麦草浆二氧化氯与氧气脱木素效率及相应漂白流程的对比

对麦草浆二氧化氯与氧气脱木素效率及相应的漂白流程进行了对比研究。结果表明,ClO2脱木素(D0)对木素的修饰和改性效果好于氧脱木素(O),在脱木素率低于及接近氧脱木素率的条件下,D0浆的可漂性均大于O浆。在D0段和O段脱木素率相同的条件下,采用D0A/QP、D0EP漂白流程漂后纸浆白度分别比OA/QP漂白流程高11.2和10.3个百分点。D0段废液和相应D0A/QP漂白流程三段混合废水的CODCr负荷均比O段和OA/QP漂白流程混合废水的CODCr负荷轻。D0段和O段废液的紫外光谱都呈现出木素苯环的特征吸收。纸浆的FT-IR谱图分析表明,D0浆和O浆中的羟基和羰基数量增多,随着漂白的进行,羰基等主要发色基团逐渐消除,纸浆白度得到提高。纸浆纤维形态的SEM分析显示,D0段和相应的D0A/QP漂白流程对纤维表面的破坏和损伤较O段和相应的OA/QP漂白流程轻。     

麦草亚铵法氧脱木素浆蒽醌强化次氯酸盐漂白

对麦草亚铵法氧脱木素浆进行蒽醌强化的次氯酸盐漂白工艺的研究,结果表明:在所选四因素三水平漂白工艺中,影响纸浆白度和卡伯值的主要因素是用氯量,当用氯量为7%时,纸浆白度为71.1%ISO;另外,在50℃和80℃的条件下,对麦草亚铵法氧脱木素浆分别进行添加氨基磺酸和蒽醌的漂白研究,发现次氯酸盐漂白时添加蒽醌比添加氨基磺酸的漂白效果好,不仅漂白浆的白度和黏度均得到提高,而且脱木素能力也显示加强。     

制浆漂白技术新进展

讨论了制浆漂白技术新进展,包括：深度脱木素蒸煮、氧脱木素、ECF无元素氯漂白）、TCF（全无氟漂白）、生物漂白。     

麦草亚铵法氧脱木素浆的短流程漂白

对麦草亚铵法氧脱木素浆进行了P、HP和HQP漂白对比研究,结果表明:在过氧化氢单段漂白时,Na2SiO3的适宜用量为0.4%,在所选过氧化氢用量、NaOH用量、温度和时间的四因素三水平方差分析漂白工艺中,影响纸浆白度的主要因素为NaOH用量;而采用HP和HQP漂白时,漂白浆的白度分别达到78.1%(ISO)和81.9%(ISO),可见采用螯合处理的效果明显。     

麦草爆破浆鼓泡塔漂白试验研究

在进行了麦草爆破浆氧脱木素实验室试验的基础上,分析了氧脱木素的影响因素,并对鼓泡塔氧脱木素的中试流程进行管路和工艺设计,进行试验,取得了预期的效果,为非木材纸浆ECF漂白和TCF漂白提供技术和理论依据.     

氯酸盐在纸浆漂白方面的新展望

若干年来,纸浆漂白的方法是采用氯化一碱煮的方法。这种方法在增加纸张的亮度而又不破坏纤维素方面却受到了限制。另外,由于氯气在漂白过程中,带来了排放废液的污染问题。因此,早在50年代就研究的二氧化氯漂白方法,现在已部分或全部代替氯气漂白纸浆。采用新的漂白方法,意味着增加氯酸钠的生产以满足二氧化氯的需要。据美国最大的氯酸钠生产与供应者—虎克化学公司(Hooker Chem Co)称,到1980年,美国氯酸盐在造纸工业漂白方面的     

二氧化氯的漂白及制备方法

我国大多数造纸厂生产漂白纸浆均采用含氯漂白技术,应用这些漂白剂漂白后的纸浆废液中含有很多的有毒甚至剧毒的有机氯化合物。本文介绍的二氧化氯是一种新的对环境污染少、对纸张漂白效果好、不影响纸张质量的漂白剂。阐述二氧化氯用于纸浆漂白原理及其优势,介绍二氧化氯的几种常见制备方法。     

二氧化氯在精制棉漂白上的应用

国产精制棉采用二氧化氯漂白工艺,粘度可超过１０００ｍＰａ·ｓ,白度可达特级水平,创出国内一流的优质精制棉。二氧化氯应用于精制棉的漂白,国内尚属首次。     

低卡伯值麦草浆无氯漂白的研究

采用麦草硫酸盐法(KP法)一级蒸煮深度脱木素技术,制取低卡伯值麦草浆,并对其进行两种不同方式的无氯漂白。结果表明:AQ(PN)P流程可将浆料漂至白度86.2%(SBD),粘度为938mL/g。QZEYP流程能漂至86.9%(SBD),粘度为851mL/g。无氯漂白的粘度和白度稳定性均优于CEH三段漂。预处理对保护浆料有着重要作用。在过氧化氢漂白中,高温高压是脱木素和提高白度的必要条件。臭氧漂白是一种重要又经济的无氯漂白方法。     

硫酸盐竹浆 ECF 漂白过程中糖类 组分变化的研究

应用高效液相色谱法研究了硫酸盐竹浆 ECF 漂白过程中二氧化氯漂白段糖类组分的变化情况。结果表明,葡聚糖、木聚糖和阿拉伯聚糖在二氧化氯漂白过程中有不同的降解率,葡聚糖降解率只有 0.133%,而木聚糖的降解率为 0.907%,阿拉伯聚糖的降解率达 79.77%,明显高于葡聚糖的降解率。     

Effects of the Preferential Oxidation of Phenolic Lignin Using Chlorine Dioxide on Pulp Bleaching Efficiency

Chlorine dioxide is widely used for pulp bleaching because of its high delignification selectivity. However, efficient and clean chlorine dioxide bleaching is limited by the complexity of the lignin structure. Herein, the oxidation reactions of phenolic (vanillyl alcohol) and non-phenolic (veratryl alcohol) lignin model species were modulated using chlorine dioxide. The effects of chlorine dioxide concentration, reaction temperature, and reaction time on the consumption rate of the model species were also investigated. The optimal consumption rate for the phenolic species was obtained at a chlorine dioxide concentration of 30 mmol·L⁻¹, a reaction temperature of 40 °C, and a reaction time of 10 min, resulting in the consumption of 96.3% of vanillyl alcohol. Its consumption remained essentially unchanged compared with that of traditional chlorine dioxide oxidation. However, the consumption rate of veratryl alcohol was significantly reduced from 78.0% to 17.3%. Additionally, the production of chlorobenzene via the chlorine dioxide oxidation of veratryl alcohol was inhibited. The structural changes in lignin before and after different treatments were analyzed. The overall structure of lignin remained stable during the optimization of the chlorine dioxide oxidation treatment. The signal intensities of several phenolic units were reduced. The effects of the selective oxidation of lignin by chlorine dioxide on the pulp properties were analyzed. Pulp viscosity significantly increased owing to the preferential oxidation of phenolic lignin by chlorine dioxide. The pollution load of bleached effluent was considerably reduced at similar pulp brightness levels. This study provides a new approach to chlorine dioxide bleaching. An efficient and clean bleaching process of the pulp was developed.     

COMPETING/PARALLEL REACTION OF CHLORINE AND CHLORINE DIOXIDE DURING KRAFT PULP BLEACHING

The nature of chlorine dioxide substitution for chlorine in the chlorination reaction sequence of pulp bleaching in not well understood. Multiple results may be obtained by simply altering the order of chlorine-chlorine dioxide addition and the amount of chlorine dioxide substitution. Kinetic curves for chlorine, chlorine dioxide, and various levels of chlorine dioxide substitution were generated. The effects of these various processes on delignification (kappa number reduction) and Adsorbable Organic Halogen (AOX) generation were investigated. More than half of the AOX was found to be generated within the first one minute of any reaction sequence. Similar portions of the delignification were also found to occur within the first one minute of chlorination. The work examines the assumption that chlorine and chlorine dioxide react with different portions of the lignin. Thus chlorine and chlorine dioxide compete for only a part of the lignin molecule. The order of chemical addition dictates which chemical most rapidly attacks the competitive region. The hypothesis that chlorine dioxide substitution is simply a competing/parallel reaction sequence was studied.     

Development of Phenolic Lignin During ClO2 Bleaching of Kraft Pulp

The development of the phenolic lignin content in kraft pulp during ClO₂ bleaching was quantitatively determined by the periodate oxidation method. The effect of hypochlorous acid, an intermediate formed during chlorine dioxide bleaching, was eliminated by addition of sulfamic acid, a scavenger of hypochlorous acid. It was found that the number of free phenolic lignin groups per 100 lignin monomer units decreased from about 29 for unbleached kraft lignin to about 6.5 after 1 minute of ClO₂ bleaching. It was also shown that the in-situ generated hypochlorous acid created phenolic hydroxyl groups during chlorine dioxide bleaching. Since it was found that delignification by chlorine dioxide itself was mostly restricted to free phenolic lignin, these findings were used to explain the effect on delignification of addition order of chlorine and chlorine dioxide during bleaching of kraft pulp.     

DMD在纸浆漂白中的应用进展

综述了二甲基二环氧乙烷（DMD）的制备方法、结构特点、选择性氧化的化学特性、与木质素的相关反应机理及DMD在纸浆漂白中的作用.DMD作为一种强的亲电氧化试剂,具有良好的脱木质素能力和选择性.DMD作为漂白剂单独用于纸浆漂白,可以使纸浆达到较高的白度;DMD作为多段漂段间的活化剂,可提高后续漂白的效果.不同于传统含氯漂白的污染性,DMD的低污染和高漂白效率的特点,使其在纸浆全无氯漂白方面有着良好的应用前景.     

黏胶纤维用落叶松溶解浆的清洁漂白

引言近年来,随着棉花价格的总体上涨和消费者对纺织材料舒适度的要求,给黏胶纤维带来了需求增长空间。作为黏胶纤维的原材料,国内目前的溶解浆产能难以满足客户需求。据统计,国内溶解浆存     

Delignification and Bleaching Response of Earlywood and Latewood

Abstract

The delignification response in cooking and the impact of bleaching on earlywood and latewood were studied. Spruce earlywood and latewood chips were pulped by the kraft process and subsequently treated with one bleaching chemical at a time. In cooking, latewood required a higher alkali charge to reach the same kappa number. No difference in the light absorption coefficient between the different fiber types was observed. After oxygen delignification the earlywood fibers had a higher light absorption coefficient at the same kappa number. The difference in light absorbing material was maintained when bleaching was performed with chlorine dioxide, ozone, and peracetic acid. Hydrogen peroxide decreased the light absorbing structures in the earlywood to the same level as for latewood. The earlywood pulp had a higher brightness at a given kappa number than the latewood. The higher brightness remained through all bleaching operations and was primarily due to a higher light scattering ability.     

氧脱木素效率的改善途径

氧脱木素被认为是除了硫酸盐蒸煮脱木素外,成本最低且最简单的脱木素方法,所以氧漂可以把制浆与漂白结合起来。且氧脱木素技术具有环境污染小、漂后纸浆质量高等优点,现已成为ECF和TCF漂白的主体工艺。氧脱木素是以分子氧为漂白剂,酚型木质素与O2反应从而消除侧链,打开苯环,脱甲基化而被氧化降解。该过程受到用碱量、反应温度、时间、氧压、浆浓等许多工艺参数的影响。为改善氧脱木素效果,研究者提出了多种方法,如两段氧脱木素、助剂强化氧脱木素及氧脱木素前预处理等。氧脱木素在我国的应用前景是很广阔的,而且环境保护法规的日益严格对实施氧脱木素技术也十分有利,因此对于氧脱木素的研究还需继续。     

Use of a Novel Extremophilic Xylanase for an Environmentally Friendly Industrial Bleaching of Kraft Pulps

Xylanases can boost pulp bleachability in Elemental Chlorine Free (ECF) processes, but their industrial implementation for producing bleached kraft pulps is not straightforward. It requires enzymes to be active and stable at the extreme conditions of alkalinity and high temperature typical of this industrial process; most commercial enzymes are unable to withstand these conditions. In this work, a novel highly thermo and alkaline-tolerant xylanase from Pseudothermotoga thermarum was overproduced in E. coli and tested as a bleaching booster of hardwood kraft pulps to save chlorine dioxide (ClO₂) during ECF bleaching. The extremozyme-stage (EXZ) was carried out at 90 °C and pH 10.5 and optimised at lab scale on an industrial oxygen-delignified eucalyptus pulp, enabling us to save 15% ClO₂ to reach the mill brightness, and with no detrimental effect on paper properties. Then, the EXZ-assisted bleaching sequence was validated at pilot scale under industrial conditions, achieving 25% ClO₂ savings and reducing the generation of organochlorinated compounds (AOX) by 18%, while maintaining pulp quality and papermaking properties. Technology reproducibility was confirmed with another industrial kraft pulp from a mix of hardwoods. The new enzymatic technology constitutes a realistic step towards environmentally friendly production of kraft pulps through industrial integration of biotechnology.     

Organochlorine Formation in Tertiary Amine Catalyzed Pulp Bleaching

An oxygen delignified eucalyptus kraft pulp was bleached by applying a catalytic amount of a tertiary amine, 1,4-diazabicyclo[2,2,2]octane, and hypochlorous acid at varying pH, temperature, and time. The bleaching filtrate was analyzed for chloroform and AOX and the pulp for residual lignin, hexenuronic acid, and OX. In comparison with chlorine dioxide bleaching, the novel catalytic bleaching (pH < 6) generated only traces of chloroform and low contents of AOX and OX. Separate catalytic oxidations of authentic hexenuronic acid showed that it was a major precursor of chloroform. The results demonstrate a practical way to reduce organochlorine formation in pulp bleaching and provide new understanding on the reaction pathways that yield chloroform.     

电化学漂白的研究进展

对电化学漂白的研究进行了简要的综述,包括电化学含氯漂白、电化学氧气漂白和电化学产生过氧化氢漂白。重点对电化学氧气漂白机理和过渡金属催化剂在电化学氧气漂白中的作用进行了概述。