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KR 进行100%全量铁水脱硫预处理,从生产布局上可以同时满足脱磷炉和脱碳炉的生产需要。为了实现 KR 的高效脱硫,对影响脱硫的因素进行了分析和讨论,认为脱硫剂中添加一定量的 CaF2可生成一定量的共熔晶体,提高了铁水中硫元素的传输和反应速率;铁水中加入一定量的铝渣可以降低铁水中的氧活度,提高脱硫反应速度;铁水温度应控制在1300~1380℃之间,温度太高会在石灰颗粒表面形成较多的液相,造成石灰颗粒聚团,减少铁水与脱硫剂的接触面积,降低了反应速率;良好的石灰质量和搅拌头形状也有利于 KR 脱硫。通过以上措施,铁水经过 KR 脱硫预处理后 w[S]≤0.002%比例达到98%以上,转炉终点平均硫质量分数为0.005%。","authors":[{"authorName":"赵长亮","id":"3c0676f9-68e9-4482-88c9-b3d4d51f384a","originalAuthorName":"赵长亮"},{"authorName":"田志红","id":"5572b7ad-fb30-4f21-8c70-b7b25afe159d","originalAuthorName":"田志红"},{"authorName":"陈虎","id":"d3cfc2d0-9226-421e-a3a7-fe6afccfb862","originalAuthorName":"陈虎"},{"authorName":"王飞","id":"fb7efba7-c142-4968-bd37-375e690d5449","originalAuthorName":"王飞"},{"authorName":"彭国仲","id":"9d1fa4e5-7d8a-4aac-a8b3-6e6c3f7ddb79","originalAuthorName":"彭国仲"}],"doi":"10.13228/j.boyuan.issn1006-9356.20140172","fpage":"60","id":"28a275b1-97cf-4fef-91a0-4d3d33a61a08","issue":"4","journal":{"abbrevTitle":"ZGYJ","coverImgSrc":"journal/img/cover/ZGYJ.jpg","id":"87","issnPpub":"1006-9356","publisherId":"ZGYJ","title":"中国冶金"},"keywords":[{"id":"8b1b1447-467e-4230-84ab-ee361cb2de86","keyword":"KR","originalKeyword":"KR"},{"id"{"currentpage":1,"firstResult":0,"maxresult":10,"pagecode":5,"pageindex":{"endPagecode":5,"startPagecode":1},"records":[{"abstractinfo":"为提高疏水疏水性能,使其可在蒸馏、吸收等领域有更广泛的应用.采用溶液相转移法制备超疏水性聚偏氟乙烯(PVDF)分离,考察了铸液中PVDE和非溶剂(低分子二醇类化合物PG)的浓度对润湿性能的影响.结果表明,通过改变铸液中PVDF、PG的浓度,能使PVDF的表面静态接触角从75.1°提高到161.7°,滚动角仅为15.8°.还研究了PVDF复合的制备条件对润湿性能的影响,结果表明,在一定的非溶剂浓度范围,增加复合涂覆液中非溶剂PG的加入量,有利于得到较高的复合表面接触角,但丝在涂覆液中的浸泡时间也需要相应延长.当非溶剂PG的质量分数为39.1%、浸泡时间为50 s时,复合表面接触角达到了155°.","authors":[{"authorName":"林汉阳","id":"c4fa1f73-8a69-43be-bf7b-8ab01dd7d73f","originalAuthorName":"林汉阳"},{"authorName":"武春瑞","id":"8a6322d7-33bd-4582-98eb-a002c81e4b16","originalAuthorName":"武春瑞"},{"authorName":"吕晓龙","id":"4ed5bacb-e94a-4006-8d64-1b6da92d2d9b","originalAuthorName":"吕晓龙"}],"doi":"10.3969/j.issn.1007-8924.2010.02.008","fpage":"39","id":"afb586b8-64ad-4ed8-919f-ffb62b813ace","issue":"2","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术 "},"keywords":[{"id":"89496cef-1ff0-4eb8-9cc2-1d682081be29","keyword":"聚偏氟乙烯","originalKeyword":"聚偏氟乙烯"},{"id":"d1a684cf-7b92-49d8-a4c5-30a531a3cbd8","keyword":"疏水","originalKeyword":"疏水膜"},{"id":"2b941c41-6795-49eb-acf3-f1bf6e12ca1f","keyword":"超疏水化","originalKeyword":"超疏水化"},{"id":"74d9669f-bf67-42d1-9390-d4d82dd601c1","keyword":"接触角","originalKeyword":"接触角"},{"id":"dd926d1b-e89e-4263-a362-0e4eb8409176","keyword":"表面改性","originalKeyword":"表面改性"}],"language":"zh","publisherId":"mkxyjs201002008","title":"聚偏氟乙烯的超疏水改性研究","volume":"30","year":"2010"},{"abstractinfo":"采用稀溶液相转化法制备出小粒径的聚偏氟乙烯(PVDF)粒子,然后通过超滤方法将其涂覆在PVDF基膜表面上,得到了高疏水性表面的PVDF疏水.初步考察了凝固浴组成和凝固浴温度等稀溶液相分离条件对PVDF粒子的形成以及疏水性能的影响.结果表明,通过稀溶液相转化方法可以在基膜表面构建微纳米结构,凝固浴组成对改性疏水的表面微纳米结构影响很大,以质量分数为60% DMAc水溶液为凝固浴条件下得到的疏水接触角最高,达到144.9°,较基膜的接触角80°显著提高;凝固浴组成对疏水的透气系数和透水压力也有影响,透水压力由0.24 MPa提升至0.28 MPa;凝固浴组成对改性后疏水的孔径没有明显影响;随着凝固浴温度的升高,接触角呈增大趋势.","authors":[{"authorName":"张如意","id":"a2bb53a8-bc4f-4221-a7fc-86dd135f56ab","originalAuthorName":"张如意"},{"authorName":"吕晓龙","id":"ee621895-3dc5-4a9d-b6ee-5e73cf8dd5ab","originalAuthorName":"吕晓龙"},{"authorName":"汪洋","id":"37eebed9-2f8b-4208-928d-e5d45a14dde2","originalAuthorName":"汪洋"},{"authorName":"武春瑞","id":"0a3d1b82-2ff6-48c5-9cd8-94c6ee0ca9bc","originalAuthorName":"武春瑞"},{"authorName":"陈华艳","id":"b6d15fc9-5d3b-40ec-8dae-4d213369b666","originalAuthorName":"陈华艳"},{"authorName":"贾悦","id":"d43c5923-fdb4-43f8-a4d8-0b04f393ac23","originalAuthorName":"贾悦"},{"authorName":"王暄","id":"93051ad2-8586-4b87-81e7-863a7725b774","originalAuthorName":"王暄"},{"authorName":"高启君","id":"8634869d-058d-45c0-815a-aba95d45a7f5","originalAuthorName":"高启君"}],"doi":"10.16159/j.cnki.issn1007-8924.2015.05.003","fpage":"13","id":"7d82daf7-40b5-46f3-9847-7b29f8d14fc4","issue":"5","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术 "},"keywords":[{"id":"2d894e7d-89f8-448a-945b-23824a8e6531","keyword":"聚偏氟乙烯","originalKeyword":"聚偏氟乙烯"},{"id":"de432c6a-0021-4de5-9f79-7264ddc4fb27","keyword":"相转化","originalKeyword":"相转化"},{"id":"0c240c5f-153b-45a4-8155-a3bba89ab358","keyword":"疏水改性","originalKeyword":"疏水改性"},{"id":"eb9fc7d7-0a01-48a2-8fa1-40925a23bf7f","keyword":"接触角","originalKeyword":"接触角"},{"id":"3bde3eb9-db4d-4534-97de-209b9cfda365","keyword":"疏水","originalKeyword":"疏水膜"}],"language":"zh","publisherId":"mkxyjs201505003","title":"高疏水表面的聚偏氟乙烯中空纤维制备方法研究","volume":"35","year":"2015"},{"abstractinfo":"利用目前国内生产的PTFE疏水,以自来水、盐水溶液作工质进行了多层并接气隙式蒸馏实验,比较了几种的分离性能,研究了料液温度、料液流量、浓度对渗透通量的影响,各种的通量稳定性及污染情况.实验结果表明:4#在长期自来水、盐水实验中通量、电导率都较稳定,特别是在后期实验中,通量最大;而孔径大、涂层薄的1#在前期实验中通量较大,而随运行时间增长,通量有所下降,特别是盐水实验中,截留率低,电导率高,因此不适合淡化苦咸水用,综合来看4#性能较好.实验后各种表面的污染情况较严重,都有黄色沉积物.","authors":[{"authorName":"吕海莉","id":"e9a761f3-2717-450e-adfa-bfccbb6723fb","originalAuthorName":"吕海莉"},{"authorName":"田瑞","id":"1a16b495-c89f-468e-9845-abe798ee2ec4","originalAuthorName":"田瑞"},{"authorName":"杨晓宏","id":"0a7fc757-4f6d-48dd-bf0f-664c331be07b","originalAuthorName":"杨晓宏"},{"authorName":"马淑娟","id":"8d885e6e-c037-476e-8e60-6fd13b608f21","originalAuthorName":"马淑娟"}],"doi":"10.3969/j.issn.1007-8924.2012.01.013","fpage":"70","id":"624f6f9c-c085-4152-ad84-92c2ab274d73","issue":"1","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术 "},"keywords":[{"id":"48a48ee3-2abf-40c1-b223-fc60f6855103","keyword":"疏水","originalKeyword":"疏水膜"},{"id":"724ffb27-3dd9-4e42-b8ea-f0682f851fc1","keyword":"通量","originalKeyword":"膜通量"},{"id":"0ea7c6ed-ca3c-4d5d-9119-c2297018964b","keyword":"组件","originalKeyword":"膜组件"},{"id":"7ad7b81b-d399-4afb-a741-ec204e0489fa","keyword":"污染","originalKeyword":"膜污染"}],"language":"zh","publisherId":"mkxyjs201201013","title":"用于蒸馏苦咸水淡化的PTFE疏水实验研究","volume":"32","year":"2012"},{"abstractinfo":"利用高孔隙率的聚偏氟乙烯(PVDF)中空纤维疏水进行真空蒸馏(VMD)脱盐实验.在真空度0.095MPa,盐水温度60℃,流速1.5kg/min的条件下,着重研究了中空纤维内径、壁厚,组件长度、装填纤维数目等结构参数对VMD性能的影响.结果表明:组件长度或装填纤维数目增加,组件产水通量明显降低而总产水通量明显提高;中空纤维内径对VMD产水通量影响较小,而壁厚增加使通量明显降低;用内径1.0mm壁厚0.1mm的制成的长度21cm装填纤维50根的组件,产水通量达到21.8kg/(m2·h).VMD过程产水的电导率保持在4μS/cm以内,脱盐率达99.99%,受、组件结构及操作条件影响很小.","authors":[{"authorName":"武春瑞","id":"56670020-047e-4383-bffd-3c97a44749cb","originalAuthorName":"武春瑞"},{"authorName":"吴刚","id":"dc75238a-ddbc-47c0-970c-7a3f93048e77","originalAuthorName":"吴刚"},{"authorName":"陈华艳","id":"075af9e3-6291-45f4-9db0-50b63ff13927","originalAuthorName":"陈华艳"},{"authorName":"贾悦","id":"d7ffede0-da29-4f4c-a53b-d4b1dc49f503","originalAuthorName":"贾悦"},{"authorName":"王暄","id":"71a9bd3c-1013-4f97-b1b6-31d136f934e4","originalAuthorName":"王暄"},{"authorName":"吕晓龙","id":"b6f32b45-badb-449b-8854-0f4190f8219e","originalAuthorName":"吕晓龙"}],"doi":"","fpage":"922","id":"8a7c9578-01ee-4ae1-8d4a-6d6768c9b313","issue":"6","journal":{"abbrevTitle":"GNCL","coverImgSrc":"journal/img/cover/GNCL.jpg","id":"33","issnPpub":"1001-9731","publisherId":"GNCL","title":"功能材料"},"keywords":[{"id":"6dac889b-1287-4c9e-a037-45e4df58e825","keyword":"真空蒸馏(VMD)","originalKeyword":"真空膜蒸馏(VMD)"},{"id":"9f272b8e-4c9c-4fb7-b917-889c58f20312","keyword":"聚偏氟乙烯(PVDF)","originalKeyword":"聚偏氟乙烯(PVDF)"},{"id":"e8899d34-3e38-4885-b6ea-3141dd6b097b","keyword":"中空纤维","originalKeyword":"中空纤维膜"},{"id":"f3b2088f-640e-4de2-b60e-105a5f5244ae","keyword":"疏水","originalKeyword":"疏水膜"},{"id":"64fc61f0-e904-45bb-97a8-4d86d2c98fc7","keyword":"组件","originalKeyword":"膜组件"}],"language":"zh","publisherId":"gncl200806014","title":"PVDF疏水中空纤维与组件对真空蒸馏性能的影响","volume":"39","year":"2008"},{"abstractinfo":"利用新型高通量聚偏氟乙烯(PVDF)中空纤维疏水,对石化企业废水经反渗透(RO)处理的浓排水进行减压蒸馏(VMD)处理实验.研究了RO浓排水流速、温度和冷侧真空度对VMD过程中PVDF性能的影响,考察了PVDF在VMD法RO浓水浓缩过程中的性能变化.结果表明,原液流速对性能无明显影响;原液温度或冷侧真空度提高都会使的产水通量明显上升,而产水电导保持稳定.在冷侧真空度为-0.095MPa、原液温度70℃、流速0.66m/s的条件下,经15.2h实验,将RO浓排水浓缩20倍,的产水通量从25.8L/(m2*h)降低至11.8L/(m2*h),产水电导低于4霺/cm,脱盐率高于99.99%,产水CODCr值约30mg/L.经过5次浓缩实验后,PVDF的通量和产水电导均保持稳定.","authors":[{"authorName":"武春瑞","id":"66e5f891-fc63-4355-a88d-d1a161c1c1ba","originalAuthorName":"武春瑞"},{"authorName":"刘东","id":"6578b6a6-9180-4e34-9608-c99df37e5f9b","originalAuthorName":"刘东"},{"authorName":"陈华艳","id":"06b70b5c-d69d-42b5-8346-8b43f131e749","originalAuthorName":"陈华艳"},{"authorName":"贾悦","id":"8bbbb8f1-4d1e-4457-a09c-03c0c2cdd844","originalAuthorName":"贾悦"},{"authorName":"王暄","id":"c0fe4a7c-be46-4847-b60f-7b7a6339060a","originalAuthorName":"王暄"},{"authorName":"吕晓龙","id":"3735b4ee-f3e8-4502-b43f-e937f7a19323","originalAuthorName":"吕晓龙"}],"doi":"","fpage":"2018","id":"4fd7fb85-9737-4523-bf83-d6cc95507fe0","issue":"12","journal":{"abbrevTitle":"GNCL","coverImgSrc":"journal/img/cover/GNCL.jpg","id":"33","issnPpub":"1001-9731","publisherId":"GNCL","title":"功能材料"},"keywords":[{"id":"c31d1ffb-6b83-4b46-83e0-2d24ecbf4949","keyword":"减压蒸馏","originalKeyword":"减压膜蒸馏"},{"id":"e5c82a97-09c2-4bdb-88b3-1a6191a716b6","keyword":"聚偏氟乙烯","originalKeyword":"聚偏氟乙烯"},{"id":"110c7fe4-099e-4c3b-bd3d-038d9759119f","keyword":"疏水","originalKeyword":"疏水膜"},{"id":"029b230e-c0b5-479b-b2a1-f2f4cb142b4e","keyword":"中空纤维","originalKeyword":"中空纤维膜"},{"id":"530eb10f-318f-4991-ada2-7a2f7a4de2bd","keyword":"废水处理","originalKeyword":"废水处理"}],"language":"zh","publisherId":"gncl200812024","title":"PVDF疏水中空纤维蒸馏含盐废水处理性能研究","volume":"39","year":"2008"},{"abstractinfo":"用甲基三乙氧基硅烷对硅溶胶进行疏水改性.研究了在不同温度下,不同甲基三乙氧基硅烷含量对硅溶胶的改性效果.用浸渍提拉法和自流法在玻璃表面制成了疏水.采用傅里叶红外光谱、差热-失质量测试仪及接触角测试仪等测试方法对疏水进行了检测分析及疏水性能的表征.结果表明:在40℃,有机硅单体质量分数为9%时,甲基三乙氧基硅烷改性硅溶胶相容性良好,在玻璃表面涂前后光学性能无明显变化,涂玻璃片表面的疏水性有了大幅的提高.","authors":[{"authorName":"陈利君","id":"3aab0738-5ff3-470b-b508-eea0c23a55f5","originalAuthorName":"陈利君"},{"authorName":"江元汝","id":"3f0f1614-41e9-4086-9c96-bfb8a38e4209","originalAuthorName":"江元汝"},{"authorName":"张漩卓一","id":"c2c55c9a-c924-4b59-9e6c-a95a0b017859","originalAuthorName":"张漩卓一"},{"authorName":"陈隆","id":"99164758-b91c-4455-b629-886a2fe7e50e","originalAuthorName":"陈隆"}],"doi":"10.3969/j.issn.0253-4312.2012.04.007","fpage":"26","id":"f3e91a2a-2c1f-463e-848e-a08995c4f40e","issue":"4","journal":{"abbrevTitle":"TLGY","coverImgSrc":"journal/img/cover/TLGY.jpg","id":"61","issnPpub":"0253-4312","publisherId":"TLGY","title":"涂料工业 "},"keywords":[{"id":"138d91b9-1e0b-4fe3-93ce-0db6ec36f5c8","keyword":"硅溶胶","originalKeyword":"硅溶胶"},{"id":"eecf5b2c-020c-4174-980b-11d3c64e0998","keyword":"硅烷偶联剂","originalKeyword":"硅烷偶联剂"},{"id":"47d8e27d-c4cb-44cc-be38-16b8f7baff86","keyword":"疏水","originalKeyword":"疏水膜"},{"id":"ba0e751e-be16-427b-8947-ca5eb8b22f69","keyword":"玻璃表面改性","originalKeyword":"玻璃表面改性"}],"language":"zh","publisherId":"tlgy201204007","title":"甲基三乙氧基硅烷改性硅溶胶及疏水性能研究","volume":"42","year":"2012"},{"abstractinfo":"讨论了蒸馏涉及的材料特性.提出水阻力概念,认为疏水材料结构的优化与蒸馏工艺有关.提出鼓泡蒸馏方法,在热流体中鼓入空气气泡,由气液两相流效应来强化热流体的扰动.提出透气蒸馏方法,通过气体的吹扫夹带作用,使孔内水蒸气的传质由低效的扩散转为高效的对流机理.提出曝气蒸发方法,利用不同温度的空气吸湿原理进行曝气.将蒸馏过程与化学除硬度、超滤耦合,可除去结垢性钙镁离子;将蒸馏过程与气浮絮凝过程耦合,可除去有机污染物,实现高倍率浓缩.提出多效蒸馏方法,组件兼有蒸发与换热功能,使蒸馏过程中的水蒸气冷凝与原水加热过程耦合,可以实现低成本的蒸馏过程.","authors":[{"authorName":"吕晓龙","id":"fb91429e-d6ca-4d23-8ef9-d9b386715f01","originalAuthorName":"吕晓龙"}],"doi":"10.3969/j.issn.1007-8924.2010.03.001","fpage":"1","id":"004a8d30-8801-4348-bd11-9827c5154252","issue":"3","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术 "},"keywords":[{"id":"4c413c64-beda-4736-8ec8-aca98346ce4f","keyword":"蒸馏","originalKeyword":"膜蒸馏"},{"id":"686b8a61-4017-4f73-9d25-018804d41fe7","keyword":"疏水","originalKeyword":"疏水膜"},{"id":"2cb63d0d-0de8-4f58-a53a-e21ee6c814da","keyword":"超疏水性","originalKeyword":"超疏水性"},{"id":"a2b063f1-b147-4a9d-b3f8-4d4b2bc05ec0","keyword":"水阻力","originalKeyword":"水膜阻力"},{"id":"1658e2d7-05f9-4b0c-a4e8-81e74cf92498","keyword":"过程","originalKeyword":"膜过程"},{"id":"a482eca9-709b-411e-b8e7-b701a32c22e8","keyword":"工艺耦合","originalKeyword":"工艺耦合"}],"language":"zh","publisherId":"mkxyjs201003001","title":"蒸馏过程探讨","volume":"30","year":"2010"},{"abstractinfo":"以魔芋葡甘聚糖和大豆油为原料通过碱催化制备魔芋葡甘聚糖脂肪酸酯疏水(F-KGM);采用紫外-可见分光光度计、傅立叶变换红外光谱仪、十八角静态激光光散射仪、X射线衍射仪、热分析仪和扫描电子显微镜对其进行结构表征。结果表明,F-KGM的重均分子量(-Mw)为3.653×106g/mol,明显高于KGM的1.619×106g/mol,魔芋葡苷聚糖与脂肪酸分子形成酯键,KGM经酯化后,改变了原有的晶体结构,结晶度降低,具有更高的热稳定性,分子乳化融合流延成过程中发生分子自组装行为,形成性质稳定且具有良好疏水性能的缓释材料。","authors":[{"authorName":"刘毅","id":"403ac3c9-4d5f-4391-9f74-bcd48050303e","originalAuthorName":"刘毅"},{"authorName":"张艳","id":"082099fc-e5e8-4d4a-8aaa-699b0525f9e5","originalAuthorName":"张艳"},{"authorName":"兰晶","id":"8c64a1c0-934b-4a3d-86d7-a0bcc9b29036","originalAuthorName":"兰晶"},{"authorName":"柯百胜","id":"1fffb861-b672-49ca-a925-eb056eb5c974","originalAuthorName":"柯百胜"},{"authorName":"王勖","id":"71c86235-65c0-41c6-8c60-fce858141225","originalAuthorName":"王勖"},{"authorName":"余文洁","id":"c24ab0d1-44d5-4733-bbae-3be2b0aa0d9f","originalAuthorName":"余文洁"},{"authorName":"钱虹","id":"df8c4ab5-5148-4ff5-8cb9-917e8f8d362b","originalAuthorName":"钱虹"},{"authorName":"姜发堂","id":"da67cc15-69f4-42fc-9054-3dfc09879cf3","originalAuthorName":"姜发堂"}],"doi":"","fpage":"88","id":"532ae9bd-e876-4d71-848f-fb09c0479512","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":"447a458c-05d4-4637-b738-ddaba4b419e0","keyword":"魔芋葡甘聚糖","originalKeyword":"魔芋葡甘聚糖"},{"id":"1ad91303-a51d-42c0-9bf2-abfff89c72a7","keyword":"脂肪酸","originalKeyword":"脂肪酸"},{"id":"58281278-f835-4962-91b9-d2ef9f5680d8","keyword":"疏水","originalKeyword":"疏水膜"},{"id":"cf535f3f-c587-481b-a48c-b9b59f1ce3d1","keyword":"缓释","originalKeyword":"缓释"}],"language":"zh","publisherId":"gfzclkxygc201204023","title":"魔芋葡甘聚糖基缓释材料的结构表征","volume":"28","year":"2012"},{"abstractinfo":"用中空纤维微孔疏水进行木瓜蛋白酶的渗透结晶,研究温度和不同pH的缓冲溶液对木瓜蛋白酶静态渗透结晶的影响,优化木瓜蛋白酶渗透结晶的结晶条件.通过监控结晶溶液中木瓜蛋白酶浓度随时间的变化,考察沉淀剂和添加剂对结晶过程的影响,并对晶体进行尺寸分布分析.结果表明,对于木瓜蛋白酶的渗透结晶,在15~32℃下,以pH 4.7的乙酸盐为缓冲溶液,在沉淀剂(硫酸铵和磷酸钠)质量分数4%时,制备出质量较好的木瓜蛋白酶晶体.添加剂PEG600和PEG4000的加入提高了溶剂跨通量,改善了晶体质量.","authors":[{"authorName":"张新妙","id":"cf26958e-6562-48f4-8dfb-bbd54cc2873f","originalAuthorName":"张新妙"},{"authorName":"左俊芳","id":"99840d87-2185-46c4-bdd7-d5ac1dd504b5","originalAuthorName":"左俊芳"},{"authorName":"魏可贵","id":"ce58c1a3-1f0e-4e23-8d95-5b2b3b27b796","originalAuthorName":"魏可贵"},{"authorName":"马润宇","id":"17aca485-0fae-4e23-b774-ac8ce69d16ea","originalAuthorName":"马润宇"}],"doi":"10.3969/j.issn.1007-8924.2008.05.019","fpage":"94","id":"40272870-ce5c-478e-8250-f5a4e829d13c","issue":"5","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术 "},"keywords":[{"id":"c837bdcf-45d8-42c6-b43d-21d36731f8a7","keyword":"结晶","originalKeyword":"膜结晶"},{"id":"448d5091-5796-4ccb-bf45-46da535e1e8a","keyword":"木瓜蛋白酶","originalKeyword":"木瓜蛋白酶"},{"id":"d5532bf4-52b4-4de9-b381-19d6d5025de2","keyword":"疏水","originalKeyword":"疏水膜"},{"id":"124c87a9-82c1-4372-a7af-4c5fec702751","keyword":"结晶条件","originalKeyword":"结晶条件"}],"language":"zh","publisherId":"mkxyjs200805019","title":"渗透结晶法结晶木瓜蛋白酶","volume":"28","year":"2008"},{"abstractinfo":"针对目前日益严重的高氨氮废水处理问题,采用吸收技术能够在常温常压下使浓度3 000~5 000 mg/L范围内的高氨氮废水流经疏水后,降为浓度低于原液1%可排放的水质,极大地提高了氨氮的去除效率.实验从原料液流速、吸收液浓度、组件长度和原料液与吸收液流向4个方面探究了不同因素对氨氮去除效率的影响.结果表明,吸收液浓度越高,氨氮去除率越高;随着原料液流速和组件长度的增加,氨氮去除率呈现先增大后减小的趋势;原液走管程,吸收液走壳程,原液与吸收液流向相同时的去除效果最好.","authors":[{"authorName":"陈卫文","id":"daa40467-47f0-428b-bc13-a020f679f1ff","originalAuthorName":"陈卫文"}],"doi":"10.16159/j.cnki.issn1007-8924.2016.05.015","fpage":"95","id":"6b5eb6dc-5703-449b-84db-64915aef2ee1","issue":"5","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术 "},"keywords":[{"id":"3484e45e-432c-4760-ae0e-b4ffdf8aaf15","keyword":"吸收","originalKeyword":"膜吸收"},{"id":"beffbc00-6309-48ea-a6f0-7f9f98309541","keyword":"高氨氮废水","originalKeyword":"高氨氮废水"},{"id":"cd63faac-dedf-401f-8b39-2dcb1a8dc531","keyword":"稀硫酸","originalKeyword":"稀硫酸"},{"id":"017d6e92-c5f5-41de-ae21-4c8a8093ac8d","keyword":"疏水","originalKeyword":"疏水膜"}],"language":"zh","publisherId":"mkxyjs201605015","title":"吸收技术用于处理高氨氮废水的研究","volume":"36","year":"2016"}],"totalpage":1993,"totalrecord":19930}