燃煤锅炉烟气NOx污染等离子体治理技术

燃煤锅炉烟气NOx污染治理技术种类较多。本文综合评述了各种烟气NOx污染等离子体治理技术，重点介绍了电晕放电脱除烟气中NOx的最新研究成果。对燃煤锅炉烟气NOx污染治理技术的研究和开发具有实用价值。     

烧结烟气污染物综合减排工艺分析

为解决钢铁企业烧结烟气污染问题，分析了烧结烟气的排放状况及其烧结烟气治理的现状，针对烧结烟气的特点，特别推荐了适合烧结机烟气治理的烧结污染物最大减排技术（Maximized Emission Reduction of Sintefing，简称MEROS工艺），介绍了该技术的工艺流程和特点，为烧结烟气污染治理提供了一种高效可靠的方法。     

燃煤锅炉烟气NOx污染等离子体治理技术

燃煤锅炉烟气NOx污染治理技术种类较多.本文综合评述了各种烟气NOx污染等离子体治理技术,重点介绍了电晕放电脱除烟气中NOx的最新研究成果.对燃煤锅炉烟气NOx污染治理技术的研究和开发具有实用价值.     

碱性皂化废水和锅炉烟道气的联合处理在环境工程中的应用

工艺中将碱性皂化废水经预处理后用泵输入锅炉湿式除尘系统进行燃煤烟气脱硫除尘，流出废水经处理后循环回用。该治理工艺采用以废治废，综合利用的方法治理皂化废水和锅炉烟气，既消除了污染又充分利用了碱性废水和锅炉烟道气作为有用的资源，取得了较好的环境效益和经济效益。     

含氟烟气的净化与回收

含氟烟气是主要的大气污染物之一,本文就铝电解、磷肥工业产生的含氟烟气的一般治理方法进行了综述,各企业应因地制宜,选用技术先进、经济合理、操作简单、可有效控制污染的含氟烟气净化工艺.     

某新型炼焦炉烟尘治理装置的工艺设计与应用探讨

某新型炼焦炉烟尘治理装置在焦炉炉顶设导烟车(配套皮带小车),并采用拦焦集尘罩进行高温烟气的收集。在装煤、出焦过程中产生的烟尘、粉尘等污染物经炉顶导烟车转送至烟气输送风管,再经管道输送到地面除尘系统,经净化处理后排放。经实际运行监测,出口烟气浓度符合《炼焦化学工业污染物排放标准》(GB 16171—2012)。     

烟道式脱硫装置处理冶炼厂高浓度SO2烟气的工程实践

本文介绍了烟道式脱硫装置的特点及工艺原理，采用该装置处理某冶炼厂高浓度SO2烟气，其脱硫率达90％以上，净化后的烟气可直拉达标排放，并年产合格脱硫石膏近万吨。烟道式脱硫装置解决了常规脱硫除尘装置共同存在的结垢和堵塞问题，在冶炼烟气治理方面具有一定的推广应用价值。     

炭素焙烧沥青烟气治理

采用生石灰吸附袋式除尘法治理炭素焙烧窑沥青烟气 ,具有很好的效果。治理前烟尘 114 8.7mg/ Nm3,沥青烟 480 .5mg/ Nm3,苯并 (a)芘 3 .462 mg/ Nm3;治理后烟尘 12 .8mg/ Nm3,沥青烟 11.0 mg/ Nm3,苯并 (a)芘 3 .0× 10 - 4m g/ Nm3。从运行效果来看 ,烟气的充分冷却和选用生石灰做吸附剂是治理成功的关键。     

煤矸石热电厂烟气治理技术及应用

介绍了一种新型喷淋泡沫塔在煤矸石热电厂烟气治理中的应用。根据离心、喷雾、泡沫相结合的多级净化原理，经旋风喷雾、二级喷淋泡沫板洗涤，脱硫效率高达92．4％。     

烟道式脱硫装置处理冶炼厂高浓度SO2烟气的工程实践

本文介绍了烟道式脱硫装置的特点及工艺原理 ,采用该装置处理某冶炼厂高浓度SO2 烟气 ,其脱硫率达 90 %以上 ,净化后的烟气可直接达标排放 ,并年产合格脱硫石膏近万吨。烟道式脱硫装置解决了常规脱硫除尘装置共同存在的结垢和堵塞问题 ,在冶炼烟气治理方面具有一定的推广应用价值。     

涂铁石英砂的制备及其对砷的吸附

采用加热蒸发法制备涂铁石英砂，并对其含铁量、比表面积、氧化铁膜的附着能力、表面形态和氧化铁物相等表面性质进行了研究。用涂铁石英砂进行了含砷废水的吸附实验，并考察了pH值、离子强度、Pb(Ⅱ)金属阳离子、Cr(Ⅵ)氧阴离子等因素对吸附的影响。     

水中总铁两种测定方法的比较

环境监测实验室常使用不同方法进行重复检测作为检测结果质量保证的手段之一。据此对测定水中总铁的两种方法 -邻菲啰啉分光光度法和火焰原子吸收法在校准曲线和检出限、方法精密度和准确度等进行了全面比较,得出两者校准曲线相关性均较好,检出限均为0.03 mg/L,精密度RSD均小于5%,加标回收率均在90%～105%。两者的测定结果无显著性差异。     

Preparation of Calcium Silicate Absorbent from Iron Blast Furnace Slag

ABSTRACT

Calcium silicate hydrate (CSH) solids were prepared from hydrated lime and iron blast furnace slag in an aqueous agitated slurry at 92 °C. While it was hoped a minimal lime/slag ratio could be used to create near-amorphous CSH, the surface area of the product improved by increasing the lime/slag weight ratio to 2. The addition of gypsum to the lime/slag system dramatically improved the formation of surface area, creating solids with 139 m²/g after 30 hr of reaction when only a minimal amount of lime was present. The SO₂ reactivity of solids prepared with gypsum greatly exceeded that of hydrated lime, achieving greater than 70-80% conversion of the alkalinity after 1 hr of reaction with SO₂. The use of CaCl₂ as an additive to the lime/slag system, in lieu of gypsum, also produced high-surface-area solids, 115 m²/g after 21 hr of reaction. However, the SO₂ reactivity of these sorbents was relatively low given the high surface area. This emphasized that the correlation between surface area and SO₂ reactivity was highly dependent on the solid phase, which was subsequently dependent on slurry composition.     

邻菲啰啉分光光度法测定水中总铁的改进

对邻菲啰啉分光光度法测定水中总铁的方法进行了改进：采用50mL比色管水浴还原水样——分光光度计比色测定水中总铁。测试结果表明，改进法精密度和准确度均优于标准方法，是测定水中总铁较为理想的方法。     

铁碳内电解法处理印染废水

对铁碳内电解法处理印染废水的作用机理,工艺过程、影响因素及存在的问题进行了综述,并对印染废水的治理提出了看法。     

Iron and organo-bentonite for the reduction and sorption of trichloroethylene

Hybrid barriers using dechlorination and immobilization were studied to remove trichloroethylene (TCE) in this study. Hybrid barriers of iron filings and organo (hexadecyltrimethylammonium, HDTMA)-bentonite were simulated in columns to assess the performance of the hybrid barriers. TCE reduction rate for the mixture of zero valent iron (ZVI) and HDTMA-bentonite was approximately seven times higher than that for ZVI, suggesting the reduction of TCE was accelerated when HDTMA-bentonite was mixed with ZVI. For the column of two separate layers of iron and HDTMA-bentonite, TCE reduction rate was nearly similar to that for ZVI alone, but the partition coefficient (Kd) was 4.5 times higher than that for ZVI only. TCE was immobilized in the first layer with HDTMA-bentonite due to sorption, and then dechlorinated in the second layer with iron filings due to reduction. The HDTMA-bentonite and minimally-desorbed HDTMA from the organo-bentonite are believed to contribute the increase in TCE concentration on iron surface so that more TCE could be available for reduction. Therefore, the incorporation of HDTMA-bentonite into ZVI not only can effectively retard the transport of chlorinated organic contaminants from landfill leachate or oil shock in subsurface environment, also can expedite the reduction rate of TCE.     

Iron isotopic fractionation in industrial emissions and urban aerosols

A study on tropospheric aerosols involving Fe particles with an industrial origin is tackled here. Aerosols were collected at the largest exhausts of a major European steel metallurgy plant and around its near urban environment. A combination of bulk and individual particle analysis performed by SEM–EDX provides the chemical composition of Fe-bearing aerosols emitted within the factory process (hematite, magnetite and agglomerates of these oxides with sylvite (KCl), calcite (CaCO₃) and graphite carbon). Fe isotopic compositions of those emissions fall within the range (0.08‰ < δ⁵⁶Fe < +0.80‰) of enriched ores processed by the manufacturer (−0.16‰ < δ⁵⁶Fe < +1.19‰). No significant evolution of Fe fractionation during steelworks processes is observed. At the industrial source, Fe is mainly present as oxide particles, to some extent in 3–4 μm aggregates. In the close urban area, 5 km away from the steel plant, individual particle analysis of collected aerosols presents, in addition to the industrial particle type, aluminosilicates and related natural particles (gypsum, quartz, calcite and reacted sea salt). The Fe isotopic composition (δ⁵⁶Fe = 0.14 ± 0.11‰) measured in the close urban environment of the steel metallurgy plant appears coherent with an external mixing of industrial and continental Fe-containing tropospheric aerosols, as evidenced by individual particle chemical analysis. Our isotopic data provide a first estimation of an anthropogenic source term as part of the study of photochemically promoted dissolution processes and related Fe fractionations in tropospheric aerosols.     

Iron isotopic fractionation in industrial emissions and urban aerosols

A study on tropospheric aerosols involving Fe particles with an industrial origin is tackled here. Aerosols were collected at the largest exhausts of a major European steel metallurgy plant and around its near urban environment. A combination of bulk and individual particle analysis performed by SEM–EDX provides the chemical composition of Fe-bearing aerosols emitted within the factory process (hematite, magnetite and agglomerates of these oxides with sylvite (KCl), calcite (CaCO₃) and graphite carbon). Fe isotopic compositions of those emissions fall within the range (0.08‰ < δ⁵⁶Fe < +0.80‰) of enriched ores processed by the manufacturer (−0.16‰ < δ⁵⁶Fe < +1.19‰). No significant evolution of Fe fractionation during steelworks processes is observed. At the industrial source, Fe is mainly present as oxide particles, to some extent in 3–4 μm aggregates. In the close urban area, 5 km away from the steel plant, individual particle analysis of collected aerosols presents, in addition to the industrial particle type, aluminosilicates and related natural particles (gypsum, quartz, calcite and reacted sea salt). The Fe isotopic composition (δ⁵⁶Fe = 0.14 ± 0.11‰) measured in the close urban environment of the steel metallurgy plant appears coherent with an external mixing of industrial and continental Fe-containing tropospheric aerosols, as evidenced by individual particle chemical analysis. Our isotopic data provide a first estimation of an anthropogenic source term as part of the study of photochemically promoted dissolution processes and related Fe fractionations in tropospheric aerosols.     

Iron oxide-loaded slag for arsenic removal from aqueous system

An effective adsorbent for arsenic removal from aqueous system was synthesized by loading iron(III) oxide on municipal solid waste incinerator melted slag. The loading was accomplished via chemical processes and thermal coating technique. The key point of the technique was the simultaneous generation of amorphous FeOOH sol and silica sol in-situ and eventually led to the formation of Fe-Si surface complexes which combined the iron oxide with the melted slag tightly. The surface morphology of the iron oxide-loaded slag was examined and the loading mechanisms were discussed in detail. The adsorbent was effective for both arsenate and arsenite removal and its removal capabilities for As(V) and As(III) were 2.5 and 3 times of those of FeOOH, respectively. Both affinity adsorption and chemical reactions contributed to arsenic removal. The effects of solution pH, contact time, arsenic concentration and adsorbent dosage on arsenic removal were examined and the optimum removal conditions were established. Furthermore, leaching of hazardous elements such as Cr(VI), As, Se, Cd and Pb from the adsorbent at a pH range of 2.5-12.5 was below the regulation values. Accordingly, it is believed that the iron oxide-loaded slag developed in this study is environmentally acceptable and industrially applicable for wastewater treatment.