CeO2-La2O3/γ-Al2O3稀土氧化物混合物催化还原SO2的实验研究

在La₂O₃ 中加入变价稀土氧化物CeO₂,组成一种稀土氧化物的混合物,以这种混合物作为CO还原SO₂的催化剂.采用连续流动固定床反应器,在反应气体SO₂和CO按SO₂∶CO = 1∶3,载流气体为N₂,气体流量为1000 mL/min的条件下,实验研究了该催化剂的活化过程以及温度和反应物浓度配比对活化反应的影响,用XRD和XPS对反应前后催化剂进行了表征,分析了相结构的变化.结果表明:CeO₂和La₂O₃ 2种稀土氧化物的混合物,在CO还原SO₂的催化反应中,活化温度比单个的CeO₂或La₂O₃氧化物下降了50℃～100℃,而且具有更高的活性.这可能是CeO₂和La₂O₃氧化物之间存在着某种协同作用所致.     

淡水沼泽湿地CO2、CH4和N2O排放通量年际变化及其对氮输入的响应

利用静态暗箱-气相色谱法自2002～2004年连续3a观测了三江平原淡水沼泽湿地CO₂、CH₄和N₂O 3种主要温室气体排放特征及外源氮素输入条件下温室气体通量的变化.结果表明,三江平原CO₂、CH₄和N₂O 3种主要温室气体排放具有明显的季节及年际变化规律.其中生态系统呼吸CO₂排放的最大值[779.33～965.40 mg·(m·h)^-1]出现在7、8月份,CH4通量最大值[19.19～30.52 mg·(m·h)^-1]出现在8月,N₂O通量最大值[0.072～0.15 mg·(m·h)^-1]出现在5月和9月,3种温室气体通量最小值CO₂为2.36～18.73 mg·(m·h)^-1;CH₄为-0.35～0.59 mg·(m·h)^-1;N₂O为-0.032～-0.009 mg·(m·h)^-1大都出现在冬季,且冬季淡水沼泽湿地表现为N2O的吸收.对气候因子的分析发现,温度条件是影响淡水沼泽湿地温室气体排放通量季节性变化的主要因子,而降水和积水水位变化是影响其排放年际变化的关键因素,特别是降水对CH₄排放通量的影响较其它2种温室气体更显著,且冬季雪融水对夏季CH₄的排放起重要作用.CO₂和CH4排放与土壤温度(5cm)呈显著的指数相关关系,而N₂O排放通量与土壤温度和水深相关性不显著.氮输入促进了三江平原CO₂、CH₄和N₂O 3种主要温室气体的排放,与对照处理相比,其排放通量分别升高了34%,145%和110%.     

Oxidation of diesel soot on binary oxide CuCr(Co)-based monoliths

Binary oxide systems(Cu Cr2O4, Cu Co2O4), deposited onto cordierite monoliths of honeycomb structure with a second support(finely dispersed Al2O3), were prepared as filters for catalytic combustion of diesel soot using internal combustion engine’s gas exhausts(O2, NOx, H2 O, CO2) and O3 as oxidizing agents. It is shown that the second support increases soot capacity of aforementioned filters, and causes dispersion of the particles of spinel phases as active components enhancing thereby catalyst activity and selectivity of soot combustion to CO2. Oxidants used can be arranged with reference to decreasing their activity in a following series: O3 NO2> H2 O > NO > O2> CO2. Ozone proved to be the most efficient oxidizing agent: the diesel soot combustion by O3 occurs intensively(in the presence of copper chromite based catalyst) even at closing to ambient temperatures.Results obtained give a basis for the conclusion that using a catalytic coating on soot filters in the form of aforementioned binary oxide systems and ozone as the initiator of the oxidation processes is a promising approach in solving the problem of comprehensive purification of automotive exhaust gases at relatively low temperatures, known as the "cold start" problem.     

环戊烯臭氧化反应瞬变物种产生机制

大气中烯烃臭氧化反应产物是二次有机气溶胶(SOA)形成的重要前体物. 运用自行组建的低温基质隔离系统研究环戊烯臭氧化反应的瞬变物种产生机制. 采用程序升温方法,将温度从6 K升至115 K,用傅里叶红外光谱仪检测不同温度下生成的活性中间体,并将试验值与理论计算值、文献报道值进行对比,以确定中间体构型. 结果表明:环戊烯臭氧化反应生成的中间体——POZ(初级臭氧化物)、SOZ(二次臭氧化物)和CI(一分子羰基氧化物和一分子醛或酮)被成功检测到. 其中,POZ的特征吸收峰在705和946 cm-1处,对应O—O—O反对称伸缩振动和环变形振动;SOZ特征吸收峰在939 cm-1处,对应C—O伸缩振动;CI的特征吸收峰在1 733和853 cm-1处,分别对应CO伸缩振动和O—O伸缩振动. 据此,环戊烯臭氧化反应遵循Criegee机制. 采用4种量子化学计算方法——B3LYP/6-311++G(d,2p)、B3LYP/6-311++G(3df,3pd)、MP2/aug-cc-pvdz和PW91PW91/6-311++G(3df,3pd),计算POZ、SOZ和CI特征吸收峰的振动频率,其中POZ在705 cm-1处吸收峰的振动频率计算值分别为725、698、703、680 cm-1;SOZ在1 030 cm-1处吸收峰的振动频率计算值分别为1 017、1 018、1 025和993 cm-1;CI在1 733 cm-1处吸收峰的振动频率计算值分别为1 796、1 803、1 732和1 745 cm-1.表明MP2/aug-cc-pvdz计算的特征振动频率与试验值最接近.      

稀土钙钛矿型催化剂对CO催化氧化活性及表面氧种的研究

研究了CO在不同催化剂La1 -xSrxMn1 -xBxO3(B =Fe、Ni、Cr)上的氧化反应活性 ,并利用程序升温热脱附(TPD)的方法对不同x值催化剂表面氧种及其含量的变化规律进行了考察 ,结合反应活性及表面吸附氧种随x值的变化规律 ,研究了催化剂对CO氧化反应的活性与表面活性氧种的关系。     

金催化剂在活性碳上负载活性的研究

探索了以活性炭为载体制备负载型金催化剂的可行性。大量实验表明,将金直接负载在活性炭上,不能够得到具有很好催化活性的催化剂。而以MOx/C作为复合载体能够制备得到具有较高催化活性的金催化剂。进一步探讨了焙烧条件,以及不同载体材料对金催化剂活性的影响。     

Au负载OMS-2催化剂的制备及其低温催化氧化性能

通过前掺杂法(QI),浸渍法(IM)和沉积-沉淀法(DP)3种方法制备了Au负载氧化锰八面体分子筛(OMS-2)Au/OMS-2催化剂,研究了制备方法和制备条件对其催化氧化CO活性的影响.采用X射线衍射(XRD)和BET比表面积测定等技术对所制样品进行表征.结果表明,沉积-沉淀法制备的Au/OMS-2-DP催化剂活性明显高于前掺杂法和浸渍法制备的催化剂,这与Au/OMS-2-DP催化剂比表面积较大和负载Au颗粒较小有关.制备条件(沉淀剂种类、制备溶液pH、Au负载量和催化剂焙烧温度)明显影响Au/OMS-2-DP催化剂的催化活性.对于各种不同的沉淀剂,以KOH为沉淀剂制备的催化剂活性最高,这可能与其无钝化作用,而且形成的Au颗粒较小有关;制备溶液的为最佳,当pH值过高或过低容易导致Au颗粒的聚集和Au沉淀量较少;XRD结果表明,当Au负载量为5wt%催化剂和催化剂焙烧为300℃时,所制备的催化剂颗粒最小,所得的催化剂活性最高.最佳条件制备的Au/OMS-2-DP催化剂活性较好,CO完全转化(100%)的温度为67℃.     

氢氟烃HFC－134a的分解实验研究

该研究进行了氢氟烃HFC－134a的催化分解和化学分解实验。实验结果表明无催化剂时HFC－134a很稳定,即使升温至500℃时也下会分解:在空气和水蒸汽存在下HFC－134a催化分解成CO和CO₂。CFC－12比HFC－134a易分解,反应产物只有CO₂。分解产物HF对催化剂有强烈的失活作用;超氧离子(O₂￣－)对液相中的HFC－134a具有很强的氧化分解能力。在常温下几乎可完全分解高浓度的HFC－134a。      

CoTPPS4催化处理敌敌畏生产废水的研究

用CoTPPS4作催化剂,Na2S2O8/H2O2为混合氧化剂处理含DDVP农药生产废水.探讨了氧化刺种类、混合氧化剂比例、催化剂投加量、农药初始浓度和pH值等因素对催化处理活性的影响,并对催化处理反应动力学进行了研究.结果表明,在pH＝9溶液中,农药初始浓度为28.93 mg/L、CoTPPS4加入量为2.4×10-...     

制备方法条件对Au/CeO2催化CO低温氧化性能研究

用共沉淀法和沉积沉淀法制备了负载型Au/CeO2催化剂,考察了不同制备方法和条件对Au/CeO2催化剂活性的影响。结果表明,制备方法和条件对Au/CeO2催化剂的活性有较大的影响,其中以Na2CO3为沉淀剂的共沉淀法制备的Au/CeO2催化剂活性最佳。最佳制备条件:343K洗涤、473K焙烧、空气预处理。金和部分氧化态的金是活性中心,而且氧化态的金催化活性更好。活性位在金与氧化物载体界面,金粒径越小,金与氧化物载体的接触面越大,活性位越多,催化活性越大。     

微波诱导催化剂Fe_2O_3/Al_2O_3制备及PEG对其活性影响

以AlCl·36H2O、FeCl·36H2O和CO(NH)22为原料,采用均匀沉淀法制备微波诱导催化剂Fe2O3/Al2O3,用X射线衍射仪(XRD)对其结构进行了表征,研究了加入聚乙二醇(PEG200)作为分散剂对产物的影响。结果表明:加入体积分数为0.05%PEG后,对于20mg/L的甲基橙模拟废水,在微波功率为900W,催化剂投加量为2g/L,处理5min后脱色率可达95.8%。     

Toluene decomposition performance and NOx by-product formation during a DBD-catalyst process

Characteristics of toluene decomposition and formation of nitrogen oxide(NOx) by-products were investigated in a dielectric barrier discharge(DBD) reactor with/without catalyst at room temperature and atmospheric pressure. Four kinds of metal oxides, i.e., manganese oxide(Mn Ox), iron oxide(Fe Ox), cobalt oxide(Co Ox) and copper oxide(Cu O), supported on Al2O3/nickel foam, were used as catalysts. It was found that introducing catalysts could improve toluene removal efficiency, promote decomposition of by-product ozone and enhance CO2 selectivity. In addition, NOx was suppressed with the decrease of specific energy density(SED) and the increase of humidity, gas flow rate and toluene concentration, or catalyst introduction. Among the four kinds of catalysts, the Cu O catalyst showed the best performance in NOx suppression. The Mn Ox catalyst exhibited the lowest concentration of O3 and highest CO2 selectivity but the highest concentration of NOx. A possible pathway for NOx production in DBD was discussed. The contributions of oxygen active species and hydroxyl radicals are dominant in NOx suppression.     

Catalytic reduction of nitric oxide with carbon monoxide on copper-cobalt oxides supported on nano-titanium dioxide

A series of copper-cobalt oxides supported on nano-titanium dioxide were prepared for the reduction of nitric oxide with carbon monoxide and characterized using techniques such as XRD, BET and TPR. Catalyst CuCoOx/TiO2 with Cu/Co molar ratio of 1/2, Cu- Co total loading of 30% at the calcination temperature of 350°C formed CuCo2O4 spinel and had the highest activity. NO conversion reached 98.9% at 200°C. Mechanism of the reduction was also investigated, N2O was mainly yielded below 100°C, while N2 was produced instead at higher temperature. O2 was supposed to accelerate the reaction between NOx and CO for its oxidation of NO to give more easily reduced NO2, but the oxidation of CO by O2 to CO2 decreased the speed of the reaction greatly. Either SO2 or H2O had no adverse impact on the activity of NO reduction; however, in the presence of both SO2 and H2O, the catalyst deactivated quickly.     

Combination of biodiesel-ethanol-diesel fuel blend and SCR catalyst assembly to reduce emissions from a heavy-duty diesel engine

In this study, the efforts to reduce NOx and particulate matter （PM） emissions from a diesel engine using both ethanol-selective catalytic reduction （SCR） of NOx over an Ag/Al2O3 catalyst and a biodiesel-ethanol-diesel fuel blend （BE-diesel） on an engine bench test are discussed. Compared with diesel fuel, use of BE-diesel increased PM emissions by 14% due to the increase in the soluble organic fraction （SOF） of PM, but it greatly reduced the Bosch smoke number by 60%-80% according to the results from 13-mode test of European Stationary Cycle （ESC） test. The SCR catalyst was effective in NOx reduction by ethanol, and the NOx conversion was approximately 73%. Total hydrocarbons （THC） and CO emissions increased significantly during the SCR of NOx process. Two diesel oxidation catalyst （DOC） assemblies were used after Ag/Al2O3 converter to remove CO and HC. Different oxidation catalyst showed opposite effect on PM emission. The PM composition analysis revealed that the net effect of oxidation catalyst on total PM was an integrative effect on SOF reduction and sulfate formation of PM. The engine bench test results indicated that the combination of BE-diesel and a SCR catalyst assembly could provide benefits for NOx and PM emissions control even without using diesel particle filters （DPFs）.     

光化学烟雾箱的表征及初步应用

介绍了一套自制的用于光化学臭氧和二次有机气溶胶生成研究的室内烟雾箱系统,对该烟雾箱系统进行了一系列表征实验,包括活性物种的壁损失速率常数的测定,以及由CO-NOx光氧化实验确定的反应器内·OH源,并进行了乙烯-NOx和苯-NOx光氧化的初步实验.结果表明,O3和NO2在新反应袋中壁损失受湿度影响很小,而在旧反应袋中影响...     

Cu/ZrO2/S2O2-8/γ-Al2O3固体酸催化剂制备与催化选择还原NO性能

以拟薄水铝石焙烧得到的γ-Al2O3为载体,分步浸渍负载（NH4）2S2O8、ZrOCl2和Cu（NO3）2,制成Cu/ZrO2/S2O28-/γ-Al2O3固体酸催化剂.考察了Cu/ZrO2/S2O8^2-/γ-Al2O3在富氧条件下对C3H6选择还原NO的催化性能,并借助SEM、XRD、Py-IR和TPR等表征方法研究了它的结构和性能的关系.性能的实验结果表明,Cu/ZrO2/S2O28-/γ-Al2O3在无水条件下能使NO的最大转化率达到82.9%,在有10%水蒸气存在条件下仍能使NO的最大转化率达到80.2%.表征测试的结果表明,S2O8^2-和ZrO2能够抑制γ-Al2O3颗粒之间的烧结及CuAl2O4尖晶石相的生成,同时促使催化剂表面新酸性中心（B酸）的形成及总酸量的增加,另外ZrO2还能提高Cu物种的还原性,从而有效地改善了催化剂的催化活性和水热稳定性.     

Ce改性Mn系催化剂结构及低温催化活性影响研究

采用浸渍法制备了Ce改性负载型Mn系TiO 2催化剂,考察了Ce负载量、反应温度等因素对催化剂效率以及选择性的影响,利用扫描电镜、氮气物理吸附(N 2-TPD)等表征手段分析了Ce/TiO 2催化剂催化活性影响机理。结果表明:改性催化剂在Ce/Ti摩尔比为0.08的条件下表现出最佳的脱硝效率及NO选择性;MnCe(0.08)Ti催化剂在180℃条件下的脱硝效率超过85%,而N 2 O体积分数仅为24×10-6(47.1 mg/m 3);Ce的加入优化了催化剂表面的孔隙结构,比表面积与和孔容积分别达到121.11 m 2/g、1.71 cm 3/g;MnCe(0.08)Ti催化剂在210℃通入体积分数为300×10-6(857.1 mg/m 3)的SO 2和8%的水蒸气,连续运行180 h过程中的脱硝效率均可保持在80%以上,具有良好的抗硫性和稳定性。     

Coupling catalytic hydrolysis and oxidation for CS2 removal

CS2 removal was Obtained by coupling catalytic hyidation on bi-functional catalyst.On the hydrolysis active sites,CS2 is hydrolyzed to H2S,while on the oxidation active sites,H2S is oxidized to elemental S or sulfuric acid deposited on the porous support.The above process can be expressed as followsCS2→H2O COS →H2O H2S→O2 S/SO2- 4.H2S oxidation eliminates its prohibition on CS2 hydrolysis so that the rate of coupling removal CS2 is 5 times higher than that of CS2 hydrolysis.The same active energy of hydrolysis and coupling reaction also indicates that H2S oxidation does not change the reaction mechanism of CS2 hydrolysis.Temperature has obvious effect on the process while the mole ratio of O2 concentration to CS2 concentration (O/S) does not,especially in excess of 2.5.The formation of sulfuric acid on the catalyst surface poisons hydrolysis active sites and causes the decrease of left OH-1 concentration on the catalysts surface.Lower temperature is suggested for this bi-functional catalyst owing to the low yield ratio of S/SO4 2-.     

羊草草原和贝加尔针茅草原生态系统呼吸的差异分析

应用静态暗箱-气相色谱法对羊草草原和贝加尔针茅草原的生态系统呼吸CO2通量进行了测算,分析了生态系统呼吸的影响因素,比较了2种草原生态系统呼吸的差异并分析了产生差异的原因.观测期间羊草草原生态系统呼吸CO2通量平均为(12.03±2.10)mg·(m2·min)-1,显著低于贝加尔针茅草原[(20.09±4.41)mg·(m2·min)-1];而羊草草原生物量显著大于贝加尔针茅草原(p0.001).羊草草原和贝加尔针茅草原生态系统呼吸都与温度(箱内气温、5cm和15cm地温)具有显著的指数函数关系.通过偏相关分析发现,在地温作为控制变量时,生态系统呼吸与土壤Eh、pH间不再具有显著的相关性,Eh、pH对CO2通量的影响可能是由地温变化间接引起的,而CO2通量与活体生物量呈现出了一定的相关性,与凋落物生物量无显著相关性.2种草原的CO2通量都可以用温度指数模型进行很好地模拟,基于地温的模拟效果(R2为0.568～0.639)显著好于基于箱内气温的(R2为0.323～0.426).地温是2种草原生态系统呼吸最重要的影响因素,它掩盖了地上部植物体对生态系统呼吸的影响.在该区域,土壤呼吸占生态系统呼吸比例较高,贝加尔针茅草原较高的有机质含量导致了其生态系统呼吸CO2通量较高.     

季节性冻融期沼泽湿地CO2、CH4和N2O排放动态

三江平原季节性冻-融时间长达7～8个月,对沼泽湿地温室气体排放有重要影响.采用静态箱/气相色谱法研究了三江平原冻、融期沼泽湿地温室气体排放特征,表明三江平原不同类型沼泽湿地冬季都有明显的CH₄和CO₂排放,且冬季沼泽湿地CH₄排放量在全年CH₄排放中占有重要份额.融冻期沼泽湿地出现明显的CH₄和CO₂排放峰值,季节性积水沼泽化草甸CH₄和CO₂排放量大于常年积水沼泽湿地,而冬季常年积水沼泽湿地CH₄排放通量大于季节性积水沼泽化草甸.融冻期CO₂排放通量与土壤温度(5cm)呈指数相关关系(R²=0.912,p<0.001),沼泽湿地CO₂排放通量与CH₄通量间也呈显著正相关关系(R²=0.751,p<0.001).冬季三江平原沼泽湿地是N₂O的汇,融冻期随着土壤温度升高逐渐成为N₂O的源,且在5月份沼泽湿地表层土壤(0～20cm)融冻期间N₂O排放通量明显增大.三江平原土壤冻、融期间沼泽湿地温室气体的排放特征,反映了冬季微生物活性的存在及融冻作用对土壤碳矿化和氮硝化、反硝化作用有重要影响.