排序方式: 共有30条查询结果,搜索用时 0 毫秒
1.
2.
将坎地沙坦酯原料药约100 mg用水超声提取15 min,离心10 min.取上清液过0.22μm滤膜,收集滤液,过预先活化好的C_(18)固相萃取小柱.洗脱液流入离子色谱仪,在IonPac AS18阴离子交换色谱柱上分离,柱温为35℃.以氢氧化钾溶液进行程序淋洗,以电导检测器进行检测.结果表明,N_(3)^(-)和Br^(-)与水中NO_(3)^(-)的分离度均大于1.50,原料药及溶剂水中其他杂质离子的干扰较小;N_(3)^(-)和Br^(-)的质量浓度在一定范围内与其对应的峰面积呈线性关系,检出限(3S/N)分别为0.00070,0.0014 mg·L^(-1);对空白样品进行3个浓度水平的加标回收试验,N_(3)^(-)和Br^(-)的回收率分别为88.2%~93.5%和101%~104%,测定值的相对标准偏差(n=6)分别为2.6%和0.55%;方法用于实际样品分析,取得了满意结果. 相似文献
3.
阳离子表面活性剂对有机颜料艳红6B光催化降解的影响 总被引:6,自引:0,他引:6
研究了阳离子表面活性剂四丁基溴化铵(TBAB)和十六烷基三甲基溴化铵(CTAB)对TiO2光催化降解艳红6B(R6B)的影响,讨论了表面活性剂与R6B的相互作用,给出了二者与TiO2之间的吸附模型. 结果表明,相同条件下,阳离子表面活性剂的加入可增加R6B的降解褪色速率,但表面活性剂自身并不降解. 在强酸(pH=3.00)和强碱(pH=12.60)条件下,R6B的降解褪色速率较快. pH值相同时,体系中TBAB的浓度变化对R6B降解褪色速率的影响不大,而CTAB浓度的变化对R6B降解褪色速率的影响较为明显,CTAB浓度为0.4 g/L时R6B的降解褪色速率最快. 相似文献
4.
TBAB修饰的负载型Wacker催化剂催化甲醇羰基化合成碳酸二甲酯 总被引:7,自引:0,他引:7
自 1 95 9年 Smidt等 [1]发现均相 Pd Cl2 - Cu Cl2 体系可高效率直接选择性氧化乙烯制乙醛以来 ,Wacker催化过程已成为乙醛工业生产的主要方法 .为解决 Wacker催化体系腐蚀性强及催化体系与产物难以分离等弊端 ,将均相 Wacker(Pd Cl2 - Cu Cl2 )催化剂固载化成为备受关注的研究课题[2 ] .多相Wacker催化剂不仅成功地应用于选择性氧化低碳烯烃制醛和酮 [3 ,4 ] ,还用于 CO深度氧化 [5~ 7] .碳酸二甲酯 (DMC)的合成与应用研究是目前绿色化学前沿课题 .在众多的 DMC合成方法中 ,常压气相法因其工艺简单、对设备无腐蚀以及产品易分离… 相似文献
5.
6.
7.
8.
CO2 capture from binary mixture via forming hydrate with the help of tetra-n-butyl ammonium bromide 总被引:2,自引:0,他引:2 下载免费PDF全文
Hydrate formation rate and separation effect on the capture of CO2 from binary mixture v/a forming hydrate with 5 wt% tetra-n-butyl ammonium bromide (TBAB) solution were studied.The results showed that the induction time was 5 min,and the hydrate formation process pressure of 7.30 MPa.The CO2 recovery was about 45% in the feed pressure range from 4.30 to 7.30 MPa.Under the feed pressure of 4.30 MPa,the maximum separation factor and CO2 concentration in hydrate phase were 7.3 and 38.2 tool%,respectively.The results demonstrated that TBAB accelerated hydrate formation and enriched CO2 in hydrate phase under the gentle condition. 相似文献
9.
In this article tetrabutylammonium bromide (TBAB) was first added in buffer to compose a convenient and environmentally friendly system, and enzymatic polymerization of phenol catalyzed by horseradish peroxidase (HRP) could proceed efficiently in this system. When TBAB was added, the most conversion of phenol could reach 99.1%. The phenol polymer was considered to consist of a mixture of phenylene (Ph) and oxyphenylene (Ox) units by IR analysis, and the ratio of phenylene to oxyphenylene units (Ph/Ox) was measured by titration. Moreover, the effects of the dosage of horseradish peroxidase (HRP) and pH value on the conversion of phenol were investigated. The reaction performed very effectively in this novel system when the addition of HRP was only 0.2 mg. In all cases, the weight-average molecular weight calculated by GPC-SLS was in a range from 12000 Da to 30000 Da. The phenol polymer prepared in the present research possessed good thermal stability shown by TG analysis. 相似文献
10.
以四丁基溴化铵(BNBr)或四丁基碘化铵(BNI)作为有机催化剂,碘(I_2)与偶氮二异丁腈(AIBN)原位生成烷基碘化物为引发剂在本体聚合中实现了甲基丙烯酸甲酯(MMA)的可逆催化络合聚合(RCMP).首先,比较了2种催化剂对该体系催化活性的大小,相同实验条件下,BNI作为催化剂时对聚合的控制效果优于BNBr,即在该体系中BNI的催化活性大于BNBr;其次,较为详细地研究了催化剂BNI的用量对MMA可控聚合的影响,结果表明,BNI的浓度在9.43~117.81 mmol/L范围内均有较好的控制效果,当[MMA]∶[I_2]∶[AIBN]∶[BNI]=100∶0.5∶0.75∶0.25,即催化剂的浓度为23.56 mmol/L时反应速率较快,理论分子量与实测分子量(通过GPC进行表征)几乎完全吻合,分子量多分散指数(PDI=M_w/M_n)较小(PDI1.27);最后,通过1H-NMR对所得聚合物的结构进行表征,证明为碘原子封端,M_(n,NMR)与M_(n,GPC)相吻合,端基保有度达到98.8%. 相似文献