柿竹园多金属矿选矿废水处理试验研究

针对柿竹园多金属矿选矿废水量大、难沉降、pH值高、COD高等特点,研究了石灰沉降+ZJYH03氧化法、石灰沉降+漂白粉氧化法、石灰沉降+NaClO氧化法、聚合硫酸铁沉降+ZJYH03氧化法和石灰沉降+生物氧化法等废水处理工艺,并对比分析了各工艺的处理效果和药剂成本,结果表明: 聚合硫酸铁沉降+ZJYH03氧化法取得了较好的处理效果,该方法具有工艺简单、水质无色透明、药剂成本低等特点。     

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。     

漆酶在造纸工业中应用的最新研究

漆酶是近年发现在造纸工业中最具潜力的生物酶,具有催化氧化木素的能力。文章综述了漆酶在制浆造纸工业中应用的最新研究进展,例如漂白、造纸废水处理、去除树脂、增加湿强度等诸多方面。     

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.     

蚕蛹蛋白纤维的阳离子改性及其漂白性能研究

研究了蚕蛹蛋白纤维经阳离子改性处理后,纤维中阳离子基团和改性剂用量的关系,对阳离子改性后蚕蛹蛋白纤维的H2O2漂白特性进行了探讨。结果表明:蚕蛹蛋白纤维经阳离子改性后漂白效果明显提高。改性纤维上的季铵正离子能加快溶液中HO2离子的吸附,在纤维内部进行“定点”漂白,从而提高纤维的漂白效果。     

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     

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.