{"title":"单氮石处理草酸镧水合物的热分解动力学","authors":"Mv Purwani, Suyanti Suyanti, W. A. Adi","doi":"10.17146/JSMI.2019.20.2.5295","DOIUrl":null,"url":null,"abstract":"THERMAL DECOMPOSITION KINETICS OF LANTHANUM OXALATE HYDRATE PRODUCT TREATMENT FROM MONAZITE . Unreacted shrinking core model variation was developed for calcination and solid thermal decomposition reaction to non catalytic gas and no gas reactants were involved. In this research, thermal decomposition of lanthanum oxalate hydrate product treatment of monazite. The parameters for modeling are the time and temperature of thermal decomposition. The time was between 0 - 150 minutes with 30 minute intervals and the temperature range between 600 – 700 o C with 100 o C intervals. Based on the experimental data it can be concluded that the most suitable model was unreacted core sphere ash diffusion controls and obtained the relation between temperature T o C with diffusion coefficient D following equation D = 0.0011 T + 0.5175 with linearity R² = 0.9561. Another possible model was the sphere reaction control and obtained the relationship between 1 / T (K) and reaction rate constant k s was k s = 48873.e -4.88 / RT with activation energy = 4.88 kJ. The relationship between time t with r c (radius of particles at time t) at various temperatures and the relation between temperature and r c at various times follows the exponential line equation. If temperature and time parameters were combined will find the relation between time and temperature with r c following the equation ln r c = -0.9536 (9E-04 T + 0.005 T) + 4.9976.","PeriodicalId":365391,"journal":{"name":"Jurnal Sains Materi Indonesia","volume":"48 2","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2019-01-31","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"4","resultStr":"{\"title\":\"THERMAL DECOMPOSITION KINETICS OF LANTHANUM OXALATE HYDRATE PRODUCT TREATMENT FROM MONAZITE\",\"authors\":\"Mv Purwani, Suyanti Suyanti, W. A. Adi\",\"doi\":\"10.17146/JSMI.2019.20.2.5295\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"THERMAL DECOMPOSITION KINETICS OF LANTHANUM OXALATE HYDRATE PRODUCT TREATMENT FROM MONAZITE . Unreacted shrinking core model variation was developed for calcination and solid thermal decomposition reaction to non catalytic gas and no gas reactants were involved. In this research, thermal decomposition of lanthanum oxalate hydrate product treatment of monazite. The parameters for modeling are the time and temperature of thermal decomposition. The time was between 0 - 150 minutes with 30 minute intervals and the temperature range between 600 – 700 o C with 100 o C intervals. Based on the experimental data it can be concluded that the most suitable model was unreacted core sphere ash diffusion controls and obtained the relation between temperature T o C with diffusion coefficient D following equation D = 0.0011 T + 0.5175 with linearity R² = 0.9561. Another possible model was the sphere reaction control and obtained the relationship between 1 / T (K) and reaction rate constant k s was k s = 48873.e -4.88 / RT with activation energy = 4.88 kJ. The relationship between time t with r c (radius of particles at time t) at various temperatures and the relation between temperature and r c at various times follows the exponential line equation. If temperature and time parameters were combined will find the relation between time and temperature with r c following the equation ln r c = -0.9536 (9E-04 T + 0.005 T) + 4.9976.\",\"PeriodicalId\":365391,\"journal\":{\"name\":\"Jurnal Sains Materi Indonesia\",\"volume\":\"48 2\",\"pages\":\"0\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2019-01-31\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"4\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Jurnal Sains Materi Indonesia\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.17146/JSMI.2019.20.2.5295\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Jurnal Sains Materi Indonesia","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.17146/JSMI.2019.20.2.5295","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 4
摘要
单氮石处理草酸镧水合物的热分解动力学。建立了煅烧和固体热分解反应到非催化气体的未反应收缩核模型变异,不涉及气体反应物。本研究采用水合草酸镧热分解产物处理独居石。建模参数为热分解时间和温度。时间范围为0 ~ 150分钟,间隔30分钟;温度范围为600 ~ 700℃,间隔100℃。根据实验数据得出最合适的模型是未反应的核球灰扩散控制,得到温度T ~ C与扩散系数D的关系为D = 0.0011 T + 0.5175,线性度R²= 0.9561。另一种可能的模型是球反应控制,得到1 / T (K)与反应速率常数K s的关系为K s = 48873。e -4.88 / RT,活化能= 4.88 kJ。在不同温度下,时间t与r c(时间t的粒子半径)之间的关系以及温度与r c在不同时间的关系遵循指数线方程。如果将温度和时间参数结合起来,可以得到时间和温度与r c的关系为ln r c = -0.9536 (9E-04 T + 0.005 T) + 4.9976。
THERMAL DECOMPOSITION KINETICS OF LANTHANUM OXALATE HYDRATE PRODUCT TREATMENT FROM MONAZITE
THERMAL DECOMPOSITION KINETICS OF LANTHANUM OXALATE HYDRATE PRODUCT TREATMENT FROM MONAZITE . Unreacted shrinking core model variation was developed for calcination and solid thermal decomposition reaction to non catalytic gas and no gas reactants were involved. In this research, thermal decomposition of lanthanum oxalate hydrate product treatment of monazite. The parameters for modeling are the time and temperature of thermal decomposition. The time was between 0 - 150 minutes with 30 minute intervals and the temperature range between 600 – 700 o C with 100 o C intervals. Based on the experimental data it can be concluded that the most suitable model was unreacted core sphere ash diffusion controls and obtained the relation between temperature T o C with diffusion coefficient D following equation D = 0.0011 T + 0.5175 with linearity R² = 0.9561. Another possible model was the sphere reaction control and obtained the relationship between 1 / T (K) and reaction rate constant k s was k s = 48873.e -4.88 / RT with activation energy = 4.88 kJ. The relationship between time t with r c (radius of particles at time t) at various temperatures and the relation between temperature and r c at various times follows the exponential line equation. If temperature and time parameters were combined will find the relation between time and temperature with r c following the equation ln r c = -0.9536 (9E-04 T + 0.005 T) + 4.9976.