CO和CO2在Cu／ZnO／Al2O3催化剂上加氢反应机理的原位红外研究

ＣｕＺｎＯＡｌ2Ｏ3催化剂用于合成甲醇的反应机理已经进行了大量的研究[1～3]。近年来,利用原位红外技术在研究合成甲醇的催化反应机理方面取得了不少研究成果[4～7]。但大多数实验是采用低铜含量催化剂[4,5]。本文采用高温加压式原位红外池,在513Ｋ和20ＭＰａ的条件下,...     

Study on Au/Al2O3 catalysts for low-temperature CO oxidation in situ FT-IR

Au/Al2O3 catalyst was prepared by a modified anion impregnation method and investigated with respect to its initial activity and stability for low-temperature CO oxidation. The activity changes of the catalyst were examined after separate treatment in CO+O2 or CO2+O2. Furthermore, in situ FT-IR studies were performed to investigate the species on the surface when CO or CO+O2 or CO2+O2 was selected separately as adsorption gas. The results showed that Au/Al2O3 catalyst exhibited very high initial activity, but the catalytic activity was found to decrease gradually during CO oxidation with time on stream. And also, the activity of the catalyst declined after treatment in CO+O2 or CO2+O2. The formation and accumulation of carbonate-like species during CO oxidation or treatment in CO+O2 or CO2+O2 might be mainly responsible for the activity decrease, which was reversible.     

H2-induced CO adsorption and dissociation over Co/Al2O3 catalyst

The activation of adsorbed CO is an important step in CO hydrogenation. The results from TPSR of pre-adsorbed CO with H2 and syngas suggested that the presence of H2 increased the amount of CO adsorption and accelerated CO dissocia-tion. The H2 was adsorbed first, and activated to form H* over metal sites, then reacted with carbonaceous species. The oxygen species for CO2 formation in the presence of hydrogen was mostly OH*, which reacted with adsorbed CO subsequently via CO*+OH* → CO2*+H*; however, the direct CO dissociation was not excluded in CO hydrogenation. The dissociation of C-O bond in the presence of H2 proceeded by a concerted mechanism, which assisted the Boudourd reaction of adsorbed CO onthe surface via CO*+2H* → CH*+OH*. The formation of the surface species (CH) from adsorbed CO proceeded as indicated with the participation of surface hydrogen, was favored in the initial step of the Fischer-Tropsch synthesis.     

Study on Au/Al_2O_3 catalysts for low-temperature CO oxidation in situ FT-IR

Au/Al2O3 catalyst was prepared by a modified anion impregnation method and investigated with respect to its initial activity and stability for low-temperature CO oxidation.The activity changes of the catalyst were examined after separate treatment in CO+O2 or CO2 +O2 .Furthermore,in situ FT-IR studies were performed to investigate the species on the surface when CO or CO+O2 or CO2 +O2 was selected separately as adsorption gas.The results showed that Au/Al2O3 catalyst exhibited very high initial activity,but the catalytic activity was found to decrease gradually during CO oxidation with time on stream.And also,the activity of the catalyst declined after treatment in CO+O2 or CO2 +O2 .The formation and accumulation of carbonate-like species during CO oxidation or treatment in CO+O2 or CO2 +O2 might be mainly responsible for the activity decrease,which was reversible.     

Enhancement of CO2 sorption uptake on hydrotalcite by impregnation with K2CO3

The awareness of symptoms of global warming and its seriousness urges the development of technologies to reduce greenhouse gas emissions. Carbon dioxide (CO(2)) is a representative greenhouse gas, and numerous methods to capture and storage CO(2) have been considered. Recently, the technology to remove high-temperature CO(2) by sorption has received lots of attention. In this study, hydrotalcite, which has been known to have CO(2) sorption capability at high temperature, was impregnated with K(2)CO(3) to enhance CO(2) sorption uptake, and the mechanism of CO(2) sorption enhancement on K(2)CO(3)-promoted hydrotalcite was investigated. Thermogravimetric analysis was used to measure equilibrium CO(2) sorption uptake and to estimate CO(2) sorption kinetics. The analyses based on N(2) gas physisorption, X-ray diffractometry, Fourier transform infrared spectrometry, Raman spectrometry, transmission electron microscopy, scanning electron microscopy, and energy dispersive X-ray spectroscopy were carried out to elucidate the characteristics of sorbents and the mechanism of enhanced CO(2) sorption. The equilibrium CO(2) sorption uptake on hydrotalcite could be increased up to 10 times by impregnation with K(2)CO(3), and there was an optimal amount of K(2)CO(3) for a maximum equilibrium CO(2) sorption uptake. In the K(2)CO(3)-promoted hydrotalcite, K(2)CO(3) was incorporated without changing the structure of hydrotalcite and it was thermally stabilized, resulting in the enhanced equilibrium CO(2) sorption uptake and fast CO(2) sorption kinetics.     

脉冲电晕放电-催化转化CO2为CO

在常温、常压下，较系统地研究了CO2在脉冲电晕等离子体条件下的活化与转化，考察了反应器参数、脉冲成形电容、应用电压、气体流量、电晕极性对二氧化碳转化的影响。在本实验条件下，最佳反应器的有效长度为125mm,内径为22mm。二氧化碳转化率和一氧化碳产率随应用电压的增加而增加。另外，随着应用电压的增加，脉冲反应器的能量利用效率反而降低。随着气体流量的增大，二氧化碳的转化率及一氧化碳的产率下降。γ-Al2O3的存在大大促进了二氧化碳的转化，CO2的最高转化率达23％。由于γ-Al2O3在物化性质方面的特性，γ－Al2O3的存在对二氧化碳的转化有重要的作用。研究表明：脉冲电晕放电－催化转化CO2为CO是可行的。     

Rh基催化剂上CO加氢制C2含氧化物的原位红外光谱研究

 用原位红外光谱考察了Rh-Mn-Li-Fe/SiO2和Rh/SiO2催化剂表面上CO的吸附态及CO加氢反应过程中吸附物种的变化. 结果表明,CO在Rh/SiO2催化剂上仅有线式吸附态存在,而CO在Rh-Mn-Li-Fe/SiO2催化剂上既有线式吸附态存在,又有孪生吸附态存在. 这说明Rh-Mn-Li-Fe/SiO2催化剂中Rh的分散度较高. 经CO加氢反应(3.0 MPa,593 K)后,在Rh-Mn-Li-Fe/SiO2催化剂上可观测到C2含氧化物前驱物种的吸收谱带,而在Rh/SiO2催化剂上未观测到相应的谱带; CO在这两种催化剂上主要以线式吸附态存在,孪生吸附态基本消失. 结合催化剂对CO加氢的催化性能,可以认为线式吸附的CO对生成C2含氧化物有贡献. Rh-Mn-Li-Fe/SiO2催化剂的高活性是由于助剂的存在削弱了其表面吸附CO的 C-O键,促进了CO的活化,从而有利于C2含氧化物前驱物的生成.     

CH_2(~3B_1)自由基与O_2的反应

用时间分辨宫里叶红外发射谱仪（TR-FTIRS），研究了自由基与O2反应的通道及产物的振动态布居．基电子态自由基由351nm紫外激光光解CH2CO生成．观测到振动激发态反应产物CO（v　10）、CO2（v3　7）、OH（H2O）和H2CO的红外发射，证实存在生成H2CO的通道．由光谱拟合得到不同时刻CO（v）和CO2（v2）的相对振动布居，发现v＝4能级的布居数相对于v3　3能级有明显反转．     

Evidence for unimolecular CO2 elimination in C-N bond metathesis reactions of basic carbamatozinc complexes Zn4O(O2CAm)6(Am=N-diethylamino, N-piperidyl, N-pyrrolidyl)

The tetranuclear basic zinc carbamates Zn4O(O2CAm)6(1, Am =N-diethylamino; 2, Am =N-piperidyl; 3, Am =N-pyrrolidyl) were shown by transient FTIR spectroscopy to undergo C-N bond metathesis reactions that result in exchange of the carboxyl group with bulk carbon dioxide and exchange of the amino group with bulk secondary amine (transamination). The net rate for CO2 exchange was measured by monitoring the uptake of 13CO2 and the concomitant release of 12CO2. This revealed a CO2-dependent and CO2-independent component to the CO2 exchange process. The CO2-dependent process was interpreted in terms of preassociation of the incoming CO2 with the complex prior to the N-CO2 bond cleavage process while the CO2-independent process was interpreted in terms of a unimolecular elimination of CO2 from the complex. The transamination reaction gave rates that are independent of the concentration of the incoming amine. Furthermore, the transamination rate for each complex was within a factor of four of the CO2-independent CO2 exchange rate for that complex. These data were interpreted in terms of a common rate-limiting process for CO2 exchange and transamination that involves unimolecular elimination of CO2. Rate-limiting unimolecular dissociation of intact carbamato ligands was eliminated as a possible pathway by showing that ligand exchange dynamics is rapid relative to the overall rate of C-N bond metathesis. The ability of these metal carbamate complexes to undergo facile C-N bond metathesis reactions of this type has implications in heterocumulene metathesis and CO2 fixation chemistry.     

CO2对Cu-Ce-O催化剂催化氧化CO活性的影响

用CO作为探针研究CeO。的表面性质,以及研究CO和CO。与CeO。的相互作用,已有不少报导［‘－’1．Br。ysse等人发现CO在CeO。上的吸附,总伴随着催化剂的还原和COZ的生成;CO。在CeO。上的吸附不总是可逆的,CO。的存在会降低其对CO的催化氧化活性,对反应有抑制的影响,甚至会使表面中毒问．也有报导在CO或COZ气氛下,有证据表明CeO。有不利干活性的碳酸盐物种形成;反应中生成的C（）。也可能吸附在表面上形成稳定的碳酸盐,从而抑制反应的继续进行k‘］．＊0。对O;－O－（）催化剂在催化氧化以）中的影响报导比较少问．…     

Rh基催化剂上CO加氢制C2含氧化合物的红外光谱研究

 用红外光谱法考察了Rh-Mn-Li-Ti/SiO2催化剂在CO加氢反应过程中表面吸附物种随压力、温度和H2/CO比的改变而变化的规律. 结果表明,高压有利于提高催化剂表面吸附的CO浓度和活性,高温有利于CO解离; 而高温、高压条件不但促进了CO吸附,而且提高并平衡了CO的解离和插入之间的相对活性,促进了C2含氧化合物的生成. H2/CO比的增大有利于CO在催化剂表面的吸附,从而促进了CO插入,尤其是CO的解离和加氢活性,但是过高的H2/CO比将导致过高的CO解离和加氢活性,引起CO插入活性的削弱而最终导致C2含氧化合物生成活性的下降. 同时,考察了助剂(Mn, Li和Ti)对Rh基催化剂表面吸附物种的影响. 结果表明,助剂的加入可提高C2含氧化合物的生成活性.     

Na 掺杂对硅酸锂吸收CO2性能的影响

通过高温固相反应法, 在添加不同比例Na2CO3的条件下, 合成出一系列可在高温500～750 ℃之间直接吸收CO2的硅酸锂材料. 利用扫描电子显微镜、X射线粉末衍射仪分别观察和评价了合成材料的表面形貌与结构特征, 用热重分析仪测量了硅酸锂材料的CO2吸收性能. 实验结果表明, 通过适量Na元素的掺杂, 能够提高硅酸锂材料吸收CO2的性能, 当Na2CO3的添加量x=0.02时, 合成的硅酸锂材料在CO2气氛下, 于700 ℃恒温保持约15 min即可达到吸收平衡, 材料的吸收量为(46±0.6)%(w), 与未经掺杂的材料相比, 吸收容量有所提高. 此外, 气氛中CO2的浓度对材料吸收CO2的速率有较大影响.     

CH2(X 3B1)自由基与O2的反应

用时间分辨富里叶红外发射谱仪（ＴＲ－ＦＴＩＲＳ）研究了ＣＨ２（Ｘ＾３Ｂ１）自由基与Ｏ２反应的通道及产物的振动动态布居，基电子态自由基ＣＨ２（Ｘ＾３Ｂ１）由３５１ｎｍ紫外激光光解ＣＨ２ＣＯ生成，观测到振动发态反应产物ＣＯ（ｖ≤１０），ＣＯ２（ｖ３≤７）ＯＨ（Ｈ２Ｏ）和Ｈ２ＣＯ的红外发射，证实存在生成Ｈ２ＣＯ的通道，由光谱拟合得到不同时刻ＣＯ（ｖ）和ＣＯ２（ｖ３）的相对振动布居，发现ｖ＝４能级的布居数     

低镍催化剂上CO和CO_2加氢反应的对比研究

采用ＣＯ和ＣＯ＿２对比加氢活性测试，ＸＲＤ及ＴＰＲ方法研究了两个不同Ｎａ助剂含量的低镍Ｎｉ／Ａｌ＿２Ｏ＿３体系的性能。实验发现，在低镍催化剂上ＣＯ＿２在较低温度下就可加氢生成甲烷，而ＣＯ则需要更高的温度，ＣＯ＿２无需先经逆变换生成ＣＯ，然后再加氢，它可直接加氢生成ＣＨ＿４。在同一催化剂上，ＣＯ＿２加氢生成ＣＨ＿４的表现活化能要低于ＣＯ加氢生成ＣＨ＿４反应的表现活化能。晶相ＮｉＯ还原后形成的活性相对ＣＯ＿２加氢反应的活性明显高于它对ＣＯ的加氢活性，非晶相镍氧化物还原后形成的活性相对ＣＯ的加氢反应特别有利。Ｎａ助剂的含量不同会造成Ｎｉ氧化物物种的分配不同，从而导致ＣＯ、ＣＯ＿２的加氢活性及其随温度的变化也不相同，催化剂对ＣＯ、ＣＯ＿２加氢反应作用的本质是不相同的。     

超临界CO2+EtOH+CO+H2四元体系压力和温度变化规律及超临界性质的研究

在5～11MPa的范围内,利用恒容静态平衡法详细考察了CO2密度在0.542～0.590g/cm3范围的不同组成的超临界CO2+EtOH+CO+H2四元体系的压力和温度的变化规律,并测定了相应的临界温度和临界压力.模拟了超临界丙烯氢甲酰反应体系的相行为.结果发现,CO+H2加入量的增多可明显改变超临界CO2+EtOH+CO+H2四元体系的超临界性质,主要表现为该体系的临界温度随着CO和H2摩尔分数的增加而线性降低,临界压力随着CO和H2摩尔分数的增加而线性增加.在相同的CO和H2组成下,超临界四元体系的压力随着体系温度的增加而线性增加,并且p-T线的斜率基本相同.在相同温度下超临界四元体系的压力随着体系中CO和H2摩尔分数的增加线性增加,并且不同温度时的变化率基本相同.     

固定床反应器中添加CO2对费托合成反应的影响

用固定床反应器研究了Fe-Mn催化剂上原料气中添加CO2对费托合成反应的影响.结果表明,在533K与反应总压为1.50MPa时,大量CO2的添加使得生成CO2的选择性迅速降低,烃的生成速率降低,烃的收率也有所降低,产物向轻组分方向偏移,有机含氧化合物的生成速率降低;在593K与合成气(H2 CO)分压为1.50MPa时,随着CO2分压的增加,CO消耗速率变化不大,而烃的生成速率缓慢升高,烃的收率有所升高,CO2的生成速率缓慢降低,H2O的生成速率明显加快.由于CO2的添加,促使水煤气变换反应向逆反应方向进行,降低了催化剂表面氢物种浓度,抑制了加氢反应,低碳烃的烯/烷比有所增大,同时提高了重质烃的选择性,且随着CO2分压的增加,有机含氧化合物的生成速率呈上升的趋势.     

STUDIES ON FISCHER TROPSCH SYNTHESIS OVER Fe-Cu-K CATALYST Ⅰ.CATALYTIC PERFORMANCE

The influence of reaction pressure, temperature, space velocity (GHSV), particle size of catalyst and H2/CO ratio of feed-gas on the steady-state product distribution, conversion of CO, H2 and syngas, olefin to paraffin ratio and CO2/ H2O ratio for FTS reaction were investigated using a coprecipitated copper- potassium promoted iron catalyst. The test was carried out in a fixed-bed reactor. Increasing the reaction temperature from 493. 2 to 5-13. 2 K shifted the hydrocarbon distribution toward the heavier hydrocarbons (C5-C23) and selectively increased CO conversion to CO2. The hydrocarbon distribution was found to be dependent on the H2/CO feed-gas ratio in the range from 1.23 to 2. 22. The CO2/H2O ratio in product decreased as the flow of feed-gas rate increased, which suggests that H2O is a primary product and its reaction with CO to form CO2 occurs via a secondary process. The CO conversion increased with the decrease of catalyst particle size from 10 to 60 mesh (2. 0- 0. 3 mm), while the CO convers     

H原子与CO2分子碰撞的化学反应与能量转移

Collisions between hot H atoms and CO2 molecules were studied experimentally by time-resolved Fourier transform infrared emission spectroscopy. H atoms with three translational energies, 174.7, 241.0 and 306.2 kJ/mol respectively, were generated by UV laser photolysis to initiate a chemical reaction of H+CO2!OH+CO. Vibrationally excited CO (v≤2) was observed in the spectrum, where CO was the product of the reaction. The highly efficient T-V energy transfer from the hot H atoms to the CO2 was verified too. The highest vibrational level of v=4 in CO2 (v≤3) was found. Rate ratio of the chemical reaction to the energy transfer was estimated as 10.     

CO在负载铂催化剂上的催化氧化,TPD及TPSR研究

研究了Pt/MeM(Me=H,Cu,Ce)系列催化剂对CO的催化氧化活性,用热导-气相色谱同步跟踪CO在MeM和Pt/MeM上的TPD,发现CO_2脱附量大小及峰温次序与对CO的催化氧化活性一致。CO吸附达稳态后的TPSR(CO_2)研究表明CO_2的脱附峰温较TPD低,且其脱附量大小、峰温次序亦与对CO的催化氧化活性次序一致。     

A solid molecular basket sorbent for CO2 capture from gas streams with low CO2 concentration under ambient conditions

In this paper, a solid molecular basket sorbent, 50 wt% PEI/SBA-15, was studied for CO(2) capture from gas streams with low CO(2) concentration under ambient conditions. The sorbent was able to effectively and selectively capture CO(2) from a gas stream containing 1% CO(2) at 75 °C, with a breakthrough and saturation capacity of 63.1 and 66.7 mg g(-1), respectively, and a selectivity of 14 for CO(2)/CO and 185 for CO(2)/Ar. The sorption performance of the sorbent was influenced greatly by the operating temperature. The CO(2)-TPD study showed that the sorbent could be regenerated under mild conditions (50-110 °C) and was stable in the cyclic operations for at least 20 cycles. Furthermore, the possibility for CO(2) capture from air using the PEI/SBA-15 sorbent was studied by FTIR and proved by TPD. A capacity of 22.5 mg g(-1) was attained at 75 °C via a TPD method using a simulated air with 400 ppmv CO(2) in N(2).