Application of LS-SVM strategy to estimate H2S loading capacity in different ionic liquids and alkanolamines

Favorable properties of aqueous solutions are improved with the addition of different materials for separation of hydrogen sulfide (H₂S). Also, equilibrium data and available equations for solubility estimation of this gas are only valid for specific solutions and limited ranges of temperature and pressure. In this regard, a machine learning model based on Support vector machine (SVM) algorithm is proposed and developed with mixtures containing different amines and ionic liquids to predict H₂S solubility over wide ranges of temperature (298–434.5 K), pressure (13–9319 kPa), overall mass concentration (3.82–100%) and mixture's apparent molecular weight (18.39–556.17 g/mol). The accuracy of the performance of this network was evaluated by regression analysis on calculated and experimental data, which had not been used in network training.     

降低天然气处理厂稳定凝析油中H2S含量的工艺参数研究

利用HYSYS软件对中亚某天然气处理厂凝析油稳定工艺流程进行了建模,分别计算了塔底温度、气提气量、稳定塔压力和塔顶进液比对稳定凝析油中H_2S摩尔分数、凝析油收率等工艺指标的影响情况,并通过现场试验验证了计算结果的正确性。根据模拟计算及现场试验结果,确定了稳定塔操作参数建议值。     

The mechanism of H2S generation in the recovery of heavy oil by steam drive

Laboratory experimental simulation reactions between heavy oil and water at different temperatures are conducted. The large amount of H₂S gas in the steam drive recovery in the Shengli oilfield is mainly formed during the aquathermolysis of sulfocompounds in heavy oil. Temperature is a controlling factor influencing the aquathermolysis of heavy oil. The higher the temperature is, the more H₂S gas is generated. Furthermore, the release of H₂S dissolved in formation water at high temperature and the catalytic effect of mineral ions on the aquathermolysis reduces the temperature of the reaction between heavy oil and formation water in the generation of H₂S gas.     

大牛地下古生界气藏天然气原生含硫成因研究

大牛地下古生界气藏多口气井在生产过程中始终伴有H2S,但含硫成因问题一直认识不清。首先对气藏含硫的全部成因进行全面分析和逐一排查。在确认为热化学成因的基础上,采用δ34S同位素分析,明确了大牛地下古气藏H2S为热化学成因中的硫酸盐热化学还原TSR成因。然后通过开展还原反应模拟试验,结合气相色谱分析、全岩XRD扫描、剩余有机质检测等手段,对下古气藏H2S的生成机理、反应条件、控制因素等进行的系统研究,结果表明,大牛地下古气藏硫酸盐热化学还原TSR反应是在富含石膏、烃类气体充足、密闭的还原环境、温度超过200℃和有地层水参与的条件下而进行的。     

硫酸盐热化学还原生成H2S实验研究

H_2S作为有毒的酸性气体,在稠油注汽热采过程中主要由硫酸盐热化学还原(TSR)产生。通过实验探究CaSO_4、Na_2SO_4、MgSO_4和Al_2(SO_4)_34种不同硫酸盐发生TSR反应生成H_2S的作用机制及影响。实验结果表明:(1)水是产生TSR反应的必要条件,固态硫酸盐并不能引发TSR反应;(2)硫酸盐的溶解度决定TSR反应速率,溶解度越高,反应速率越快;(3)水溶性硫酸盐的金属阳离子电荷数决定TSR反应的难易程度,电荷数越多,反应越容易进行。     

Implementation of CPA EoS for simultaneous solubility modeling of CO2 and H2S in ionic liquid [OMIM][Tf2N]

In this study, solubility of pure CO₂ and H₂S and their mixture in [OMIM][Tf₂N] modeled applying CPA EoS. CPA combines the SRK equation with an advanced association term, which is similar to that of SAFT. From a practical point of view, the target in the CPA project was to develop a thermodynamic model capable of describing complex equilibria of mixtures containing polar/associating chemicals through a simple procedure with respect to the SAFT.

The AAD% for binary systems, including H₂S+ IL and CO₂+ IL are 6.81, 5.21 respectively. Moreover, AAD% equal to 13.89 was achieved for the ternary system.     

Correlation of H2S solubility in aqueous MDEA solutions using electrolyte-modified Peng-Robinson plus association equation of state

In this survey, we use the emPR-CPA equation of state to model a ternary system of H₂S solubility in MDEA aqueous solution at different solution compositions, temperatures, pressures, and acid gas loadings. For electrolyte part of the model, MSA theory and the Born term were used. There were 302 experimental data used in this work. To model a ternary system, at first pure components, then binary subsystems, and finally ternary system were modeled using a reactive bubble point pressure calculation method. An overall absolute average deviation percentage equal to 20.85 was achieved so that show the model efficiency for correlation of such systems.     

Modeling of H2S solubility in aqueous MDEA solution using electrolyte SRK plus association equation of state

H₂S solubility in MDEA aqueous solution at different solution compositions, temperatures, pressures, and acid gas loadings was correlated using electrolyte SRK-cubic plus association equation of state. A total of 302 experimental data were used in this work. At first pure components parameters were obtained from literatures. Then binary interaction parameters were calculated through binary subsystems investigation. Finally, ternary system modeled using a reactive bubble point pressure calculation method. Considering number of binary interaction parameters that should be optimized, three scenarios were proposed. All of the scenarios present good results with acceptable absolute average deviation percentage (AAD%) but the third one shows better outputs. The AAD% in this scenario is 17.02.     

天然气净化厂液硫储罐腐蚀原因分析与防护措施

以四川某天然气净化厂液硫储罐为例,考察了液硫储罐出现腐蚀的原因。主要采用挂片法,并结合EDS分析,考察了H_2S、O_2、H_2O等因素对腐蚀的影响。同时,考察了热喷铝、喷锌的防腐蚀效果。结果表明,在无液态水的条件下,液硫对Q235腐蚀轻微,H_2S溶解在液膜内以及硫磺沉积是导致储罐顶部腐蚀的主要原因,加强顶部保温是控制腐蚀的有效方法,采用金属喷涂技术值得进一步研究。     

Selective absorption of H2S from CO2 using sterically hindered amines at high pressure

Selective absorption of H₂S from gas mixture containing H₂S and CO₂ into aqueous solutions of 2–(tert–butylamino) ethanol (TBE) and 2–amino–2–methyl–1–propanol (AMP) at different temperature was investigated at high pressure by using a static gas absorption method. The influence of temperature and contact time on the absorption of H₂S was investigated. The rates of absorption of H₂S and the selectivity factor decreased with the increase of absorption temperature. With increasing contact time for both alkanolamine solutions, the selectivity factor increased at first and then decreased.     

长庆油田某天然气净化厂实现GB 17820-2018达标工艺方案研究

针对GB 17820-2018《天然气》标准中更为严格的天然气气质要求,长庆油田某天然气净化厂存在净化气中H 2S含量不满足进入长输管道要求的现象。为解决这一问题,利用HYSYS软件对该厂MDEA脱硫工艺进行了流程模拟。分析了溶液循环量、MDEA质量分数、吸收塔塔板数、原料气温度、原料气压力以及贫液入塔温度对净化气中H 2S、CO2含量的影响,并根据不同工艺参数的影响程度对参数进行排序。在此基础上,建立以最小能耗为目标函数的多参数优化模型,利用HYSYS自带的工具箱求解模型,得到满足净化气中H 2S质量浓度<5 mg/m^3、CO2摩尔分数<2.8%的最优操作参数组合。优化结果可对指导现场采取调整措施提供参考。     

我国硫磺回收装置排放烟气中SO2达标方案探讨

针对硫磺回收装置烟气中SO_2排放问题,指出烟气中SO_2主要有液硫脱气、加氢还原吸收尾气及其他非共性原因3个来源,提出了根据不同来源分别处理以降低排放烟气中总SO_2质量浓度的对策,形成了天然气研究院硫磺回收及加氢还原吸收尾气升级达标核心技术,主要包括H2S深度脱除溶剂CT8-26、钛基硫磺回收催化剂CT6-8和新型加氢还原吸收尾气水解催化剂CT6-11B,适用于现有带加氢还原尾气处理的硫磺回收装置,特别是具有独立加氢还原溶剂再生的装置,可将硫磺回收及尾气处理装置排放尾气中SO_2质量浓度降至100mg/m3以下,为解决硫磺回收装置尾气达标排放问题提供了新的实施方案。     

绥中36-1油田A油藏生物竞争排斥技术治理下H2S主控因素及机理研究

目的绥中36-1油田A油藏采用生物竞争排斥技术治理因注入海水引入硫酸盐还原菌(SRB)而产生的H₂S,以油藏为研究对象,进行了H₂S生长主控因素和机理研究。 方法选取油藏典型油井考查其停药期间不同油井的H₂S含量、硫化物含量、微生物含量,观察SRB生长曲线规律,对H₂S生长主控因素和机理进行研究。 结果生物竞争排斥法能够抑制SRB生长,单井H₂S质量浓度降至30 mg/m³以下。停药期间,油藏H₂S生长趋势符合Compertz模型,单井A1、A4、A17、A20、A22模型拟合度在0.8以上,方差的统计量较高,显著性为0.001~0.002。 结论H₂S不受油藏生产动态的控制,海水提供了丰富的SO2-₄营养源,绥中36-1油田A油藏H₂S生长的主控因素为油藏中的SO2-₄含量。该油藏已经形成了非常稳定的生态菌群,稳定的生态系统能自动消除外部引入的硫酸盐,从而系统地控制H₂S的生长。      

胍类氨基酸离子液体捕集烟气中CO2实验研究

目的 通过开展胍类氨基酸离子液体捕集烟气中CO₂性能研究实验,找到吸收性能好、溶剂损失少和能耗低的新型CO₂吸收剂。方法 以四甲基胍(TMG)为阳离子,赖氨酸(Lys)、丙氨酸(Ala)和天冬氨酸(Asp)为阴离子,制备了[TMG][Lys]、[TMG][Ala]和[TMG][Asp]3种低黏度胍类氨基酸离子液体,并对其脱碳性能进行评价。结果 碱性较大的[TMG][Lys]具有较高CO₂吸收量,在常压、45℃、80 mL/min的条件下,吸收量为0.64 mol CO₂/mol IL。水的加入对CO₂的吸收有积极的影响,30%(w)[TMG][Lys]水溶液的吸收量增加到0.99 mol CO₂/mol IL,且经过5次吸收-解吸循环后仍能达到0.81 mol CO₂/mol IL。通过傅里叶红外光谱(FT-IR)、核磁共振氢谱(¹H-NMR)对[TMG][Lys]的脱碳机理进行分析,CO₂...