{"currentpage":1,"firstResult":0,"maxresult":10,"pagecode":5,"pageindex":{"endPagecode":5,"startPagecode":1},"records":[{"abstractinfo":"通过正交试验考察了水性环氧丙烯酸酯、水性聚氨酯丙烯酸酯和水性活性稀释剂的不同用量对光固化涂层性能的影响。结果表明：水性环氧丙烯酸酯与水性聚氨酯丙烯酸酯配比为3∶7，水性活性稀释剂用量为12%时，涂层的力学性能优异，涂层凝胶率超过90%，吸水率为2.36%，击穿强度达到100 MV/m。","authors":[{"authorName":"杜峰","id":"f87af056-9363-4274-b85d-ff48d8d618b9","originalAuthorName":"杜峰"},{"authorName":"鲁钢","id":"63cb3d95-bd0c-4fce-8dae-637e21c81471","originalAuthorName":"鲁钢"},{"authorName":"邹巍巍","id":"91fc92a1-1cc0-4ddc-a68c-2193a6522b8f","originalAuthorName":"邹巍巍"},{"authorName":"<span style=\"color:red\">章</span><span style=\"color:red\">文</span><span style=\"color:red\">贵</span>","id":"0c72efed-75e6-443b-b9a7-bd8ceca1f8a4","originalAuthorName":"章文贵"}],"doi":"","fpage":"64","id":"6ba23003-771b-4412-8a78-e9d3f39cb5ec","issue":"2","journal":{"abbrevTitle":"JYCL","coverImgSrc":"journal/img/cover/JYCL.jpg","id":"50","issnPpub":"1009-9239","publisherId":"JYCL","title":"绝缘材料"},"keywords":[{"id":"b2407f59-65c0-42a7-a2e6-10aaf3a408d3","keyword":"水性","originalKeyword":"水性"},{"id":"339c0644-c96b-40f5-a890-a829863eff81","keyword":"光固化","originalKeyword":"光固化"},{"id":"43f8ca1d-ac07-4269-b5b1-a7a3acd7bff0","keyword":"涂料","originalKeyword":"涂料"}],"language":"zh","publisherId":"jycltx201402015","title":"水性光固化涂料涂层性能评价","volume":"","year":"2014"},{"abstractinfo":"从理论上分析了采用真空蒸馏法分离<span style=\"color:red\">贵</span>铅中铅、银、铜、铋、锑的可行性，研究了蒸馏时间、蒸馏温度对<span style=\"color:red\">贵</span>铅中金属分离效果的影响规律。实验结果表明，当系统压力在10~20 Pa，温度在800℃以上，保温时间≥2 h时，铅和铋的挥发率接近100%，银和锑的挥发率随温度的升高、保温时间的增长而逐渐增大。当温度为850℃，保温时间为2 h时，所得残留物中铅、银、铜、铋、锑的含量分别为0.21%、45.31%、13.24%、0.0001%、33.6%，挥发物中铅、银、铜、铋、锑的含量分别为46.15%、0.236%、0.022%、8.87%、35.4%。","authors":[{"authorName":"包崇军","id":"892754f3-82fd-4d26-8b2a-7a985d5be010","originalAuthorName":"包崇军"},{"authorName":"蒋<span style=\"color:red\">文</span>龙","id":"ee09dad7-109d-407f-ad7c-5cc4de1efe34","originalAuthorName":"蒋文龙"},{"authorName":"李晓阳","id":"b6dfdb2f-f43d-42f2-b146-94ad2c089d63","originalAuthorName":"李晓阳"},{"authorName":"吴红林","id":"3dd5453d-7baa-4ee2-b02f-1c00703c8d91","originalAuthorName":"吴红林"},{"authorName":"邹利明","id":"14252ee7-e2ee-4b12-bd47-b0bb974eabe3","originalAuthorName":"邹利明"},{"authorName":"罗凌艳","id":"d4dadb7b-ba4a-4489-afbd-dfdf5ada3e4b","originalAuthorName":"罗凌艳"},{"authorName":"柯浪","id":"1ed7aced-dded-4cd8-9b24-2ef93472f036","originalAuthorName":"柯浪"},{"authorName":"许娜","id":"2ecfc2ad-da25-4c8f-ab3e-bea9cea9b8fa","originalAuthorName":"许娜"},{"authorName":"田林","id":"7dd6811d-a25d-4985-9dcc-e24c9eab878f","originalAuthorName":"田林"}],"doi":"","fpage":"31","id":"8d276d92-5362-4625-b264-5da4f70330d8","issue":"z1","journal":{"abbrevTitle":"GJS","coverImgSrc":"journal/img/cover/GJS.jpg","id":"38","issnPpub":"1004-0676","publisherId":"GJS","title":"贵金属"},"keywords":[{"id":"b67ae8fb-8a6e-499c-b899-bb81257fef54","keyword":"有色金属冶金","originalKeyword":"有色金属冶金"},{"id":"37726ddb-e999-45ef-a001-03fcbb31aedb","keyword":"真空蒸馏法","originalKeyword":"真空蒸馏法"},{"id":"f68cb13c-d6df-45ec-bb8f-cc9af58293cd","keyword":"<span style=\"color:red\">贵</span>铅","originalKeyword":"贵铅"},{"id":"3bf693ce-1bb1-4d15-a3c2-4c3b39b2b500","keyword":"金属分离","originalKeyword":"金属分离"}],"language":"zh","publisherId":"gjs2014z1008","title":"真空蒸馏法处理<span style=\"color:red\">贵</span>铅新工艺研究","volume":"","year":"2014"},{"abstractinfo":"目前,氰化浸金仍是从矿石中提取金最主要方法.从氰化浸出<span style=\"color:red\">贵</span>液(矿浆)中回收金在工业生产中应用的方法主要有锌粉置换法、活性炭吸附法、离子交换树脂吸附法、电沉积法等,而溶剂萃取法、液膜法等尚在试验研究中.文中叙述了从氰化<span style=\"color:red\">贵</span>液中(矿浆)回收金的各种方法的发展、机理、优缺点及行业应用和研究现状,并对回收方法的选择进行了分析讨论.","authors":[{"authorName":"陈淑萍","id":"f0bab11d-6da1-4cf4-a1a8-da8181289e57","originalAuthorName":"陈淑萍"}],"doi":"10.3969/j.issn.1001-1277.2012.02.011","fpage":"43","id":"af133372-dfec-47b8-a2b8-cd4d14b0a30a","issue":"2","journal":{"abbrevTitle":"HJ","coverImgSrc":"journal/img/cover/HJ.jpg","id":"44","issnPpub":"1001-1277","publisherId":"HJ","title":"黄金"},"keywords":[{"id":"d66a50a9-e205-437e-a61e-f77a1a393fb6","keyword":"氰化<span style=\"color:red\">贵</span>液","originalKeyword":"氰化贵液"},{"id":"8bc659fc-aef0-4545-a37b-edf158513fa8","keyword":"锌粉置换","originalKeyword":"锌粉置换"},{"id":"13b51b0b-0f28-4b3a-b457-22f155cb8e0c","keyword":"吸附","originalKeyword":"吸附"},{"id":"96ffb9b7-eda7-4432-877d-7d5e97932077","keyword":"回收金","originalKeyword":"回收金"}],"language":"zh","publisherId":"huangj201202011","title":"从氰化<span style=\"color:red\">贵</span>液(矿浆)中回收金技术进展","volume":"33","year":"2012"},{"abstractinfo":"提出了一个实用而简便的测定<span style=\"color:red\">贵</span>液中金和钯的方法.在瓷坩埚中蒸干<span style=\"color:red\">贵</span>液,残渣与混合试剂熔炼,灰吹,贵金属合粒用酸溶解,原子吸收法测定金和钯.该方法准确,适用范围广.","authors":[{"authorName":"林海山","id":"018ae545-a511-4550-80be-4839cc21187a","originalAuthorName":"林海山"}],"doi":"10.3969/j.issn.1001-1277.2002.05.014","fpage":"44","id":"acfc0866-2e86-44d3-80c5-6c8b2f050987","issue":"5","journal":{"abbrevTitle":"HJ","coverImgSrc":"journal/img/cover/HJ.jpg","id":"44","issnPpub":"1001-1277","publisherId":"HJ","title":"黄金"},"keywords":[{"id":"84a060b4-6883-4de1-a3cc-e03de16d5175","keyword":"简易试金","originalKeyword":"简易试金"},{"id":"9d57c679-96fe-4c8e-b676-6fe541de8136","keyword":"<span style=\"color:red\">贵</span>液","originalKeyword":"贵液"},{"id":"5ff6e6db-3dfd-4d22-b3d9-032c8cbf54a6","keyword":"金","originalKeyword":"金"},{"id":"5ac2cb9d-e763-4695-90c1-c27d3bbf9519","keyword":"钯","originalKeyword":"钯"}],"language":"zh","publisherId":"huangj200205014","title":"简易试金法测定<span style=\"color:red\">贵</span>液中的金和钯","volume":"23","year":"2002"},{"abstractinfo":"高铅金银矿粉氰化过程产生的高铅<span style=\"color:red\">贵</span>液，进一步采用锌粉置换时其中溶解的铅易被置换出来，从而使银泥品位大幅下降，且会对后续的冶炼作业带来困难。为解决<span style=\"color:red\">贵</span>液中高含量铅造成的影响，进行了降铅试验研究。其结果表明：通过控制浸出工艺碱度，<span style=\"color:red\">贵</span>液二次置换、Na2 CO3预先除铅，均可有效解决<span style=\"color:red\">贵</span>液中铅含量过高而对生产造成的影响。","authors":[{"authorName":"王<span style=\"color:red\">文</span>强","id":"2814c8ae-d491-48e5-bf2f-6160fb4a13a2","originalAuthorName":"王文强"},{"authorName":"王金超","id":"4a899c1d-e13f-437f-9aee-e4b5919b2634","originalAuthorName":"王金超"},{"authorName":"姜传进","id":"3755613f-e2e3-4fa6-9702-4d20fc1f5111","originalAuthorName":"姜传进"}],"doi":"10.11792/hj20160314","fpage":"64","id":"20d7db5b-6494-48b4-a5aa-3e0cc1d8e30c","issue":"3","journal":{"abbrevTitle":"HJ","coverImgSrc":"journal/img/cover/HJ.jpg","id":"44","issnPpub":"1001-1277","publisherId":"HJ","title":"黄金"},"keywords":[{"id":"7b55b97b-e6ad-49a6-af9c-1e3abd23dc53","keyword":"高铅<span style=\"color:red\">贵</span>液","originalKeyword":"高铅贵液"},{"id":"962d0e7a-6972-42aa-85fb-3178fcc59e02","keyword":"Na2 CO3除铅","originalKeyword":"Na2 CO3除铅"},{"id":"4f622fb3-e982-4bf2-9243-9bf42cb74f6c","keyword":"锌粉置换","originalKeyword":"锌粉置换"},{"id":"983efbd2-48a4-4dec-a81f-c9067f85d50d","keyword":"氰化","originalKeyword":"氰化"}],"language":"zh","publisherId":"huangj201603015","title":"金银氰化浸出中高铅<span style=\"color:red\">贵</span>液的产生原因及处理方法","volume":"37","year":"2016"},{"abstractinfo":"用电极过程动力学对从氰化<span style=\"color:red\">贵</span>液中直接电沉积金过程进行分析,可得出提高Au(CN)-2离子与阴极碰撞几率和减小析H2副反应是提高电沉积金效率的关键因素.采用多孔电极、析出H2小的电极材料和分两段电解措施,使从低浓度含金贵液中直接电沉积金的效率达到98%以上.","authors":[{"authorName":"张建武","id":"0ec1ec43-c401-4702-9d5d-af0840ccffa1","originalAuthorName":"张建武"},{"authorName":"张桂珍","id":"30afc453-8964-403c-ad9a-73d8a5940334","originalAuthorName":"张桂珍"},{"authorName":"吴仙花","id":"2082eeb5-479c-4b71-a10d-e2db3c715cb1","originalAuthorName":"吴仙花"},{"authorName":"盛桂云","id":"2bcfabcc-e002-4f0c-a3a1-63bbf1ef2db2","originalAuthorName":"盛桂云"}],"doi":"10.3969/j.issn.1001-1277.2006.10.010","fpage":"36","id":"e2572222-89a6-4f27-95d8-c8d6326b4cd1","issue":"10","journal":{"abbrevTitle":"HJ","coverImgSrc":"journal/img/cover/HJ.jpg","id":"44","issnPpub":"1001-1277","publisherId":"HJ","title":"黄金"},"keywords":[{"id":"18a81aec-d228-4001-9514-2c64403cdd1e","keyword":"直接电沉积金","originalKeyword":"直接电沉积金"},{"id":"5c7ac6f8-4531-4146-bbc2-111704f9b628","keyword":"碰撞几率","originalKeyword":"碰撞几率"},{"id":"657714fb-50fe-4c90-a004-b6ceb4354155","keyword":"析H2副反应","originalKeyword":"析H2副反应"},{"id":"79e4adf2-1985-409a-88c6-6f662fefce95","keyword":"稀<span style=\"color:red\">贵</span>液","originalKeyword":"稀贵液"}],"language":"zh","publisherId":"huangj200610010","title":"从稀<span style=\"color:red\">贵</span>液中直接电沉积金的研究","volume":"27","year":"2006"},{"abstractinfo":"研究了大洋多金属锰结核酸浸<span style=\"color:red\">贵</span>液中铁锰元素与铜、钴、镍有价金属的分离.根据溶液所含金属的特点,选用可以回收利用的MnO2作为Fe2+的氧化剂先将Fe2+氧化为Fe3+;采用黄铵铁矾法与Fe(OH)3相结合的二步法除铁工艺,并对溶液pH、反应温度、反应时间等操作参数进行优化,铁的沉淀率达到99.8%,净化后溶液中含铁量低于0.01 g/L,钴、铜、镍、锰的回收率分别达到99.5%、93.3%、99.6%、99.3%;硫化沉淀分离锰和铜、钴、镍过程中,硫化钠适宜用量为理论用量的4.5倍,适宜pH值4.5,适宜温度80℃,沉淀时间1 h,铜、钴、镍的沉淀率在99%左右,而锰的沉淀率仅为0.46%.","authors":[{"authorName":"孙春宝","id":"d1a44b57-ff7c-4df2-bdf9-abde7c42a488","originalAuthorName":"孙春宝"},{"authorName":"吕继有","id":"0b20399e-b239-46d1-b7f9-e91665550564","originalAuthorName":"吕继有"},{"authorName":"李浩然","id":"634531c5-b27d-418b-b2e8-0cf136e2b81c","originalAuthorName":"李浩然"}],"doi":"","fpage":"542","id":"90ecc86b-77b1-4ccb-9639-951ccffa0ada","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":"5bb1fc6a-aba5-4eb9-bebf-21545f0b1525","keyword":"大洋多金属结核","originalKeyword":"大洋多金属结核"},{"id":"a28ecdff-7ebe-4309-9c3b-b853ae8c0a94","keyword":"溶液净化","originalKeyword":"溶液净化"},{"id":"89828b07-7463-4c49-a348-ef0accd77f99","keyword":"沉淀法","originalKeyword":"沉淀法"}],"language":"zh","publisherId":"zgysjsxb200603027","title":"大洋多金属锰结核酸浸<span style=\"color:red\">贵</span>液中铁锰元素的脱除","volume":"16","year":"2006"},{"abstractinfo":"从含高铜、铅、锌<span style=\"color:red\">贵</span>液中直接用锌粉置换回收金,效果差.通过在锌粉置换作业中控制Pb(AC)2适宜用量,解决了铅、锌在流程溶液体系中积累、金置换率低及影响氰化浸出问题,保证了锌粉置换作业技术指标.","authors":[{"authorName":"卢辉畴","id":"4fff4ddf-528e-4abf-b674-43c2cf3285e5","originalAuthorName":"卢辉畴"}],"doi":"10.3969/j.issn.1001-1277.2004.04.012","fpage":"36","id":"7491ee59-964c-4460-a386-c221acff1797","issue":"4","journal":{"abbrevTitle":"HJ","coverImgSrc":"journal/img/cover/HJ.jpg","id":"44","issnPpub":"1001-1277","publisherId":"HJ","title":"黄金"},"keywords":[{"id":"7096c6be-8ded-4bd6-a95f-d6cd24191de7","keyword":"锌粉置换","originalKeyword":"锌粉置换"},{"id":"47703d7a-d084-4548-8947-af05a4a2b964","keyword":"Pb(AC)2","originalKeyword":"Pb(AC)2"},{"id":"d2818b0f-8b0e-4f0e-859f-f2bd9488dcd0","keyword":"积累","originalKeyword":"积累"},{"id":"f054feac-7d5a-4c7b-aa25-6f022bc89283","keyword":"置换率","originalKeyword":"置换率"}],"language":"zh","publisherId":"huangj200404012","title":"锌粉置换法从含高铜、铅、锌<span style=\"color:red\">贵</span>液中回收金的研究及生产实践","volume":"25","year":"2004"},{"abstractinfo":"采用XRD、XPS和EPMA对中原油田<span style=\"color:red\">文</span>23-1、23-8气井油管腐蚀产物和管材进行分析,并试验了碳钢在CO_2介质中的腐蚀。研究结果表明,天然气中的CO_2及凝析水是气井腐蚀的主要原因。管材的非金属夹杂物(MnS、Al_2O_3)含量超标,是加速油管在CO_2环境中局部腐蚀穿孔破坏的另一原因。还探索了应用缓蚀剂防止气井CO_2腐蚀的可能性。","authors":[{"authorName":"郑家燊","id":"4aa259a3-9890-4b94-9b92-98f14b4e4f42","originalAuthorName":"郑家燊"},{"authorName":"傅朝阳","id":"a1cacedc-6258-4398-b16d-88cd84d16bb2","originalAuthorName":"傅朝阳"},{"authorName":"刘小武","id":"bf9d6195-ac31-4120-af98-9fe37c032278","originalAuthorName":"刘小武"},{"authorName":"彭芳明","id":"b12594db-16cd-4fed-acee-6a3b80c2e3e0","originalAuthorName":"彭芳明"},{"authorName":"黄先球","id":"81f57758-cf1b-4278-85f5-8487745c85f5","originalAuthorName":"黄先球"},{"authorName":"赵景茂","id":"2585fd88-4683-4422-a42d-a7e16622f802","originalAuthorName":"赵景茂"},{"authorName":"吴灿奇","id":"f5df895d-4271-4238-9ffd-b90f59bcfea3","originalAuthorName":"吴灿奇"},{"authorName":"徐卫东","id":"d818fdc7-f940-4272-876f-da920464a5be","originalAuthorName":"徐卫东"},{"authorName":"王选奎","id":"0e7fcc50-e2ce-4b16-b99e-966d1599adb8","originalAuthorName":"王选奎"}],"categoryName":"|","doi":"","fpage":"227","id":"0d85a2b4-88c6-4d26-9da8-44ae165c2bb0","issue":"3","journal":{"abbrevTitle":"ZGFSYFHXB","coverImgSrc":"journal/img/cover/中国腐蚀封面19-3期-01.jpg","id":"81","issnPpub":"1005-4537","publisherId":"ZGFSYFHXB","title":"中国腐蚀与防护学报"},"keywords":[{"id":"e9abd684-3d59-4d32-afed-0dc9a6ebb526","keyword":"气井","originalKeyword":"气井"},{"id":"419b9942-a4fd-4ee8-a6d7-8dc4eefbc226","keyword":" Oil pipe corrosion","originalKeyword":" Oil pipe corrosion"},{"id":"feeaf218-889a-414d-b05a-0280637a071b","keyword":" Failure analysis","originalKeyword":" Failure analysis"},{"id":"fa46cf1b-a087-49db-976c-f2d91ed2912a","keyword":" Inhibitor","originalKeyword":" Inhibitor"}],"language":"zh","publisherId":"1005-4537_1998_3_5","title":"中原油田<span style=\"color:red\">文</span>23气田气井腐蚀原因分析","volume":"18","year":"1998"},{"abstractinfo":"以<span style=\"color:red\">文</span>拉法辛为原料,分别以新的脱甲基试剂半胱氨酸钠盐和青霉胺钠盐制备了O-去甲基<span style=\"color:red\">文</span>拉法辛,收率为86％和82％.一锅中分别完成了半胱氨酸钠盐、青霉胺钠盐的制备与<span style=\"color:red\">文</span>拉法辛脱甲基反应,简化了操作步骤.最优反应条件为溶剂N-甲基吡咯烷酮,反应温度175℃,产物析晶pH值9.5.","authors":[{"authorName":"史兰香","id":"7597e205-02a8-4085-8343-0c2ab51f36d3","originalAuthorName":"史兰香"},{"authorName":"张宝华","id":"7ba9bf25-7bfc-4318-8efb-de8c0b997697","originalAuthorName":"张宝华"}],"doi":"10.3724/SP.J.1095.2013.20351","fpage":"608","id":"1c34983e-fdfa-4f09-8d73-f19f35b652d1","issue":"5","journal":{"abbrevTitle":"YYHX","coverImgSrc":"journal/img/cover/YYHX.jpg","id":"73","issnPpub":"1000-0518","publisherId":"YYHX","title":"应用化学"},"keywords":[{"id":"e00801ae-0af6-4f60-8558-f9affd1bf34b","keyword":"O-去甲基<span style=\"color:red\">文</span>拉法辛","originalKeyword":"O-去甲基文拉法辛"},{"id":"8ca7db3f-40ec-418b-8cdf-abfa3eb3f31f","keyword":"<span style=\"color:red\">文</span>拉法辛","originalKeyword":"文拉法辛"},{"id":"68c5308b-5920-423a-8b00-745e3794cf01","keyword":"脱甲基化","originalKeyword":"脱甲基化"},{"id":"9a3870aa-9adf-42e1-ba5c-d1ec47baacb2","keyword":"半胱氨酸钠盐","originalKeyword":"半胱氨酸钠盐"},{"id":"cc5917c0-e45e-49e1-ba0f-753dc1f71b26","keyword":"青霉胺钠盐","originalKeyword":"青霉胺钠盐"}],"language":"zh","publisherId":"yyhx201305020","title":"O-去甲基<span style=\"color:red\">文</span>拉法辛合成的新方法","volume":"30","year":"2013"}],"totalpage":21,"totalrecord":201}