可再分散乳胶粉对抗裂抹面砂浆的影响

通过对含有不同掺量可再分散乳胶粉的抗裂抹面砂浆的试验,得出相应的抗裂抹面砂浆的拉伸粘结强度,绘制出可再分散乳胶粉掺量变化时拉伸粘结强度的变化曲线,得出了抗裂抹面砂浆的拉伸粘结强度和可再分散乳胶粉掺量的变化规律,研究结果为配制不同应用要求的抗裂抹面砂浆提供了一些基础试验数据和参考.     

聚烯丙硫醇/丙烯酸甲酯羰基铑(Ⅰ)配合物的分子内取代反应

合成了一种新的含有S、O未配位原子的高分子顺二羰基铑配合物 ,用IR和XPS数据研究了其分子内羰基取代反应 ,结果表明在遇热且无CO保护下S、O与铑形成的弱的S→Rh、O→Rh键可取代强的Rh→Cπ键 ,形成稳定的四配位结构 ,从而保护了铑不因末端羰基脱落而分解 ,提高了它的稳定性 ;其分子内取代反应是可逆的 ,在CO气氛下该结构又能够回复到二配位结构     

N-[2-(2-吡啶)乙基]苯胺及其COCl_2配合物的晶体结构及配体的构象研究

本文制备了二氯[N-(2-吡啶乙基)苯胺]钴配合物,并用 X 射线衍射法测定了配合物及配体的晶体结构。结合 EHMO 和 DPCILO 计算,从能量角度,跟踪配体从构象1(配体的晶态构象)变至构象2(配体在配合物中的晶态构象)的变化过程。     

［顺－二羰基（N－2－（2－吡啶）乙基芳胺）铑］的四苯硼酸盐的合成及其催化性能

［顺－二羰基（Ｎ－２－（２－吡啶）乙基对取代苯胺）铑］的四苯硼酸盐作为催化剂，用于催化甲醇羰基化反应，在温和的条件下，可顺利催化甲醇羰基化反应得到乙酸和乙酸甲酯而无其它副产物．若以甲醇和乙酸的混合液作反应物，则得到乙酸酐和乙酸甲酯．即使在大量水存在下，也仅有微量的水煤气转换反应发生．实验证明对位取代基团的电子效应对铑配合物的催化活性影响甚微．在不同位置以不同链长相联的二吡啶配体对铑阳离子配合物性能的影响是明显的．其中α，α＇－联吡啶铑阳离子结构不利于催化反应的进行．由此证明，作为催化剂活性物种除必须的Ｒｈ－ＣＯ键存在外，配体的空间结构是影响配合物活性的决定因素．羰基化发生在碘甲烷的氧化加成与乙酰碘的还原消除之间，同时还伴有一个在配位的乙酰基与铑的顺－空配位之间甲基的１，２移动变化．     

新型Ni－La催化剂催化甲醇气相羰基化反应

 制备和测试一种全新的甲醇气相羰基化催化剂。催化剂的活性金属为Ni, La为第二组分，本身无催化羰基化活性，采用一种我们自行开发的新型碳分子筛为载体。在制备过程中，采用了一种全新的负载路线，即：以Ni-La双核配合物为金属微晶的前体，使得Ni-La按确定的原子比混合，由此得到全新Ni-La羰基化催化剂。La有很强的助催化作用，与未添加La的Ni催化剂相比，Ni-La催化剂表现出更高的催化活性和选择性。     

STUDY OF CARBONYLATION OF METHANOL TO ACETIC ACID AND ACETIC ANHYDRIDE OVER A BIDENTATE POLYMER BOUND CIS-DICARBONYLRHODIUM COMPLEX AS CATALYST

Copolymer of 2-vinylpyridine and vinylacetate coordinated with dicarbonylrhodiumused as a catalyst for carbonylation of methanol to acetic acid and anhydride has beenstudied. The structural characteristics of the copolymer ligand and complex, and the in-fluences of the reaction conditions on the carbonylation catalyzed by this polymer complexhave been investigated. In comparison with small molecule catalyst of Rh complex, thebidentate copolymer coordinated complex has better thermal stability. The reactionmechanism of the carbonylation reaction is also illustrated.     

2-乙烯吡啶-丙烯酸甲酯共聚物与四羰基二氯二铑反应所得配合物的结构与催化甲醇羰基化性能的研究

聚(2-乙烯吡啶—丙烯酸甲酯)共聚物与四羰基二氯二铑形成的配合物是一种催化甲醇羰基化的新型催化剂.本文用X-射线衍射(XRD),光电子能谱(XPS)和红外光谱(IR)对其键合状态进行了表征,并探索了其分子骨架结构与催化甲醇羰基化活性之间的关系.     

A catalyst for the carbonylation of methanol to acetic acid in gaseous phase

A novel Rh/Ys catalyst for the carbonylation of methanol to acetic acid in gaseous phase is reported. The porous carbon beads (Ys) prepared from the carbonation of poly(vinylidene chloride) were used as the support. This catalyst has a specific surface area of 1 000 m2/g, high mechanical strength and thermal stability. The average diameter of the pore is in the range of 0.8 - 1.2nm. Experimental evidence showed that this catalyst was of high activity and selectivity, which could compare to those of the homogeneous catalyst from Monsanto. The catalytic rate could get to 900 g AcOH/g Rh·h during the carbonylation of methanol to acetic acid. The fine spreading of Ph over the Ys surface is the key factor for the activity.     

A NOVEL COPOLYMER-BOUND CIS-DICARBONYLRHODIUM COMPLEX FOR THE CARBONYLATION OF METHANOL TO ACETIC ACID AND ACETIC ANHYDRIDE

A series of porous microspheres of linear and ethylene diacrylate (M') cross-linked copolymers of 2-vinylpyridine (V) and methyl acrylate (M) reacted with tetracarbonyldichlorodirhodium to form a series of cis-dicarbonylrhodium chelate complex (MVRh and MVM 'Rh). They are thermally stable yet very reactive in the carbonylation of methanol to acetic acid, and of methanol-acetic acid mixture to acetic acid and acetic anhydride with a selectivity of 100% under relatively mild and anhydrous conditions.