炼油废白土在水泥厂燃煤自备电厂中再利用的实践

本项目主要研究和实现了工业废白土在BAYAH燃煤自备电厂中的再利用,实现变废为宝,减少了环境污染,同时为企业创造了一定的经济效益。针对废白土的特性,对燃料输送系统给煤机、皮带机、煤仓、下料溜子和排渣系统进行了改造。通过修改操作规程消除废白土对锅炉运行的影响。     

死髓变色前牙的激光漂白治疗临床评价

本文的研究目的是探讨激光冠内漂白治疗死髓牙变色的治疗作用。材料与方法 :漂白基本操作同激光活髓牙变色的漂白操作程序。先将牙龈及口唇有效防护 ,将漂白药物放在唇舌两面并同时封入根冠内。结果 :所有牙齿的灰暗变色均有 3- 5级的色度提高。平均治疗次数为 3.4± 0 .75 ,脱色 85 %以上的占 89%。结论 :牙齿创伤和牙髓分解是冠内变色的常见原因 ,激光冠内漂白是治疗这种变色的有效手段 ,可以完全恢复患者的自信。     

Varnish layer hardness of oriental beech (fagus orientalist L.) wood as affected by impregnation and bleaching

The impacts of impregnation and bleaching on the varnish layer hardness of Oriental beech (Fagus orientalist L.) wood were investigated. A number of bleaching combinations {[NaOH−H₂O₂], [NaOH−Ca(OH)₂−H₂O₂], [NaOH−MgSO₄−H₂O₂] [NaHSO₃−H₂C₂O₄], [NaSiO₃−H₂O₂], [KMnO₄+NaHSO₃+H₂O₃]} were applied at 18% concentration for bleaching to both impregnated and unimpregnated specimens of Oriental beech wood. Subsequently, water-based (WB) varnish was coated over the samples and the varnish layer hardness values were determined in accordance with ASTM D 4366-95. All of the chemicals used for bleaching reduced the surface hardness. However, after varnish coating, the hardness of most samples was similar to that of the varnish-coated natural (control) samples.     

还原性有机酸络合铁负载活性炭纤维降解染料废水

采用还原性有机酸络合铁离子并负载到活性炭纤维(ACFs)上,制备出非均相Fenton催化剂用于去除染料废水中有机污染物.采用SEM、FTIR和ICP-AES对制备出的草酸铁(Oxa-Fe)络合物负载ACFs(Oxa-Fe/ACFs-3)进行了表征.发现草酸铁络合物均匀负载在ACFs上,其中铁的质量分数为0.96％.在Oxa-Fe/ACFs-3和H2O2添加量分别为10 g/L和100 mmol/L(以染料废水体积计),50℃条件下对20 mL染料废水进行了降解,染料废水化学需氧量(COD)去除率在100 min内可达62.2％.此外,考察了该催化剂pH适用范围以及重复使用性能.结果表明,Oxa-Fe/ACFs-3促进了H2O2活化产生活性自由基?OH和?O2–,实现了对染料废水中有机污染物的降解.对比了不同还原性有机酸络合铁负载ACFs处理染料废水的性能,发现有机酸还原性越强,越有利于染料废水COD去除率的提高.     

聚二烷基硅烷的合成及其表征

以二甲基二氯硅烷、二苯基二氯硅烷为原料，通过Wurtz还原反应合成出聚二甲基硅烷、聚二苯基硅烷，并用UV、^1H NMR、FT—IR以及GPC、DSC—TGA等方法进行了光谱分析和结构表征。     

以废白土制备洗涤膏

植物油脱色用过的活性白土是含油的废白土 ,本文探索了一种充分利用废白土的方法。以强碱与废白土含的油按化学计量比进行皂化反应可得一种洗涤膏。这种洗涤膏主要适用机械工人洗手 ,也可用以清洗瓷砖等硬表面。通过对比试验 ,表明该洗涤膏在这两类应用场合中的洗涤效果良好     

羰基化法合成氨基甲酸酯催化剂的研究进展

对氧化羰基化法、还原羰基化法及氧化还原羰基化法3种羰基化合成氨基甲酸酯方法中催化剂的研究进展进行了综述,其中着重讨论了各种配体及助剂对催化剂活性的影响。指出今后的研究应集中在寻找高效、价廉及可重复使用的催化体系或对高效的均相催化体系进行负载化以及研究多相催化体系的催化机理。     

新型螺旋式浓硝酸漂白塔及其应用

针对传统的帽罩式浓硝酸漂白塔存在的缺点和不足，找出原因并予以改进，开发研制出螺旋式浓硝酸漂白塔，改进了工艺状况，减少了维修工作量，达到了节能降耗的目的，确保了直接法浓硝酸装置的长周期运行。     

Kinetics of hydrogen peroxide bleaching of ALCELL® derived pulp

In this study, a kinetic model of the final bleaching stage with hydrogen peroxide in a totally chlorine free (TCF) bleaching sequence for ALCELL® processed pulp was developed. The model was based on the rate of chromophore destruction characterized by the decrease in the light absorption coefficient of bleached pulp at 457 nm, C_K. Based on the fact that the chromophore destruction proceeds rapidly in an initial phase followed by a much slower reaction during which a “floor-level” chromophore concentration is approached asymptotically, we propose that the hydrogen peroxide stage of the ALCELL® derived pulp in the studied TCF sequence consists of two distinct phases. The initial phase is a very fast reaction. The rate equation of the second phase was determined as: which is valid in a pH range of 10.5 to 11.5 and a temperature range of 60 to 92.5°C.     

De-oiling contaminated bleaching clay by high-pressure extraction

The disposal and re-use of spent bleaching clay from the vegetable oil processing industry is a problem of growing importance. Although today the only practical way of removal of the spent material is disposal, extraction with organic solvents is a well-known method of de-oiling contaminated bleaching clay. In our investigations we compare the extractibility of two different types of bleaching clays with CO₂ as a solvent. All experiments were carried out with a high-pressure extraction plant. The extraction and separation conditions, temperature and pressure, as well as the CO₂ mass flow, were varied during experiments. The aim of our investigations was a complete separation of the oil from the adsorbent. The latter should then be re-used as bleaching clay. The oil and the bleaching clay were analyzed and tested, respectively. The results show that oil of good quality can be recovered and the bleaching clay still has an activity approximately 50% of fresh clay.