VOCs在吸附剂上吸附性能的热力学研究

采用色谱法与热重(TG)法,测量了正己烷、甲苯和乙酸乙酯在活性炭、5A、NaY、13X、ZSM-5 (SiO_2/Al_2O_3=27、300)、Hβ以及M CM-41等吸附剂上不同温度下的吸脱附行为,并基于反相气相色谱法测得的数据,计算了其吸附热力学参数ΔH、ΔS和ΔG,分析了上述VOCs分子与吸附剂之间的作用机制,并借助FT-IR验证了吸附质在分子筛表面的吸附机制。结果表明,上述吸附过程存在物理吸附和化学吸附两种方式,其中,物理吸附的作用力大小与吸附剂的孔径分布和分子直径相关,而化学吸附的作用力大小依赖于分子筛硅铝比和Ca~(2+)、Na~+、H~+等阳离子及吸附质分子的偶极矩,且强的化学吸附使得部分吸附质分子的脱附温度高于200℃。     

苯基键合高比表面积活性炭的制备及其对挥发性有机化合物的吸附性能研究

以核桃壳为原料,经过碳化、KOH活化, 制备了高比表面积活性炭,通过三甲基氧基苯基硅烷对活性炭表面进行改性,制得苯基键合高比表面积活性炭吸附材料.通过氮气吸附法测定了苯基键合活性炭的比表面积及孔径分布;采用红外光谱、X射线光电子能谱、X射线粉末衍射技术对苯基键合活性炭的有机官能团、表面元素的化学环境及晶体结构进行了表征.将该吸附材料制成采样管,吸附空气中的挥发性有机物,二硫化碳解吸后使用气相色谱进行分析.考察了苯基键合活性炭对乙醇、丙酮、正己烷、乙酸乙酯、四氢呋喃、1,2-二氯乙烷和苯共7种挥发性有机化合物(VOCs)的吸附性能,饱和吸附量在129~216 mg/g之间;在0.05~ 2.50 mg/mL范围内,7种组分的峰高与浓度呈良好的线性关系,检出限在0.92~3.60 mg/m3之间.     

改性活性炭热反应安全性研究

针对活性炭吸附VOCs过程的安全性问题进行了研究,采用咪唑-脯氨酸离子液体对活性炭进行改性,优化吸附性能。以典型的甲苯气体为例,讨论了改性前后活性炭结构的变化对甲苯吸附性能的影响,并探索了改性前后活性炭的热反应安全性。研究结果表明:咪唑-脯氨酸改性活性炭表面的孔隙数量增多、孔径变大、含氧官能团增加、比表面积和体积增大。改性活性炭对甲苯的吸附量78 mg·g~(-1)是改性前活性炭吸附量36.03 mg·g~(-1)的2.17倍,吸附能力明显提升;粒径为51μm和111μm的两种改性活性炭的自燃温度比未改性活性炭的自燃温度分别提高了22.4℃和19.4℃且到达自燃温度所需时间分别延长了11.17 h和0.75 h。改性活性炭所需活化能为47.32kJ·moL~(-1),热稳定性优于未改性活性炭。     

孔结构对活性炭吸附水溶液中铅离子的影响

选取三种表面化学性质相近的活性炭(AC),通过等温吸附实验考察活性炭对水溶液中铅离子的吸附性能,利用扫描电子显微镜(SEM)观察活性炭的表面微观形貌,通过低温(77 K)液氮吸附测定活性炭的比表面积和孔容,并分别以密度泛函理论(DFT)和Barrett-Joyner-Halenda (BJH)法计算微孔和中孔的孔径分布.结果表明:选用的三种活性炭AC1、AC2、AC3在比表面积和总孔容上呈依次下降的趋势,但表面开放孔均匀分布的AC2,具有最高的饱和吸附量,孔结构类似颗粒堆积孔的AC3,具有与表面开放孔分布集中的AC1相近的饱和吸附量;通过对孔结构与吸附量的关联分析可知,在活性炭吸附铅离子的过程中, 0.4-0.6 nm的孔是有效吸附孔, 10.5-20.6 nm、20.6-55.6 nm、5.2-10.5 nm三个区间的孔则会对吸附产生阻碍作用.     

一步法制备糖蜜基活性炭及其界面吸附行为

以糖厂废弃的糖蜜为原料,Na_2CO_3为活化剂,采用一步直接化学活化法制备了糖蜜基活性炭(AC).采用X射线衍射(XRD)、扫描电子显微镜(SEM)、N_2吸附-脱附及元素分析手段对产物进行了表征,证实其为多孔的石墨化碳材料,比表面积高达1023 m~2/g.研究了糖蜜基活性炭对溶液中的重金属离子Pb(Ⅱ)的脱除性能,结果表明:糖蜜基活性炭的吸附容量高于市售活性炭(CC),且所需吸附时间和投炭量均低于市售活性炭;其吸附动力学符合准二级动力学的Langmuir吸附,为单分子层的化学吸附;吸附Pb(Ⅱ)的糖蜜基活性炭可循环再生和重复使用.     

几种典型国产活性炭吸附各种烃类的NMR研究——Ⅱ.苯、环己烷、正戊烷和正己烷吸附的~1H NMR研究

活性炭吸附苯、环己烷、正戊烷和正已烷的测量表明,在同一种活性炭中各烃的饱和吸附体积相同,四种烃的吸附量与其摩尔体积成反比。同一种被吸附物在不同活性炭中的吸附量与各活性炭的比孔容和孔径分布有关。活性炭的比孔容大,且孔径小于30的微孔比例大时,其吸附和解吸容量也大。这些体系的~1H NMR研究进一步证实了孔径小于30的微孔中发生毛细管凝聚,导致吸附和解吸的容量增大。被吸附分子的自旋晶格弛豫时间几乎不随被吸附物的种类而异。他们与活性炭表面上酸性基团总量有较好的曲线关系。     

几种典型国产活性炭吸附各种烃类的NMR研究——Ⅱ. 苯、环己烷、正戊烷和正己烷吸附的1H NMR研究

活性炭吸附苯、环己烷、正戊烷和正已烷的测量表明, 在同一种活性炭中各烃的饱和吸附体积相同, 四种烃的吸附量与其摩尔体积成反比。同一种被吸附物在不同活性炭中的吸附量与各活性炭的比孔容和孔径分布有关。活性炭的比孔容大, 且孔径小于3.0 nm的微孔比例大时, 其吸附和解吸容量也大。这些体系的~1H NMR研究进一步证实了孔径小于3.0 nm的微孔中发生毛细管凝聚, 导致吸附和解吸的容量增大。被吸附分子的自旋晶格弛豫时间几乎不随被吸附物的种类而异。他们与活性炭表面上酸性基团总量有较好的曲线关系。     

四氟硼酸改性活性炭的制备及其吸附脱除二苯并噻吩性能

采用浸渍法制备了四氟硼酸(HBF₄)改性活性炭,并研究了其对模拟油中二苯并噻吩(DBT)的吸附脱除性能。利用傅里叶红外光谱(FT-IR)、差示热分析仪(TG-DTA)、X射线光电子能谱(XPS)以及N₂吸附技术对吸附剂的表面态和孔结构进行了表征,考察了四氟硼酸浓度、热处理温度以及模拟油中DBT浓度对吸附脱硫效果的影响。结果表明,经质量分数0.5%的HBF₄溶液浸渍、140 ℃热处理后,在剂油比1:100条件下,活性炭的吸附容量为352 mg/g,较未改性活性炭提高了72.5%。     

氧化多壁碳纳米管对Pb~(2+)的吸附性能研究

该文研究了氧化多壁碳纳米管(o-MWNTs)对Pb2+的吸附性能,考察了平衡时间、溶液pH值、溶液体积等因素对吸附行为的影响。在静态吸附条件下:Pb2+能大量并快速地被o-MWNTs吸附,45 min内即可达到吸附平衡,而活性炭(ACs)的吸附平衡时间为90 min。溶液pH值在1.0~7.0范围对吸附量有显著影响,在pH5.0~6.0时o-MWNTs对Pb2+的静态吸附容量为17.43 mg.g-1。o-MWNTs对铅离子的吸附量随着溶液体积的增加而增加,并逐渐趋于稳定,最大吸附量可达25 mg.g-1。在动态吸附实验中,30 mg.L-1的铅离子溶液在SPE小柱的穿透体积为235 mL,溶液体积为400 mL时可完全穿透。动态吸附实验表明,o-MWNTs对铅离子具有较大的吸附容量且萃取回收率高达94%。研究表明,氧化碳纳米管装填的固相萃取小柱可用于中药提取物中Pb2+的残留分析。     

CuCl_2/13X催化剂在乙炔氢氯化反应中的应用

将13X分子筛与氯化铜活性组分相结合,制备了稳定性和选择性优异的乙炔氢氯化反应催化剂CuCl_2/13X.系统考察了氯化铜负载量、反应温度、反应气空速、预处理温度对CuCl_2/13X催化剂反应性能的影响.发现经300℃预处理后,在反应温度220℃和乙炔空速30 h~(-1)条件下,氯化铜负载量25%的25CuCl_2/13X催化剂具有最佳的反应性能,乙炔转化率高于78%、氯乙烯选择性超过99%,反应16 h后催化剂的活性和选择性稳定且略有升高.运用低温氮气物理吸附、穿透实验、热重分析以及X射线衍射分析等手段对催化剂及反应过程进行了表征.分析了反应条件对结果产生影响的原因,并发现催化剂对HCl的强吸附性能和13X与氯化铜之间的相互促进作用,是CuCl_2/13X性能优于CuCl_2/AC的原因.     

Zeolites modified by CuCl for separating CO from gas mixtures containing CO2

Although zeolites such as NaY and 13X adsorb CO₂ much more than CO, the adsorption amount of CO₂ and CO can be reversed if the zeolites are modified with CuCl. When zeolite NaY or 13X is mixed with CuCl and heated, high CO adsorption selectivity and capacity can be obtained. Isotherms show the adsorbents have CO capacity much higher than CO₂. This is because CuCl has dispersed onto the surface of the zeolites to form a monolayer after the heat treatment and the monolayer dispersed CuCl can provide tremendous Cu(I) to selective adsorb CO and inhibit the CO₂ adsorption. The monolayer dispersion of CuCl is confirmed by XRD and EXAFS studies. The loading of CuCl on the zeolites has a threshold below which the CuCl forms monolayer after heating and crystalline phase of CuCl can not be detected by XRD. An adsorbent of CuCl/NaY with CuCl content closed to the monolayer capacity shows very high CO selective adsorbability for CO₂, N₂, H₂ and CH₄. At temperature higher than room temperature, the adsorbent has even better CO selectivity for CO₂. Using the adsorbent, a single-stage 4 beds PSA process, working at 70°C and 0.4 MPa to 0.013 MPa, can obtain CO product with purity >99.5% and yield >85%.     

Adsorption and solvent desorption behavior of ion-exchanged modified Y zeolites for sulfur removal and for fuel cell applications

Typical ion-exchanged modified Y zeolites (AgY and CeY) were prepared for sulfur removal. The adsorption and desorption behavior of typical sulfur and hydrocarbon molecules in various Y zeolites has been investigated by the adsorption breakthrough and on site solvent washing experiments, as well as computer simulation. Breakthrough experiments showed that the adsorption capacity for thiophenic sulfur increased for the studied adsorbents as follows: CeY > AgY > NaY. The higher initial sulfur concentration accelerated the appearance of breakthrough, and the outlet sulfur concentration, in all cases, cannot reach the corresponding initial sulfur level. The concentration profile of washing solvent during desorption process showed that most of the sulfur compounds could be recovered at initial desorption stage. The desorption rates of typical Y zeolites follow the order: NaY > AgY > CeY, which is the reverse as that found in adsorption capacity. The distinct adsorption and desorption behavior of CeY, AgY, and NaY zeolites was markedly related with their various binding force (S-M coordination, π-complexation, and Van der Waals force) with sulfur compounds. The adsorption isotherms and density distribution snapshots study by computer simulation confirmed the preferential adsorption of thiophenic sulfur.     

原位水热合成Ce(Ⅳ)-X分子筛及对噻吩的吸附性能

通过原位水热合成方法直接制备出不同载Ce量的Ce(Ⅳ)-X分子筛,并考察了其对模拟汽油中噻吩的吸附性能。采用粉末X射线衍射(XRD)、傅里叶变换红外(FT-IR)、紫外-可见漫反射(UV-vis DRS)、全谱直读等离子体原子发射光谱(ICP-AES)、氮气吸附和NH₃程序升温热脱附(NH₃-TPD)等方法对分子筛进行表征。结果表明,合成分子筛均具备典型的X型分子筛结构,同时Ce(Ⅳ)被较好地引入到分子筛的骨架结构中;载Ce分子筛的酸性大于X分子筛,而且Ce(Ⅳ)-X分子筛的酸性随着Ce掺杂量的增加而增强。吸附实验表明,载Ce分子筛对噻吩的吸附性能明显好于X分子筛。其中,n(Ce)/n(Si)=0.05的分子筛脱硫效果最佳,饱和吸附容量达到52.541 9 mg/g。再生实验表明,加热再生的Ce(Ⅳ)-X分子筛对噻吩仍具有理想的吸附效果。n(Ce)/n(Si)=0.05的分子筛再生后饱和吸附容量为47.512 1 mg/g,约为新鲜吸附剂的90.43％。     

Inverse GC Investigation of the Adsorption of Thiophenic Compounds on Zeolites

Inverse gas chromatography (IGC) has been used to examine the adsorption of organo-sulfur compounds on various zeolites. Results obtained were used to explain the behaviour of these materials as adsorbents for ultra-deep desulfurisation of fuels. The model compounds chosen were thiophene and 2,5-dimethylthiophene, with zeolite adsorbents NaX, HX, NaY and HY. Zeolite NaY showed the largest adsorption capacity. Adsorption isotherms in the gas phase are not representative of saturation adsorption in the liquid phase. However, the heat of adsorption and the specific interaction parameter were found to be well correlated to the strength and the selectivity of adsorption in the liquid phase by the different zeolites. The main conclusion of this work is that IGC is a useful tool for preliminary comparison of different adsorbents for the removal of sulfur compounds from fuels.     

晶种法合成UZM-9分子筛及其CO2/CH4/N2吸附分离性能

以TEAOH和TMAOH为有机模板剂,酸处理的UZM-9分子筛为晶种,采用水热法在48 h内合成出分子筛UZM-9,并对其CO₂/CH₄/N₂的吸附分离性能进行了研究。采用XRD、ICP、TG、SEM与气体吸附等手段对晶种法合成的UZM-9分子筛结构、耐水稳定性与吸附性能进行了研究。结果表明,晶种法可以在2 d内合成出硅铝原子比在3以上、收率达到65%的UZM-9分子筛;所得分子筛的CO₂吸附容量可以达到5 mmol/g以上,吸附热为34 kJ/mol,CO₂/CH₄、CO₂/N₂与CH₄/N₂的平均分离因子分别为100、240与2.4,CO₂分离性能优良且具有一定耐水性能。     

Equilibrium and kinetic analysis of CO2-N2 adsorption separation by concentration pulse chromatography

CO2 and N(2) adsorption kinetics and equilibrium behaviours have been studied with silicalite, NaY and 13X by using concentration pulse chromatography for the separation of these gases in the present study. Adsorption Henry's Law constants, the heat of adsorption values, micropore diffusion coefficients and corresponding activation energies are determined experimentally and the three different mass transfer mechanisms are discussed. From the equilibrium data, the corresponding separation factors are obtained for the adsorption separation processes. The heat of adsorption values as well as the Henry's Law adsorption equilibrium constants of CO(2) are much higher than those of N(2) for all the adsorbents studied. 13X, NaY and silicalite all have good separation factors for CO(2)/N(2) system based on equilibrium processes. The order of the equilibrium separation factors is 13X (Ceca)>13X (Zeochem)>NaY (UOP)>silicalite (UOP). Equilibrium selectivity favours CO(2) over N(2). Micropore diffusion resistance is the definite dominant mass transfer mechanism for CO(2) with silicalite and NaY.     

负载型氨基酸离子液体的制备及其对二氧化碳的吸附性能

采用浸渍蒸发法将四甲基铵甘氨酸([N1111][Gly])和四甲基铵赖氨酸([N1111][Lys])两种离子液体分别负载到硅胶(SG)表面,利用EA、TGA、BET和FT-IR等技术对所得到的吸附剂进行表征,考察了离子液体种类、离子液体负载量和温度等条件对其CO_2吸附性能的影响。结果表明,离子液体成功负载到硅胶表面,所制得的负载型氨基酸离子液体对二氧化碳具有良好的吸附性能。在所考察的温度范围(303.15-323.15 K)内,温度越高,平衡吸附量越小;在负载量为10%-60%,随着负载量的增加,平衡吸附量先增加后减小。对于[N1111][Gly]/SG,当负载量为22.4%(质量分数)、吸附温度为30℃、压力为0.1 M Pa时,二氧化碳的平衡吸附量可达到41 mg/g(相对于1 mol AAILs吸附0.62 mol CO_2),而且,吸附20 min即可达到平衡吸附量的90%。吸附剂在循环使用六次之后,其结构与性能均保持良好。     

Adsorption of hydrogen isotopes on micro- and mesoporous adsorbents with orderly structure

The equilibrium and dynamic adsorption data of H(2) and D(2) on different micro- and mesoporous adsorbents with orderly structure including 3A, 4A, 5A, Y, and 10X zeolites; carbon CMK-3; silica SBA-15; and so forth were collected. Critical effect of the nanodimension of adsorbents on the adsorption behavior of hydrogen and its isotopes is shown. The highest adsorption capacity was observed at pore size 0.7 nm, but equal or even larger isotope difference in the equilibrium adsorption was observed at larger pore sizes, whereas the largest isotope difference in the dynamic adsorption was observed at 0.5 nm. The adsorption rate of D(2) is larger than that of H(2) in microporous adsorbents, but the sequence could be switched over in mesoporous materials. Linear relationship was observed between the adsorption capacity for hydrogen and the specific surface area of adsorbents although the adsorbents are made of different material, which provides a convincing proof of the monolayer mechanism of hydrogen adsorption. The linear plot for microporous adsorbents has a larger slope than that for mesoporous adsorbents, which is attributed to the stronger adsorption potential in micropores.     

环已胺在沸石分子筛上的吸脱附行为研究

本文以程序升温脱附(TPD)为主要实验手段,对环己胺在5种不同沸石分子筛上的吸脱附行为进行了研究。结果表明,沸石分子筛对环己胺有着较强的吸附作用,不同的沸石分子筛对环己胺的吸附能力受其结构和表面酸性特征的影响而异。有效吸附部位为与沸石分子筛表面酸性有关的弱化学吸附位;环己胺从不同沸石分子筛表面脱附的动力学与晶内扩散有关,其表观脱附活化能分别为:63.6kJ/mol(5A),68.6kJ/mol(13X),20.1kJ/mol(菱沸石),46.9kJ/mol(NaY)和47.3KJ/mol(ZSM-5)。