IMC-80缓蚀剂的研究和应用

合成了具有炔醇基、氨基和季铵结构的系列化合物,并在此基础之上研制出缓蚀剂IMC－80。利用腐蚀失重和电化学方法,对其在CO₂饱和盐水和盐酸体系中的缓蚀性能进行研究.研究结果表明,它们在酸性介质、油田污水介质和含有少量H₂S和CO₂的伴生水介质中具有优良的缓蚀性能.该级蚀剂在中原油田试用,在控制油井及其相关的集油管线腐蚀上,其效果优于美国同类产品CI－203,     

IMC—80缓蚀剂的研究和应用

合成了具有炔醇基、氨基和季铵结构的系列化合物，并在此基础上研制出缓蚀剂ＩＭＣ－８０，利用腐蚀失重和电化学方法。地其在ＣＯ２饱和盐水和盐酸体系中的缓蚀性能进行研究，研究结果表明，它们在酸性介质、油田污水介质和含有少量Ｈ２Ｓ和Ｃ煌伴生水介质中具有优良的缓蚀性能，该缓蚀剂在中原油田试用，在控制油井及其相关的集油管线腐蚀上，其效果优于美国同类产品ＣＩ－２０３。     

聚丙烯酰胺在油井堵水中的应用

油井出水是目前油田开发过程中普遍存在的一个问题,特别是为了保持地层压力,采用早期注水开发的油田,出水尤为严重。这不仅使地面脱水工作量越来越大,而且最后会导致原来经济效果好的生产井,变为无工业开采价值。因此,油井堵水是保持油田稳产、增产的一项技     

中性介质中铜缓蚀剂的成膜过程

使用光电化学与电化学石英晶体微天平联用（PECQCM）技术对中性介质铜缓蚀剂成膜过程进行了现场研究．结果表明，在中性Na2SO4溶液中钝化型缓蚀剂Na2OrO4对Cu成膜生长有抛物线规律，而由于Cl-的影响，在中性NaCl溶液中，该缓蚀剂膜生长曲线为折线型．沉淀型缓蚀剂Na2SiO3在Na2SO4溶液中的铜晶振电极上不成膜，而在NaCl溶液中可成膜．     

LD-2复合缓蚀剂对海水介质混凝土中钢筋阻锈作用研究

利用电化学检测技术和海水浸泡试验等方法 ,观测和研究了经筛选研制的LD_2复合缓蚀剂对海水介质中钢筋腐蚀电化学行为的影响 ,考察和评价了复合缓蚀剂对钢筋的阻锈作用 .结果表明 ,LD_2复合缓蚀剂主要起阳极型缓蚀剂作用 .在海水中加入 2 5 g·L- 1复合缓蚀剂后 ,钢筋的腐蚀电位提高约 0 .2 2 0V ,腐蚀电流降低至未加缓蚀剂的 1% ,缓蚀效率达 99% .钢筋混凝土试样在海水中浸泡 2年 ,表明混凝土中加入占水泥重量 1.0 %～ 2 .5 %LD_2复合缓蚀剂时 ,能有效阻止混凝土中钢筋的腐蚀     

噻二唑衍生物对银的缓蚀性能研究

本文研究了主要成分为5-甲基-2-戊基二硫代-1,3,4-噻二唑的复配型缓蚀剂TSJ-T6,在浓度为5.0×10-5g/g的H2S中对银的缓蚀性能。通过增重实验、接触角分析、电化学极化曲线测试以及分子动力学模拟研究了该缓蚀剂的缓蚀效率及缓蚀机理。增重实验结果证明,缓蚀剂TSJ-T6对银片在H2S中的腐蚀具有良好的缓蚀效果,缓蚀剂浓度为2.5×10-5g/g时,缓蚀效率高达94.51%。接触角分析结果表明,该缓蚀剂分子在银片和腐蚀液的界面形成了一层疏水保护膜。极化曲线结果表明,缓蚀剂TSJ-T6的存在降低了阴、阳极的塔菲尔斜率,为混合型缓蚀剂;同时,该缓蚀剂的存在显著降低了腐蚀电流密度,表明该缓蚀剂对银片在H2S中的腐蚀有良好的缓蚀效果。分子动力学模拟表明,缓蚀剂分子通过噻二唑环和链上的硫、氮原子吸附在银表面,烷基链则以一定角度指向溶液。     

流动条件下两种不同亲水基团咪唑啉型缓蚀剂的缓蚀性能

选择了两种含有不同亲水基团的咪唑啉型缓蚀剂, 即1-胺乙基-2-十一烷基咪唑啉(AEI-11)和1-羟乙基-2-十一烷基咪唑啉(HEI-11), 分别在静态及动态条件下,采用失重法、极化曲线法、电化学阻抗谱法研究了上述缓蚀剂对N80钢在CO2饱和的3%(w)NaCl溶液中的缓蚀性能. 研究结果表明, 无论在静态和动态条件下, HEI-11均表现出更佳的缓蚀性能, 即咪唑啉型缓蚀剂的缓蚀性能与亲水基团的极性成正比; 在流动条件为5 m·s-1时, 缓蚀剂的缓蚀效率显著降低. 为了进一步研究缓蚀剂的缓蚀性能与其结构的关系, 运用量子化学法计算了缓蚀剂的EHOMO(最高占有分子轨道)、ELUMO(最低空分子轨道), 结果表明缓蚀剂的缓蚀效率与EHOMO成正比, 与ELUMO及ELUMO与EHOMO的差值驻E成反比.     

酸洗缓蚀剂ПБ-5的制备

酸洗缓蚀剂有着广泛的用途。当在硫酸或盐酸中加入少量酸洗缓蚀剂时,这些酸对于钢铁的腐蚀作用几乎完全消失了。因此加有缓蚀剂的盐酸常被用来清除锅炉中的水垢、清除精密另件上的锈斑以及石油井中的岩石。在这种情况下可以提高锅炉的热效率和油井的产油率而不使金属设备受到损害。在苏联,广泛地采用一种名为ПБ-5的酸洗缓蚀剂。它的缓蚀性能极好,但其制法迄今并未发表,只是从苏联化学商品目录中可以知道,它是苯胺和乌洛妥品(圜六次甲基四胺)的缩聚物。     

缓蚀剂

用缓蚀剂来防止腐蚀——也就是在介质中加入少量添加剂以防止腐蚀——是防蚀中用得最广泛的方法之一。就其所处理的介质而言,可以有酸性溶液、中性溶液、石油、蒸汽和大气等;就其所保护的金属而言,可以有钢、铁、铝、锌、镁、锡、铜等;就其在各经济部门使用的广泛性而言,那么,无论是国防工业、机械工业、钢铁工业、化学工业、石油工业、电力工业,甚至食品工业及化妆品工业等都需广泛地应用缓蚀剂。由于在防蚀学的领域中日新月异地出现了许多新的问题(例如高压锅炉以及油井的腐蚀等),积极地寻找新品种的缓蚀剂或是研究更有效的复合缓蚀剂以及联合保护法(例如阴极保护法和缓蚀剂联用)就变成防蚀工作人员和腐蚀学者们的重要任务之一。另外,虽然有关缓蚀剂方面的文献相当丰富,但是     

碱土金属离子与EDTA对纯铝在碱性溶液中的协同缓蚀作用

通过集气实验、极化曲线和电化学阻抗谱等方法研究了碱土金属离子与乙二胺四乙酸(EDTA)对纯铝在4 mol•L-1 KOH溶液中的协同缓蚀作用. 实验结果表明铝在含0.02 mol•L-1 EDTA和饱和Ca(OH)2、Sr(OH)2的溶液中具有最小的腐蚀速率. EDAX分析表明碱土金属离子和EDTA没有参与到铝表面氧化膜的组成中, 说明缓蚀剂是通过吸附在铝表面起作用的, 这表明它们是界面型缓蚀剂而非相间型缓蚀剂.     

Performance of Waterborne Polyurethanes in Inhibition of Gas Hydrate Formation and Corrosion: Influence of Hydrophobic Fragments

The design of new dual-function inhibitors simultaneously preventing hydrate formation and corrosion is a relevant issue for the oil and gas industry. The structure-property relationship for a promising class of hybrid inhibitors based on waterborne polyurethanes (WPU) was studied in this work. Variation of diethanolamines differing in the size and branching of N-substituents (methyl, n-butyl, and tert-butyl), as well as the amount of these groups, allowed the structure of polymer molecules to be preset during their synthesis. To assess the hydrate and corrosion inhibition efficiency of developed reagents pressurized rocking cells, electrochemistry and weight-loss techniques were used. A distinct effect of these variables altering the hydrophobicity of obtained compounds on their target properties was revealed. Polymers with increased content of diethanolamine fragments with n- or tert-butyl as N-substituent (WPU-6 and WPU-7, respectively) worked as dual-function inhibitors, showing nearly the same efficiency as commercial ones at low concentration (0.25 wt%), with the branched one (tert-butyl; WPU-7) turning out to be more effective as a corrosion inhibitor. Commercial kinetic hydrate inhibitor Luvicap 55 W and corrosion inhibitor Armohib CI-28 were taken as reference samples. Preliminary study reveals that WPU-6 and WPU-7 polyurethanes as well as Luvicap 55 W are all poorly biodegradable compounds; BOD_t/COD_cr (ratio of Biochemical oxygen demand and Chemical oxygen demand) value is 0.234 and 0.294 for WPU-6 and WPU-7, respectively, compared to 0.251 for commercial kinetic hydrate inhibitor Luvicap 55 W. Since the obtained polyurethanes have a bifunctional effect and operate at low enough concentrations, their employment is expected to reduce both operating costs and environmental impact.     

咪唑啉缓蚀剂膜抑制腐蚀介质扩散行为的MD研究

采用分子动力学模拟的方法,对5种1-(2-氨乙基)-2-烷基-咪唑啉缓蚀剂[(NH2)C2H4-C3H4N2-CH2(CH2)nCH3,n=5,7,9,11,13]抑制CO2腐蚀的缓蚀机理进行了研究.计算了4种腐蚀介质粒子(H2O,H3O+,Cl-和HCO-3)在不同缓蚀剂膜中的扩散系数,并从自由体积分数、腐蚀介质粒子与缓蚀剂膜的相互作用、膜的自扩散性能等方面对缓蚀剂膜抑制腐蚀介质粒子扩散行为的微观机理进行了分析.扩散系数的计算结果表明:缓蚀剂膜能有效抑制腐蚀介质的迁移,削弱其腐蚀能力;与中性H2O分子对比,缓蚀剂膜对H3O+,Cl-和HCO-3带电离子的扩散具有更强的抑制效果;随烷基链长的增加,5种缓蚀剂膜对腐蚀粒子扩散的抑制能力呈增强趋势.综合分子动力学计算结果,5种缓蚀剂缓蚀性能随着烷基链长的增加逐渐增强,理论评价结论与实验结论相吻合.     

Corrosion Inhibition of a Green Scale Inhibitor Polyepoxysuccinic Acid

The corrosion inhibition of a green scale inhibitor, polyepoxysuccinic acid (PESA) was studied based on dynamic tests. It is found that when PESA is used alone, it had good corrosion inhibition. So, PESA should be included in the category of corrosion inhibitors. It is not only a kind of green scale inhibitor, but also a green corrosion inhibitor. The synergistic effect betweenPESA and Zn2 or sodium gluconate is poor. However, the synergistic effect among PESA, Zn2 and sodium gluconate is excellent, and the corrosion inhibition efficiency for carbon steel is higher than 99%. Further study of corrosion inhibition mechanism reveals that corrosion inhibition of PESA is not affected by carboxyl group, but by the oxygen atom inserted. The existence of oxygen atom in PESA molecular structure makes it easy to form stable chelate with pentacyclic     

蛋氨酸衍生物的合成及其缓蚀性能研究

本文合成了一种新型蛋氨酸衍生物酸洗缓蚀剂,运用红外光谱及核磁共振氢谱对其结构进行了鉴定。采用失重法和电化学法研究了在0. 5mol·L~(-1)硫酸介质中其对碳钢试片的缓蚀性能,并通过吸附等温模型对缓蚀机理进行初步的探讨。结果表明,蛋氨酸衍生物的缓蚀效率约为90%,整体用量适中,是一种有望得到良好应用的绿色缓蚀剂。电化学分析表明,蛋氨酸衍生物为混合型缓蚀剂,其通过增大金属表面的电荷转移电阻而降低电化学腐蚀速率。     

药物莫西沙星对Q235钢在盐酸溶液中的缓蚀作用

为了探寻新的环境友好型缓蚀剂,采用电化学方法、失重法和量子化学计算研究了莫西沙星在1 mol/L HCl溶液中对Q235钢的缓蚀性能和缓蚀机理。结果表明,莫西沙星对Q235钢在盐酸溶液中是一种良好的以抑制阴极为主的混合抑制型缓蚀剂,缓蚀效率随其浓度的增加而增大,但随温度增加而减小,35℃下,在其浓度为200 mg/L时,缓蚀效率达90%;莫西沙星在Q235钢表面的吸附为自发过程,且符合Langmuir和El-Awady等温方程,同时,计算和讨论了相关的热力学和动力学参数。此外,采用量子化学计算对莫西沙星的缓蚀机理进行了进一步的分析,结果发现,莫西沙星的缓蚀作用由物理吸附和化学吸附共同产生。     

苯并咪唑类缓蚀剂缓蚀性能的理论评价

采用量子化学计算和分子动力学模拟相结合的方法, 对2-巯基苯并咪唑(A)、2-氨基苯并咪唑(B)、2-甲基苯并咪唑(C)和苯并咪唑(D)等四种缓蚀剂抑制HCl对碳钢腐蚀的性能进行理论评价, 并对其缓蚀机理进行分析. 全局活性指数的计算表明, 四种分子中, 2-巯基苯并咪唑分子具有最强的反应活性; 对于其他三种分子, Fukui指数和全电子密度分布指出, 2-氨基苯并咪唑具有两个亲电攻击中心, 可在金属表面形成双中心吸附, 其缓蚀性能应优于2-甲基苯并咪唑和苯并咪唑; 缓蚀剂分子与三层铁原子表面相互作用的分子动力学模拟进一步确认2-甲基苯并咪唑比苯并咪唑在金属表面吸附更稳定. 综合量子化学计算和分子动力学模拟的计算结果, 四种缓蚀剂分子缓蚀效率的顺序应为A>B>C>D, 缓蚀性能的理论评价结论与实验结果相吻合.     

Cupressus arizonica fruit essential oil: A novel green inhibitor for acid corrosion of carbon steel

Natural-based corrosion inhibitors have gained great research interest thanks to their low cost and higher performance. The Cupressus arizonica fruit essential oil (CAFEO) has a higher extraction yield than leaves; however, it has less antibacterial and antifungal activities. The three main components in the CAFEO were α-pinene (51.07%), myrcene (17.92%), and limonene (9.66%). Essential oils with a higher percentage of α-pinene were found to have outstanding corrosion inhibition properties. Therefore, herein, the CAFEO was investigated as a green corrosion inhibitor for carbon steel (CS) in 1.0 mol/L HCl using electrochemical, i.e., potentiodynamic polarization (PDP) and electrochemical impedance spectroscopy (EIS), and scanning electron microscope (SEM) techniques. The experimental results revealed that CAFEO successfully inhibited the carbon steel corrosion in 1.0 mol/L HCl solution. Results from PDP indicated that the inhibitor had a mixed-type effect with a predominance cathodic character. EIS data showed that the charge transfer resistance of the CS electrode increased from 20.9 Ω cm² in blank solution to 294.5 Ω cm² in HCl solution inhibited with 0.5 g/L of CAFEO at 298 K, leading to a significant decrease in the double layer capacitance values and an inhibition efficiency (η%) of 93%. The high temperatures showed a negative effect on the corrosion inhibition efficiency of the tested inhibitor. At 323 K, the η% of CAFEO decreased to 77%. Besides, SEM images showed that the inhibitor formed a protective barrier against acid attack, preventing carbon steel from corrosion. Theoretical calculations by Density Functional Theory (DFT) were performed to investigate the reactivity of the three main components of CAFEO.     

Water-soluble inhibitor on microbiologically influenced corrosion in diesel pipeline

The effect of water-soluble corrosion inhibitor on the growth of bacteria and its corrosion inhibition efficiency were investigated. Corrosion inhibition efficiency was studied by rotating cage test and flow loop techniques. The nature of biodegradation of corrosion inhibitor was also analyzed by using Fourier transform infrared spectroscopy (FT-IR), nuclear magnetic resonance spectroscopy (NMR) and Gas chromatography and mass spectrometer (GC–MS). The bacterial isolates (Serratia marcescens ACE2, Bacillus cereus ACE4) have the capacity to degrade the aromatic and aliphatic hydrocarbon present in the corrosion inhibitor. The degraded products of corrosion inhibitor and bacterial activity determine the electrochemical behaviour of API 5LX steel. The influence of bacterial activity on degradation of corrosion inhibitor and its influence on corrosion of API 5LX have been evaluated by employing weight loss techniques and electrochemical studies. The main finding of this paper is that the water-soluble corrosion inhibitor is consumed by the microbial action, which contributes to the decrease in inhibitor efficiency. The present study also emphasis the importance of evaluation of water-soluble corrosion inhibitor in stagnant model (flow loop test) and discusses the demerits of the water-soluble corrosion inhibitors in petroleum product pipeline.     

Measurement of oilfield chemical residues in produced water discharges and marine sediments

During oil production, significant quantities of water are produced with the crude oil which, following treatment on the platform, are discharged to the marine environment. This produced water contains residues of oilfield chemicals added by the platform operators to the topside processing equipment to aid oil-water separation and mitigate operational problems. The levels of oilfield chemicals entering the marine environment via this route were investigated using electrospray ionisation tandem mass spectrometry (ESI-MS/MS) and wet chemical analysis techniques. The generic nature of different chemical types was shown by ESI-MS/MS. Studies of the partitioning behaviour of corrosion inhibitors and demulsifiers between the oil and water phases of the produced fluids suggested corrosion inhibitors partitioned primarily into the aqueous phase and demulsifiers into the oil phase. This was reflected in levels observed in produced water although, in the case of a corrosion inhibitor, lower than expected concentrations were measured. Scale inhibitors were discharged with the produced water at their dosing concentrations. Marine sediments in the proximity of two North Sea oil platforms contained low levels of benzalkonium quaternary ammonium salts (0.74-10.84 ng/g), typical corrosion inhibitor chemicals.