电炉铁合金飞灰中金属和二噁英分布特性研究

分别利用高分辨气相色谱-低分辨质谱(HRGC-LRMS)联用仪、原子吸收分光光度计对4个电炉铁合金飞灰中4-8氯取代PCDD/Fs和12种金属进行检测,结果表明,飞灰中金属元素浓度高,其中重金属以Zn浓度最高,为19835.918~36729.200mg/kg;Ni浓度最低,为9.000~43.627mg/kg.4个灰样中PCDD/Fs的浓度差别较大,总量在33.792~88.125ng/g范围内,该浓度水平与生活垃圾焚烧飞灰相当.4个灰样中PCDD/Fs的分布特征不尽相同,但是均以OCDD/F的浓度最高.飞灰中较高的二噁英浓度水平与高浓度的Fe、Cu、Ca和Ni等金属存在一定的相关性.     

Characterization of chlorine and heavy metals for the potential recycling of bottom ash from municipal solid waste incinerators as cement additives

Bottom ash is an inevitable by-product from municipal solid waste (MSW) incineration plants. Recycling it as additives for cement production is a promising disposal method. However, the heavy metals and chlorine are the main limiting factors because of the potential environmental risks and corrosion of cement kilns. Therefore, investigating heavy metal and chlorine characteristics of bottom ash is the significant prerequisite of its reuse in cement industries. In this study, a correlative analysis was conducted to evaluate the effect of the MSW components and collection mode on the heavy metal and chlorine characteristics in bottom ash. The chemical speciation of insoluble chlorine was also investigated by synchrotron X-ray diffraction analysis. The results showed that industrial waste was the main source of heavy metals, especially Cr and Pb, in bottom ash. The higher contents of plastics and kitchen waste lead to the higher chlorine level (0.6 wt.%–0.7 wt.%) of the bottom ash. The insoluble chlorine in the MSW incineration bottom ash existed primarily as AlOCl, which was produced under the high temperature (1250°C) in incinerators.

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生活垃圾焚烧飞灰差异性特征对脱氯除盐效果影响研究——以重庆和天津飞灰为例

随着生活垃圾焚烧技术的普及,垃圾焚烧飞灰的资源化利用迫在眉睫,然而飞灰中的高浓度氯元素严重阻碍了其资源化进程.水洗技术作为常用的脱氯除盐技术,得到越来越多的应用,但除氯效果受飞灰自身性质特征影响较大.本研究从重庆和天津采集了两种理化性质具有较大差异的垃圾焚烧飞灰,在对其粒径分布、化学组成、矿物组成、pH值和浸出毒性等基本特征进行分析表征的基础上,采用水洗技术和碳酸化水洗技术对两种飞灰进行了脱氯处理.结果表明,重庆飞灰氯元素的赋存形态包括NaCl、KCl等可溶性氯盐,还含有较高浓度的难溶氯盐(如CaClOH、Friedel盐和Ca₆(CO₃)₂(OH)₇Cl),因此,水洗技术难以达到理想的脱氯效果,氯盐去除率最高为88%.在水洗过程中通入CO₂可以显著降低反应体系的pH值,促进难溶盐的转化和溶解,进而提高飞灰氯盐的去除率.重庆飞灰采用加速碳酸化水洗技术,氯盐去除率最高可达94%.天津飞灰中氯元素主要以可溶性氯盐的形式存在,难溶盐占比很少,因此,水洗技术可以达到较高的脱盐率(96%).采用加速碳酸化技术对天津飞灰进行处理,发现氯盐去除率较纯水洗技术反而有所降低,分析其主要原因可能与加速碳酸化过程中碳酸钙等物质的再沉淀对氯盐的裹挟作用有关.由此可知,飞灰自身性特征尤其是氯盐的赋存形态对于脱氯除盐技术的选择有重要影响.因此,实际资源化利用过程中,可根据飞灰性质来决定预处理手段,从而最大化提升效率和节约成本.     

垃圾渗沥液腐蚀下污泥灰改性黏土压缩特性及孔隙结构

采用市政污泥为原材料烧制污泥灰,并将污泥灰作为改良添加剂对传统填埋场压实黏土衬垫系统进行改性,以达到实现污泥资源化利用以及减少黏土作为衬垫防渗材料的用量.为评价污泥灰改性黏土作为填埋场衬垫材料的工程特性以及微观结构,通过固结压缩试验、低温氮气吸附试验、颗粒分析试验分别检测改性黏土的压缩特性、微观孔隙结构、颗粒组成.压缩试验结果表明,受垃圾渗沥液腐蚀后的改性黏土,随污泥灰含量的增加,孔隙比增大、压缩量减小;经垃圾渗沥液腐蚀后,改性黏土的压缩系数(α1-2)为0.310~0.391MPa-1,固结系数(Cv)为2.446~2.768cm2/s.低温氮气吸附试验结果表明,改性黏土的吸附-脱附等温线属于Ⅴ型等温线;对于垃圾渗沥液腐蚀的改性黏土,孔径分布呈双肩峰形式,孔径为3~7nm的孔隙占比较大,累计孔容为0.509~0.530cm3/g.颗粒分析试验结果显示,受渗沥液腐蚀后改性黏土颗粒组成差异性明显,粒径>11.5 μm的颗粒为35.09%~49.42%;粒径为2.3~1.5 μm的颗粒为2.35%~7.28%;粒径<2.3 μm的颗粒为46.57%~57.63%.污泥灰改性黏土具有较好的抗垃圾渗滤液腐蚀效果,可将其作为填埋场衬垫材料使用.     

垃圾焚烧飞灰成型及低温烧结稳定化研究

对焚烧飞灰进行水泥固化成型,并对成型体进行烧结研究。通过XRD、SEM等表征方法探索垃圾了焚烧飞灰在高温条件下的反应机理,以及添加助熔剂对烧结的影响。结果表明:添加Na2CO3可促进水泥早期的固化,但对水泥后期的固化不利;在养护时间为2 d时,水泥固化飞灰试块抗压强度达到1.91 MPa,完全满足成型的要求;XRD和SEM分析结果表明:固化体烧结后主要生成钙铝黄长石、硅酸钙等,Na2B4O7·10H2O的助熔效果明显;随着烧结温度的升高,重金属Ni、Cu、Pb和Cd的浸出浓度和浸出率下降,随着助熔剂Na2B4O7·10H2O添加量的增加,重金属Cu和Cd的浸出率增加,Pb的浸出率降低;浸出实验结果表明:重金属Ni、Cu、Pb和Cd的浸出浓度远低于国家标准。     

利用改性钒钛钢渣和飞灰吸附模拟烟气中的Hg0

固体废弃物钒钛钢渣(VTS)、飞灰(FA)含有Fe、V、Ti等可促进Hg0氧化吸附的过渡金属氧化物,为提高VTS吸附Hg0性能、改性FA的抗硫特性,利用蒸汽活化、浸渍FeCl₃方法改性FA/VTS、FA/CaO,在固定吸附床上研究了不同改性方法、反应温度(T)、烟气ρ(SO₂)和ρ(HCl)对η(吸Hg0效率)的影响. 结果表明:蒸汽活化对提高η的作用有限. 经浸渍FeCl₃方法改性的FA/VTS,其η显著提高,在200 ℃下,吸附20 min时可达93%,吸附10 h后的Q(吸附容量)为0.42 mg/g;而浸渍FeCl₃方法改性的FA/CaO,其η随温度呈先升后降趋势,在120 ℃、吸附20 min时达到最高(74%). SO₂抑制Hg0的吸附,但FA/VTS的抗硫性能较FA/CaO有显著提高,具有低温抗硫吸附Hg0的潜势,可能与VTS中Ti的质量分数高有关. HCl可促进Hg0的吸附,在ρ(HCl)为30 mg/m3条件下,浸渍FeCl₃方法改性的FA/VTS吸附2 h的η在90%以上. 研究表明,经FeCl₃浸渍改性的FA/VTS是较好的Hg0吸附剂,具有实际应用的潜势.      

城市生活垃圾焚烧灰渣浸出试验

选择了城市生活垃圾焚烧炉渣中8种含量高、危害大的金属元素进行了静态和动态浸出性试验。结果表明,钙含量和温度是影响有害金属离子溶出的主要因素。对8种金属离子的浸出率和迁移规律进行了排序和分析,为灰渣安全处理和合理利用提供了科学依据。     

Aggravation of membrane fouling and methane leakage by a three-phase separator in an external anaerobic ceramic membrane bioreactor

The existence of three-phase separator did not affect COD removal in the EAnCMBR. The existence of three-phase separator aggravated methane leakage of EAnCMBR. The existence of three-phase separator aggravated membrane fouling rate of EAnCMBR. Start-up of EAnCMBR equipped three-phase separator was slightly delayed. The three-phase separator is a critical component of high-rate anaerobic bioreactors due to its significant contribution in separation of biomass, wastewater, and biogas. However, its role in an anaerobic membrane bioreactor is still not clear. In this study, the distinction between an external anaerobic ceramic membrane bioreactor (EAnCMBR) unequipped (R1) and equipped (R2) with a three-phase separator was investigated in terms of treatment performance, membrane fouling, extracellular polymers of sludge, and microbial community structure. The results indicate that the COD removal efficiencies of R1 and R2 were 98.2%±0.4% and 98.1%±0.4%, respectively, but the start-up period of R2 was slightly delayed. Moreover, the membrane fouling rate of R2 (0.4 kPa/d) was higher than that of R1 (0.2 kPa/d). Interestingly, the methane leakage from R2 (0.1 L/d) was 20 times higher than that from R1 (0.005 L/d). The results demonstrate that the three-phase separator aggravated the membrane fouling rate and methane leakage in the EAnCMBR. Therefore, this study provides a novel perspective on the effects of a three-phase separator in an EAnCMBR.     

粉煤灰基吸附剂对模拟废水中Cd2+的吸附性能

以粉煤灰为原料、Na2CO3为助熔剂,采用盐熔融—水浴结晶法制备粉煤灰基吸附剂。探讨了吸附剂的最佳制备条件及其对模拟废水中Cd2+的最佳吸附条件、吸附动力学和吸附机理。实验结果表明:制备吸附剂的最佳工艺条件为m(粉煤灰)∶m(Na2CO3)为1∶2,焙烧温度为450℃;采用最佳制备工艺条件下制备的吸附剂(记作2-450℃-FA吸附剂),在初始Cd2+质量浓度为300 mg/L、初始溶液pH为7.7、振荡时间为120 min的条件下,对模拟废水中Cd2+的去除率为98.0%。2-450℃-FA吸附剂对Cd2+的吸附主要受颗粒内扩散控制,吸附过程可用准二级吸附动力学方程很好地描述。Ea为77.22 kJ/mol,吸附过程主要为化学吸附。     

粉煤灰吸附—石灰沉淀处理高浓度含氟废水

采用粉煤灰吸附—石灰沉淀处理高浓度含氟废水.正交实验得到的最佳工艺条件为:反应温度10℃,石灰加入量3.0 g/mL,反应时间60 min,废水pH 6.88.在此最佳工艺条件下处理F质量浓度为150 mg/L的含氟废水,Fˉ去除率为97.53％.Mn2+,Fe3+,Mg2+,A13+,Zn2+单独存在时,随5种阳离子质量浓度增大,Fˉ去除率略有增加;当5种阳离子共同存在且质量浓度均大于500 mg/L时,Fˉ去除率下降.PO43-,SO42-,CO32-,NO3-单独存在时对Fˉ去除率影响不大;当4种阴离子共同存在且质量浓度均大于800 mg/L时,Fˉ去除率低于对照实验.