THE TCF BLEACHING OF NS-AQ ASPEN HIGH YIELD CHEMICAL PULP

INTRODUCTIONNowadays, under the pressure of energy crisis, Methods押The pulp was put in the high-density polyethylene plastic bag in the of thermostatic water bath where the pulp was treated with chelated environment pollution and market competition, the pulp industry has being developed in the direction of "Three Highness" and " Three Lowness". "Three Highness" means high yield, high strength and high brightness; on the other hand, " Three Lowness" means low energy consumption, low wa…     

桉木硫酸盐浆TCF漂白的研究

研究桉木硫酸盐浆H2O2强化的氧脱木素效果;研究KMnO4和螯合物对桉木硫酸盐氧漂浆H2O2漂白的改善效果,并对其最佳工艺条件及各种因素对漂白效果的影响进行探讨。结果表明：在氧脱木素过程中加入少量的H2O2,就能起到很好的强化效果;氧漂浆在KMnO4的预处理、DTPA处理后再经过H2O2漂白,可使KP法桉木浆白度达80％以上。     

ENZYMATIC BLEACHING OF WHEAT STRAW SODA-AQ PULP BY LMS TREATMENT

Laccase has been proven that it has a good selectivity and efficiency in pulp bleaching. In this paper, the effects of LMS (Laccase Mediator System) treatment on delignification and bleaching of wheat straw pulp at various conditions, such as laccase dosage,temperature, oxygen pressure and pH, were investigated. The TCF sequence including LMS can bleach the wheat straw pulp to 81% ISO brightness with good strength. The synergetic biobleaching of LMS and xylanase of wheat straw pulp was also investigated. It was found that the final brightness and strength of synergetic biobleaching pulps increased to a certain extent and the bleaching selectivity was improved. The combination of the enzymes is feasible for the delignification and bleaching.     

中浓纸浆清洁漂白技术的理论与实践

纸浆传统低浓含氯漂白方法(如CEH)存在对环境污染、水耗和能耗大、不可能适应大产能的要求等问题,需要用中浓氧脱木素、中浓二氧化氯漂白、中浓过氧化氢漂白及它们的组合等清洁漂白技术来取代.文中结合各类清洁漂白技术的特点,研究适用于各浆种的中浓氧脱木素、中浓过氧化氢等漂白技术,结合工程实践,提出适合我国国情的中浓纸浆少污染漂白技术及全无氯漂白技术,从而满足日益严格的环保要求,实现清洁漂白生产.     

桉木硫酸盐浆LMS生物漂白的研究

进行了桉木硫酸盐将漆酶一介体系统（LMS）生物漂白的研究,漆酶由白腐菌Panus conchatus固体发酵并分纯化而制得;一种新的介体－－N－羟基乙酰苯胺（NHA）自行合成,采用L／MQP漂白流程,仅用2％（质量分数）的H2O2就将桉木常规硫酸盐浆（EMCC－O）可达到87．6％ISO的白度,生物漂白的CK浆和EMCC－O浆的粘度都很高,说明漆酶／NHA生物漂白的脱木素选择性很好。     

活化剂在麦草硫酸盐浆中无氯和少氯漂白中的应用

在麦草ＫＰ浆的无氯和少氯漂白程序中使用活化剂,可促进脱木素作用并提高浆的白度。在氧脱木素前用ＮＯ２,硫酸和过氧酸进行预处理比较,以ＮＯ２效果最佳。ＮＯ２用量２％,处理后浆的卡伯值比未处理降低了６％,白度提高４％,粘度只下降１．６％。在Ｄ／ＣＥＤＤ漂白程序中,漂前用对有效氯用量８％的Ｓ１２预处理,白度提高２．３％ＩＳＤ,粘度基本无变化;活化剂ＴＡ用于ＮＯＰ三段漂的Ｐ段,用量４％（对浆）,可提高白度４．３％ＩＳＯ,粘度也有明显提高。本试验采用ＧＯＰＡＰＴＡ无氯漂白程序,可使麦草ｋｐ浆漂后白度达８０％ＩＳＯ,但粘度下降较大     

KINETICS OF DELIGNIFICATION AND CARBOHYDRATE DEGRADATION DURING OXYGEN BLEACHING

Carbohydrate degradation during oxygen bleaching is associated with cleavage reactions. It is apparent that the loss of the cellulose DP (degree ofpolymisation)is strongly affected by the extent of the delignification. A strong linear correlation can be established between the DP of cellulose chains and the residual lignin in the pulp. The Nuclear Growth concept and Percolation Theory for heterogenous system can be combined to formulate kinetic models for both the delignification and the degradation of carbohydrate. The models prediction is statistically robust and can be applied to different pulps at different bleaching conditions.     

蔗渣浆的全无氯漂白工艺

对蔗渣浆采用过氧化氢强化的氧脱木素(OP)-螯合预处理(Q)-压力过氧化氢漂白(PO)的短序漂白,探讨了将蔗渣浆漂至82%ISO和用非硅过氧化氢漂白稳定剂代替硅酸钠用于过氧化氢漂白的可行性.研究表明,非硅过氧化氢稳定剂PP-1与PP-2耐高温、耐高压,可用于压力过氧化氢漂白.OP段氢氧化钠用量为2.0%(相对于绝干浆质量,下同)、过氧化氢用量为0.5%,PO段过氧化氢用量为3.0%、PP-1用量为0.1%、PP-2用量为0.5%时,蔗渣浆采用OPQPO流程漂白后,浆的白度可达到85%ISO.而且OPQPO从根本上消除了可吸附有机卤化物的产生;经测定,漂白废水属于可生物降解废水.     

蔗渣浆全无氯漂白的研究

本本文探讨了在Op段低NaOH用量,P段低H2O2用量的条件下采用OpQP流程将蔗渣浆漂至82%ISO的可行性,并讨论了非硅过氧化氢漂白稳定剂代替硅酸钠用于过氧化氢漂白的可行性。研究表明非硅过氧化氢稳定剂PP-2,PP-1耐高温、高压,可用于压力过氧化氢漂白。在Op段2%NaOH,0.5%H2O2;P段3% H2O2,PP-1 0.1%, PP-2 0.5%条件下,蔗渣浆采用OpQPo流程,漂后浆白度达到85%ISO。OpQPo从根本上消除了AOX的产生,经测定漂白废水属于可生物降解废水,只有Q和P段的部分废水进入废水处理系统, 容易通过常规的污水处理方法达到日益严格的国家排放标准。     

混合商品桉木片原料硫酸盐浆氧脱木素工艺优化

针对混合商品桉木片硫酸盐法制浆漂白过程强度损失较为严重问题,利用正交实验方法完成混合商品桉木片硫酸盐浆氧脱木素工艺优化,确定在NaOH用量2%、时间60,min、温度100,℃、氧压0.5,MPa、MgSO4用量0.2%的条件下,纸浆的打浆度为15°SR,其抗张指数达到39,N·m/g以上,黏度780,mL/g.通过单因素实验,进一步探讨氧脱木素工艺中NaOH用量对于纸浆性能的影响,提出氧脱木素工段NaOH用量与纸浆黏度、卡伯值分别具有线性关系:Yη=-17.84,XNaOH+829.92,R2=0.989,8;Ykappa=-0.62,X NaOH+10.56,R2=0.995,9.     

硫酸盐木浆漂白前木聚糖酶预处理的研究

研究了木聚糖酶用于硫酸盐木浆 H2 O2 漂白前预处理的工艺条件 ,结果表明 ,预处理最佳工艺条件为 :酶用量为每克浆 2 0 IU ,时间 3h,浆浓为 6 %。在相同的 H2 O2 漂白条件下 ,经酶处理后的浆料白度可提高 2 %～ 3% SBD。     

过氧化氢漂白磨石磨木浆的工艺研究

本文简述了过氧化氢漂白的作用机理，通过实验室小试，找出过氧化氢漂白磨石磨木浆的影响因素及最佳漂白条件，为抄制白度65％以上的胶印书刊纸提供依据。     

自由基与纸浆漂白(Ⅰ)——自由基的产生及其在漂白中的作用

论述在纸浆的常用漂白剂漂白过程中自由基的产生、自由基与过渡金属离子的关系,自由基的漂白作用及其对碳水化全物的影响等。     

马尾松硫酸盐浆两段氧脱木素的影响因素

研究了马尾松硫酸盐浆段间不洗涤时第二段氧脱木素的影响因素。结果表明,在给定的第一段氧脱木素的条件下,第二段氧脱木素采用氧压0．4－0．5MPa、温度80－90℃、时间40－60min、碱用量（质量分数）2％－4％的条件,可以在纸浆粘度不致降低很大的前提下,得到较高的木素总脱除率。     

废报纸脱墨浆H_2O_2漂前预处理

研究了Na2SO3与DTPA联合用于废报纸脱墨浆H2O2漂前预处理的效果,并与尿素、DTPA、硫酸、EDTA预处理剂的预处理效果进行了比较。结果表明,Na2SO3与DTPA联合是种优良的预处理剂,与其他预处理剂相比,可使漂后浆白度提高1.4%～4.2%ISO。     

微波辐射应用于麦草浆漂白工艺的研究

将微波辐射代替传统水浴加热应用于H2O2麦草浆漂白工艺中。研究了微波辐射时间、辐射功率、H2O2用量和NaOH用量等因素对纸浆漂白效果的影响。通过与传统水浴加热漂白对比发现,达到相应白度时微波辐射漂白时间大大缩短;微波辐射漂白纸浆粘度没有过多下降;微波辐射漂白废水中的残余过氧化物只有水浴漂白的10%。正交实验结果表明H2O2用量的影响最大,其次是微波辐射时间和NaOH用量,影响最小的是微波输出功率。最佳实验条件为微波辐射功率240?W、辐射时间25?min、H2O2用量5％和NaOH用量4％时纸浆白度约为59％ISO,纸浆粘度大于620?mL·g-1,纸浆硬度约为390。     

过渡金属离子对废纸浆H_2O_2漂白的影响

研究了过渡金属离子对废纸浆H2O2漂白的影响.研究结果表明,经较强的螯合处理之后重新加Cu2 ,Fe2 和Mn2 ,漂后纸浆的白度降低,残余H2O2减少,漂白效率降低.     

PEROXYACID ENHANCED OXYGEN DELIGNIFICATION OF KRAFT PULP

1INTRODUCTIONNew pulping and bleaching technologies, which do not use chlorine-base chemicals, continue to be developed in the pulp and paper industry worldwide to meet stricter environmental regulation and increased public environmental awareness. ECF (Element-chlorine-free) and TCF (Total-chlorine-free) bleaching sequence had been used in bleaching plant to reduce the amount of chlorinated organic compounds in the bleach plant effluent. Oxygen delignification was gradually becoming a …     

单段氧脱木素特性的研究

研究了马尾松硫酸盐浆单段氧脱木素的特性,研究结果表明：影响马尾松硫酸盐浆氧脱木素的因素有：时间,温度,用碱量,氧压,保护剂MgSO4的用量及反应浆浓,从纸浆中木素的脱出和纸浆的粘度出发,各因素都有一较合适的用量,其中,氧压在0．5－0．6MPa之间,时间80min,温度100℃,NaOH用量3％－5％,MgSO4用量0．5％－1．0％,浆浓10％－12％,在以上条件并保证浆粘度不致降低很大的条件下,纸浆的木素脱出率较大。     

INFLUENCES OF BLAECHING ADDITIVES ON REED PULP FAST BLEACHING

SUMMARYWith the development of paper machine and the enlarger of cooking capability, higher requirement of bleaching system in paper mill is brought forward. At present, many straw-pulp mills completed single-stage hypochlorite bleaching through horizontal bleaching machine, which had the disadvantages of large area and low product ability. So there always was no enough space for paper mills to increase the product ability. Bleaching process became the key handicap to increase the product a…