氧化铝上吸附平衡与动力学的分形特性

在实验测定氧化铝吸附氮气的平衡和动力学过程的基础上 ,由平衡数据得到分形维数 ,对动力学结果分别用欧氏几何和分形几何的动力学模型进行处理 ,比较两种方法得到的扩散系数之间的差别。结果表明 :粉状氧化铝的分形维数为 2 .12 ;采用分形动力学模型得到的扩散系数同欧氏几何扩散模型的结果不一样 ,扩散系数不随浓度的变化而改变 ;而欧氏几何扩散模型中的扩散系数随浓度变化发生改变 ,且变化符合Darken关系     

改性兰炭末对对硝基苯酚的吸附平衡和动力学

采用硝酸改性-高温活化法对废弃的兰炭末进行处理,对改性前后的兰炭末进行了SEM和BET表征,测定了改性后的兰炭末对对硝基苯酚的吸附性能,通过静态吸附实验研究了改性兰炭末对对硝基苯酚的吸附平衡和动力学特征。结果表明,兰炭末经改性后表面粗糙度明显增加,孔道明显增多,总孔容和比表面积分别增加了7.1倍和4.3倍; Langmuir方程可较好地描述对硝基苯酚在改性兰炭末上的吸附平衡,特征分离系数R_L为0~1,为优惠吸附,温度升高有利于吸附的进行;动力学研究表明,对硝基苯酚在改性兰炭末上的吸附过程符合HO准二级动力学模型,颗粒外的液膜扩散是决定吸附速率的控制步骤,吸附过程的表观活化能E_a为9.825kJ/mol。改性兰炭末对对硝基苯酚有较好的吸附能力,328K下平衡吸附量达158.5mg/g,可作为一种廉价、高效的酚类废水处理用吸附剂,有很好的工业化应用前景。     

Adsorption equilibrium of citric acid from supercritical carbon dioxide/ethanol on cyano column

Supercritical adsorption equilibrium has a significant role in defining supercritical adsorption behavior. In this paper, the adsorption equilibrium of citric acid from supercritical CO2/ethanol on a cyano column was systemat-ical y investigated with the elution by characteristic point method. Equilibrium loading was obtained at 313.15 K and 321.15 K with supercritical CO2/ethanol densities varying from 0.7068 g·cm?3 to 0.8019 g·cm?3. The exper-imental results showed that the adsorption capacity of citric acid decreased with increasing temperature and in-creasing density of the supercritical CO2/ethanol mobile phase. The adsorption equilibrium data were fitted wel by the Quadratic Hill isotherm model and the isotherms showed anti-Langmuir behavior. The monolayer satura-tion adsorption capacity of citric acid is in the range of 44.54 mg·cm?3 to 64.66 mg·cm?3 with an average value of 56.86 mg·cm?3.     

大孔树脂对竹叶总黄酮的吸附平衡和动力学

考察了7种大孔树脂对竹叶总黄酮的吸附及解吸特性,发现AB-8大孔树脂具有较高的吸附选择性和良好的脱附性能,并采用静态吸附实验研究了AB-8大孔树脂对竹叶总黄酮的吸附平衡和动力学特性。结果表明,Freundlich方程可较好地描述竹叶总黄酮在AB-8树脂上的吸附平衡;吸附自由能变?G<0,熵变?S>0,吸附为自发的熵增过程,升高温度有利于吸附分离。焓变?H为13.45 kJ/mol,在氢键键能范围内;吸附竹叶总黄酮前后树脂的红外谱图也表明,AB-8树脂对竹叶总黄酮分子的吸附是以氢键形式发生的物理吸附。动力学研究表明,吸附过程符合二级动力学方程,颗粒外的液膜扩散是决定吸附速率的主要步骤。     

活性炭改性及其对SO_2的吸附动力学与吸附平衡研究

在微波改性基础上,分别用KMnO_4、K_2Cr_2O_7和H_2O_2对椰壳活性炭进行氧化改性,采用BET和FTIR分析其表面物理化学性质,进行了吸附实验和吸附模型的研究。结果表明,活性炭改性后,微孔容积减小,平均孔径增大,含氧官能团含量增加;对SO_2的吸附动力学可通过粒内扩散和Bangham动力学模型较好的描述;微波分别与KMnO_4,K_2Cr_2O_7改性样品的吸附平衡能被Freundlich等温吸附模型较好的预测,而Langmuir等温吸附模型能准确预测微波与H_2O_2改性样品的吸附平衡,各样品Freundlich拟合常数n>1,故易于吸附SO_2。实验表明,活性炭改性有助于提高其对SO_2的吸附能力。     

乙醇在MIL-101上的吸附相平衡及其吸附机理

主要研究了MIL-101材料对乙醇的吸附性能和吸附机理。采用水热合成法制备了MIL-101(Cr),并分别应用N₂静态吸附、X射线粉末衍射(PXRD)、傅里叶红外光谱(FTIR)等分析手段对MIL-101晶形结构、孔隙结构参数进行分析表征。应用静态吸附法测定乙醇和水蒸气在不同温度下的吸附等温线,并讨论乙醇吸附在MIL-101(Cr) 4种吸附位的机理,根据吸附等温线估算出乙醇和水蒸气在MIL-101上的等量吸附热,并测试了乙醇在MIL-101上的吸附循环性能。研究表明,在298 K下,MIL-101的乙醇吸附容量为20.3 mmol·g^-1,远高于传统吸附材料。在低压下MIL-101对乙醇的吸附量高于水蒸气的吸附量,这是由于乙醇的偶极矩和分子动力学直径均比水大,使得乙醇分子在孔道中受到更大吸附力场作用;在低吸附量范围,乙醇在MIL-101上的等量吸附热要高于水蒸气的等量吸附热。在较高吸附压力条件下,主要发生多层吸附或孔填充,受吸附剂的孔容限制效应,尺寸越大的分子被吸附的物质的量会越少,由于乙醇的动力学直径(0.45 nm)大于水分子的动力学直径(0.268 nm),所以在较高吸附压力下乙醇在MIL-101上吸附量要小于水蒸气的吸附量。多次吸附脱附等温线测试显示MIL-101具有良好的乙醇吸附循环性能。     

硅胶表面上聚酰胺-胺的合成及其对Ag(I)的吸附

用硅烷偶联剂对硅胶表面进行氨基功能化,利用氨基与丙烯酸甲酯发生的Michael加成反应和乙二胺与酯进行的交换反应.在硅胶表面合成了聚酰胺-胺(PAMAM-SG)树状大分子,用红外光谱对PAMAM-SG的结构进行了表征.研究了溶液pH、浓度和吸附温度对PAMAM-SG吸附Ag(I)的影响.结果表明,溶液的最佳吸附pH值范围为4.0～7.0,吸附速率随时间的增加逐渐降低,随温度的升高有一定升高,在30℃时具有较好的吸附性能,吸附量达59.9 mg/g;各代PAMAM-SG的吸附量大小依次为2.0G>1.5G>1.0G>0.5G>0G>-0.5G;吸附容量随浓度的增大而增加,直至平衡.     

Adsorption equilibrium and kinetics of H2O on zeolite 13x

The adsorption characteristics of H₂O on zeolite 13X were measured by a gravimetric method. The adsorption isotherm showed type II isotherm and was fitted by using both the excess surface work (ESW) model and Langmuir-Freundlich model. The results predicted by the Langmuir-Freundlich model were much smaller than the experimental results at higher-pressure region. However, the ESW model agreed well with the experimental data over the whole pressure region. In this case, a plot of the change in chemical potential versus the amount adsorbed gave two linear regions due to secondary effects such as capillary condensation. The experimental uptake curves were well fitted by several LDF models and solid diffusion model with the error range of 1.5-3.5%. Unlike the expectation that the more rigorous solid diffusion model would fit better, Nakao-Suzuki model showed the best agreement with experimental uptake data.     

Chitosan functionalized with 2[-bis-(pyridylmethyl) aminomethyl]4-methyl-6-formyl-phenol: equilibrium and kinetics of copper (II) adsorption

The complexation agent 2[-bis-(pyridylmethyl) aminomethyl]-4-methyl-6-formyl-phenol (HL) was immobilized in chitosan in order to obtain a new adsorbent material to be employed in studies on adsorption and pre-concentration of Cu(II). The chitosan modified by the complexation agent was characterized by infrared spectroscopy, DSC and TGA. The studies were conducted as a function of the pH of the medium and the mechanism of Cu(II) adsorption in the solid phase was analyzed utilizing several kinetic models. The parameters for the adsorption of Cu(II) ions by chitosan-HL were determined with a Langmuir isotherm, the maximum saturation capacity of the monolayer being 109.4 mg of Cu(II) per gram of polymer. Electron paramagnetic resonance spectroscopy revealed that Cu^II ions coordinate to the donor atoms of the HL ligand anchored to the surface of the polymer forming a stable chelate complex in the solid state.     

Adsorption of bark derived polyphenols onto functionalized nanocellulose: Equilibrium modeling and kinetics

This article describes the kinetics and capacity of adsorbing condensed conifer tannins onto cationic cellulose nanocrystals (CCNCs). Batch adsorption experiments were carried as a function of pH, contact time, and initial tannin concentration with constant cationic cellulose nanocrystal concentration (0.01%). The adsorption process was highly pH dependent as adsorption capacities ranged from 13.2 mg/g to 112.7 mg/g at pH of 3–10. The amount of tannin adsorbed per unit mass of the cationic cellulose nanocrystals increased with increasing of tannin concentration until equilibrium was attained. The experimental data followed the Langmuir adsorption model, and the maximum experimental and theoretical adsorption capacities for the cationic nanocrystals reached 1,008 mg/g and 1,111 mg/g, respectively. The kinetics of adsorption was described best by the pseudo-second-order kinetics indicating a chemisorption process. The inherent adsorption has interesting applications for CCNC-complexes with natural polyphenolics in green chemical applications for adhesives, adsorbents, preservatives, and packaging materials.     

Adsorption of cationic dye on N,O-carboxymethyl-chitosan from aqueous solutions: equilibrium, kinetics, and adsorption mechanism

In order to improve the adsorption capacity of chitosan (CTS) for methylene blue (MB) cationic dye, a series of N,O-carboxymethyl-chitosans (N,O-CMCTS) were prepared under heterogeneous conditions by controlling the reaction time. The adsorption of MB from aqueous solution onto N,O-CMCTS was studied. The effects of degree of substitution (DS) of N,O-CMCTS, initial pH of the dye solution and adsorption temperature were investigated in detail. The results showed that the adsorption capacities of N,O-CMCTS increased with the increase of DS and N,O-CMCTS with DS of 0.72 exhibited the highest adsorption capacity (349 mg/g). The adsorption kinetics of N,O-CMCTS was found to follow the pseudo-second-order model. The adsorption equilibrium of N,O-CMCTS fitted very well with the Langmuir isotherm model, showing maximum monolayer adsorption capacity of 351 mg/g. The adsorption mechanism of N,O-CMCTS was also discussed by means of FTIR spectra and XPS. The results revealed that the –OH, –NH₂, and –COOH groups of N,O-CMCTS were involved in the adsorption process. The desorption studies showed that N,O-CMCTS could be regenerated and used for the adsorption of MB repeatedly.     

生物基活性炭对有机-水共混溶剂中的甲基橙吸附平衡与动力学研究

探究生物基活性炭对有机-水共混溶剂中的甲基橙的吸附性能、吸附平衡和动力学研究。结果表明,生物基活性炭对甲基橙的最大单层吸附量为80. 4 mg/g。相比准一级动力学模型,准二级动力学模型更适合于描述有机-水共混溶剂中活性炭吸附甲基橙的过程。     

Adsorption equilibrium and kinetics studies of divalent manganese from phosphoric acid solution by using cationic exchange resin

There are numerous impurities in wet-process phosphoric acid, among which manganese is one of detrimental metallic impurities, and it causes striking negative effects on the industrial phosphoric acid production and downstream commodity. This article investigated the adsorption behavior of manganese from phosphoric acid employing Sinco-430 cationic ion-exchange resin. Resorting FT-IR and XPS characterizations, the adsorption mechanism was proved to be that manganese was combined with sulfonic acid group. Several crucial parameters such as temperature, phosphoric acid content and resin dose were studied to optimize adsorption efficiency. Through optimization, removal percentage and sorption capacity of manganese reached 53.12 wt%, 28.34 mg·g^-1, respectively. Pseudo-2nd-order kinetic model simulated kinetics data best and the activation energy was evaluated as 6.34 kJ·mol^-1 for the sorption reaction of manganese. In addition, the global adsorption rate was first controlled by film diffusion process and second determined by pore diffusion process. It was found that the resin could adsorb up to 50.24 mg·g^-1 for manganese. Equilibrium studies showed that Toth adsorption isotherm model fitted best, followed by Temkin and Langmuir adsorption isotherm models. Thermodynamic analysis showed that manganese adsorption was an endothermic process with enhanced randomness and spontaneity.     

Adsorption equilibrium and kinetics studies of divalent manganese from phosphoric acid solution by using cationic exchange resin

There are numerous impurities in wet-process phosphoric acid, among which manganese is one of detrimental metallic impurities, and it causes striking negative effects on the industrial phosphoric acid production and downstream commodity. This article investigated the adsorption behavior of manganese from phosphoric acid employing Sinco-430 cationic ion-exchange resin. Resorting FT-IR and XPS characterizations, the adsorption mechanism was proved to be that manganese was combined with sulfonic acid group. Several crucial parameters such as temperature, phosphoric acid content and resin dose were studied to optimize adsorption efficiency. Through optimization, removal percentage and sorption capacity of manganese reached 53.12 wt%, 28.34 mg·g⁻¹, respectively. Pseudo-2nd-order kinetic model simulated kinetics data best and the activation energy was evaluated as 6.34 kJ·mol⁻¹ for the sorption reaction of manganese. In addition, the global adsorption rate was first controlled by film diffusion process and second determined by pore diffusion process. It was found that the resin could adsorb up to 50.24 mg·g⁻¹ for manganese. Equilibrium studies showed that Toth adsorption isotherm model fitted best, followed by Temkin and Langmuir adsorption isotherm models. Thermodynamic analysis showed that manganese adsorption was an endothermic process with enhanced randomness and spontaneity.     

沸石对废水中Fe3+的吸附平衡和动力学特性

铁是影响饮用水质安全性的主要因子之一,为了研究沸石去除水中铁的反应机制,通过振荡试验分析了沸石对溶液中Fe3+的吸附平衡和动力学过程.结果表明,吸附平衡过程极显著符合Langmuir、Freundlich和RedlichPeterson方程,为优惠型吸附,最大理论吸附容量为2.486 g/kg;吸附动力学方程极显著遵循...     

Adsorption equilibrium constants of methyl oleate and methyl linoleate in vapor phase on supported copper and nickel catalysts

Adsorption equilibrium constants for methyl oleate and methyl linoleate in vapor phase on supported copper and nickel catalysts have been determined using the technique of pulse gas chromatography. The results are discussed in relation to selectivity in fat hydrogenation. Notation: A, column cross-section, m₂ ; a_n,b_n, nth Fourier coefficients; c, concentration of adsorbate in bulk flow, mol/m³ ; c^* = c/ ∫ ₀ ^∞ cdt, normalized concentration of adsorbate in bulk flow; C_i, concentration of adsorbate in catalyst pores, mol/m³ ; c_a, concentration of adsorbate on catalyst surface, mol/kg; c_TOT, active area of catalyst as measured by hydrogen adsorption, mol/kg; D_e, effective diffusion coefficient of adsorbate in catalyst, m²/s; D_ea, axial dispersion coefficient based on void cross-section, m²/s; h_n, nth coefficient in Hermite polynomial expansion; H_n nth Hermite polynomial; ΔH_A, adsorption enthalpy, kJ/mol; ΔH_vap , heat of vaporization, kJ/moll; k_a, adsorption rate constant, m³/kgs;K_A, adsorption equilibrium constant, m³/kg; K₀ , preexponential factor defined in Eqn. 8, m³/kg; k_f, mass transfer coefficient, m/s; L, bed length, m; q, flow rate, m³/s; R, particle radius, m; R_g, gas constant; t, time, s; T, temperature, K; T_F, period of Fourier expansion, s; u = q/A, linear velocity, m/s; z, length coordinate in packed column, m. Greek symbols: δ(t), Dirac delta function; ∈_B, void fraction of bed; ∈_-p, particle void fraction, ρ_rp, particle density, kg/m³ ; ξ, radial coordinate in particle, m; μ₁, first absolute moment, μ₂, second central moment.     

Syntheses and properties of cross‐linked polymers from functionalized triglycerides

A number of functionalized triglycerides were synthesized from glyceryl trioleoate via epoxidation followed by reduction to give glyceryl tris(9‐hydroxy)trioleoate (a triol) or hydrolytic ring opening to obtain glyceryl tris(9,10‐dihydroxy)trioleoate (a hexaol). A selective monoepoxidation reaction of glyceryl trioleoate was also carried out and the resulting monoepoxide was hydrolyzed to give glyceryl 9,10‐dihydroxytrioleoate (a diol). Glyceryl tris(9‐hydroxy)trioleoate was brominated followed by displacement with sodium azide and reduction to give glyceryl tris(9‐amino)trioleoate (a triamine) and glyceryl tris[9‐(N‐isopropylamino)]trioleoate. These functionalized triglycerides were crosslinked with 1,4‐phenylene diisocyanate. The crosslinked polymers exhibit thermoset characteristics. Thermal analysis results suggest that the polymers are in amorphous states, and their thermal stability was significantly affected by crosslink degree. The crosslinked polymer derived from the diol retained 56% of its weight at 408°C, whereas the polymers derived from the aforementioned hexaol with higher crosslink degree retained only 36% of the original weight. Glass transition temperatures of these polymers range from ?1.0°C to 10.2°C. The thermal stable polymer, 12 , derived from the aforementioned diol exhibits a linear viscoelastic character and can be used as thermoplastics. © 2008 Wiley Periodicals, Inc. J Appl Polym Sci, 2008     

利用海带渣生产燃料乙醇的初步研究

对海带渣中的纤维成分进行了测定,并以海带渣为原料进行了发酵产纤维素乙醇的研究。通过实验初步建立了海带渣生产乙醇的预处理方法并确立了发酵方式,同时对南极低温纤维素酶QP7复配降解海带渣生产乙醇的效果进行了研究。实验结果表明,海带渣中纤维素含量达28.3%;稀酸预处理后,海带渣经分步糖化发酵得到的乙醇浓度高于相同条件下的秸秆乙醇浓度;在海带渣同步糖化发酵中以低温纤维素酶作为复配酶进行酶解,乙醇产量提高21%以上。海带渣作为生产纤维素乙醇的原料,具有良好的应用前景;既能为海带产业的综合利用提供新方向,而且能够为其它海藻的生物质能源开发提供数据和方法参考。     

十六烷基三甲基溴化铵改性X分子筛对铬酸盐的吸附平衡及动力学

用十六烷基三甲基溴化铵(HTAB)对X分子筛改性,考察改性分子筛对水中铬酸盐的吸附平衡及吸附动力学。采用XRD和FT-IR对样品进行表征,结果表明改性后HTAB-X分子筛在保持原有结构和形貌同时,接枝了一定量的长链季铵盐阳离子功能基团。吸附实验表明,0.7 g改性分子筛在25℃、pH=6条件下,去除率为94.14%,比X分子筛提高了近36%。HTAB-X分子筛对铬酸盐的吸附遵循Langmuir模型,最大吸附容量为16.33 mg/g。热力学和动力学分析表明,该吸附过程为自发的放热过程,适合在常温下进行;吸附过程遵循准二级动力学模型,平衡吸附容量qe,cal达到2.71 mg/g,速率常数k2为0.362 g/(mg·min)。