(pH=9,11)和低初始pH条件(pH=3,5)下均低于中性条件下苯胺的降解效率。4体系的温度变化对降解率影响不明显。     

电化学循环井驱动模拟含水层化学氧化降解三氯乙烯

传统原位化学氧化地下水修复技术存在氧化剂迁移距离短和利用率低等问题。本研究在双井循环模式促进传质的基础上,通过注水井中的地下水电解原位提供O₂和H₂,配合乙二胺四乙酸(ethylenediamine tetraacetic acid,EDTA)络合溶解出含水层Fe(Ⅱ),活化O₂产生羟基自由基(•OH),实现地下水三氯乙烯(TCE)的氧化降解。在填充了砂土和黏土互层的二维砂槽中,设置电流为0.2 A、流速为72 cm/d、初始TCE浓度为3 mg/L,经过9 d的连续通电处理后,TCE浓度降低到1 mg/L,降解率达到67%。通电前投加0.5 mmol/L EDTA,经过1 d水流循环后含水层中溶解态Fe(Ⅱ)浓度从02 mg/L增加到414 mg/L,黏土区域较高。通电过程中,循环井促进O₂、Fe(Ⅱ)-EDTA和TCE的有效接触与反应,使TCE氧化降解。通电初期,黏土区域Fe(Ⅱ)氧化速率、TCE降解速率较周围慢,后期差异逐渐减小。未通电时加入醋酸钠可促进Fe(Ⅲ)还原,使含水层中铁循环利用。该修复过程通过循环井提升了氧化剂迁移距离,使用源于含水层的Fe(Ⅱ)-EDTA和稳定性较好的O₂提高了氧化剂利用率,有望应用于有机污染地下水修复。     

AlCl3对细颗粒泥沙絮凝沉降的影响

铝类絮凝剂对细颗粒泥沙絮凝沉降有重要作用,常应用于浑水澄清、农业污水处理等研究中。在AlCl₃浓度为0～1.7mmol/L,泥沙浓度为10g/L时,用吸管法研究了AlCl₃对细颗粒泥沙絮凝沉降的影响,结果表明:在液面下同一深度,泥沙浓度随时间呈指数衰减;悬液经多次搅拌后再沉降,其沉速减缓;当AlCl₃浓度为0.9～1.7mmol/L时,出现明显的清浑水交界面,交界面随时间等速下降,平均沉速为4.756cm/min,对应的絮团平均粒径为0.0315mm;土娄土絮凝临界粒径为0.027mm。     

A hydrothermal investigation of the system FeO, Fe2O3, TiO2

Phase relations in the system FeO---Fe₂O₃---TiO₂, at temperatures ranging between 300°C and 700°C, have been investigated experimentally with special refference to the reaction Fe₃O₄ + TiO₂ = Fe₂O₃ + FeTiO₃. Pressure was varied between 500 and 2000 bars but its effect was negligible. Magnetite and rutile are the stable assemblage at temperatures above 550 dgC, and hematite and ilmenite are stable for lower temperatures. The equilibrium oxygen fugacity is estimated to be 10^−17.5 bars at equilibrium temperature. It is suggested that intermediate hematite-ilmenite solid solutions are inhomogeneous, consisting of ‘domains’ of hematite and ilmenite. The ‘domains’ are too small to be resolved by X-ray diffraction techniques. The top of the solvus curve in the hematite-ilmenite solution corresponds to a temperature of 660°C. Regular solution theory is not applicable to the solid solution.     

The influence of Cr on the garnet–spinel transition in the Earth''s mantle: experiments in the system MgO–Cr2O3–SiO2 and thermodynamic modelling

The position of the transition from spinel peridotite to garnet peridotite in a simplified chemical composition has been determined experimentally at high pressures and high temperatures. The univariant reaction MgCr₂O₄+2Mg₂Si₂O₆=Mg₃Cr₂Si₃O₁₂+Mg₂SiO₄, has a negative slope in P–T space between 1200 °C and 1600 °C. The experimental results, combined with assessed thermodynamic data for MgCr₂O₄, MgSiO₃ and Mg₂SiO₄ give the entropy and enthalpy of formation of knorringite garnet (Mg₃Cr₂Si₃O₁₂). Thermodynamic calculations in simplified chemical compositions indicate that Cr shifts the garnet-in reaction to much higher pressures than previously anticipated. Moreover, in Cr-bearing systems a pressure–temperature field exists where garnet and spinel coexist. The width of this divariant field strongly depends on the Cr/(Cr+Al) of the system.     

Fenton试剂氧化-微电解-接触氧化法处理丙烯腈废水实验研究

实验采用Fenton试剂氧化-微电解-接触氧化组合工艺处理丙烯腈废水。研究了各单元工艺的最佳控制参数和操作条件。结果表明,在废水pH值为3左右、反应时间2 h的前提下,双氧水投加量40 mL/L,二价铁离子质量浓度为0.4 g/L,再经过微电解处理后的出水进入接触氧化阶段。在溶解氧为4.5 mg/L左右,水力停留时间为10 h、容积负荷1.0 kg COD_Cr/（m³·d）左右的条件下,出水COD_Cr小于100 mg/L,可达到国家对丙烯腈废水处理要求的一级标准。     

Marcasite precipitation from hydrothermal solutions

Pyrite and marcasite were precipitated by both slow addition of aqueous Fe²⁺ and SiO₃²⁻ to an H₂S solution and by mixing aqueous Fe²⁺ and Na₂S₄ solutions at 75°C. H₂S₂ or HS₂⁻ and H₂S₄ or HS₄⁻ were formed in the S₂O₃²⁻ and Na₂S₄ experiments, respectively. Marcasite formed at pH < pK₁ of the polysulfide species present (for H₂S₂, pK₁ = 5.0; for H₂S₄, pK₁ = 3.8 at 25°C). Marcasite forms when the neutral sulfane is the dominant polysulfide, whereas pyrite forms when mono-or divalent polysulfides are dominant. In natural solutions where H₂S₂ and HS₂ are likely to be the dominant polysulfides, marcasite will form only below pH 5 at all temperatures.

The pH-dependent precipitation of pyrite and marcasite may be caused by electrostatic interactions between polysulfide species and pyrite or marcasite growth surfaces: the protonated ends of H₂S₂ and HS₂ are repelled from pyrite growth sites but not from marcasite growth sites. The negative ions HS₂ and S₂²⁻ are strongly attracted to the positive pyrite growth sites. Masking of 1π_g^* electrons in the S₂ group by the protons makes HS₂ and H₂S₂ isoelectronic with AsS²⁻ and As₂²⁻, respectively ( et al., 1981). Thus, the loellingitederivative structure (marcasite) results when both ends of the polysulfide are protonated.

Marcasite occurs abundantly only for conditions below pH 5 and where H₂S₂ was formed near the site of deposition by either partial oxidation of aqueous H₂S by O₂ or by the reaction of higher oxidation state sulfur species that are reactive with H₂S at the conditions of formation e.g., S₂O₃²⁻ but not SO₄²⁻. The temperature of formation of natural marcasite may be as high as 240°C ( and , 1985), but preservation on a multimillion-year scale seems to require post-depositional temperatures of below about 160°C ( , 1973; and , 1985).     

Status report on stability of K-rich phases at mantle conditions

Experimental research on K-rich phases and observations from diamond inclusions, UHP metamorphic rocks, and xenoliths provide insights about the hosts for potassium at mantle conditions. K-rich clinopyroxene (Kcpx–KM³⁺Si₂O₆) can be an important component in clinopyroxenes at P>4 GPa, dependent upon coexisting K-bearing phases (solid or liquid) but not, apparently, upon temperature. Maximum Kcpx content can reach 25 mol%, with 17 mol% the highest reported in nature. Partitioning ^(K)D_(cpx/liquid) above 7 GPa=0.1–0.2 require ultrapotassic liquids to form highly potassic cpx or critical solid reactions, e.g., between Kspar and Di. Phlogopite can be stable to about 8 GPa at 1250 °C where either amphibole or liquid forms. When fluorine is present, it generally increases in Phl upon increasing P (and probably T) to about 6 GPa, but reactions forming amphibole and/or KMgF₃ limit F content between 6 and 8 GPa. The perovskite KMgF₃ is stable up to 10 GPa and 1400 °C as subsolidus breakdown products of phlogopite upon increasing P. ^(M4)K-substituted potassic richterite (ideally K(KCa)Mg₅Si₈O₂₂(OH,F)₂) is produced in K-rich peridotites above 6 GPa and in Di+Phl from 6 to 13 GPa. K content of amphibole is positively correlated with P; Al and F content decrease with P. In the system 1Kspar+1H₂O K-cymrite (hydrous hexasanidine–KAlSi₃O₈·nH₂O–Kcym) is stable from 2.5 GPa at 400 to 1200 °C and 9 GPa; Kcym can be a supersolidus phase. Formation of Kcym is sensitive to water content, not forming within experiments with H₂O2O>Kspar. Phase X, a potassium di-magnesium acid disilicate ((K_1−x−n)₂(Mg_1−nM_n³⁺)₂Si₂O₇H_2x), forms in mafic compositions at T=1150–1400 °C and P=9–17 GPa and is a potential host for K and H₂O at mantle conditions with a low-T geotherm or in subducting slabs. The composition of phase-X is not fixed but actually represents a solid solution in the stoichiometries □₂Mg₂Si₂O₇H₂–(K□)Mg₂Si₂O₇H–K₂Mg₂Si₂O₇ (□=vacancy), apparently stable only near the central composition. K-hollandite, KAlSi₃O₈, is possibly the most important K-rich phase at very high pressure, as it appears to be stable to conditions near the core–mantle boundary, 95 GPa and 2300 °C. Other K-rich phases are considered.     

镁铝对烧结矿中铁酸钙的矿物学特性影响

铁酸钙是高碱度烧结矿中的主要黏结相矿物,它的含量、结晶形态、化学成分及晶体结构等矿物学特性对烧结矿质量起着关键性作用,而烧结原料中各组分的含量直接影响着铁酸钙的生成。以Fe₃O₄、SiO₂、CaO、MgO、Al₂O₃的化学纯试剂为原料,在实验室进行微型烧结实验,运用XRD、偏光显微镜、电子探针等手段,定量分析研究了原料组分中MgO、Al₂O₃对烧结矿中铁酸钙的生成及其矿物学特性的影响。原料中MgO含量的增加对铁酸钙的生成有一定抑制作用,尤其在MgO含量为2.0%~3.0%时,烧结矿中铁酸钙含量明显减少,其晶体形态也从以板柱状和针状为主逐渐过渡为它形不规则状;原料中Al₂O₃的增加,对烧结矿中铁酸钙的形成具有促进作用,即随着Al₂O₃的增加铁酸钙含量呈明显增加趋势,且铁酸钙的形态也由以柱状和针状为主向板柱状变化。电子探针成分分析及矿物化学式计算结果表明,铁酸钙是由Fe₂O₃、CaO、SiO₂、Al₂O₃及MgO组成的复杂结晶体,其化学通式为Ca_2.60Mg_0.44Si_1.07Al_0.96Fe_8.92O₂₀。原料中MgO、Al₂O₃含量的变化,对铁酸钙的化学成分中Fe₂O₃/CaO摩尔分数比影响不大,均接近3∶2。上述研究结果对于深刻理解烧结工艺条件下铁酸钙晶相的晶体化学特征及其对烧结矿质量的影响具有重要指导意义。