锰助剂对Fe／ZrO2催化剂F—T反应催化性能的影响

应用ＸＲＤ，ＸＰＳ，Ｍｏｓｓｂａｕｅｒ谱，ＴＰＲ，ＣＯ化学吸附ＣＯ－ＴＰＤ，ＣＯ＋Ｈ２反应性能测试等手段研究了锰助剂对Ｆ－Ｔ合成制低碳烯烃Ｍｎ－Ｆｅ／ＺｒＯ２催化剂结构及催化性能的影响。结果表明，与Ｆｅ／Ｚｒ催化相比，加锰助剂后的催化剂Ｆ－Ｔ反应催化活性上升，甲烷选择性降低，低碳烯烃选择性增加。     

Ti—Si沸石表面吸附物种的TPSR—TPD研究

氯丙烯在不同催化剂表面上吸附的ＴＰＤ结果表明在ＴＳ－１上有三重附峰，而在ＴｉＯ２／Ｓｉｌｉｃａｌｉｔｅ上仅有单峰，Ｈ２Ｏ２或分子Ｏ２在催化剂表面吸附后，在脱附物种中可用质谱检测到原子Ｏ（１６）物种；说明Ｈ２Ｏ２或分子Ｏ２在样品表面存在解离吸附；并发现解离子分子Ｏ２的活性很低，ＴＳ－１能同时吸附内烯和Ｈ２Ｏ２，而在ＳｉＯ２／Ｓｉｌｉｃａｌｉｔｅ表面的吸附却与吸附顺序有关，环氧化活性顺序如下：ＴＳ－１     

Ti－Si沸石表面吸附物种的TPSR－TPD研究

氯丙烯在不同催化剂表面上吸附的ＴＰＤ结果表明：在ＴＳ－１上有三重脱附峰，而在ＴｉＯ２／Ｓｉｌｉｃａｌｉｔｅ上仅有单峰。Ｈ_２Ｏ_２或分子Ｏ_２在催化剂表面吸附后，在脱附物种中可用质谱检测到原子Ｏ（１６）物种；说明Ｈ_Ｏ_２或分子Ｏ_２在样品表面存在解离吸附；并发现解离分子Ｏ_２的活性很低。ＴＳ－１能同时吸附氯丙烯和Ｈ_２Ｏ_２，而在ＳｉＯ_２／Ｓｉｌｉｃａｌｉｔｅ表面的吸附却与吸附顺序有关。环氧化活性顺序如下：ＴＳ－１（ＴＰＡＯＨ）＞ＴＳ－１（ＴＰＡＢｒ＋ＮａＯＨ）＞ＴｉＯ_２／Ｓｉｌｉｃａｌｉｔｅ。ＴＳ－１沸石的高氧化活性可能与Ｈ_２Ｏ_２吸附后表面原子Ｏ（１６）的形成有关。     

合成气制低碳烯烃K—Fe—MnO／MgO催化剂的研究：Ⅰ.MnO助剂的作用

采用ＣＯ加氢反应、ＣＯ－ＴＰＤ、ＣＯ／Ｈ２－ＴＰＳＲ及Ｃ２Ｈ２／Ｈ２－ＴＰＳＲ等手段，研究合成气制低碳烯烃反应Ｋ－Ｆｅ－ＭｎＯ／ＭｇＯ催化剂中ＭｎＯ的助剂作用。结果表明ＭｎＯ能大幅度提高低碳烯烃的选择性，尤其是乙烯的选择性；ＭｎＯ能抑制催化剂表面的乙烯加氢，因而有利于提高低碳烯烃的选择性及烯／烷的比值。     

氧化铈对F-T反应铁锆催化剂的助催化作用

应用ＸＲＤ、ＸＰＳ、Ｍｏｓｓｂａｕｅｒ谱、ＴＰＲ、ＣＯ－ＴＰＤ、ＣＯ＋Ｈ２反应性能测量试等手段研究了ＣｅＯ２对Ｆ－Ｔ合成制低碳烯烃Ｃｅ－Ｆｅ／ＺｒＯ２催化剂催化性能的影响。结果表明，与Ｆｅ／Ｚｒ催化剂相比，加铈助剂后的催化剂Ｆ－Ｔ反应催化活性明显上升。     

合成气制低碳烯烃K－Fe－MnO／MgO催化剂的研究Ⅰ．MnO助剂的作用

采用ＣＯ加氢反应、ＣＯ－ＴＰＤ、ＣＯ／Ｈ＿２－ＴＰＳＲ及Ｃ＿２Ｈ＿４／Ｈ＿２－ＴＰＳＲ等手段，研究合成气制低碳烯烃反应Ｋ－Ｆｅ－ＭｎＯ／ＭｇＯ催化剂中ＭｎＯ的助剂作用。结果表明ＭｎＯ能大幅度提高低碳烯烃的选择性，尤其是乙烯的选择性；ＭｎＯ能抑制催化剂表面的乙烯加氢，因而有利于提高低碳烯烃的选择性及烯／烷的比值。     

Fe2O3/ZrO2催化剂上一氧化碳加氢反应制低碳烯烃Ⅱ.预处理条件对催化剂结构及性能的影响

用ＴＰＲ，Ｍｏｓｓｂａｕｅｒ谱法，ＸＰＳ，ＳＲＤ及反应评价等手段了Ｆｅ２Ｏ３／ＺｒＯ２催化剂的还原行为，铁物种状态和ＣＯ加氢反应性能，结果表明，预处理条件明显影响Ｆｅ２Ｏ３／ＺｒＯ２催化剂表面铁原子的数量、铁锆间的相互作用，催化剂的物相变化以及Ｃ氢反应的催经性能，以Ｆｅ２Ｏ２／ＺｒＯ２经氢氩混合氯程序升温至７５３Ｋ还原生成的Ｆｅ－Ｚｒ－Ｏ物种为前身，在合成气中进一步还原得到的铁锆催化剂，具有较好的     

K2O和MnO助剂对Fe/Silicalite-2催化剂CO加氢制低碳烯烃性能的影响

在Ｓｉｌｉｃａｌｉｔｅ－２分子筛担载的铁催化剂中添加ＭｎＯ和Ｋ２Ｏ助剂，可显著提高其ＣＯ加氢制碳烯烃的选择性及催化活性，ＭｎＯ助剂主要抑制乙烯和丙烯的加氢反应而提高烯／烷比值，Ｋ２Ｏ助剂则增加催化剂对ＣＯ的吸附能力，同时抑制乙烯在催化剂表二次反应（主要是乙烯的歧化反应），从而有利于提高低碳烯烃的选择性及催化剂活性。     

K_2O和MnO助剂对Fe／Silicalite－2催化剂CO加氢制低碳烯烃性能的影响

在Ｓｉｌｉｃａｌｉｔｅ－２分子筛担载的铁催化剂中添加ＭｎＯ和Ｋ２Ｏ助剂，可显著提高其ＣＯ加氢制低碳烯烃的选择性及催化活性．ＭｎＯ助剂主要抑制乙烯和丙烯的加氢反应而提高烯／烷比值；Ｋ２Ｏ助剂则增加催化剂对ＣＯ的吸附能力，同时抑制乙烯在催化剂表面的二次反应（主要是乙烯的歧化反应），从而有利于提高低碳烯烃的选择性及催化剂活性．     

Fe_2O_3／ZrO_2催化剂上一氧化碳加氢反应制低碳烯烃 Ⅱ．预处理条件对催化剂结构及性能的影响

用ＴＰＲ，Ｍｏｓｓｂａｕｅｒ谱法，ＸＰＳ，ＸＲＤ及反应评价等手段研究了Ｆｅ２Ｏ３／ＺｒＯ２催化剂的还原行为、铁物种状态和ＣＯ加氢反应性能．结果表明，预处理条件明显影响Ｆｅ２Ｏ３／ＺｒＯ２催化剂表面铁原子的数量、铁锆间的相互作用、催化剂的物相变化以及ＣＯ加氢反应的催化性能．以Ｆｅ２Ｏ３／ＺｒＯ２经氢氟混合气程序升温至７５３Ｋ还原生成的Ｆｅ－Ｚｒ－Ｏ物种为前身，在合成气中进一步还原得到的铁锆催化剂，具有较好的Ｆ－Ｔ反应合成低碳烯烃的选择性．     

PRODUCTION OF LIGHTOLEFINS FROM CO_2 HYDROGENATION OVER Fe/SILICALITE-2 CATALYST Ⅱ. PROMOTION EFFECT OF MnO PROMOTER

IntroductionItilasbeenshot'-nthattileadditionofMnOpromotertoFocatal}stcanresultinaremarkableimprovementinthesclectivit}'to11ghtalkenesforCOh}!drogenationll'l.Ho-c'cvcr.thecadetofMnOonCH4formationandCOconversionisvery'ambigUouslltolMoreover.MnOpromotergrca…     

PRODUCTION OF LIGHT OLEFINS FROM CO2 HYDROGENATION OVER Fe/SILICALITE-2 CATALYST. I.CATALYTIC REACTIVI-FY AND REACTION MECHANISM

K-Fe-MnO/Silicalite-2 is a desirable catalyst for the production of light olefins from CO2 hydrogenation The activity can be improved greatly with increasing the Fe loading, and the selectivities to hydrocarbons rise with Fe loading increase However, an ambiguous effect of Fe loading on the selectivity of light olefin in hydrocarbon products is observed. The CO2 hydrogenation containing a two-step mechanism CO2+H2=CO+H2O, a reversible water gas shift reaction, and CO+(m/2n+1)H2 =1/nCnHm+H2O2, a Frscher-Tropsch reaction, is suggested by the results of CO2-TPD and CO2/H2-TPSR as well as CO/H2-TPSR characterizations.     

EFFECTS OF K_2O AND MnO PROMOTERS ON THE PRODUCTION OF LIGHT ALKENES VIA SYNGAS OVER Fe/SILICALITE-2 CATALYST I.ACTIVITY OF K-Fe-MnO/SILICALIT-2 CATALYST

The activity and the selectivity to light alkenes of silicalite-2 (Si-2) zeolite supported F'e catalyst tor CO hydrogenation can he improved obviously with the addition of K2O and MnO promoters. The results of CO hydrogenation, CO-TPD, CO/H2-TPSR, C2H4/H2-TPSR and C2H4/H2 pulse reaction over K-Fe-MnO/Si-2 catalysts clearly show that the K2O additive into Fe-MnO/Si-2 catalyst leads to a remarkable increase in both the capacity and strength of the strong CO ad-species that will produce much more |Cad| via their disproportionation at higher temperatures. This results in an increase in the CO conversion and the selectivity to light olefins, and a decrease in CH4 formation. Moreover, K2O can suppress the disproportionate of C2H4 that occurs during the reaction as a side-reaction Meanwhile, the MnO promoter mainly prohibits the hydrogenation of C2H4 and C3H6, which is favorable to enhancing the selectivity to C2H4 and C3H6 and decreasing the formation of C2H6, and C3H8. It is also of interest that MnO has har     

EFFECTS OF BINDERS ON THE PRODUCTION OF LIGHT ALKENES FROM SYNGAS OVER K-Fe-MnO/SILICALITE-2 CATALYST Ⅱ. MODIFICATION EFFECT OF Al_2O_3 BINDER ON CO HYDROGENATION

lntroductionInordcrtoselcctivcl}'produccIightoIcfinsfroms}'ngas.thcbinderusedforimprovingthecatal}'ststrcngthshouldbcfavorabIcforprimary'formingofligl1tolcfinsfroms}ngasandforprohibitingsidereactionsoflightoIcfi.sIll.lthasbccnshownthattheundesirablcstrengthofsilicalitc-2zcolitccanbcimprovcdb}addingbindcrs.Hot`ycver.thcadditionofthcbinder`"illcauscsomcchangcsinthcph}'sical-chcmicalstatcofthecatal}ticactivemetalas``cllasitscatal}ticbcha.io,ll'2I.InourprcviouspaperTiO2wasprovedtobcadcsirablcbi…     

PRODUCTION OF LIGHT ALKENES FROM CO AND/OR CO_2 HYDROGENATION OVER K-Fe-MnO/SILICALITE-2 CATALYST

High selectivity to light alkenes can be achieved from CO and CO_2hydrogenation over K-Fe-MnO/Si-2 catalyst.The alkene selectivity isinsensitive to reaction temperature for CO hydrogenation,while apparentlyincreases for CO_2 hydrogenation with raising reaction temperature.An increasein alkene selectivity is observed for both CO and CO_2 hydrogenation with GHSVrising,While a decrease with the elevation of reaction pressure for both CO/H_2and CO_2/H_2 reaction.A two-step mechanism is suggested forCO_2 hydrogenation to form hydrocarbons,by which the variations incontributions of CO and HC as products of CO_2/H_2 reaction with change ofreaction temperature,GHSV and pressure are explained.Moreover,thecatalyst is favorable for selective production of light olefins,which can alsoconcern the slightly secondary reactions of light olefins to some extent.     

PRODUCTION OF LIGHT OLEFINS FROM CO_2 HYDROGENATION OVER Fe/SILICALITE-2 CATALYSTⅢ. PROMOTION EFFECT OF K_2O PROMOTER

ThisprojectissllpportedbytheNationalNaturalScienceFotmdationofChina.IntroductionRecentstUdyonCOZhydrogenationfortheformationofhydrocarbonshascausedagreatinterest,especiallyintheproductionoflightalkenes.msreactionwillprovideanalternativeroutetoproducebasic…     

PRODUCTION OF LIGHT OLEFINS FROM CO2 HYDROGENATION OVER Fe/SILICALITE-2 CATALYST III. PROMOTION EFFECT OF K2O PROMOTER

K2O is a vital promoter to the Fe-MnO/silicalite-2 catalyst for light olefin formation from CO2 hydrogenation. With addition of it into the Fe-MnO/Si-2 catalyst the selectivity to light olefins increases greatly, while CH4 formation is inhibited evidently. Meanwhile, an obvious increment in CO2 conversion is also observed with the addition of K2O promoter. And it has been manifested that adding K2O to the Fe-MnO/Si-2 catalyst leads to remarkable increases in both the capacity and strength of the strong CO2 and CO adspecies. These produce much more[Cad] via their disproportionation at higher temperatures. This results in increase in the CO2 conversion and the selectivity to light olefins, and a decrease in CH4 formation.     

EFFECTS OF BINDERS ON THE PRODUCTION OF LIGHT ALKENES FROM SYNGAS OVER K-Fe-MnO/SILICALITE-2 CATALYST I. EFFECT OF VARIOUS BINDERS ON CO HYDROGENATION

The performance of the K-Fe-MnO/Si-2 catalyst for the production of light olefins via Co hydrogenation changes obviously with the addition of binders. The results of CO hydrogenation. TPR, Mossbauer spectra CI0TPF, CO/H2-TPSR and C2H4/H2-TPSR are employed to investigate the effects of various binders on the physical-chemical states and catalytic behaviors of K-Fe-MnO/Si-2 catalyst to produce light olefins via syngas, TiO2 can promote the reduction of Fe and strengthen the adsorption of CO resulting in raising olefin selectivity. Other binders such as Al2O3, SiO2, MgO, once added into the catalyst, may cause formation of inorganic salts between FeO and Binders leading to a decrease of Fe reduction and a loss of olefin selectivity for CO hydrogenation. Especially, For K-Fe-MnO/Si-2 catalyst with Al2O3 binder directly, the strong secondary reactions of ethylene during CO hydrogenation cause a very poor light olefin selectivity, which will be improved greatly by modifying Al2O3.     

PRODUCTION OF LIGHT OLEFINS FROM CO_2 HYDROGENATION OVER Fe/SILICALITE-2 CATALYST Ⅰ.CATALYTIC REACTIVI-FY AND REACTION MECHANISM

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