{"currentpage":1,"firstResult":0,"maxresult":10,"pagecode":5,"pageindex":{"endPagecode":5,"startPagecode":1},"records":[{"abstractinfo":"对宝钢COREX-3000风口破损现象进行了分析研究,得出风口破损是高温熔损和气流冲刷磨损共同作用的结果.通过对COREX风口燃烧区热分布的分析,提出可以从5个方面采取措施减少高温熔损,延长风口寿命.基于以上研究,宝钢采用了使用宝钢小块焦代替部分山西焦和<span style=\"color:red\">氧气</span><span style=\"color:red\">氮气</span><span style=\"color:red\">混合</span>鼓风代替纯氧鼓风的措施,有效改善了风口使用寿命；同时,全面分析了该改进措施对COREX所产生的影响.分析结果表明:宝钢小块焦的使用改善了炉料的透气性,避免了风口燃烧区的热量聚集；<span style=\"color:red\">氧气</span><span style=\"color:red\">氮气</span><span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>减少了风口燃烧区的热量产生量、降低了气流的导热能力,同时在风口表面形成了氮化碳保护薄层,从而起到保护风口、延长风口使用寿命的作用.","authors":[{"authorName":"田广亚","id":"94468a82-afbd-4581-b130-c60e289594e7","originalAuthorName":"田广亚"},{"authorName":"李京社","id":"6dfc4b78-dc99-4f13-9059-1be56f66f53c","originalAuthorName":"李京社"},{"authorName":"杨宏博","id":"71e80c64-d3a4-4a04-a050-11571b1a7db2","originalAuthorName":"杨宏博"}],"doi":"","fpage":"25","id":"d39ce6d1-1a38-41b6-b66b-f84231721c5e","issue":"10","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":"50d454be-ad29-4d63-89ae-69673255b292","keyword":"风口破损","originalKeyword":"风口破损"},{"id":"2833f8e1-fd3d-4971-8124-a9b6c2793d75","keyword":"<span style=\"color:red\">氧气</span><span style=\"color:red\">氮气</span><span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>","originalKeyword":"氧气氮气混合喷吹"},{"id":"2e9564a8-fed6-4f8d-bc0d-0aaefa77bb0a","keyword":"氮化碳","originalKeyword":"氮化碳"}],"language":"zh","publisherId":"gtyjxb201310006","title":"COREX风口破损原因及对策分析","volume":"25","year":"2013"},{"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<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>循环煤气流程的理论燃烧温度过高,而炉缸<span style=\"color:red\">喷</span><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<span style=\"color:red\">喷</span><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":"<span style=\"color:red\">喷</span><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"},{"abstractinfo":"为降低<span style=\"color:red\">氧气</span>高炉炼铁流程中循环煤气脱除CO2及煤气预热成本,提出了<span style=\"color:red\">氧气</span>高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>焦炉煤气炼铁流程,并建立了新流程能质平衡数学模型,应用该模型分别对传统高炉、传统高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>焦炉煤气、<span style=\"color:red\">氧气</span>高炉(鼓风氧体积分数为30%、40%、50%、100%)<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>焦炉煤气炼铁流程主要技术参数进行计算并对比.结果表明,传统高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>少量焦炉煤气(30 m3/t)可降低燃料比13 kg/t,焦炉煤气置换焦炭的置换比为0.433 kg/m3,但是对其他参数影响不大.<span style=\"color:red\">氧气</span>高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>焦炉煤气流程随着富氧率提高,炉内还原势提高,CO和氢利用率下降,炉内存在还原剂表观过剩,非全氧鼓风条件下炉内没有发生<span style=\"color:red\">氮气</span>富集.新流程外供煤气总热值为3000 MJ/t左右,与传统高炉相比变化不大,对现有钢铁联合企业煤气供需平衡影响较小.全氧高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>焦炉煤气炼铁流程相较于目前的高炉炼铁流程可节焦43%,增煤33%,总燃料比降低20%.","authors":[{"authorName":"董择上","id":"5cb6af65-8449-4d7f-b22b-08475d9faebb","originalAuthorName":"董择上"},{"authorName":"薛庆国","id":"d03d64f1-65fb-4220-9f33-784448c14f61","originalAuthorName":"薛庆国"},{"authorName":"左海滨","id":"e54c4090-cd2f-4df4-8438-9089976bd9c0","originalAuthorName":"左海滨"},{"authorName":"佘雪峰","id":"6015e35a-0635-4ea8-b0e6-93a8a1d33eb9","originalAuthorName":"佘雪峰"},{"authorName":"王广","id":"a4237767-e7c9-4ed6-8e7f-2cbb94e92951","originalAuthorName":"王广"},{"authorName":"王静松","id":"1db05bfa-0eba-4f66-8a4e-b5a7bfe91afb","originalAuthorName":"王静松"}],"doi":"10.13228/j.boyuan.issn0449-749x.20160321","fpage":"18","id":"8507c68b-0946-4939-8001-eaa97de53765","issue":"4","journal":{"abbrevTitle":"GT","coverImgSrc":"journal/img/cover/GT.jpg","id":"27","issnPpub":"0449-749X","publisherId":"GT","title":"钢铁"},"keywords":[{"id":"1523c9a6-d3b3-474d-bf6f-581b0b58d2dd","keyword":"<span style=\"color:red\">氧气</span>高炉炼铁","originalKeyword":"氧气高炉炼铁"},{"id":"23dc1e3c-cfd4-41bd-943a-fe4945159d18","keyword":"<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>焦炉煤气","originalKeyword":"喷吹焦炉煤气"},{"id":"30225a6b-3369-430e-ac0e-bf6af887f4a0","keyword":"数学模型","originalKeyword":"数学模型"},{"id":"5a870684-2dc2-4492-9d61-768c0fa1492c","keyword":"工艺参数","originalKeyword":"工艺参数"},{"id":"07cf53a1-5303-4721-b881-1baecf9dc148","keyword":"节能减排","originalKeyword":"节能减排"}],"language":"zh","publisherId":"gt201704005","title":"<span style=\"color:red\">氧气</span>高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>焦炉煤气数学模型","volume":"52","year":"2017"},{"abstractinfo":"测定了攀西地区<span style=\"color:red\">混合</span>煤的理化性能,并在攀钢高炉上进行了<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span><span style=\"color:red\">混合</span>煤的工业性试验,瘦煤配比由10%逐渐增加到25%,煤比达到113.81?kgtFe;2000年上半年瘦煤配比平均为35.00%,煤比达到139.14?kgtFe.","authors":[{"authorName":"李真才","id":"bbbb635b-5523-4c51-8270-b1d7b720feac","originalAuthorName":"李真才"},{"authorName":"张文新","id":"a5a44327-320e-4795-ac58-7000dbe04ea3","originalAuthorName":"张文新"},{"authorName":"饶家庭","id":"8462a457-98a5-4c02-bf9d-ba9ad273ab31","originalAuthorName":"饶家庭"},{"authorName":"范云东","id":"a45ce8f1-66f7-4e0d-a175-c2e199f933dc","originalAuthorName":"范云东"},{"authorName":"钟余明","id":"291a8187-263e-4d61-86ac-9a3854ba9d36","originalAuthorName":"钟余明"},{"authorName":"王华","id":"6c51d9c9-3bc2-46ba-8d41-5f83e60b5e2f","originalAuthorName":"王华"}],"doi":"10.3969/j.issn.1004-7638.2000.04.002","fpage":"5","id":"d471a739-77ac-417c-a1e2-5b9048e6f636","issue":"4","journal":{"abbrevTitle":"GTFT","coverImgSrc":"journal/img/cover/gtft1.jpg","id":"28","issnPpub":"1004-7638","publisherId":"GTFT","title":"钢铁钒钛"},"keywords":[{"id":"f925f711-ddc6-43f4-9d86-2dffb5fb2d6e","keyword":"高炉","originalKeyword":"高炉"},{"id":"ab1f9e3a-a11d-4593-8411-6f09164a33d8","keyword":"<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span><span style=\"color:red\">混合</span>煤","originalKeyword":"喷吹混合煤"},{"id":"f3cb7120-5e9f-4205-a330-9075169fde87","keyword":"瘦煤挥发分","originalKeyword":"瘦煤挥发分"},{"id":"ed4a724d-e631-4546-aae7-84ab5eaf835d","keyword":"煤比","originalKeyword":"煤比"},{"id":"cd3d818a-e134-4eb1-a127-d02fddb59e96","keyword":"置换比","originalKeyword":"置换比"}],"language":"zh","publisherId":"gtft200004002","title":"攀钢高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span><span style=\"color:red\">混合</span>煤的工业性试验","volume":"21","year":"2000"},{"abstractinfo":"计算分析了<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>条件下,添加粉料成分及添加量对高炉炉渣性能的影响.","authors":[{"authorName":"高斌","id":"171db8f7-f40f-4b11-bccf-e88a95989802","originalAuthorName":"高斌"},{"authorName":"顾飞","id":"0d43d991-c670-4ca9-904d-f58b534fd4a9","originalAuthorName":"顾飞"},{"authorName":"史俊","id":"11ee9bd2-6087-426e-af10-6b9abecbe8af","originalAuthorName":"史俊"}],"doi":"","fpage":"11","id":"5aafa86e-03e3-476b-a789-b435cb227a4e","issue":"8","journal":{"abbrevTitle":"GT","coverImgSrc":"journal/img/cover/GT.jpg","id":"27","issnPpub":"0449-749X","publisherId":"GT","title":"钢铁"},"keywords":[{"id":"6d524122-3c53-4730-b707-3d5294c40083","keyword":"高炉","originalKeyword":"高炉"},{"id":"11b13bef-6ea8-42b0-9573-97e17db6b755","keyword":"<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>","originalKeyword":"混合喷吹"},{"id":"08b7a252-93ed-4f35-98fe-8a5d4129f337","keyword":"炉渣性能","originalKeyword":"炉渣性能"}],"language":"zh","publisherId":"gt199908004","title":"<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>对高炉炉渣性能影响的计算分析","volume":"34","year":"1999"},{"abstractinfo":"采用数学模型预测高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤与废塑料<span style=\"color:red\">混合</span>燃料在直吹管的燃烧过程，数学模型包括气相流动、<span style=\"color:red\">混合</span>燃料的燃烧、辐射传热等子模型。模拟结果表明，燃料总的燃烧效率能达到90%以上，高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤与废塑料<span style=\"color:red\">混合</span>燃料在高炉的燃烧行为介于高炉单独<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤粉和废塑料两者之间，高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤与废塑料<span style=\"color:red\">混合</span>燃料在理论上是切实可行的。","authors":[{"authorName":"吴复忠，金会心，李军旗","id":"07f3a272-d990-4067-9674-61d1d33cfcff","originalAuthorName":"吴复忠，金会心，李军旗"}],"categoryName":"|","doi":"","fpage":"11","id":"9e2e8c95-6518-434f-8aeb-aa7669dc7880","issue":"3","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":"a644b631-6e59-4d3e-a64d-4d5533dfa38e","keyword":"高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span> ","originalKeyword":"高炉喷吹 "},{"id":"8d13b189-fa24-4107-86f4-ddd0b4d2b497","keyword":" blends fuel ","originalKeyword":" blends fuel "},{"id":"b854058d-fdc2-426b-8ed4-d126f6886904","keyword":" numerical simulation","originalKeyword":" numerical simulation"}],"language":"zh","publisherId":"1001-0963_2011_3_4","title":"高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤和废塑料<span style=\"color:red\">混合</span>燃料燃烧过程的数值模拟","volume":"23","year":"2011"},{"abstractinfo":"采用数学模型预测高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤与废塑料<span style=\"color:red\">混合</span>燃料在直吹管的燃烧过程,数学模型包括气相流动、<span style=\"color:red\">混合</span>燃料的燃烧、辐射传热等子模型.模拟结果表明,燃料总的燃烧效率能达到90%以上,高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤与废塑料<span style=\"color:red\">混合</span>燃料在高炉的燃烧行为介于高炉单独<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤粉和废塑料两者之间,高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤与废塑料<span style=\"color:red\">混合</span>燃料在理论上是切实可行的.","authors":[{"authorName":"吴复忠","id":"c37d75a1-acba-42dc-868f-50674d013d73","originalAuthorName":"吴复忠"},{"authorName":"金会心","id":"68254af9-50d7-4f99-86b3-34a21bc5cdde","originalAuthorName":"金会心"},{"authorName":"李军旗","id":"0ae6edd2-a399-41d5-a5da-b04a5b2cbfab","originalAuthorName":"李军旗"}],"doi":"","fpage":"11","id":"d532f287-a233-4ee1-be0c-ca57068dca9d","issue":"3","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":"25fe34af-04c6-44c2-80ec-1f1ac5192035","keyword":"高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>","originalKeyword":"高炉喷吹"},{"id":"0d4e7a6b-869e-4473-97a0-92861f1984b2","keyword":"<span style=\"color:red\">混合</span>燃料","originalKeyword":"混合燃料"},{"id":"64814637-6153-4547-8e4f-83a3fe1f0e0b","keyword":"数值模拟","originalKeyword":"数值模拟"}],"language":"zh","publisherId":"gtyjxb201103003","title":"高炉<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤和废塑料<span style=\"color:red\">混合</span>燃料燃烧过程的数值模拟","volume":"23","year":"2011"},{"abstractinfo":"为了研究<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>时煤粉和废塑料对高炉炉腹煤气的影响,通过计算,得到<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>不同比例<span style=\"color:red\">混合</span>的煤粉与废塑料时高炉炉腹煤气量及煤气成分.结果表明:随着<span style=\"color:red\">混合</span>燃料中废塑料比例增加,炉腹煤气量增加,煤气成分也相应改变；当PE(煤粉与聚乙烯)∶PP(聚丙烯)按5∶5<span style=\"color:red\">混合</span>时,炉腹煤气中φ(CO+H2)所占比例为47.96％,而单一<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤粉时φ(∞+H2)所占比例为44.44％.","authors":[{"authorName":"孙向伟","id":"b3979c35-9888-4cf4-99e6-36e8938440ba","originalAuthorName":"孙向伟"},{"authorName":"沈龙龙","id":"500859c2-fbaa-4cce-9822-804e77dd3f47","originalAuthorName":"沈龙龙"},{"authorName":"刘彪","id":"b889c134-9512-4c1c-b894-937ef6ddd25d","originalAuthorName":"刘彪"},{"authorName":"魏亲睿","id":"323c8bed-d5d6-4409-89a7-92463d5ed48d","originalAuthorName":"魏亲睿"},{"authorName":"高斌","id":"5e75d172-4edc-45fd-8524-bcd098205f26","originalAuthorName":"高斌"}],"doi":"","fpage":"15","id":"e0032bd5-88ce-41cc-971f-e265769aff11","issue":"3","journal":{"abbrevTitle":"GTYJ","coverImgSrc":"journal/img/cover/GTYJ.jpg","id":"29","issnPpub":"1001-1447","publisherId":"GTYJ","title":"钢铁研究"},"keywords":[{"id":"b719cd6e-fb0c-49ed-aa82-60adbc9745e8","keyword":"废塑料","originalKeyword":"废塑料"},{"id":"57f58579-93f1-4580-8291-f4108e4d867b","keyword":"煤粉","originalKeyword":"煤粉"},{"id":"c5cac5ae-dcdf-428b-bde9-8cc32406c2a2","keyword":"<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>","originalKeyword":"混合喷吹"},{"id":"c4fbda04-00e1-486f-9b6c-779b7b0e5822","keyword":"炉腹煤气","originalKeyword":"炉腹煤气"}],"language":"zh","publisherId":"gtyj201303005","title":"<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤粉和废塑料对高炉炉腹煤气的影响","volume":"41","year":"2013"},{"abstractinfo":"运用数值模拟方法,对废塑料和煤粉<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>条件下直吹管和风口内的燃烧特性进行了研究.将废塑料与煤粉按不同比例<span style=\"color:red\">混合</span>,在不同粒径分布下<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>时,分析了直吹管和风口内的挥发分析出和燃烧的规律.结果表明,随着<span style=\"color:red\">混合</span>燃料中废塑料比例增加,颗粒粒径减小,<span style=\"color:red\">混合</span>燃料的燃烧性能提高；从<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>单一煤粉到<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤粉与废塑料比为5∶5的<span style=\"color:red\">混合</span>燃料时,直吹管和风口内燃烧率从3.35％提高到36.31％.","authors":[{"authorName":"孙向伟","id":"b45acef6-9566-4b43-8a18-c54772135f1f","originalAuthorName":"孙向伟"},{"authorName":"沈龙龙","id":"eeae2746-a54e-4c35-9707-1e9246ee8b32","originalAuthorName":"沈龙龙"},{"authorName":"刘彪","id":"07f355f1-c10f-495d-80bd-45ce557246dc","originalAuthorName":"刘彪"},{"authorName":"魏亲睿","id":"e3797316-96ef-4ea3-a31b-ec01fc1c5b74","originalAuthorName":"魏亲睿"},{"authorName":"高斌","id":"1cac9996-16e1-4a58-89b9-77e94b3f6b02","originalAuthorName":"高斌"}],"doi":"","fpage":"1","id":"55e760ae-b9cb-4e2b-a180-ef1c8a4a2892","issue":"1","journal":{"abbrevTitle":"GTYJ","coverImgSrc":"journal/img/cover/GTYJ.jpg","id":"29","issnPpub":"1001-1447","publisherId":"GTYJ","title":"钢铁研究"},"keywords":[{"id":"38fd04c3-de30-4c28-8657-88dc795fa76a","keyword":"废塑料","originalKeyword":"废塑料"},{"id":"14e1879f-fb5f-4713-b05f-5db28ef8e936","keyword":"煤粉","originalKeyword":"煤粉"},{"id":"38fb0649-836e-404e-86db-c7090ddba3d6","keyword":"<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>","originalKeyword":"混合喷吹"},{"id":"9908fee2-4daf-45a6-8566-fd84996288d9","keyword":"数值模拟","originalKeyword":"数值模拟"}],"language":"zh","publisherId":"gtyj201301001","title":"在直吹管和风口内<span style=\"color:red\">混合</span><span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>煤粉和废塑料的数值模拟","volume":"41","year":"2013"},{"abstractinfo":"利用数值模拟的方法对几种典型<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>方式的底<span style=\"color:red\">吹</span>钢包内的流动与<span style=\"color:red\">混合</span>过程进行了理论分析结果表明,变化<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>方式,即从中心<span style=\"color:red\">喷</span>吹到偏心<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>、从单喷嘴<span style=\"color:red\">喷</span>吹到双喷嘴<span style=\"color:red\">喷</span><span style=\"color:red\">吹</span>,钢包内的流动<span style=\"color:red\">混合</span>状态得到改善,因而有助于缩短钢包内的均匀<span style=\"color:red\">混合</span>时间","authors":[{"authorName":"李宝宽","id":"77389e1b-508f-4fcf-99bc-1e17b11a24f0","originalAuthorName":"李宝宽"},{"authorName":"赫冀成","id":"300adbf6-5198-48da-b72c-2d6113b62fdd","originalAuthorName":"赫冀成"},{"authorName":"陆钟武","id":"db5eee25-821d-4937-9956-f14fd9f42037","originalAuthorName":"陆钟武"}],"categoryName":"|","doi":"","fpage":"47","id":"2254f080-0815-4558-87da-babd123cb437","issue":"4","journal":{"abbrevTitle":"JSXB","coverImgSrc":"journal/img/cover/JSXB.jpg","id":"48","issnPpub":"0412-1961","publisherId":"JSXB","title":"金属学报"},"keywords":[{"id":"c0742e8c-4816-4efa-a3af-fc450a8ec77a","keyword":"底<span style=\"color:red\">吹</span>钢包","originalKeyword":"底吹钢包"},{"id":"6b5f8b2a-90c7-4a65-abbe-6b995443ab31","keyword":"numerical simulation","originalKeyword":"numerical simulation"},{"id":"055de414-d969-4ff5-acff-58f616974c68","keyword":"flow","originalKeyword":"flow"}],"language":"zh","publisherId":"0412-1961_1993_4_4","title":"底<span style=\"color:red\">吹</span>钢包内流动与<span style=\"color:red\">混合</span>的数值模拟","volume":"29","year":"1993"}],"totalpage":1412,"totalrecord":14112}