{"currentpage":1,"firstResult":0,"maxresult":10,"pagecode":5,"pageindex":{"endPagecode":5,"startPagecode":1},"records":[{"abstractinfo":"通过分析<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span><span style=\"color:red\">吹</span>铜熔炼渣及铜锍，结合冶金过程原理，研究渣－铜锍间多组元含量的映射关系及熔炼过程优化。结果表明：铜锍中Cu、S、Fe含量之间呈现出较强的相关性；渣中Cu、SiO 2、Fe含量及渣型铁硅比(SiO )(Fe)2m /m 相互之间也呈现出一定的相关性；铜锍中Cu、Fe、S含量对渣中S含量的映射关系较为明显；基于铜锍中S、Cu含量和渣中S含量，或基于渣型铁硅比(SiO )(Fe)2m /m 和铜锍品位都可对渣中Cu含量进行预测，后者的准确度较高，说明铜锍品位和渣型对渣中Cu含量有较大影响。","authors":[{"authorName":"郭学益","id":"451a7765-6e41-411c-9fba-037153879fb1","originalAuthorName":"郭学益"},{"authorName":"王亲猛","id":"bf84e133-0cdd-4c8e-9291-c6d904a4fc1d","originalAuthorName":"王亲猛"},{"authorName":"田庆华","id":"e590fbd0-4039-44c9-ad69-ff5f097ac4b2","originalAuthorName":"田庆华"},{"authorName":"ZHAO Bao-jun","id":"bd39493f-e17c-4962-9338-9e52042605d6","originalAuthorName":"ZHAO Bao-jun"}],"doi":"","fpage":"689","id":"b94c0a88-fbc6-461e-8e15-d79a5893bc87","issue":"3","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":"213a5f41-9c3c-4610-94f6-d07349664939","keyword":"铜冶金","originalKeyword":"铜冶金"},{"id":"fd6b7525-2fb9-4903-ad62-b5c3b44be288","keyword":"<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span><span style=\"color:red\">吹</span>","originalKeyword":"氧气底吹"},{"id":"89cd863e-2332-41fd-948b-30fec81efa35","keyword":"性能分析","originalKeyword":"性能分析"},{"id":"70ba8e86-27f4-4222-9509-6c630bb7c8ba","keyword":"过程优化","originalKeyword":"过程优化"}],"language":"zh","publisherId":"zgysjsxb201603026","title":"<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span><span style=\"color:red\">吹</span>铜熔炼工艺分析及过程优化","volume":"26","year":"2016"},{"abstractinfo":"通过分析<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span>吹炼铜过程产生的高品位铜锍中Cu、Fe、S、SiO2等组元含量变化趋势,结合冶金过程原理,研究上述各组元造锍行为及组元含量间的映射关系.结果表明:Cu、Fe、S、SiO2等组元在铜锍中的造锍行为具有相互关联性,其中Cu、Fe、S相互之间的关联性较强,Cu-Fe、Cu-S、Fe-S含量之间线性相关系数R2分别为0.96、0.89、0.79,但SiO2与Cu、Fe、S之间的关联性较弱.构造了Cu、Fe、S组元含量复合映射模型,该复合模型预测精确度高于单因素模型的预测精确度,可为生产过程中高品位铜锍多组元含量的精细调控,及熔炼-吹炼过程热量精确分配提供指导.","authors":[{"authorName":"王亲猛","id":"474a3e74-787a-4172-b75c-fbc8a84ce802","originalAuthorName":"王亲猛"},{"authorName":"郭学益","id":"fb103245-5af3-4127-9f64-4bc508c0bae4","originalAuthorName":"郭学益"},{"authorName":"廖立乐","id":"08f55350-e040-4669-9f69-bf214ca78972","originalAuthorName":"廖立乐"},{"authorName":"田庆华","id":"4dd66a43-13df-441f-ac94-26381378bd5f","originalAuthorName":"田庆华"},{"authorName":"张永柱","id":"61590965-decc-4fb1-af3c-f1ad7b504ddf","originalAuthorName":"张永柱"}],"doi":"","fpage":"188","id":"5477c742-ada2-4219-9039-1d03eba65d2b","issue":"1","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":"8f9916f2-f3bf-493a-8cc5-19a008e46484","keyword":"<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span><span style=\"color:red\">吹</span>","originalKeyword":"氧气底吹"},{"id":"29cf8845-6dd7-4f82-9b64-d35b0a1f9e1a","keyword":"炼铜","originalKeyword":"炼铜"},{"id":"7bf46f74-b9d1-441d-b669-103952c4e177","keyword":"铜锍","originalKeyword":"铜锍"},{"id":"06171bf0-ba3b-413e-bdd8-fab68c50ec77","keyword":"预测模型","originalKeyword":"预测模型"}],"language":"zh","publisherId":"zgysjsxb201601022","title":"<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span>吹炼铜多组元造锍行为及组元含量的映射关系","volume":"26","year":"2016"},{"abstractinfo":"<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span><span style=\"color:red\">吹</span>炉是一种类似诺兰达炉的卧式旋转反应器,但富氧空气从炉体底部喷入熔体.通过分析<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>熔炼特性,提出了<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span>吹炼铜机理.在机理模型中,<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>炉内由上到下分成7个功能层,分别是烟气层、矿料分解过渡层、渣层、造渣过渡层、造锍过渡层、弱氧化层和强氧化层;沿轴线方向分成3个功能区,分别是反应区、分离过渡区、液相澄清区.模型中所有的层和区分别具有不同的作用.<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span><span style=\"color:red\">吹</span>熔炼过程处于非稳态的近似多相平衡状态,且炉内不同空间位点的氧势、硫势呈梯度变化;通过合理控制不同层、区的氧势、硫势,可进一步提高<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span><span style=\"color:red\">吹</span>炉的熔炼能力.","authors":[{"authorName":"王亲猛","id":"cdf8f53b-01a3-4352-8655-4fecbc198c28","originalAuthorName":"王亲猛"},{"authorName":"郭学益","id":"435e3dc0-a1d4-4818-9670-bb6520647eae","originalAuthorName":"郭学益"},{"authorName":"田庆华","id":"148df3b4-0416-4f68-8e35-4b7b1bbdb660","originalAuthorName":"田庆华"}],"doi":"10.1016/S1003-6326(17)60110-9","fpage":"946","id":"01436900-4593-4214-a11f-a0628d69e643","issue":"4","journal":{"abbrevTitle":"ZGYSJSXBEN","coverImgSrc":"journal/img/cover/ZGYSJSXBEN.jpg","id":"757390d2-7d95-4517-96f1-e467ce1bff63","issnPpub":"1003-6326","publisherId":"ZGYSJSXBEN","title":"中国有色金属学报(英文版)"},"keywords":[{"id":"f2e448f9-e279-4b8d-b2bf-1a0682f757b1","keyword":"<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span>吹炼铜","originalKeyword":"氧气底吹炼铜"},{"id":"6c057c36-d2b0-46d8-9ac9-ed8ceac9847d","keyword":"机理","originalKeyword":"机理"},{"id":"5e4567a1-d288-4ddd-ab4a-e2d75f97cf83","keyword":"多相平衡","originalKeyword":"多相平衡"},{"id":"a65138c4-ca52-49bf-9f93-290c0e65bdef","keyword":"氧势","originalKeyword":"氧势"},{"id":"610e392a-2886-4e11-a479-e7e586c7fa93","keyword":"硫势","originalKeyword":"硫势"},{"id":"e60c8970-2640-4159-b756-42f25968135d","keyword":"SKS工艺","originalKeyword":"SKS工艺"}],"language":"zh","publisherId":"zgysjsxb-e201704027","title":"<span style=\"color:red\">氧气</span><span style=\"color:red\">底</span>吹炼铜机理","volume":"27","year":"2017"},{"abstractinfo":"为研究钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>孔布置对钢液混匀时间及液面波动的影响，确定钢包最优<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>工艺，以某厂210 t钢包为原型，根据相似原理建立钢包物理模型，模拟钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩工艺。通过研究不同<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>孔位置与角度对混匀时间和液面波动的影响，确定钢包最优<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>工艺。结果表明，最优<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>位置为<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>孔位于距钢包底部圆心距离为0.60R/0.60R，夹角为100°。<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>孔在0.40R的位置，两气柱会相互影响；<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>孔在0.60R的位置是较理想的位置；<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>孔在0.79R的位置，气流对包壁冲刷严重。","authors":[{"authorName":"董鹏莉","id":"d64b5989-cb6e-49db-8fac-e6b0dd821dd1","originalAuthorName":"董鹏莉"}],"doi":"10.13228/j.boyuan.issn0449-749x.20150546","fpage":"41","id":"0d3ef894-ded3-4482-85d2-4add7e683a0c","issue":"7","journal":{"abbrevTitle":"GT","coverImgSrc":"journal/img/cover/GT.jpg","id":"27","issnPpub":"0449-749X","publisherId":"GT","title":"钢铁"},"keywords":[{"id":"dd5488c7-8853-4e51-9894-6c2bf15709ca","keyword":"钢包","originalKeyword":"钢包"},{"id":"9dcf0ebb-b007-4bd1-a080-de29991bf67d","keyword":"<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩","originalKeyword":"底吹氩"},{"id":"23a4e963-adc1-43b2-9017-4120bc1f0b1e","keyword":"混匀时间","originalKeyword":"混匀时间"},{"id":"d073ffcd-48c6-44ba-81b5-8b775bd9229d","keyword":"物理模拟","originalKeyword":"物理模拟"}],"language":"zh","publisherId":"gt201607007","title":"210 t钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>工艺优化物理模拟","volume":"51","year":"2016"},{"abstractinfo":"在1:6物理模型上,通过水模实验对复<span style=\"color:red\">吹</span>转炉<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>喷粉时熔池搅拌情况进行了研究.结果表明:喷粉对熔池搅拌有明显的促进作用.喷粉条件下,均混时间随顶吹气体流量的增加存在最小值,最佳顶吹气体流量为117.0 m3/h,增加<span style=\"color:red\">底</span>吹气体流量对降低均混时间有利.在本实验范围内最佳顶吹流量为117.0 m3/h、最佳<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>流量为2.36 m3/h.","authors":[{"authorName":"王学斌","id":"469074fe-b3e4-4795-9e6f-fe00270a7ddd","originalAuthorName":"王学斌"},{"authorName":"冯明霞","id":"2ad651e1-5640-4b63-a52e-c724d55934c9","originalAuthorName":"冯明霞"},{"authorName":"刘崇林","id":"14ce668f-4ac2-41d1-ba82-e50a300dc9e6","originalAuthorName":"刘崇林"},{"authorName":"邹宗树","id":"e1793516-f866-4461-9c1e-8b5f6a74cacb","originalAuthorName":"邹宗树"}],"doi":"10.3969/j.issn.1671-6620.2009.01.003","fpage":"12","id":"c1e09472-f525-4625-abef-eb78de6767ec","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":"092ee325-76f6-4e5f-9319-84a34d71a950","keyword":"复<span style=\"color:red\">吹</span>转炉","originalKeyword":"复吹转炉"},{"id":"3885e738-4c31-47d0-82e8-f8bd4e362b52","keyword":"喷粉","originalKeyword":"喷粉"},{"id":"c5c1c23e-7747-47dc-8d44-6e141782c152","keyword":"<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>","originalKeyword":"底吹"},{"id":"0cba4f32-bfc4-4c90-aa35-ce72f1d8d8a1","keyword":"水模型","originalKeyword":"水模型"},{"id":"dd936dea-3c2c-4eeb-a4dc-196920083ba0","keyword":"均混时间","originalKeyword":"均混时间"}],"language":"zh","publisherId":"clyyjxb200901003","title":"复<span style=\"color:red\">吹</span>转炉<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>喷粉实验研究","volume":"8","year":"2009"},{"abstractinfo":"钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩是一种操作简单、精炼效果明显的炉外精炼装置.新兴铸管炼钢厂为改善钢水精炼效果,采用钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩代替顶吹,即用狭缝式透气砖代替<span style=\"color:red\">吹</span>氩棒.生产实践证明,<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩能改善和提高钢水的内在质量,降低钢中夹杂物含量和气体含量,<span style=\"color:red\">吹</span>氩后钢质的力学性能符合国家标准.","authors":[{"authorName":"范英俊","id":"afc04eb5-10bd-449a-b20a-f858747c8fa9","originalAuthorName":"范英俊"},{"authorName":"杨明生","id":"ce1b4eed-c7d3-48f6-a538-4bf6b9fcf6d4","originalAuthorName":"杨明生"}],"doi":"","fpage":"20","id":"44e10b67-8105-4b3c-9b7a-d0c78008d51a","issue":"4","journal":{"abbrevTitle":"GT","coverImgSrc":"journal/img/cover/GT.jpg","id":"27","issnPpub":"0449-749X","publisherId":"GT","title":"钢铁"},"keywords":[{"id":"f074cea5-aee7-4757-9f86-460bef20c8df","keyword":"转炉","originalKeyword":"转炉"},{"id":"3c6754b3-cb38-43de-bc00-79425d140288","keyword":"钢包","originalKeyword":"钢包"},{"id":"90e4e34f-8eeb-46d8-b675-2505c167ec82","keyword":"<span style=\"color:red\">吹</span>氩","originalKeyword":"吹氩"}],"language":"zh","publisherId":"gt200104006","title":"钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩在转炉生产中的应用","volume":"36","year":"2001"},{"abstractinfo":"分析了影响钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩成功率的各种因素,提出了改进措施.实践证明:改进措施的实施使钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩成功率由90%提高到99%,满足了品种钢生产的需要.","authors":[{"authorName":"米源","id":"f2f439a6-ada0-4202-87ba-83e958a90168","originalAuthorName":"米源"}],"doi":"10.3969/j.issn.1001-1935.2007.04.014","fpage":"287","id":"283323c9-4e30-45a0-8dde-5c05e98e732d","issue":"4","journal":{"abbrevTitle":"NHCL","coverImgSrc":"journal/img/cover/NHCL.jpg","id":"55","issnPpub":"1001-1935","publisherId":"NHCL","title":"耐火材料   "},"keywords":[{"id":"40671938-d7a9-4211-ad46-946f1e5ca5ca","keyword":"钢包","originalKeyword":"钢包"},{"id":"0bf6442a-ffa2-45ba-ad3f-7c2e095bf25c","keyword":"透气砖","originalKeyword":"透气砖"},{"id":"9057fda6-f5c9-407a-ae64-428bf4d14553","keyword":"<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩","originalKeyword":"底吹氩"}],"language":"zh","publisherId":"nhcl200704014","title":"钢包<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>氩工艺技术改进","volume":"41","year":"2007"},{"abstractinfo":"概述了唐钢第一钢轧厂转炉顶<span style=\"color:red\">底</span>复<span style=\"color:red\">吹</span>工艺的情况,通过对转炉冶炼工艺的优化,炉渣成分的有效控制、<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>模式的优化、溅渣护炉工艺的改进,解决了炉<span style=\"color:red\">底</span>上涨与透气砖侵蚀的问题,提高了<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>效果,改善了钢水质量.","authors":[{"authorName":"张大勇","id":"b3bd80d6-19bd-4098-bc62-b9608989fe91","originalAuthorName":"张大勇"},{"authorName":"张彩军","id":"c776bda3-d64f-4184-9294-aef5ffbbd76a","originalAuthorName":"张彩军"},{"authorName":"刘玉生","id":"962754ee-cff1-4014-b822-8bd7782be106","originalAuthorName":"刘玉生"}],"doi":"10.3969/j.issn.1000-6826.2007.04.003","fpage":"9","id":"f3a6aee9-34bc-447d-8ed5-5fbebb88e9b0","issue":"4","journal":{"abbrevTitle":"JSSJ","coverImgSrc":"journal/img/cover/3abe017a-2574-4821-8152-4ae974ef0471.jpg","id":"47","issnPpub":"1000-6826","publisherId":"JSSJ","title":"金属世界"},"keywords":[{"id":"6415a5e8-865b-4dbe-8787-b9645926e9ae","keyword":"转炉","originalKeyword":"转炉"},{"id":"aab3f661-1a32-4ca9-b990-f281ec0b06cc","keyword":"顶<span style=\"color:red\">底</span>复<span style=\"color:red\">吹</span>","originalKeyword":"顶底复吹"},{"id":"a9676db9-be0f-42ce-b78a-46f3b134a446","keyword":"透气砖","originalKeyword":"透气砖"},{"id":"43d152b1-9fd9-47b2-a24f-eb5f70995e31","keyword":"透气性","originalKeyword":"透气性"},{"id":"64ad18f2-8c3d-444f-81f3-092e49bf6ddb","keyword":"供气模式","originalKeyword":"供气模式"}],"language":"zh","publisherId":"jssj200704003","title":"150吨转炉顶<span style=\"color:red\">底</span>复<span style=\"color:red\">吹</span>工艺的实践","volume":"","year":"2007"},{"abstractinfo":"根据重庆钢铁股份公司复<span style=\"color:red\">吹</span>转炉生产过程中实际结构尺寸和改造设计的特点,设计制作了复<span style=\"color:red\">吹</span>转炉冷态模型.针对实际生产过程中转炉<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>喷枪可能出现的异常堵塞情况,研究了<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>喷枪正常、部分堵塞或全部堵塞等不同工况下,复<span style=\"color:red\">吹</span>转炉熔池内的搅拌混匀时间与<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>供气强度的关系.","authors":[{"authorName":"周远华","id":"08752751-a355-44dc-afce-46fbbe2e914c","originalAuthorName":"周远华"},{"authorName":"温良英","id":"8ab4137e-eb4b-4e30-ab5d-c94c9d7e1b83","originalAuthorName":"温良英"},{"authorName":"李斌","id":"7e724a5c-3f1d-49e3-a8ae-2a88ea9e8465","originalAuthorName":"李斌"},{"authorName":"陈登福","id":"92b298b9-bf96-4687-b173-104e0ccdba49","originalAuthorName":"陈登福"}],"doi":"","fpage":"14","id":"33601fb4-92ad-45b6-ba0a-fae4e84342ae","issue":"5","journal":{"abbrevTitle":"GTYJXB","coverImgSrc":"journal/img/cover/GTYJXB.jpg","id":"30","issnPpub":"1001-0963","publisherId":"GTYJXB","title":"钢铁研究学报"},"keywords":[{"id":"e0d7be4e-9f5e-42bb-9fe2-8a749dab5620","keyword":"转炉","originalKeyword":"转炉"},{"id":"f0ddda26-3c01-4136-bdcb-f03295add8f8","keyword":"<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>","originalKeyword":"底吹"},{"id":"9b74e63d-c12f-4584-9108-8afc1a9bacd8","keyword":"供气强度","originalKeyword":"供气强度"},{"id":"2d060e73-6c33-4efb-9eda-15a3c08fab57","keyword":"堵塞","originalKeyword":"堵塞"}],"language":"zh","publisherId":"gtyjxb200605004","title":"<span style=\"color:red\">底</span><span style=\"color:red\">吹</span>喷枪异常堵塞时复<span style=\"color:red\">吹</span>转炉的熔池搅拌","volume":"18","year":"2006"},{"abstractinfo":"根据整体及各区域的物理化学约束条件建立了<span style=\"color:red\">氧气</span>高炉工艺综合数学模型.通过模型的计算结果对能量在不同区域的利用情况进行了分析3得出结论如下:<span style=\"color:red\">氧气</span>高炉无煤气循环流程的一次能耗很高,燃料比在600 kg/tHM以上,并且无法实现高温区和固体炉料区之间的能量匹配.炉顶煤气循环后,可以实现能量在高温区和固体炉料区的同时平衡；在同时满足全炉热平衡和区域热平衡的条件下,<span style=\"color:red\">氧气</span>高炉炉身喷<span style=\"color:red\">吹</span>循环煤气流程的理论燃烧温度过高,而炉缸喷<span style=\"color:red\">吹</span>循环煤气流程的理论燃烧温度偏低；对于<span style=\"color:red\">氧气</span>高炉炉身、炉缸同时喷<span style=\"color:red\">吹</span>循环煤气流程,随着循环煤气量的增大,焦比升高,煤比降低,理论燃烧温度可以维持在合理的范围内.","authors":[{"authorName":"高攀","id":"67e3160b-81f2-490d-b1c7-9c1c926dcae3","originalAuthorName":"高攀"},{"authorName":"李强","id":"0e69022a-8987-48d8-8d37-f82b04e602d1","originalAuthorName":"李强"},{"authorName":"张作良","id":"c562e776-544e-49b8-a59c-eee10f072a08","originalAuthorName":"张作良"},{"authorName":"张伟","id":"96f9d670-10e6-4d97-a3e9-dd71f11134e3","originalAuthorName":"张伟"},{"authorName":"邹宗树","id":"aac7152e-1b08-49f4-af4a-19d5585d8551","originalAuthorName":"邹宗树"},{"authorName":"干勇","id":"f2583ea9-25be-4bd6-b10b-66890d8f289d","originalAuthorName":"干勇"}],"doi":"","fpage":"7","id":"4aff6219-f479-48a6-94d4-046900623c17","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":"1e9f7591-4bf7-4268-80f6-2b0e19ce1b9b","keyword":"炼铁","originalKeyword":"炼铁"},{"id":"1ebafbd4-7cc8-4a29-b6a6-d6437aeefd7f","keyword":"<span style=\"color:red\">氧气</span>高炉","originalKeyword":"氧气高炉"},{"id":"5cb0e477-380b-4541-acee-41331ff31941","keyword":"物料平衡","originalKeyword":"物料平衡"},{"id":"14b01bb6-657d-4452-baf7-ed1cd83333ce","keyword":"热平衡","originalKeyword":"热平衡"},{"id":"064b3e41-001f-46c0-bb83-752c5d606596","keyword":"数学模型","originalKeyword":"数学模型"}],"language":"zh","publisherId":"clyyjxb201301003","title":"喷<span style=\"color:red\">吹</span>循环煤气<span style=\"color:red\">氧气</span>高炉的静态模型","volume":"12","year":"2013"}],"totalpage":292,"totalrecord":2913}