铬酸钴催化剂上苯酚和甲醇气相邻位烷基化反应

研究了具有尖晶石结构的铬酸钴及负载钾的铬酸钴催化剂上苯酚和甲醇气相邻位烷基化反应. 结果表明, 相对较高的反应温度有利于提高催化剂的反应活性和2,6-二甲酚的选择性; 随着质量空速的降低, 苯酚的转化率和2,6-二甲酚的选择性逐渐增加, 邻甲酚的选择性逐渐降低, 这表明2,6-二甲酚是邻甲酚进行连续反应的结果. 另外, 钾的引入能明显提高邻甲酚的选择性, 降低苯酚的转化率和2,6-二甲酚的选择性, 原因可能主要是由于负载钾后铬酸钴催化剂上的较强的酸中心数目明显减少所致.     

Mg-La-HY-SBA-15分子筛催化甲醇烷基化反应

用两步浸渍法制备了Mg-La-HY-SBA-15复合分子筛,在小型固定床反应器上考察了苯酚甲醇烷基化性能;通过SEM-EDS、Py-FTIR等表征手段分析了Mg-La-HY-SBA-15分子筛的孔结构和酸性。结果表明,Mg负载到HY-SBA-15分子筛上且未改变其微介孔结构; Mg改性后降低了载体的总酸量,增加了总Lewis酸,提高了邻甲酚的选择性和收率。     

Mg/Ce-USY分子筛催化苯酚甲醇烷基化

采用Mg、Ce双金属对USY分子筛催化剂进行改性.通过XRD、SEM、N_2吸附-脱附、NH3-TPD、Py-FTIR和TG-DTA分析方法对催化剂进行了表征.结果表明,双金属改性并没有改变USY的孔道结构,活性组分均匀负载在USY分子筛表面;Mg的加入能够更好地促进Ce元素在USY表面的分散,改性金属元素之间的酸碱相互作用显著提高催化剂表面弱酸强度的L酸中心数量.将改性催化剂应用于苯酚甲醇烷基化反应,邻甲酚选择性达到68.7%,高于Ce-USY的42.4%.     

Ce-SBA-15的制备及其苯酚甲醇烷基化性能

采用后合成法制备Ce-SBA-15介孔分子筛.通过XRD、N_2吸附-脱附、SEM、EDS、NH_3-TPD、Py-FTIR和TGDTA手段对样品进行表征.结果表明,Ce-SBA-15催化剂具有介孔结构,活性组分CeO_2能够很好地分散在载体表面.在固定床反应装置上,考察了Ce负载量、焙烧温度和焙烧时间对Ce-SBA-15催化苯酚甲醇烷基化性能的影响.最佳组成和制备条件为:Ce负载量为15%,焙烧温度为550℃,焙烧时间为4.5 h.在苯酚/甲醇摩尔比1/4,反应温度460℃,质量空速3.0 h~(-1),常压的条件下,Ce-SBA-15分子筛催化苯酚甲醇烷基化性能最好,苯酚转化率达到66.89%,邻甲酚选择性达到55.43%.     

HZSM-5沸石分子筛上苯酚与甲醇的烷基化反应

 在n（PhOH）／n（CH3OH）＝1,WGSV＝0．5h－1,T＝673K的反应条件下,研究了HZSM－5,HZSM－23和改性HZSM－5分子筛上苯酚与甲醇烷基化反应的规律．结果表明,分子筛外表面的酸中心对苯酚烷基化反应的贡献较大．用4－甲基喹啉使分子筛外表面的酸中心中毒后,影响反应产物选择性的主要因素是分子筛的孔径．孔径较小的HZSM－23分子筛对提高芳香醚的选择性,抑制二甲酚的生成和提高对甲酚的选择性有利．间甲酚和二甲酚可以在HZSM－5沸石的孔道内生成,但在HZSM－23的孔道内受到抑制．用P2O5,MgO和Sb2O3对HZSM－5改性都可以提高芳香醚的选择性,降低甲酚和二甲酚的选择性．随着氧化物负载量的增加,邻甲酚选择性升高．适度的氧化物改性可以提高对甲酚的选择性,改性效果为Sb2O3＞P2O5＞MgO．     

改性纳米HZSM-5催化剂上甲苯与甲醇的烷基化反应

以Si,P,Mg复合改性的纳米HZSM-5为催化剂,进行了甲苯与甲醇的烷基化反应;并采用X射线衍射,NH3程序升温脱附,红外和低温N2吸附等方法研究了改性前后催化剂酸性质和孔结构的变化.在小型固定床反应器上,考察了载气量、反应温度和重时空速等反应条件对烷基化反应性能的影响.在2h-1,460℃,甲苯/甲醇比,水/烃比和...     

P-HZSM-5催化剂上合成对异丙基苯酚的研究

研究了在Ｐ－ＨＺＳＭ－５ 上苯酚与异丙醇烷基化合成对异丙基苯酚（ｐ－ＩＰＰ）的反应, 考察了磷含量对催化反应性能的影响, 用ＮＨ３－ＴＰＤ和Ｐｙｒ－ＩＲ表征了Ｐ－ＨＺＳＭ－５ 的表面酸性质． 结果表明, 磷改性ＨＺＳＭ－５ 可提高ｐ－ＩＰＰ选择性（达９５％ ）, 而降低了苯酚的转化率, 并导致酸量减少和酸强度减弱． 磷与分子筛的相互作用引起了分子筛脱铝． 焙烧温度对活性和选择性均有影响． 分子筛在９７３ Ｋ、Ｐ－ＨＺＳＭ－５ 在８２３ Ｋ焙烧时, ｐ－ＩＰＰ选择性最高     

Mg/Ce-SBA-15的制备及其苯酚甲醇烷基化性能的研究

以Ce-SBA-15为载体,硝酸镁为活性组分前驱体,通过浸渍法制备了Mg/Ce-SBA-15催化剂。利用XRD、N₂吸附-脱附、SEM、EDS、NH₃-TPD、Py-FTIR和TG-DTA手段对催化剂进行表征。结果表明,Mg掺杂并未破坏载体结构,催化剂表面弱酸含量有所增加,L酸增加明显。在固定床反应器中评价了Mg/Ce-SBA-15分子筛催化苯酚甲醇烷基化的反应性能。结果表明,Mg负载量为7%、焙烧温度为550℃、焙烧时间为4.5 h制备的Mg/Ce-SBA-15催化剂催化效果最佳。在反应温度460℃,n（苯酚）：n（甲醇）为1：4,质量空速为3.0 h^-1,常压的条件下,苯酚转化率为80.1%,邻甲酚选择性为86.4%。     

硼,钾改性KX沸石上甲苯和甲醇的则链烷基化反应

研究了硼,钾改性ＫＸ沸石催化剂的甲苯侧链烷基化反应性能。结果表明,硼和钾同时改性可显著地提高了甲苯侧链烷基化的应活性,Ｈ３ＢＯ３和ＫＯＨ在催化剂样品浸渍过程中形成了不同经化计量比的碱金属硼酸盐,该硼酸盐在沸石上作为新的碱性中心而有利于醇的催化脱氢。     

HF改性的Pt/ZSM-5催化剂在苯和甲醇烷基化反应中的应用

以HF改性的Pt/ZSM-5为催化剂,研究了其在苯和甲醇烷基化反应的应用,并用XRD、NH₃-TPD、BET等表征方法研究了改性前后催化剂酸性和孔结构变化。 结果表明,经HF改性后,Pt/ZSM-5催化剂的酸性增强、酸量增加,苯和甲醇烷基化反应性能明显提升。 3%HF-0.2%Pt/ZSM-5催化剂催化苯和甲醇烷基化反应时,甲苯和二甲苯选择性达到92.20%。 但是,HF负载量大于6%时,HF脱除的部分骨架硅和骨架铝会堆积在催化剂孔道内部,限制了反应物和产物的扩散,造成其催化性能下降。 通过计算得到了HF改性的Pt/ZSM-5催化剂上苯和甲醇烷基化反应的活化能为118 kJ/mol。     

Ortho‐Alkylation of Phenol with Methanol Using Pb‐Cr Promoted Magnesium Oxide Catalysts

In this study, Pb‐Cr promoted magnesium oxide catalysts were used to catalyze the ortho‐alkylation of phenol in the presence of excess methanol. The Cr/MgO catalyst exhibited a high conversion of phenol and a relatively high selectivity for the ortho‐alkylation of phenol. The catalytic activity and the stability of Cr/MgO were improved by the addition of a fairly small amount of Pb. The Pb‐Cr/MgO catalyst showed specificity for the ortho‐alkylation of phenol, which was proved by a series of phenol derivative reactions with methanol.     

Alkylation of Phenol with Methanol Over Rare Earth Promoted Sulfated Tin Oxide Catalyst

A comparative account of the tin-samarium binary oxide and its sulfate modified analogue (SO₄ ^2- / SnO₂-Sm₂O₃) in the alkylation of phenol with methanol is reported. Sulfate modification resulted in a large variation in product selectivity and reaction pathway due to the creation of strong acid sites, which alters the nature of adsorption of phenol on the catalyst surface.     

Alkylation of Phenol with Methanol over Basic X Zeolites

Alkylationofphenolprovidesmanyindustrialintermediatessuchasagrochemicalsandpolymers.Thealkylationofphenolwithmethanolproceedsviaoxygen(O)-alkylationproducinganisole(An)aswellasmethylanisoleisomers(InAn)andring(C)-alkylationproducingmainlycresols(m.p.o-Cr)aswellasxylenols(Xy).Vapor-phasealkylationofphenolwithmethanolhasbeenexaminedovervarioussolidcatalysts'-'.Thecatalyticpropertiesandtheproductselectivityarestfonglyaffectedbythestructureofcatalystinadditiontoacidic-basiccharacter.Strongacidc…     

Liquid Phase Friedel‐Crafts Alkylation over Mixed Metal Oxide Catalyst

Liquid phase Friedel‐Crafts alkylation of benzene with benzyl chloride was carried out over various ferrites viz. CuFe₂O₄, NiFe₂O₄, CoFe₂O₄, ZnFe₂O₄, and MgFe₂O₄. Among the various ferrites ZnFe₂O₄ showed the highest activity. These ferrites were prepared by co‐precipitation technique. The effect of variation of catalyst, speed of agitation and reaction temperature has been studied. Benzylation of other substrates such as toluene, anisole and chlorobenzene was also studied. The catalyst ZnFe₂O₄ was found to be reusable. The acid base properties of the catalyst were studied by cyclohexanol dehydration reaction and the data was correlated with activity.     

改性X型沸石催化甲苯、甲醇侧链烷基化反应的研究进展

综述了三十年来国内外有关在改性Ｘ型沸石催化剂上,甲苯、甲醇侧链烷基化制备苯乙烯反应的研究状况。经过性改性的Ｘ型沸石具有合适的孔径和适当强度及数量的表面酸碱中心、表面酸碱中心的协同作用有利于反应活性及选择性的提高。参考文献１２６篇。     

Alkylation of aromatics. Kinetics of phenol alkylation with methanol

A kinetic study of phenol alkylation with methanol in the presence of -Al₂O₃ has been carried out. A mechanism involving the reaction of phenol and methanol adsorbed on acid-base pair sites is proposed.     

The Mechanism Study on the Catalytic Synthesis of 2,6‐Dimethylphenol from KA‐Oil and Methanol over Magnesium Oxide Catalysts

Catalytic synthesis of 2,6‐dimethylphenol from KA‐oil (a mixture of cyclohexanol and cyclohexanone) and methanol was achieved by using magnesium oxide‐supported chromium oxide catalysts in one step. At higher conversion (> 90%), dimethylphenol was formed in high yield (>60 %). The activity of Cr/MgO catalysts depended on the concentration of chromium. The yield of 2,6‐dimethylphenol was also affected by the composition of the ratio of cyclohexanol to cyclohexanone in KA‐oil. Cyclohexanol and cyclohexanone reacting with methanol under the same conditions indicated that pure cyclohexanol or cyclohexanone is less reactive than their mixture, KA‐oil. The adsorption properties of cyclohexanol and cyclohexanone on the surface of Cr/MgO determined by FT‐IR spectroscopy suggest that cyclohexanone is easily reduced to cyclohexanol by the hydrogen which formed in the reaction, and then further reacted with methanol to form 2,6‐dimethyphenol.