离子液体和醇胺溶液复配脱硫剂吸收H2S及再生性能

将5种离子液体[Bmim]HCO₃, [TMG]L, [MEA]L, [Bmim]Cl和[Bmim]BF₄分别与N-甲基二乙醇胺(MDEA)水溶液混合, 得到新型复配脱硫剂, 考察了离子液体的消泡性能和复配脱硫剂在不同离子液体、 吸收温度以及复配比例下的脱硫性能, 并且对较优脱硫剂进行了再生性能的研究. 采用离子色谱仪对经臭氧深度处理的再生液进行了S\begin{array}{c}{O}_4^{2-}\end{array}离子浓度测试, 并对脱硫剂进行了密度泛函理论研究, 从而进一步分析了吸收机理. 结果表明, 室温下复配脱硫剂脱硫能力大小顺序为[Bmim]Cl-MDEA-H₂O>[Bmim]HCO₃-MDEA-H₂O>[Bmim]BF₄-MDEA-H₂O>MDEA-H₂O>[TMG]L-MDEA-H₂O>[MEA]L-MDEA-H₂O. 离子液体与MDEA结合的稳定性为主要影响因素, [Bmim]HCO₃的消泡能力最强, [Bmim]Cl-MDEA-H₂O, [Bmim]BF₄-MDEA-H₂O和[Bmim]HCO₃-MDEA-H₂O脱硫剂可以通入空气获得基本再生, H₂S与离子液体的结合越稳定, 脱硫效率越高, 但脱硫剂的再生程度会降低.     

Solubility of carbon dioxide in aqueous solutions of diisopropanolamine and methyldiethanolamine

The solubility of carbon dioxide in aqueous solutions of alkanolamines was measured by means of two experimental methods. The solubility of carbon dioxide was measured at 298 K with a static total pressure apparatus in solutions of water + diisopropanolamine (DIPA) having mass fraction of DIPA equal to 10.1%, 11.0% and 33.9%. The density of the water + DIPA solution was measured continuously during the experiments to investigate the changes in density introduced by the absorption of carbon dioxide. A correlation for the density of CO₂-loaded aqueous solutions of DIPA is presented.     

γ-Al2O3的添加对MDEA溶液脱除COS效果的影响

通常石油炼厂气、煤制气和天然气中都含有羰基硫（COS）等有机硫化物，它们会污染环境，腐蚀设备，导致后续生产工艺的催化剂中毒．COS呈中性或弱酸性，化学性质比较稳定，难以用常规的脱硫方法脱除干净．氢解与水解都能将COS绝大部分转化为H2S然后用脱硫剂脱除．近年来国内外研究开发了常温COS水解催化剂，它们多以活性氧化铝为主要成分，     

离子色谱法同时测定脱硫液中的四种醇胺

建立了同时分离测定异丙醇胺(IPA)、三异丙醇胺(TIPA)、N-甲基二乙醇胺(MDEA)、N,N-二甲基二乙醇胺(DMAE)和6种阳离子的离子色谱法。色谱柱为TSKgelSuperIC-CR阳离子交换柱,流动相为冠醚(2.0mmol/L)、甲基磺酸(2.2mmol/L)、L-组氨酸(0.5mmol/L)混合溶液,流速为0.5mL/min,抑制电导检测。DMAE、MDEA、TIPA、IPA的检出限分别为0.48、36.9、47.04和1.39μg/L;样品中DMAE、MDEA、TIPA、IPA平均回收率为103.15%,95.48%,97.64%,92.41%。方法具有简单、快速、灵敏、抗干扰等优点,用于测定脱硫液中的DMAE、MDEA、TIPA和IPA,结果令人满意。     

Thermodynamics of aqueous solutions of methyldiethanolamine and diisopropanolamine

The vapour–liquid equilibrium (VLE) of the systems of water + methyldiethanolamine (MDEA) and water + diisopropanolamine (DIPA) was measured at several temperatures with a static total pressure apparatus. The solid–liquid equilibrium (SLE) of the same systems was measured at low amine concentrations by means of two experimental methods: a visual method and a Differential Scanning Calorimeter (DSC). The activity coefficients of water + MDEA were modelled with the NRTL equations. The model parameters were regressed from VLE, SLE and excess enthalpy data from this work and from the literature. The model developed in this work was compared with models found in the literature. The NRTL equations were also used to model the activity coefficients of the system of water + DIPA. The model parameters were fitted from the VLE and SLE data measured in this work.     

Highly sensitive capillary electrophoresis-mass spectrometry for rapid screening and accurate quantitation of drugs of abuse in urine

The combination of capillary electrophoresis (CE) and mass spectrometry (MS) is particularly well adapted to bioanalysis due to its high separation efficiency, selectivity, and sensitivity; its short analytical time; and its low solvent and sample consumption. For clinical and forensic toxicology, a two-step analysis is usually performed: first, a screening step for compound identification, and second, confirmation and/or accurate quantitation in cases of presumed positive results. In this study, a fast and sensitive CE-MS workflow was developed for the screening and quantitation of drugs of abuse in urine samples. A CE with a time-of-flight MS (CE-TOF/MS) screening method was developed using a simple urine dilution and on-line sample preconcentration with pH-mediated stacking. The sample stacking allowed for a high loading capacity (20.5% of the capillary length), leading to limits of detection as low as 2 ng mL⁻¹ for drugs of abuse. Compound quantitation of positive samples was performed by CE-MS/MS with a triple quadrupole MS equipped with an adapted triple-tube sprayer and an electrospray ionization (ESI) source. The CE-ESI-MS/MS method was validated for two model compounds, cocaine (COC) and methadone (MTD), according to the Guidance of the Food and Drug Administration. The quantitative performance was evaluated for selectivity, response function, the lower limit of quantitation, trueness, precision, and accuracy. COC and MTD detection in urine samples was determined to be accurate over the range of 10–1000 ng mL⁻¹ and 21–1000 ng mL⁻¹, respectively.     

Acid gases partial pressures above a 50 wt% aqueous methyldiethanolamine solution: Experimental work and modeling

Aqueous amine solutions are widely used in the industry for acid gas removal. In order to treat natural gas or refinery process streams, an accurate knowledge of solubility data of carbon dioxide, hydrogen sulfide and other sulfur species in aqueous amine solutions is required. In this paper, new equilibrium measurements on 50 wt% aqueous methyldiethanolamine solution with CO₂ and H₂S have been produced. A simple way to correlate the data has been searched and found. First, a model proposed by Posey et al. in 1996, then a Deshmukh–Mather model are used to correlate “vapor–liquid” equilibria. The Posey et al. model lacks accuracy to represent the experimental data, especially for high loadings. The Deshmukh–Mather model shows good agreement as long as the total loading (H₂S + CO₂) does not reach 1.0.     

Measuring solubility of carbon dioxide in aqueous blends of N-methyldiethanolamine and 2-((2-aminoethyl)amino)ethanol at low CO2 loadings and modelling by electrolyte SAFT-HR EoS

In this work, new solubility values for CO₂ absorption in aqueous solutions of N-methyldiethanolamine (MDEA) in the presence of different mole ratios of 2-((2-aminoethyl)amino)ethanol (AEEA) at low pressures are obtained. The total molar amine concentration of all the solutions has been fixed equal to 3.360 mol · L⁻¹ (5.370 mol amine · kg⁻¹ water). The mole ratio of AEEA/MDEA was set to 0.12500, 0.10000 and 0.05000. The experimental total pressure varied from (7.3 to 386.6) kPa and the experimental temperature was set to (313.15, 328.15, 343.15 and 358.15) K. The electrolyte SAFT-HR (eSAFT-HR) equation of state (EoS) (Najafloo et al., 2014) has been successfully applied to model the solubility of CO₂ in aqueous mixtures of AEEA and MDEA. The overall average absolute relative per cent deviation (AAD%) in calculating the total pressure as a function of CO₂ loading is 7.74 for (AEEA + MDEA + CO₂ + H₂O) quaternary system at the four values of temperature. To verify the predictive ability of the model, the eSAFT-HR EoS was extrapolated to the Zoghi and Feyzi (2013) solubility results of the same quaternary system that were obtained at higher pressures or higher CO₂ loadings at the same temperatures. The AAD of the present model is 11.39% lower.     

区间MDEA模型及其求解

将一种改进的DEA模型-MDEA模型[1]拓展到区间投入产出情形,得到区间MDEA模型.定义了一种反映决策者满意度的区间数序关系,当决策者给定一满意度水平,将区间MDEA中的区间不等式约束转化为确定型约束.研究了该满意度水平的另一层含义,即决策者对除被评价决策单元外的其它决策单元的偏好程度,据此将区间MDEA中的区间等式约束和区间目标函数转化为确定型.最终将区间MDEA转化为某一满意度水平下的确定型MDEA,并进行求解.最后给出算例分析.     

Experimental determination of the solubility of aromatic compounds in aqueous solutions of various amines

A new apparatus to measure solubility data of aromatics in aqueous solutions has been designed. It is based on a static-analytic method with Rolsi™ pneumatic samplers for on line gas chromatograph analysis. Operating pressures and temperatures are between 0.3 and 10 MPa and between 293 and 393 K.

Solubility measurement results are reported for several aromatic compounds (benzene, toluene, ethylbenzene and xylene) in different amine aqueous solutions (monoethanolamine (MEA), diethanolamine (DEA), methyldiethanolamine (MDEA), diglycolamine (DGA)). Several influent parameters are studied (temperature, total pressure, etc.).