无烟煤流化床气化飞灰的结渣特性

通过烧结特性实验研究了无烟煤流化床气化飞灰在"近灰熔点"处的烧结特性,并利用X射线衍射分析(XRD)进行了结晶矿物质和玻璃相的定量分析以研究其烧结机制。结果表明,飞灰中矿物质间的相互转化控制着其结渣特性。由于铁、钙和镁等碱性组分的部分富集,飞灰的灰熔点与原煤相比要低;在低于灰熔点DT 100~200℃附近,由于长石类矿物质的转变熔融形成了具有黏结性的液相,灰样发生液相烧结导致收缩变形而结块;大部分的钙和铁等助熔组分赋存于玻璃相中提高了其浓度,且在热处理过程中它们并未发生析晶行为,从而促进灰样的烧结致密化过程,进一步使得飞灰的结渣倾向增强。     

未燃炭对粉煤灰涂层耐盐及防腐性能的影响研究

废物利用是当前节能减排和绿色环保的要求,固体废弃物——粉煤灰,是一种有效的涂料填料,而且低品质的粉煤灰也可以用作填充剂增强涂料性能.尽管未燃炭对涂层的机械性能有不利影响,但是一定量的含炭粉煤灰反而提高了涂层的耐磨性能.672h后的中性盐雾试验结果表明,含有34.9％UC的粉煤灰涂层具有比脱炭粉煤灰涂层更好的耐盐雾性能....     

高变质福建无烟煤连续流化床混合气催化气化

连续流化床（内径123mm、高1．2m）中,采用工业纯碱（碳酸钠）为催化剂进行了高变质程度无烟煤一福建永安煤（低挥发分k=5．47％、高灰Aad=29．45％）混合气（空气／水蒸气）催化气化的研究,考察了催化剂质量分数、气化温度、水汽比等操作参数的影响。实验结果表明,工业纯碱作为催化剂添加5％可使碳转化率增加3倍,实现了煤的高效转化;气化温度有明显催化气化促进作用,超过900℃时,流化床内易结渣。从同时满足高产气率及高煤气热值两个指标出发,在适宜操作条件（碳酸钠质量分数5％、850℃～880℃、适宜水汽比）下,产气率提高2倍,从无催化剂时的2．13m^3／kg～2．15m^3／kg提高到4．2m^3／kg～5．1m^3／kg;煤气热值提高5倍,从1．0MJ／m^3左右提高到5．0MJ／m^3;表明工业纯碱进行高变质福建无烟煤流化床混合气催化气化具有重要的工业应用价值和现实的开发意义。     

循环流化床锅炉氮氧化物的生成与分解模型

在国内外研究基础上，依据循环流化床锅炉炉内氮氧化物（ＮＯ和Ｎ２Ｏ）的生成与分解特性，建立了一个以化学反应动力学为基础的炉内ＮＯ和Ｎ２Ｏ的生成和分解模型，模型有机地结合在已有的循环流化床锅炉总体数学模型之中。模型对一台７５ｔ／ｈ循环流化床锅炉炉内氮氧化物的生成和分解特性的模拟预测结果与工业试验结果吻合良好。模型的预测和工业试验表明循环流化床锅炉的氮氧化物（ＮＯ和Ｎ２Ｏ）的排放受锅炉运行参数如温度、一二次风比例等的影响，可以通过调整锅炉运行参数来控制锅炉氮氧化物的排放。     

煤中痕量元素在循环流化床锅炉中的迁移行为与富集特性

对天津市某电厂循环流化床(CFB)锅炉燃用的原煤及燃烧产物底灰、飞灰、细飞灰(≤50 μm)进行痕量元素含量的测定,分析了Be、Zn、Hg、V、Cr、Mn、Co、Ni、Cu、As、Se、Cd、Pb 13种痕量元素在燃烧过程中的迁移行为,揭示了痕量元素在CFB锅炉中的分配、富集特性。结果表明,CFB锅炉中,较低的炉温对于痕量元素的迁移富集产生了较大的影响。由相对富集系数得知,Be、V、Co、Se在底灰中耗散,在飞灰中富集,Zn、Mn倾向于在底灰中富集,元素Cd、Pb、Ni、Cu挥发性较强,在底灰和飞灰中均是耗散。As受钙氧化物影响,挥发性表现并不明显。Hg在底灰和飞灰中相对富集系数均很低,表明Hg在整个燃烧过程中以气态形式排放;Hg、As、Se、V、Cr、Mn、Co、Ni、Cu、Zn、Pb均有向小颗粒物中富集的趋势。根据相对富集系数以及研究的13种元素在低温CFB锅炉中的迁移行为,将这些元素分为三类:A类(E_R<0.1),主要是以气态形式排放元素Hg;B类(0.1R≤0.85),较易挥发元素As、Be、Ni、Cu、Se、Cd、Pb、Co、V;C类(E_R>0.85),主要残留在固体产物中元素Zn、Mn、Cr。     

生物质飞灰未燃尽炭制备活性炭及其超级电容性能研究

生物质燃料在锅炉中经过热解和燃烧后,飞灰中含有孔隙丰富的未燃尽炭.但其孔隙率和比表面积无法满足商用超级电容炭的要求,改善材料孔隙结构的活化方法成为未燃尽炭提质改性的关键.本研究通过对筛分粒径＞0.2 mm的未燃尽炭进行KOH一步活化处理后发现,在浸渍比3.5:1时活性炭拥有较大的比表面积(1982 m2/g),且在电流...     

循环流化床燃煤锅炉中的汞迁移研究

采用美国环保署颁布的吸附剂吸附汞采样方法30B(USEPA 40 CFR Part 60 30B)采集燃煤烟气中汞。选择一循环流化床燃煤机组进行现场采样,吸附剂吸附烟囱处烟气中的汞、入炉煤样、锅炉底灰、静电除尘器飞灰等样品同时采集。对该机组中汞质量平衡率进行衡算,通过汞质量平衡率说明了汞采样方法的准确性和有效性。评价了汞在飞灰、底灰和烟气中的分布,循环流化床锅炉底灰中对脱汞的贡献率仅0.55%,飞灰脱除汞的效率高达83.37%,剩余的16.08%的汞排放入大气环境,表明循环流化床机组是有效控制汞的清洁煤燃烧技术。     

木屑在鼓泡流化床和循环流化床中气化特性的对比研究

对木屑在内径分别为0.3m×0.3m的鼓泡流化床气化炉（BFBG）和内径0.4m的循环流化床气化炉(CFBG)中的气化特征进行了对比,重点考察了当量比对生物质气化特性的影响。实验结果表明,在相同当量比下,由于CFBG操作气速明显高于BFBG,床内强烈的气固传热传质,使得CFBG可以获得较高的热解速率,同时可以使 CFBG在较高温度下运行。较高的运行温度不仅有利于二次裂解气化反应,使可燃气体质量明显好于BFBG,同时也减少了燃气中焦油的量。在较低气化当量比下(ER≤0.28),CFBG比BFBG可以获得更高的气体产率、碳转化率和气体效率;在较高当量比下,(ER＞0.28),CFBG和BFBG的气体产率、碳转化率和气体效率则相差不大。     

大型循环流化床锅炉与煤粉炉汞排放特性研究

选取600 MW循环流化床锅炉及1000 MW煤粉炉的电厂进行汞迁移转化及排放特性研究,采用EPA 30B法对烟气汞质量浓度进行采样,同时采集了入炉煤、飞灰、底渣、石灰石、工艺水、脱硫石膏、脱硫废水等固体液体样品进行对比分析.研究了两电厂现有污染物控制装置对汞的协同脱除作用,分析了汞的迁移转化规律.两电厂烟气经过污染物...     

循环流化床煤燃烧/热解双反应器压力分布的实验研究

实验测量了一种新型的循环流化床煤燃烧/热解冷模反应器中提升管及立管内的压力分布，其中提升管的内径为100 mm、高为6 m;立管内径为44 mm、高为3 m，热解室的截面为200 mm×200 mm、高为770 mm。分别考察了提升管内的表观气速Ur、循环量Gs、加到热解室内的松动气量Qa以及初始装料量G等对系统压力分布的影响。结果表明，在立管底部阀门开度不变的情况下随着Ur的增加，提升管及立管内的压力梯度都趋于减小；在提升管内表观气速一定的情况下随着循环量Gs的增加，提升管及立管内的压力分布也随之增大；加到热解室内的松动气对立管内的压力分布影响较大，而对提升管内的压力分布影响相对较小；在立管底部阀门开度及Ur一定的情况下，随着初始装料量的增加提升管及立管内的压力分布也趋于增大。     

基于密度泛函理论的燃煤飞灰未燃尽碳与烟气砷作用机理

基于密度泛函理论研究了燃煤飞灰中未燃尽碳（unburned carbon， UBC）组分对气态单质砷As及其氧化物AsO、AsO₂和As₂O₃的作用机理。结果表明，单质砷优先吸附于碳桥位，吸附能在（-5.95）-（-5.88） eV。AsO分子中的砷、氧原子分别与碳原子成键时，吸附构型最稳定，吸附能最低为-7.87 eV。当AsO₂在未燃尽碳表面解离形成一个AsO和表面活性氧时，体系最稳定，吸附能为-10.65 eV。当三角双锥As₂O₃分子以两个氧原子首先碰撞未燃尽碳表面时，将解离形成AsO和AsO₂小分子，并分别与表面碳成键，此时体系吸附能相较于未解离情形而言显著降低，达到-10.64 eV。飞灰未燃尽碳与AsO或AsO₂小分子的结合较紧密，局部倾向于形成特殊的五元环结构。毒性最强的三价态砷As₂O₃，相较于As、AsO和AsO₂而言，化学性质稳定，不易发生吸附。将其催化裂解为AsO、AsO₂小分子，有望成为可行的燃煤电厂烟气砷污染控制措施。     

Preparation and characterization of activated carbon from bagasse fly ash

Activated carbons from bagasse fly ash (BFA) were prepared by one step chemical activation using ZnCl₂ as activating agent, or combination method of chemical with CO₂ physical activation (physicochemical activation). The development of porosity was studied in correlation with the method of activation, activation temperature, and also the chemical weight ratio. A typical sample by the combination method at 600 °C and weight ratio of ZnCl₂:BFA = 2 exhibited micropore volume of 0.528 cc/g, mesopore volume of 0.106 cc/g and surface area of 1200 m²/g. For determining the adsorption capacity of the carbon samples in solutions, phenol and methylene blue equilibrium adsorption experiments were conducted. The properties and adsorption capacity of the synthesized activated carbons has been compared to commercial activated carbon (Norit^® SX Plus).     

山西典型无烟煤灰流动性的调控

为满足气化炉液态排渣的要求,考察和比较了CaO、MgO和Fe₂O₃三种助熔剂对山西典型无烟煤煤灰流动性(熔融性和黏温特性)的影响.研究发现,MgO对硅铝比在1.2~2.0的高硅铝煤灰的流动温度降低最有效,其次为CaO和Fe₂O₃,这是由于使用各种助熔剂时生成不同的高温稳定矿物组分造成的.针对三种助熔剂建立了流动温度和完全液相温度的关系式,并得到了CaO和Fe₂O₃含量与流动温度的关系:FT = 1 593-9.573 × w_CaO (R²=0.9429) 和FT =1 576-8.330 6 × w_Fe2O3 (R²=0.955 9),可以用于指导助熔剂的添加.CaO无论从降低黏度数值或降低临界黏度温度都具有最好的效果.Ca²⁺、Mg²⁺、Fe²⁺的电负性差异和高温下的产物不同是三种助剂对黏度数值影响不同的根本原因; Mg²⁺、Fe²⁺具有较小的离子半径以及单质铁在高温下析出是导致临界黏度温度较高的原因.     

Characterization of FDR fly ash and brick/lime mixtures

The present research is concerning the characterization of FDR (fuel derived from residues) fly ash and mixtures with lime/brick hydraulic binder by DTA/TG/DTG thermo-analysis, X-ray diffractometry and chemical analysis. The use of hydraulic binder obtained from building brick rejects, which is less expensive than the usual solidifiers such as cementitious binder and silicates, allows us to reutilize, in the meantime, this wreckage material, to the advantage of environmental sustainability. Fly ash samples investigated in the present study were separated in a thermo-incineration plant. Mineralogical DTA/TG/DTG and XRD investigations reveal the presence of different phases as well as chemical analysis shows a moderate concentration of heavy metals and high content of chloride and sulphate. Results obtained from leaching tests with water carried out on hardened pastes containing fly ash lead to interesting results, which highlight behaviour to the release of contaminants. The whole of the results obtained in the present study make it possible to regard the objective of disposing such hardened materials in inert waste landfill sites as achievable.     

Studies of fly ash using thermal analysis techniques

Improved thermoanalytical methods have been developed that are capable of quantitative identification of various components of fly ash from a laboratory-scale fluidized bed combustion system. The thermogravimetric procedure developed can determine quantities of H₂O, Ca(OH)₂, CaCO₃, CaSO₄ and carbonaceous matter in fly ash with accuracy comparable to more time-consuming ASTM methods. This procedure is a modification of the Mikhail-Turcotte methods that can accurately analyze bed ash, with higher accuracy regarding the greater amount of carbonaceous matter in fly ash. In addition, in conjunction with FTIR and SEM/EDS analyses, the reduction mechanism of CaSO₄ as CaSO₄+4H₂ CaS + 4H₂O has been confirmed in this study. This mechanism is important in analyzing and evaluating sulfur capture in fluidized-bed combustion systems.     

New ceramic microfiltration membranes from mineral coal fly ash

This work aims to develop a new mineral porous tubular membrane based on mineral coal fly ash. Finely ground mineral coal powder was calcinated at 700 °C for about 3 h. The elaboration of the mesoporous layer was performed by the slip casting method using a suspension made of the mixture of fly ash powder, water and PVA. The obtained membrane was submitted to a thermal treatment which consists in drying at room temperature for 24 h then a sintering at 800 °C. SEM photographs indicated that the membrane surface was homogeneous and did not present any macro defects (cracks, etc.). The average pore diameter of the active layer was 0.25 μm and the thickness was around 20 μm. The membrane permeability was 475 l/h m² bar.This membrane was applied to the treatment of the dying effluents generated by the washing baths in the textile industry. The performances in term of permeate flux and efficiency were determined and compared to those obtained using a commercial alumina microfiltration membrane. Almost the same stabilised permeate flux was obtained (about 100 l/h m²). The quality of permeate was almost the same with the two membranes: the COD and color removal was 75% and 90%, respectively.     

燃煤飞灰中铁质微珠的显微结构及其组成研究

选用我国三个典型燃煤煤种的电厂飞灰中铁质微珠,进行显微结构与物相组成等方面的研究。揭示出铁质微珠中存在空心微珠、子母珠和实心微珠三种显微颗粒类型,在这些显微颗粒表面可识别出以微粒状和八面体自形晶两种方式存在的赤铁矿和磁铁矿析晶;元素分析表明,燃烧褐煤电厂铁质微珠主要由Fe、Ca、Al、和Si元素组成,燃烧烟煤和无烟煤的电厂铁质微珠主要由Fe、Al和Si元素组成;物相分析发现,Fe在铁质微珠中以四种存在形式：Fe3O4、α-Fe2O3、γ-Fe2O3和Fe3+-玻璃相。这些物相在三个电厂飞灰中呈现出不同的分布特征,反映出不同的燃煤煤种在锅炉中燃烧温度的差异。随着温度的升高,Fe3O4先氧化为γ-Fe2O3,或γ-Fe2O3与Fe3O4的固熔体,然后再转变为α-Fe2O3,当温度超过 1 400 ℃时,Fe2O3又转化为Fe3O4。     

Fast physics-chemical characterization of fly ash

This paper analyzes the effect of fly ash chemical character on early Portland cement hydration and the possible adverse effects generated by the addition of gypsum. Behaviour was analyzed for pure Portland cements with varying mineralogical compositions and two types of fly ash, likewise differing in chemical composition, which were previously characterized under sulphate attack as: silicic-ferric-aluminic or aluminic-silicic ash in chemical character, irrespective if they are in nature, siliceous or siliceous and aluminous materials according to the ASTM C 618-94a. The experimental results showed that water demand for paste with a normal consistency increased with the replacement ratio in fly ash with a more aluminic than silicic chemical character, whereas it declined when silicic-ferric-aluminic ash was used. On the other hand, the differences between the total heat of hydration released at the first valley and the second peak also clearly differentiated the two types of ash. While the relative differences increased in the more aluminic than silicic ash, they declined in the more silicic than aluminic. In another vein, the findings indicate that within a comparable Blaine fineness range, the reactive alumina (Al₂O₃^r−) content in pozzolanic additions has a greater effect on mortar strength than the reactive silica (SiO₂^r−) content, at least in early ages up to 28 days. Finally, the adverse effect generated in the presence of excess gypsum is due primarily to the chemical interaction between the gypsum and the C₃A in the Portland cement and the reactive alumina (Al₂O₃^r−) in the fly ash.     

Speciation of chromium in Australian fly ash

The concentrations of chromium (III) and (VI) in fly ash from nine Australian coal fired power stations were determined. Cr(VI) was completely leached by extraction with 0.01 M NaOH solution and the concentration was determined by inductively coupled plasma atomic emission spectrometry (ICP-AES). This was confirmed by determining Cr(III) and Cr(VI) in the extracts of fly ash that had been spiked with chromium salts. These analytical measurements were done using a combination of ion-exchange chromatography and ICP-AES. The elutant was 0.05 M HNO₃ containing 0.5%-CH₃OH. When the column was operated at a flow rate of 1.2 ml min⁻¹ and samples were injected by use of a sample loop with a volume of 100 μl, Cr(III) and Cr(VI) in sample solution was exclusively separated within approximately 10 min. The detection limits (3σ) were 5 ng for Cr(III) (0.050 mg l⁻¹) and 9 ng for Cr(VI) (0.090 mg l⁻¹), respectively. A relative standard deviation of 1.9% (n = 6) was obtained for the determination by IC-ICP-AES of 0.25 mg l⁻¹ Cr(III) and Cr(VI).