CO2吸收模型中容积传质系数的确定

气泡微细化是“原位机械搅拌法铁水炉外脱硫技术”的关键.气液传质系数是研究气液吸收过程的基本参数.本文根据相似性原理建立水模型实验装置,并通过测定NaOH吸收CO2的速率来研究气泡微细化过程,同时根据吸收原理定量计算出容积传质系数Ak及CO2气体利用率η.当溶液pH值从12降低到9的过程中,容积传质系数为2.938×10 4m3/s,本实验所用CO2的利用率的公式可简化为:η=18.98/Qt.本论文的研究结果可为进一步研究吸收速率提供理论依据.     

Ca(OH)_2改性活性炭及其吸附CO_2的研究

采用Ca(OH)2为化学活化剂,对颗粒活性炭进行改性。结果表明,在Ca(OH)2用量为100mL、改性温度80℃、改性时间2h、干燥时间6h时,改性后的活性炭吸附容量达到最大,为3.91mmol/g。     

Solid Phase Synthetic Reaction of Sodium Pyroxene for Na2 CO3-Fe （OH） 3-H2 SiO3 System

In order to explore synthetic method of pure sodium pyroxene,the pure chemical reagents of Na2CO3,Fe(OH)3 and H2SiO3were used as raw materials,and the possible solid phase reactions for Na2CO3-Fe(OH)3-H2SiO3system in heating process had been studied by means of differential thermal analysis(DTA)and X-ray diffraction(XRD). The influencing factors of sodium pyroxene(NaFeSi2O6)synthetic reaction,such as sintering temperature and holding time,had also been studied.The results show that sodium pyroxene can be largely synthesized at 737℃;it is helpful for synthesis of sodium pyroxene to increase sintering temperature appropriately,and the best temperature should be controlled at 900℃or so,because it will melt and decompose at temperatures higher than 900℃.In those influencing factors of sodium pyroxene synthesis the most important is temperature.The results will be helpful for providing pure NaFeSi2O6for further research on the formation of SFCA for NaFeSi2O6-KAlSi2O3-CaO-Fe2O3-CaF2 system in the sintering process of Bayan-obo iron ore.     

治理钼精矿焙烧烟气中低浓度SO2的新工艺--柠檬酸吸收法

采用柠檬酸溶液吸收焙烧烟气中低浓度SO2 ,使烟气达到国家排放标准。用气提法解析 ,解析率达 99.78%,试验效果良好。     

NH3-CO2系统中Y(OH)3完全沉淀条件的研究

Ｙ３＋在氨的水溶液中可形成Ｙ（ＯＨ）３沉淀。在该体系中通入二氧化碳气体，随终点ｐＨ的不同，体系中存在的ＨＣＯ３－、ＣＯ３２－使Ｙ（ＯＨ）３溶解为［Ｙ（ＣＯ３）ｎ］３－２ｎ或［Ｙ（ＨＣＯ３）］３－络合离子。本试验研究了体系终点ｐＨ及起始氨浓度对ＣＯ３２－、ＨＣＯ３－浓度的影响以及进而对Ｙ（ＯＨ）３沉淀率的影响，得到了使Ｙ（ＯＨ）３完全沉淀的反应条件。     

钢厂烟气CO2捕捉技术的开发及其应用前景分析

 近年来,许多国家开展钢铁工业CO2捕捉与封存（CCS）技术研究。在CCS成本中,CO2捕捉成本约占70%,因此,降低CO2捕捉成本是CCS首先要解决的问题。目前钢厂开发的CO2捕捉工艺主要以化学吸收法和物理吸附法为主,并在试验规模取得成本降低的效果。介绍日本新日铁和JFE、韩国浦项、中国台湾中钢等开发的CO2捕捉技术,并对CO2捕捉技术的工业化应用前景进行分析。     

反应条件对小粒径Ni_(0.5)Co_(0.2)Mn_(0.3)(OH)_(2)产品性能的影响北大核心

本文通过共沉淀实验,研究了反应条件中镍钴锰硫酸盐溶液浓度、温度、PH和反应时间对小粒径Ni_(0.5)Co_(0.2)Mn_(0.3)(OH)_(2)产品振实密度、比表面积、硫质量分数的影响。结果表明:过高或者过低的镍钴锰硫酸盐溶液浓度、温度、PH反应条件都不利于产品质量控制,当PH为12.00~12.20、浓度为2.5 mol/L、温度为35~40℃、反应时间为30 h时,可以合成较高性能的小粒径Ni_(0.5)Co_(0.2)Mn_(0.3)(OH)_(2)产品。     

20CrMnTi冶炼过程形成CaO(CaS)-Al2O3-MgO夹杂的分析

 FactSage对钙处理前后钢液的平衡计算以及典型夹杂物在CaO-CaS-Al2O3三元相图中演变规律的研究结果表明：钢中硫含量大于0.01%(质量分数,下同)时,难以得到理想的钙处理效果,主要原因在于钙处理过程中钙主要与硫结合生成CaS夹杂,同时少部分钙将对Al2O3进行变性;钙处理过程中CaO(CaS)-Al2O3演变规律为Al2O3→Al2O3+CaO·6Al2O3+CaS→CaO·2Al2O3+CaS(CaO含量较少)→Al2O3·CaO+CaS(CaO含量较多)。通过对复合夹杂物电镜面分布扫描结果的描边处理能够有效辨别复合夹杂物的成分,发现典型CaO(CaS)-Al2O3-MgO夹杂物成分为xCaO·yAl2O3+xMgO·yAl2O3+Al2O3+CaS,并据此提出了一种新的评价钙处理效果的方法。     

Cu掺杂对硫化镍精矿制备高效异相类Fenton催化剂(Ni,Mg, Cu)Fe2O4的影响

以硫化镍精矿为原料,采用共沉淀–煅烧法成功制备出Cu掺杂尖晶石铁氧体(Ni, Mg, Cu)Fe₂O₄异相类Fenton催化剂。利用X射线衍射(XRD)、扫描电子显微镜(SEM)及X射线光电子能谱(XPS)等手段系统研究了Cu掺杂量对所制备产物微观结构、形貌及催化性能的影响;确立了最优催化体系为光助类Fenton催化体系“(Ni, Mg, Cu)Fe₂O₄催化剂/H₂O₂/可见光”,揭示了Cu掺杂对(Mg, Ni)Fe₂O₄催化活性的增强机制。结果表明:在选定的实验条件下,制备得到的产物均为纯相立方尖晶石铁氧体。当Ni与Cu摩尔比为1∶1时,合成的(Ni, Mg, Cu)Fe₂O₄在可见光照180 min条件下对质量浓度为10 mg?L?1的罗丹明B(RhB)溶液的降解率可达94.5%。究其主要原因为:随着Cu掺杂量的增加,占据(Ni, Mg, Cu)Fe₂O₄八面体位的Fe3+和Cu2+的相对含量增加,即裸露于铁氧体表面的Fe3+和Cu2+数量增多,以及两者的协同作用,加速了羟基自由基(·OH)反应的发生,最终使得RhB溶液的降解效率从73.1%提高至94.5%。      

转炉烟气中金属氧化物催化煤焦-CO2气化反应

 提出了利用转炉烟气中金属氧化物催化煤焦 CO2气化反应的新方法来提高CO2转化效率。利用热重分析对金属氧化物催化煤焦 CO2气化进行理论研究,并通过滴管炉研究了不同温度下金属氧化物对煤粉 CO2气化反应的影响。计算不同条件下的α、β、LHV值,对催化效率进行评估。结果表明,金属氧化物对煤焦 CO2气化具有显著的催化作用,并表现出不同的特征温度。添加催化剂后,可燃性气体含量增加,CO2含量降低。根据α、β、LHV值的计算,复合催化剂催化效率最佳,而且催化效率随温度升高而增加。对于单一催化剂,在1 000~1 200 ℃温度范围内,CaO的催化效率优于FeO,FeO稍优于Fe2O3。滴管炉试验结果初步验证了利用转炉烟气中金属氧化物提高CO2的转化效率以及转炉煤气热值的可行性。     

Study on Absorption Rate by Eccentric Mechanical Stirring in Gas Injection Refining for Iron and Steel Making

In gas injection refining processes, a great amount of gas is injected into molten metal in short time, so that very large bubbles are inevitably formed. Wide dispersion of small bubbles in the bath is indispensable for high refining efficiency. Eccentric mechanical stirring with unidirectional impeller rotation was tested using a water model for pursuing better bubble disintegration and dispersion. Absorption rate are used to research on the influence law of the bubble dispersion and disintegration and gas-liquid absorption by the influence of, rotation mode, rotation speed and gas flow rate. Compared to the experimental results of absorption rate under eccentric stirring and centric stirring ,provide the scientific experimental and theoretical guidance for high-temperature experiment of hot metal desulfurization .According to experimental and theoretical analysis, this paper has studied various factors effecting on gas absorption process and volumetric mass transfer coefficient using the system of CO2-NaOH-H2O.The results show that:the volumetric mass transfer coefficient and absorption efficiency of CO2 can be increased under eccentric stirring mode, Because bubble disperse quickly with eccentric mechanical stirring, which results in promoting complete reaction between CO2 and NaOH, and improving the mass transfer coefficient and absorption. Volumetric mass transfer coefficient and efficiency of CO2 increase with the increasing rotation speed under the condition of eccentric stirring .But volumetric mass transfer coefficient and efficiency of CO2 decrease with the increasing rotation speed under the condition of centric stirring.