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Energy efficient refining of Black spruce TMP by using acid hydrogen peroxide : Part 2. Washing, chelating and bleaching studies

机译:酸性双氧水精炼黑云杉TMP的能源效率:第2部分。洗涤,螯合和漂白研究

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摘要

The acid hydrogen peroxide system has the potential to significantly reduce the specific energy consumption in the production of softwood thermomechanical pulps (TMPs). A drawback of the chemical system is discoloration of the pulp during refining. The work presented in this study evaluates the possibility to regain the lost brightness by washing, chelating and sodium dithionite or hydrogen peroxide bleaching of the treated pulps. A washing or chelating procedure can reduce the metal ion content of the chemically treated TMPs considerably, though brightness can be increased by a maximum of two ISO units. The amount of iron can be further reduced to a level similar to that of untreated pulps by performing a reducing agent-assisted chelating stage (Q(Y)) with dithionite. The discoloration cannot,, however, be completely eliminated. The brightness decrease-of the treated pulps is thus not only caused by higher iron content in the pulp, but is also dependent on the type of iron compound and/or other coloured compounds connected with the acid hydrogen peroxide treatment. Oxidative bleaching with hydrogen peroxide (P) is more effective than reductive bleaching with sodium dithionite in regaining the brightness lost during the energy reductive treatment. By using a Q(Y) P sequence, a hydrogen peroxide charge of 3.8% was needed to reach an ISO brightness of 75% for the chemically treated pulps. The corresponding hydrogen peroxide charge for the untreated TMP reference was 2.5%.  
机译:酸性过氧化氢系统有潜力显着降低软木热机械纸浆(TMP)生产中的单位能耗。化学系统的缺点是在精制过程中纸浆变色。这项研究中提出的工作评估了通过洗涤,螯合,连二亚硫酸钠或过氧化氢漂白处理过的纸浆来恢复失去的亮度的可能性。洗涤或螯合程序可以大大降低化学处理过的TMP的金属离子含量,尽管亮度最多可以增加两个ISO单位。通过与连二亚硫酸盐进行还原剂辅助的螯合阶段(Q(Y)),可以将铁的量进一步减少到与未处理纸浆相似的水平。但是,不能完全消除变色。因此,处理后的纸浆的亮度降低不仅由纸浆中较高的铁含量引起,而且还取决于与酸性过氧化氢处理有关的铁化合物和/或其他有色化合物的类型。用过氧化氢(P)进行氧化漂白比用连二亚硫酸钠进行还原性漂白更有效地恢复在能量还原处理过程中损失的亮度。通过使用Q(Y)P序列,化学处理后的纸浆需要3.8%的过氧化氢才能达到ISO亮度的75%。对于未经处理的TMP参考,相应的过氧化氢装料为2.5%。

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