马尾松化学预热机械浆镁碱过氧化氢漂白

研究了用镁碱代替钠碱的马尾松化学预热机械浆（CTMP）浆过氧化氢漂白工艺及其对纸浆性能的影响,分析了镁碱和钠碱过氧化氢漂白废液对环境的影响.试验结果表明,马尾松CTMP浆镁碱漂白过氧化氢的最佳漂白工艺条件为：H2O2体积浓度为4%,Mg（OH）2质量浓度为1.2%,Na2SiO3质量浓度为1.5%、漂白温度为80℃、漂白时间为120 min,其白度可至63.5%（ISO）,而经钠碱漂白后纸浆的白度值为61.4%（ISO）.镁碱过氧化氢漂白废液化学耗氧量（CODcr）为193.6 g/L,比钠碱过氧化氢漂白废液化学耗氧量（CODcr=312.86 g/L）降低了38.12%.     

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。     

蔗渣氧脱浆二氧化氯漂白工艺参数的优化

采用三因素二次通用旋转组合实验设计,对蔗渣氧脱浆二氧化氯漂白的主要工艺参数(ClO2用量、NaOH用量和漂白时间)进行了优化,建立了工艺参数与纸浆卡伯值、白度及可吸附有机卤化物(AOX)产生量之间的二次多项式非线性回归数学模型.结果表明:通过实验设计建立的数学模型回归显著,失拟不明显;3个工艺参数对纸浆卡伯值、白度及AOX产生量的影响由大到小的顺序均依次为ClO2用量、漂白时间、NaOH用量;在优化模拟得到的较佳工艺条件(ClO2用量0.79%,NaOH用量0.43%,漂白时间53 min)下,纸浆卡伯值为1.83,白度为73.3%ISO,废水中AOX质量浓度为10.8 mg/L,与验证实验得到的纸浆卡伯值(1.76)、白度(75.0%ISO)和废水中AOX质量浓度(11.3mg/L)接近.     

蔗渣浆的压力过氧化氢漂白

对烧碱-蒽醌(Soda-AQ)法蔗渣浆分别进行了螯合预处理(Q)和常压过氧化氢(P)、压力过氧化氢(PO)漂白的研究,探讨了单段PO漂白蔗渣浆的可行性.正交试验结果表明,PO漂白蔗渣浆优化的漂白条件为漂白温度100℃、时间80min、压力0.6MPa、NaOH用量0.4%.PO漂白浆的白度较高,达84.0%ISO,特性黏度为825.3mL/g,比QP漂白浆的白度高9.9%ISO;PO漂白浆的物理强度性能也较好,浆料的抗张指数为66.67N.m/g,撕裂指数为9.34mN.m2/g,耐破指数为4.31 kPa.m2/g,耐折度为39次.PO漂白废水的化学耗氧量、生化耗氧量及色度较低,漂白废水可全部逆流回用,大大减少了污染排放.     

新型造纸原料洋麻的硫酸盐法制浆及ECF漂白

以洋麻为研究对象,分析了洋麻的化学成分,研究了不同H因子下硫酸盐法制浆(KP)的较优工艺,以及KP浆的ECF漂白性能及较优的漂白工艺.结果表明:洋麻的硝酸-乙醇纤维素含量为45.00%,酸不溶木素含量为16.50%,聚戊糖和抽出物含量均较低,是优良的造纸用原料;KP法蒸煮较优的制浆工艺为H因子1000、活性碱用量20%、硫化度22%,该工艺下细浆得率达44.9%、卡伯值为20.4、残碱质量浓度为11.67 g/L;ECF漂白的较优ODED漂白工艺为OD0,2%EpD1,1.5%,该工艺条件下终漂浆白度可达82.3%ISO.     

云南松-蓝桉混合浆漂白的研究

改进的硫酸盐蒸煮浆比常规硫酸盐浆有较好的漂白性，在相同的漂白工艺条件下，改进的硫酸盐蒸煮浆比常规硫酸盐浆所用的化学药品少而成浆白度高。用改良硫酸盐法制得的浆比常规硫酸盐法制得的浆易漂；用氧碱次氯酸钠漂白，蓝桉比例大的成浆白度高，比例少的白度较差，且氧碱次氯酸钠漂白比常规次氯酸钠漂白成浆白度可提高2～3倍；过氧化物H2O2的漂白过程聚合度下降较少，很适合强煮弱漂的制浆工艺，成浆白度与次氯酸钠相差不大，但可减少污染。用蓝桉60％的混合材制的浆粕，进行纺丝验证试验，纺丝的各种性能好，能纺出质量较好的粘胶纤维。     

微波技术在竹浆漂白中的应用

用正交实验法探讨了在微波辐射下次氯酸钠漂白硫酸盐竹浆的工艺条件,结果表明,微波辐射用于硫酸盐竹浆次氯酸盐单段漂白的最佳工艺条件为:微波辐射功率480W,辐射时间2min,用氯量4.29%,氢氧化钠用量1%,浆料浓度12%.在此条件下,纸浆白度可达72.9%IS0;而在相同条件下达到此白度,传统水浴加热则需要90min的时间。因此,微波辐射竹浆次氟酸钠单段漂白能节约能源和提高生产效率.     

重组木聚糖酶预处理对麦草浆漂白性能的影响

利用来自里氏木霉不含纤维素酶的重组木聚糖酶对麦草浆进行预处理,以减少后续漂白药剂 的用量,降低漂白废水污染负荷。结果表明：采用重组木聚糖酶预处理时较合适的预处理条件为 pH=60、温度50 ℃、浆浓(质量分数)7 %、时间1 h、酶用量5 μmol/(min·g)。在此处理条件下 ,浆料的卡伯值与原浆和对照浆相比分别降低了27.98 %和18.71 %。麦草浆经过重组木聚糖酶预处 理后再采用次氯酸钠漂白至与对照浆相近白度时(72.6 %,ISO),可以节省用氯量50 %。经重组木聚 糖酶处理后浆料的纤维素结晶度反而有所提高,由原来的60.0 %上升到63.5 %。通过电镜照片观察 ,从理论上证明了重组木聚糖酶预处理可节省后续漂白时漂剂用量。     

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.     

烧碱-AQ法麦草浆全无氯漂白的研究

研究了烧碱-AQ法麦草浆全无氯漂白(OQP)流程中氧脱木素、整合处理和过氧化氢漂白的影响因素．结果表明;氧脱木素段NaOH用量2．5％,MgSO4用量0．5％,浆浓10％,温度105℃,氧压0．7MPa,时间75min时脱木素效果较好,对后续漂白有利．整合处理pH值为3时,浆料的自度最高,卡伯值最低．压力H2O2漂白的最佳工艺条件为;浆浓10％,H2O2 3．5％,NaOH1．5％,MgSO2 0．05％,EDTA 0．2％,氧压0．6MPa,温度105℃,时间2h．在优化条件下,漂终白度达82．2％ ISO．     

STUDY ON FORMAMIDINE SULPHINIC ACID BLEACHING OF POPLAR APMP

Bleaching of poplar APMP with Formamidine sulphinic acid (FAS) was investigated in this paper.The effects of FAS charges, ratio of treatment on the brightness gain, color reduction and pulp strength were studied. A single-stage FAS bleaching was optimized. Under the conditions of 10 % pulp consistency, 60 minutes time and 70℃ reaction temperature and 0.6 %, FAS (on 0.d.pulp), ratio of FAS to NaOH was 2, we produced a bleached pulp with a brightness of 62.3 %(SBD), a brightness gain of 9.2 units.     

MODIFIED OPAL:A NOVEL STABILIZER FOR HYDROGEN PEROXIDE BLEACHING OF PULPS

The possibility of modified opal as the stabilizer of hydrogen peroxide bleaching was investigated. The results showed that the modified opal in place of sodium silicate as the stabilizer of hydrogen peroxide bleaching is feasible. At the same dosage, above 3% ISO can be increased for both wheat straw pulp and deinked pulp. The stabilizing ability of the modified opal to hydrogen peroxide bleaching of pulp is improved markedly. It is favorable for bleaching to increase temperature and time within a permissive extent. The suitable process conditions are 10% of pulp consistency, 3% of hydrogen peroxide, 1.5% of sodium hydroxide, 3% of the modified opal, 70℃ and 60 min when the modified opal is used as the stabilizer of hydrogen peroxide bleaching. At these conditions, the brightness gain can reach about 16% ISO for wheat straw pulp. In addition, it is favorable for bleaching to add a little magnesium sulfate when the modified opal is used as the stabilizer of hydrogen peroxide bleaching, the brightness of pulp can increase I%ISO if0.05% of magnesium sulfate is added. The cost analysis indicated that the modified opal is superior to sodium silicate as the stabilizer of hydrogen peroxide bleaching in economical aspect and has further the potential of market development.     

STUDY ON THE ELEMENTAL CHLORINE FREE BLEACHING OF BAMBOO KRAFT PULP

1INTRODUCTIONChina is a country using the most variety of non-wood fiber raw material and is the largest country producing non-wood fiber pulp and paper in the world[1]. Bamboo is one kind of the main non-wood species for papermaking in China. Although the structure of raw materials for papermaking has being adjusted through increasing the proportion of wood pulp and by effectively utilizing waste paper source, non-wood species will still remain an important fiber resource[1,2].At present…     

CHLORINE DIOXIDE BLEACHING OF NaOH-AQ WHEAT STRAW PULP

The influences of chlorine dioxide bleaching of NaOH-AQ wheat straw pulp were studied in this paper. The results showed that the optimal conditions were as follows: chlorine dioxide dosage 1.0%,initial pH 4.0, pulp consistency 8% and 70℃ for 150 minutes. Furthermore, some ways of rebuild the conventional CEH bleaching sequence were put forward, such as CED, DED, DCED, and we draw a conclusion that CED, DCED has higher bleaching efficiency than the CEH bleaching process.     

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.     

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。     

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…