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Effects of silica on chemical recovery in the direct causticization of wheat straw black liquor

机译:二氧化硅对麦草黑液直接苛化中化学回收的影响

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Straw black liquor is relatively difficult to recover using the Tomlinson process because of the presence of silica in inorganic components. Gasification with direct causticization might serve as a promising alternative; however, the interaction between silica and direct causticization agents needs to be evaluated. In this work, desilication was achieved using a laboratory-scale membrane electrolysis cell adopted from the chlor-alkali industry. Then raw and desilicated straw black liquors were carried out through direct causticization with titanium dioxide (TiO2) and recycled sodium tri-titanate (Na2O center dot 3TiO(2)) at 850 degrees C using a tube furnace. The results show that these two agents exhibit different silica transfer mechanisms. When using TiO2, approximately 80% of the silica is retained in the solid residue after hydrolysis because of chemical interactions. Almost all of the silica transfers to the hydrolysis-derived white liquor when using Na2O center dot 3TiO(2). This means that the process of treating straw black liquor by direct causticization might need additional lime causticization to improve the efficiency of sodium recovery. This observation also indicates that silica will not consume the direct causticization agent Na2O center dot 3TiO(2) after the initial step using TiO2. The sodium hydroxide (NaOH) yield was 60% when using raw black liquor as the feed to the Na2O center dot 3TiO(2) recycling tests and 80% when using desilicated straw black liquor. Considering the NaOH recovered in the electrolysis cell, the total NaOH yields exceed 85% of total titratable alkali. No detectable deterioration of the direct causticization agents was found within the limited number of recycles tested. A greater number of cycles need to be tested at a larger scale to evaluate the feasibility of applying a direct causticization process to straw black liquor.
机译:由于汤姆林森法中的无机成分中存在二氧化硅,秸秆黑液相对较难回收。直接苛化的气化可以作为一种有前途的选择。然而,二氧化硅和直接苛化剂之间的相互作用需要进行评估。在这项工作中,使用氯碱工业采用的实验室规模的膜电解槽实现了脱硅。然后,使用管式炉在850℃下通过用二氧化钛(TiO2)和再循环的三钛酸钠(Na2O中心点3TiO(2))直接苛性化处理粗制和脱硅质的秸秆黑液。结果表明,这两种试剂表现出不同的二氧化硅转移机理。当使用TiO2时,由于化学相互作用,水解后约80%的二氧化硅保留在固体残留物中。使用Na2O中心点3TiO(2)时,几乎所有的二氧化硅都会转移到水解白液中。这意味着通过直接苛化处理秸秆黑液的过程可能需要额外的石灰苛化,以提高钠回收的效率。该观察结果还表明,在使用TiO2的初始步骤之后,二氧化硅不会消耗直接苛化剂Na2O中心点3TiO(2)。当使用粗制黑液作为Na2O中心点3TiO(2)循环测试的进料时,氢氧化钠(NaOH)的产率为60%,而使用脱硅酸盐的秸秆黑液为80%。考虑到在电解池中回收的NaOH,总NaOH产量超过可滴定碱总量的85%。在测试的有限循环次数内,未发现直接腐蚀剂的可检测到的劣化。需要以更大的规模测试更大数量的循环,以评估将直接苛化工艺应用于秸秆黑液的可行性。

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