{"currentpage":1,"firstResult":0,"maxresult":10,"pagecode":5,"pageindex":{"endPagecode":5,"startPagecode":1},"records":[{"abstractinfo":"利用Setsys Evolution同步热分析仪,以<span style=\"color:red\">非</span><span style=\"color:red\">等温热重法</span>对焦炭-CO2气化动力学进行了研究.结果显示:当气化温度高于1200 K时,碳转化率和气化反应速率均显著增大;当气化温度达到1500 K左右时,焦炭的气化反应速率达到最大值.由相关系数可知,改良Coats-Redfern积分法是求取焦炭-CO2气化反应动力学参数的较好方法.鞍钢焦炭的活化能大于宝钢焦炭.宝钢焦炭的气化性能优于相同粒度的鞍钢焦炭.","authors":[{"authorName":"刘忠锁","id":"afa40849-83d4-4719-b7f6-ef37eeff9bc0","originalAuthorName":"刘忠锁"},{"authorName":"汪琦","id":"0c086fa2-5529-49e3-b4cb-3ba7c4724f7d","originalAuthorName":"汪琦"},{"authorName":"邹宗树","id":"5bfd653d-5649-4cd1-8f22-0c3ac4e057cd","originalAuthorName":"邹宗树"},{"authorName":"谭广雷","id":"30c63bfe-be6e-449c-8d96-5704ad9f5c10","originalAuthorName":"谭广雷"}],"doi":"","fpage":"1","id":"c59a6ebb-04dd-4c12-9ea0-53da17528197","issue":"6","journal":{"abbrevTitle":"GTYJ","coverImgSrc":"journal/img/cover/GTYJ.jpg","id":"29","issnPpub":"1001-1447","publisherId":"GTYJ","title":"钢铁研究"},"keywords":[{"id":"fb41111a-ad24-4008-8234-f2ea66455f7d","keyword":"焦炭","originalKeyword":"焦炭"},{"id":"ab9fb99a-7071-4dae-accc-33a591bcd08a","keyword":"气化","originalKeyword":"气化"},{"id":"608083d2-7566-4d0e-b155-b97edbcaf668","keyword":"动力学","originalKeyword":"动力学"},{"id":"021732e5-a071-4dac-8f97-42d1453f316f","keyword":"<span style=\"color:red\">非</span><span style=\"color:red\">等温热重法</span>","originalKeyword":"非等温热重法"},{"id":"b7a24161-4ce8-4f0b-90cf-84bef026e34d","keyword":"CO2","originalKeyword":"CO2"}],"language":"zh","publisherId":"gtyj201006001","title":"焦炭-CO2气化动力学的<span style=\"color:red\">非</span><span style=\"color:red\">等温热重法</span>研究","volume":"38","year":"2010"},{"abstractinfo":"在半封闭系统中采用直接热解三聚氰胺的方法制备了C3N4,XRD、XPS及元素分析的结果证明了产物是类石墨相C3N4(g-C3N4).用热分析(TG/DTG)研究了g-C3N4的热分解过程.通过迭代法计算了热分解反应活化能Ea,采用积分法结合36种动力学函数来判断g-C3N4热分解的机理函数.计算结果表明,g-C3N4的平均热分解活化能Ea为178.59kJ/mol,可能的动力学函数积分形式是g(a)=[-In(1-a)]4,指前因子A为21.67s-1,对应的热分解动力学方程为:dα/dT=(21.67/β)exp(-178.59×103/RT)×1/4(1-α)[-ln(1-α]-3","authors":[{"authorName":"杭祖圣","id":"74dde9fe-9358-445b-9af9-3322936c2b63","originalAuthorName":"杭祖圣"},{"authorName":"谈玲华","id":"e8d909b3-3f78-4036-8a2f-c0d490018873","originalAuthorName":"谈玲华"},{"authorName":"黄玉安","id":"28ac52a9-4981-4848-a71d-bed6436c03a4","originalAuthorName":"黄玉安"},{"authorName":"应三九","id":"63664f46-a726-4b0a-9a2d-cdc87556694c","originalAuthorName":"应三九"},{"authorName":"徐复铭","id":"5dd02722-9118-4cb7-88cf-d9e75f7b7c07","originalAuthorName":"徐复铭"}],"doi":"","fpage":"329","id":"a04d7e0e-0b2d-4f76-9303-f123185ccaac","issue":"2","journal":{"abbrevTitle":"GNCL","coverImgSrc":"journal/img/cover/GNCL.jpg","id":"33","issnPpub":"1001-9731","publisherId":"GNCL","title":"功能材料"},"keywords":[{"id":"01ecc63a-9eae-4f3d-b0b8-c544aeeb0266","keyword":"<span style=\"color:red\">非</span><span style=\"color:red\">等温热重法</span>","originalKeyword":"非等温热重法"},{"id":"1226bf1c-4fb4-4bfb-9ab5-5acfe65cacbb","keyword":"g-G3N4","originalKeyword":"g-G3N4"},{"id":"beadce9b-b27c-409d-82e9-432cea17bce5","keyword":"热分解动力学","originalKeyword":"热分解动力学"},{"id":"650f1bea-0472-4e87-a625-803edaae5e2e","keyword":"迭代法","originalKeyword":"迭代法"}],"language":"zh","publisherId":"gncl201102036","title":"<span style=\"color:red\">非</span><span style=\"color:red\">等温热重法</span>研究g-C3N4热分解动力学","volume":"42","year":"2011"},{"abstractinfo":"以硝化纤维(NC)、异佛尔酮二异氰酸酯(IPDI)三聚体、二羟甲基丙酸(DMPA)为原料,通过自乳化方法合成了水性硝化纤维(WNC).通过傅里叶变换红外光谱(FT-IR)对目标产物的结构进行表征;采用<span style=\"color:red\">热重法</span>(TG)研究了WNC薄膜中硝化纤维基体的热分解行为;并分别采用Kissinger法、Ozawa法求解出热分解反应的活化能和频率因子等动力学常数,结合9种常用的动力学函数来判断WNC中硝化纤维基体的热分解机理函数.结果表明:水性硝化纤维基体的热稳定性明显提高,平均热分解活化能为221.31 kJ/mol、频率因子为1.108 2×1024 s-1,热分解反应遵从Sigmoidal类型中的随机核化机理.","authors":[{"authorName":"张丹","id":"fee2c04f-9895-4574-8ced-cfde416e95cc","originalAuthorName":"张丹"},{"authorName":"苏秀霞","id":"1eb994e8-3c73-420d-8a75-729388d4ef8d","originalAuthorName":"苏秀霞"},{"authorName":"毛敏","id":"7599aea5-bf56-42ba-9f25-88be0ae8ce92","originalAuthorName":"毛敏"},{"authorName":"郭明媛","id":"c9d005a7-7a74-4091-9227-4b5e13e7e8f6","originalAuthorName":"郭明媛"}],"doi":"","fpage":"13","id":"70b06509-955f-4e47-98d2-a5983e4993ab","issue":"8","journal":{"abbrevTitle":"TLGY","coverImgSrc":"journal/img/cover/TLGY.jpg","id":"61","issnPpub":"0253-4312","publisherId":"TLGY","title":"涂料工业   "},"keywords":[{"id":"d7f6f149-58ec-4a94-a202-d423872680c0","keyword":"水性硝化纤维","originalKeyword":"水性硝化纤维"},{"id":"0c4e1e41-58ac-41c6-8841-848c33f287ee","keyword":"<span style=\"color:red\">非</span><span style=\"color:red\">等温热重法</span>","originalKeyword":"非等温热重法"},{"id":"921f135c-6b66-422d-932c-30edbb239e57","keyword":"TGA/DTG","originalKeyword":"TGA/DTG"},{"id":"09f2f733-bc96-4711-aff4-27ff872c603d","keyword":"热分解动力学","originalKeyword":"热分解动力学"}],"language":"zh","publisherId":"tlgy201308003","title":"水性硝化纤维涂膜的热分解动力学","volume":"43","year":"2013"},{"abstractinfo":"为了清楚地阐述半焦的燃烧过程,采用<span style=\"color:red\">非</span><span style=\"color:red\">等温热重法</span>研究了氧气体积分数对半焦燃烧动力学的影响.得出挥发分析出燃烧、碳燃烧失重规律及其描述函数,挥发分析出燃烧和碳燃烧所需的表观活化能和表观指前因子.结果表明:挥发分析出燃烧所需的表观活化能和表观指前因子的最小值处于φ(O2) =28％的条件下,最大值处于φ(O2)=30％的条件下;碳燃烧所需表观活化能和表观指前因子的最小值处于φ(O2) =24％,最大值处于φ(O2)=30％条件下.","authors":[{"authorName":"郝丽莹","id":"8adca6a1-b2dc-4f16-9e78-f453f2cc5924","originalAuthorName":"郝丽莹"},{"authorName":"龚志军","id":"8d6695e6-0c03-4160-86c9-900ee878a723","originalAuthorName":"龚志军"},{"authorName":"郑坤灿","id":"37a932e0-dfbc-4538-87af-f1c638a0d387","originalAuthorName":"郑坤灿"},{"authorName":"武文斐","id":"dccc0936-2f72-4561-b0c6-9c8aaa6be105","originalAuthorName":"武文斐"}],"doi":"","fpage":"5","id":"63e904cc-c902-4ac3-93bf-1659423ac57a","issue":"2","journal":{"abbrevTitle":"GTYJ","coverImgSrc":"journal/img/cover/GTYJ.jpg","id":"29","issnPpub":"1001-1447","publisherId":"GTYJ","title":"钢铁研究"},"keywords":[{"id":"828c684f-965a-4f16-8f1c-7e047e9ca954","keyword":"半焦","originalKeyword":"半焦"},{"id":"bf58fb0a-c2b2-4f62-968c-16b51cebf10b","keyword":"<span style=\"color:red\">热重法</span>","originalKeyword":"热重法"},{"id":"a20f6331-7d3d-407d-b2f7-354b6c8fd0a8","keyword":"动力学","originalKeyword":"动力学"}],"language":"zh","publisherId":"gtyj201602002","title":"分峰法分析半焦燃烧动力学的<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>重实验","volume":"44","year":"2016"},{"abstractinfo":"利用德国耐驰STA 409 CD型热分析仪对YBCO化合物合成过程进行了研究.采用普适积分法,微分法及多重速率扫描Kissinger法相结合的方式来确定合成反应的机理,求解动力学参数.结果表明,YBCO超导体合成反应遵守随机成核和随后生长模型.利用积分法和微分法求得合成反应的平均表观活化能为174 kJ·mol-1.","authors":[{"authorName":"洪成哲","id":"8a773a35-ddd5-4626-a9ba-492b2ee0a38b","originalAuthorName":"洪成哲"},{"authorName":"罗清威","id":"757b83e5-abcb-4304-ad0d-480cc87e5034","originalAuthorName":"罗清威"},{"authorName":"冉阿倩","id":"617305ce-5e3c-486b-9d16-4ad346624494","originalAuthorName":"冉阿倩"},{"authorName":"樊占国","id":"bf738b06-9f88-4268-9401-6b644fdc7cdc","originalAuthorName":"樊占国"}],"doi":"10.3969/j.issn.1671-6620.2011.01.005","fpage":"19","id":"4f81f4bd-7bb7-437a-bfde-2816bd44198a","issue":"1","journal":{"abbrevTitle":"CLYYJXB","coverImgSrc":"journal/img/cover/CLYYJXB.jpg","id":"17","issnPpub":"1671-6620","publisherId":"CLYYJXB","title":"材料与冶金学报"},"keywords":[{"id":"7cc8d776-b91d-4a43-941b-e67b7fea51a2","keyword":"化学溶液沉积","originalKeyword":"化学溶液沉积"},{"id":"70ed8851-8955-4b2b-bc91-292323d1afaa","keyword":"YBCO合成","originalKeyword":"YBCO合成"},{"id":"030bdf3b-2e0b-418c-b5f8-8ceae3db3d46","keyword":"<span style=\"color:red\">非</span><span style=\"color:red\">等温热重法</span>","originalKeyword":"非等温热重法"},{"id":"5fb20b59-4660-4dfd-b0b8-3c22f54e62b5","keyword":"动力学","originalKeyword":"动力学"}],"language":"zh","publisherId":"clyyjxb201101005","title":"化学溶液沉积法中YBaCuO超导体合成反应动力学","volume":"10","year":"2011"},{"abstractinfo":"利用Labsys同步热分析仪以<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>重分析研究了碳气化反应动力学,考察了升温速率对碳气化反应的影响.在<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>重分析中,Doyle和Gorbatchev近似函数都可以模拟碳气化反应过程.通过对比这两个函数拟合实验数据的相关系数,确定在使用<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>重分析研究碳气化反应动力学时,使用Gorbatchev函数是求取反应动力学参数的较好方法.结果表明:活化能和指前因子都随着升温速率的增加而减小.活化能和指前因子之间有着较好的线性关系,碳气化反应过程中存在着动力学补偿效应.","authors":[{"authorName":"刘忠锁","id":"97b073bc-d3d6-4d9c-b1a9-506af0b1946e","originalAuthorName":"刘忠锁"},{"authorName":"汪琦","id":"555d70ef-65bf-4b73-9c19-7357a0785938","originalAuthorName":"汪琦"},{"authorName":"邹宗树","id":"26813d85-f754-4a99-bf58-44eada999a8e","originalAuthorName":"邹宗树"},{"authorName":"谭广雷","id":"4ccfb93e-fc2d-47c4-bc1f-4f756f906592","originalAuthorName":"谭广雷"}],"doi":"10.3969/j.issn.1671-6620.2010.01.015","fpage":"68","id":"4395df9c-6f98-4d8c-a06a-a215fcffeff0","issue":"1","journal":{"abbrevTitle":"CLYYJXB","coverImgSrc":"journal/img/cover/CLYYJXB.jpg","id":"17","issnPpub":"1671-6620","publisherId":"CLYYJXB","title":"材料与冶金学报"},"keywords":[{"id":"03d38946-c165-404f-aa64-0c0304a9ff4b","keyword":"<span style=\"color:red\">非</span><span style=\"color:red\">等温</span>","originalKeyword":"非等温"},{"id":"56c08be6-eeca-4acd-9329-cdbd10930e90","keyword":"热重分析","originalKeyword":"热重分析"},{"id":"96b2f84c-b5b1-4e55-a1e1-fcb8e0b6e28c","keyword":"碳气化","originalKeyword":"碳气化"},{"id":"c0a009e2-1ee6-477e-8f66-4238d785eb60","keyword":"动力学","originalKeyword":"动力学"}],"language":"zh","publisherId":"clyyjxb201001015","title":"<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>重分析研究碳气化动力学","volume":"9","year":"2010"},{"abstractinfo":"以天青石还原分解产物的浸取液(SrS)为原料, 氢氧化钠为辅助化工原料制备纯度>99.70%的Sr(OH)2·8H2O.利用差示扫描量热-<span style=\"color:red\">热重法</span>(DSC-TG)对Sr(OH)2·8H2O进行<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>分解试验研究, 并用Kissinger法和Freeman-Carroll法分析计算了热分解脱水反应动力学参数.结果表明: Sr(OH)2·8H2O在50℃左右开始脱水分解, 至130℃以上基本完全分解成粉末状的Sr(OH)2; Sr(OH)2·8H2O的热分解过程以两个阶段进行, 且两阶段吸热峰之间的温度范围小; 两阶段的热分解反应表观活化能分别为E1＝75.26kJ/mol, E2＝95.11kJ/mol, 其热分解反应级数依次为n1＝1.17, n2＝1.29.","authors":[{"authorName":"刘相果","id":"16b35d95-475c-4f8c-8a9d-2dd8d1b6f872","originalAuthorName":"刘相果"},{"authorName":"彭晓东","id":"3c0154d5-e76d-49cd-b987-96b0e6e168ab","originalAuthorName":"彭晓东"},{"authorName":"谢卫东","id":"d35453ed-43ce-4a09-a5d3-bac4c286c471","originalAuthorName":"谢卫东"},{"authorName":"刘江","id":"a22d4706-7cfc-4733-8794-eca52c1d5418","originalAuthorName":"刘江"},{"authorName":"权燕燕","id":"5a8e5474-e05d-4aa1-b409-a51e76509e6d","originalAuthorName":"权燕燕"}],"doi":"","fpage":"686","id":"ac9060ac-c3b1-4446-82c1-a3b66be57073","issue":"4","journal":{"abbrevTitle":"ZGYSJSXB","coverImgSrc":"journal/img/cover/ZGYSJSXB.jpg","id":"88","issnPpub":"1004-0609","publisherId":"ZGYSJSXB","title":"中国有色金属学报"},"keywords":[{"id":"ddb5fdc0-5f38-485b-a0c5-d5caf4e2b8a3","keyword":"八水氢氧化锶","originalKeyword":"八水氢氧化锶"},{"id":"ae0e2fef-2aa4-43f8-95ba-ba9618204824","keyword":"制备","originalKeyword":"制备"},{"id":"a6312b22-aa15-43f9-b173-59392050cc5d","keyword":"<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>分解","originalKeyword":"非等温热分解"},{"id":"cd229781-297b-4324-9546-5dfe1de28c3d","keyword":"动力学参数","originalKeyword":"动力学参数"}],"language":"zh","publisherId":"zgysjsxb200404029","title":"Sr(OH)2·8H2O<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>分解动力学分析","volume":"14","year":"2004"},{"abstractinfo":"用<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>重分析法对氢气还原不同粒度细微氧化铁的动力学进行了研究。研究表明：铁矿粉粒度越小，起始反应温度越低，反应速度越快,反应达到平台期时所对应的还原率越高；平均粒度为3.5 mm的铁矿粉在400 ℃还原反应开始，700 ℃左右开始反应加快，达到平台期时的还原率为77%，而平均粒度为2 μm的铁矿粉在100 ℃已经开始反应，350 ℃反应加快，达到平台期时的还原率为98%，而且在600 ℃时还原率就达到了100%；铁矿粉粒度从3.5 mm降到2 μm后，还原反应的表观活化能从73.3 kJ/mol降低到30.46 kJ/mol；同时通过分析氢气还原氧化铁的反应机理得出，内扩散和界面化学反应均对整个反应过程起限制作用。","authors":[{"authorName":"庞建明","id":"db417ea5-ab00-4fda-9a54-f2130526fd8b","originalAuthorName":"庞建明"},{"authorName":"郭培民","id":"dbdcebff-358b-46b0-89c7-44c26b231ffa","originalAuthorName":"郭培民"},{"authorName":"赵沛","id":"b0385aba-0e0f-470c-ad0d-e001a76002a7","originalAuthorName":"赵沛"},{"authorName":"曹朝真","id":"bc6f1d80-344f-47ac-96e5-be7ed01b02bb","originalAuthorName":"曹朝真"}],"categoryName":"|","doi":"","fpage":"11","id":"563eaf6c-a245-4374-ae67-cb78bc2c37df","issue":"2","journal":{"abbrevTitle":"GT","coverImgSrc":"journal/img/cover/GT.jpg","id":"27","issnPpub":"0449-749X","publisherId":"GT","title":"钢铁"},"keywords":[{"id":"aec603c3-af3a-4814-9567-1ee6de5ae0fa","keyword":"<span style=\"color:red\">非</span><span style=\"color:red\">等温</span>方法;氧化铁;动力学;热重分析","originalKeyword":"非等温方法;氧化铁;动力学;热重分析"}],"language":"zh","publisherId":"0449-749X_2009_2_3","title":"氢气还原氧化铁动力学的<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>重方法研究","volume":"44","year":"2009"},{"abstractinfo":"利用热重（TG）分析技术研究了端羟基超支化聚酯（HBP）以及十八酸改性的超支化聚酯（MHBP）的热失重行为,运用Flynn-Wal-l Ozawa法和Coats-Redfern法对<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>分解动力学数据进行了分析。结果表明,HBP的分解过程分为三个阶段,三个阶段的表观活化能分别为120.238 kJ/mol、149.775 kJ/mol、173.540 kJ/mol,指前因子分别为1.386×10^9min^-1、1.341×10^9min^-1、4.569×10^12min^-1;MHBP的分解过程仅有一个阶段,表观活化能和指前因子分别为204.275kJ/mol和2.417×10^14min^-1。超支化聚酯的热稳定性与其端基有关,十八酸改性的超支化聚酯由于长链烷烃具有结晶性,因而热稳定性优于端羟基超支化聚酯。","authors":[{"authorName":"刘晶如","id":"e9bcba3f-e6ef-4ef2-9b68-b84339bb5038","originalAuthorName":"刘晶如"},{"authorName":"巢玲玲","id":"52d8ff68-6d55-4620-8501-e1240d9d55c3","originalAuthorName":"巢玲玲"},{"authorName":"俞强","id":"363db2d5-5c35-4b70-ad08-cdd6cf658597","originalAuthorName":"俞强"}],"doi":"","fpage":"76","id":"8e160d28-53a9-493f-aad1-1d5823e47caf","issue":"4","journal":{"abbrevTitle":"GFZCLKXYGC","coverImgSrc":"journal/img/cover/GFZCLKXYGC.jpg","id":"31","issnPpub":"1000-7555","publisherId":"GFZCLKXYGC","title":"高分子材料科学与工程"},"keywords":[{"id":"99ba7c6b-a143-404b-9464-209ab8acb161","keyword":"超支化聚酯","originalKeyword":"超支化聚酯"},{"id":"811948b8-e60a-44f3-a7f0-62af393d83b0","keyword":"热分解动力学","originalKeyword":"热分解动力学"},{"id":"e63a208e-5706-4fb8-93f0-d87eeeee315f","keyword":"热重分析","originalKeyword":"热重分析"}],"language":"zh","publisherId":"gfzclkxygc201204020","title":"超支化聚酯的<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>分解动力学","volume":"28","year":"2012"},{"abstractinfo":"用<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>量分析法对氢气还原不同粒度细微氧化铁的动力学进行了研究.研究表明:铁矿粉粒度越小,起始反应温度越低,反应速度越快,反应达到平台期时所对应的还原率越岛;平均粒度为3.5 mm的铁矿粉在400℃还原反应开始,700℃左右开始反应加快,达到平台期时的还原率为77%,而平均粒度为2 μm的铁矿粉在100℃已经开始反应,350℃反应加快,达到平台期时的还原率为98%,而且在600℃时还原率就达到了100%;铁矿粉粒度从3.5 mm降到2 μm后,还原反应的表观活化能从73.3 kJ/mol降低到30.46 kJ/mol;同时通过分析氢气还原氧化铁的反应机理得出,内扩散和界面化学反应均对整个反应过程起限制作用.","authors":[{"authorName":"庞建明","id":"2b92e157-5961-49db-a3ac-441faecc4fc5","originalAuthorName":"庞建明"},{"authorName":"郭培民","id":"55f1196f-d0d6-4aad-9032-7bb049f1af07","originalAuthorName":"郭培民"},{"authorName":"赵沛","id":"4a81302c-4aac-450d-b76a-a4474a1dfd16","originalAuthorName":"赵沛"},{"authorName":"曹朝真","id":"3f9213dc-a245-478a-abce-0ebf9b6fdada","originalAuthorName":"曹朝真"}],"doi":"","fpage":"11","id":"d009ba73-2fed-4ddb-8194-b973c216685a","issue":"2","journal":{"abbrevTitle":"GT","coverImgSrc":"journal/img/cover/GT.jpg","id":"27","issnPpub":"0449-749X","publisherId":"GT","title":"钢铁"},"keywords":[{"id":"9a52cd29-38e7-4033-9e8a-0c6541f7c634","keyword":"<span style=\"color:red\">非</span><span style=\"color:red\">等温</span>方法","originalKeyword":"非等温方法"},{"id":"ad7bea6f-cde3-4c38-a2ba-6fc61bd4f5e2","keyword":"氧化铁","originalKeyword":"氧化铁"},{"id":"b89a635d-50dd-47a1-9bda-a3ca8dfa73f4","keyword":"动力学","originalKeyword":"动力学"},{"id":"33db8d12-6e50-4849-b5d9-36fca02628f3","keyword":"热重分析","originalKeyword":"热重分析"}],"language":"zh","publisherId":"gt200902002","title":"氢气还原氧化铁动力学的<span style=\"color:red\">非</span><span style=\"color:red\">等温热</span>重方法研究","volume":"44","year":"2009"}],"totalpage":1544,"totalrecord":15432}