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分馏塔结盐原因分析及应对措施 被引量:2
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作者 王汉玺 黄立强 张晓峰 《辽宁化工》 CAS 2012年第7期689-691,695,共4页
催化裂化原料中有氯和氮存在,在高温条件下HCl气体不断逸出,同时催化裂化原料中的氮化物在催化裂化反应条件下,在催化裂化分馏塔内形成NH4Cl。分馏塔内随着油气不断上升,而分馏温度下降,NH4Cl结晶的速度越快,同时在设备表面的NH4Cl晶体... 催化裂化原料中有氯和氮存在,在高温条件下HCl气体不断逸出,同时催化裂化原料中的氮化物在催化裂化反应条件下,在催化裂化分馏塔内形成NH4Cl。分馏塔内随着油气不断上升,而分馏温度下降,NH4Cl结晶的速度越快,同时在设备表面的NH4Cl晶体也聚积越多,最终导致降液管流通面积减小,直至堵塞降液管,造成塔盘液层增厚,导致分馏效果变得很差,造成产品质量不合格。根据NH4Cl易溶于热水的原理,采用在线水洗的方法,去除结盐,恢复生产,降低成本,提升经济效益。 展开更多
关键词 分馏塔 NH4CL 结盐 热水水洗
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Recovery of titanium from undissolved residue(tionite) in titanium oxide industry via NaOH hydrothermal conversion and H_2SO_4 leaching 被引量:3
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作者 孟凡成 薛天艳 +2 位作者 刘亚辉 张国之 齐涛 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2016年第6期1696-1705,共10页
To recover titanium from tionite, a new process consisting of NaOH hydrothermal conversion, water washing, and H2SO4 leaching for TiO2 preparation was developed. The experimental results show that under the optimum ... To recover titanium from tionite, a new process consisting of NaOH hydrothermal conversion, water washing, and H2SO4 leaching for TiO2 preparation was developed. The experimental results show that under the optimum hydrothermal conversion conditions, i.e., 50% NaOH (mass fraction) solution, NaOH/tionite mass ratio of 4:1, reaction temperature of 240 ℃reaction time of 1 h and oxygen partial pressure of 0.25 MPa, the titanium was mainly converted into Na2TiO3, and the conversion was 97.2%. The unwanted product Na2TiSiO5 remained stable in water washing, and its formation was prevented by improving NaOH concentration. In water washing process, about 97.6% of Na+ could be recycled by washing the hydrothermal product. The NaOH solutions could be reused after concentration. 96.7% of titanium in the washed product was easily leached in H2SO4 solution at low temperatures, forming titanyl sulfate solution to further prepare TiO2. 展开更多
关键词 tionite titanium recovery NaOH hydrothermal conversion water washing H2SO4 leaching
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