Pub Date : 2021-01-01DOI: 10.1515/9783110691023-006
J. Schulze
Thank you very much for downloading chapter 6 production. As you may know, people have look hundreds times for their favorite novels like this chapter 6 production, but end up in infectious downloads. Rather than reading a good book with a cup of coffee in the afternoon, instead they cope with some infectious bugs inside their desktop computer. chapter 6 production is available in our digital library an online access to it is set as public so you can download it instantly. Our books collection spans in multiple countries, allowing you to get the most less latency time to download any of our books like this one. Merely said, the chapter 6 production is universally compatible with any devices to read.
{"title":"Chapter 6 Production","authors":"J. Schulze","doi":"10.1515/9783110691023-006","DOIUrl":"https://doi.org/10.1515/9783110691023-006","url":null,"abstract":"Thank you very much for downloading chapter 6 production. As you may know, people have look hundreds times for their favorite novels like this chapter 6 production, but end up in infectious downloads. Rather than reading a good book with a cup of coffee in the afternoon, instead they cope with some infectious bugs inside their desktop computer. chapter 6 production is available in our digital library an online access to it is set as public so you can download it instantly. Our books collection spans in multiple countries, allowing you to get the most less latency time to download any of our books like this one. Merely said, the chapter 6 production is universally compatible with any devices to read.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"6 1","pages":""},"PeriodicalIF":0.0,"publicationDate":"2021-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"80507411","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2019-01-02DOI: 10.7569/jnge.2018.692505
W. Afzal, A. Valtz, C. Coquelet
Abstract This work reports high-quality isothermal vapor–liquid equilibrium data for ethane + ethanethiol (or ethyl mercaptan) at 303 K, 323 K and 343 K and pressures up to 6.25 MPa. A sapphire-tube equilibrium cell with an online micro sampler and GC-TCD are employed to measure equilibrium phase concentrations at specific temperatures and pressures. Peng Robinson equation of state with classical alpha function is found adequate for data treatment and thermodynamic modelling.
{"title":"Vapour-Liquid Equilibria of Ethane and Ethanethiol: Experiments and Modelling","authors":"W. Afzal, A. Valtz, C. Coquelet","doi":"10.7569/jnge.2018.692505","DOIUrl":"https://doi.org/10.7569/jnge.2018.692505","url":null,"abstract":"Abstract This work reports high-quality isothermal vapor–liquid equilibrium data for ethane + ethanethiol (or ethyl mercaptan) at 303 K, 323 K and 343 K and pressures up to 6.25 MPa. A sapphire-tube equilibrium cell with an online micro sampler and GC-TCD are employed to measure equilibrium phase concentrations at specific temperatures and pressures. Peng Robinson equation of state with classical alpha function is found adequate for data treatment and thermodynamic modelling.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"46 1","pages":"108 - 96"},"PeriodicalIF":0.0,"publicationDate":"2019-01-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"77544448","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2019-01-02DOI: 10.7569/jnge.2018.692504
W. Wermink, D. Spinu, G. Versteeg
Abstract The solubility of sulfur in toluene, o-xylene, m-xylene and p-xylene was investigated at temperatures ranging from 303.15 K to 363.15 K. This study was required for the design of the regeneration section of the novel Vitrisol® desulfurization process. It was determined that, for experimental conditions studied, o-xylene exhibited the highest sulfur solubility and toluene the lowest sulfur solubility from the investigated aromatic hydrocarbons. The sulfur solubility data reported in this study were in good agreement with sulfur solubility data in toluene, m-xylene and p-xylene published in open literature. Sulfur solubility data in o-xylene was not published in open literature. The temperature dependences of the solubility of sulfur in toluene, o-xylene, m-xylene and p-xylene were determined from solubility equilibria. The enthalpies of dissolution ΔHo of sulfur in toluene, o-xylene, m-xylene and p-xylene were determined to be 27.93 kJ/mol, 27.95 kJ/mol, 26.98 kJ/mol and 27.70 kJ/mol respectively.
{"title":"Sulfur Solubilities in Toluene, o-Xylene, m-Xylene and p-Xylene at Temperatures Ranging from 303.15 K to 363.15 K","authors":"W. Wermink, D. Spinu, G. Versteeg","doi":"10.7569/jnge.2018.692504","DOIUrl":"https://doi.org/10.7569/jnge.2018.692504","url":null,"abstract":"Abstract The solubility of sulfur in toluene, o-xylene, m-xylene and p-xylene was investigated at temperatures ranging from 303.15 K to 363.15 K. This study was required for the design of the regeneration section of the novel Vitrisol® desulfurization process. It was determined that, for experimental conditions studied, o-xylene exhibited the highest sulfur solubility and toluene the lowest sulfur solubility from the investigated aromatic hydrocarbons. The sulfur solubility data reported in this study were in good agreement with sulfur solubility data in toluene, m-xylene and p-xylene published in open literature. Sulfur solubility data in o-xylene was not published in open literature. The temperature dependences of the solubility of sulfur in toluene, o-xylene, m-xylene and p-xylene were determined from solubility equilibria. The enthalpies of dissolution ΔHo of sulfur in toluene, o-xylene, m-xylene and p-xylene were determined to be 27.93 kJ/mol, 27.95 kJ/mol, 26.98 kJ/mol and 27.70 kJ/mol respectively.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"19 1","pages":"71 - 95"},"PeriodicalIF":0.0,"publicationDate":"2019-01-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"72864161","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2019-01-02DOI: 10.7569/jnge.2018.692507
Gao Li, B. Guo, Xiaohui Zhang
Abstract Radial fractures are created in unconventional gas and oil reservoirs in modern well stimulation operations such as Hydraulic Re-Fracturing (HRF), Explosive Fracturing (EF) and High Energy Gas Fracturing (HEGF). This paper presents a mathematical model to describe fluid flow from reservoir through radial fractures to wellbore. The model can be applied to analyzing angles between radial fractures. Field case studies were carried out with the model using pressure transient data from three typical HRF wells in a lower-permeability reservoir. The studies show a good correlation between observed well performance and model-interpreted fracture angle. The well with the highest productivity improvement by the HRF corresponds to the interpreted perpendicular fractures, while the well with the lowest productivity improvement corresponds to the interpreted conditions where the second fracture is much shorter than the first one or where there created two merged/parallel fractures. Result of the case studies of a tight sand reservoir supports the analytical model.
{"title":"Mathematical Modeling of Fluid Flow to Radially Fractured Wells in Unconventional Reservoirs","authors":"Gao Li, B. Guo, Xiaohui Zhang","doi":"10.7569/jnge.2018.692507","DOIUrl":"https://doi.org/10.7569/jnge.2018.692507","url":null,"abstract":"Abstract Radial fractures are created in unconventional gas and oil reservoirs in modern well stimulation operations such as Hydraulic Re-Fracturing (HRF), Explosive Fracturing (EF) and High Energy Gas Fracturing (HEGF). This paper presents a mathematical model to describe fluid flow from reservoir through radial fractures to wellbore. The model can be applied to analyzing angles between radial fractures. Field case studies were carried out with the model using pressure transient data from three typical HRF wells in a lower-permeability reservoir. The studies show a good correlation between observed well performance and model-interpreted fracture angle. The well with the highest productivity improvement by the HRF corresponds to the interpreted perpendicular fractures, while the well with the lowest productivity improvement corresponds to the interpreted conditions where the second fracture is much shorter than the first one or where there created two merged/parallel fractures. Result of the case studies of a tight sand reservoir supports the analytical model.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"23 1","pages":"114 - 132"},"PeriodicalIF":0.0,"publicationDate":"2019-01-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"76063237","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2019-01-02DOI: 10.7569/jnge.2018.692506
F. Jou, A. E. Mather
Abstract The solubility of benzene in aqueous solutions of monoethanolamine has been measured at temperatures ranging from 25 °C to 100 °C.
在25 ~ 100℃的温度范围内，测定了苯在单乙醇胺水溶液中的溶解度。
{"title":"Solubility of Benzene in Aqueous Solutions of Monoethanolamine","authors":"F. Jou, A. E. Mather","doi":"10.7569/jnge.2018.692506","DOIUrl":"https://doi.org/10.7569/jnge.2018.692506","url":null,"abstract":"Abstract The solubility of benzene in aqueous solutions of monoethanolamine has been measured at temperatures ranging from 25 °C to 100 °C.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"51 1","pages":"109 - 113"},"PeriodicalIF":0.0,"publicationDate":"2019-01-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"77843653","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2018-07-26DOI: 10.7569/jnge.2018.692502
A. Tagiuri, A. Henni
Abstract The observed pseudo first order rate constants (k0) were measured for the reaction between CO2 and tertiary amines such as [2-(Diisopropylamino) ethanol (2-DIPA), N,n,n′,n′-tetrakis(2-hydroxypropyl)ethylenediamine (THPEDA), and Tris[2-(2-methoxyethoxy) ethyl]amine (TMEEA) in aqueous systems, and in methanol for N-(2-hydroxyethyl)aniline (2-HEAN)]. The measurements were performed from (298.15 to 323.15) K using the stopped flow technique, and at concentrations ranging from (200 to1100) mol/m3. The base catalysis mechanism was used to correlate the data obtained for both aqueous and non-aqueous systems, and to calculate the second order reaction rate constants k2 (m3mol−1s−1). The reaction rate of CO2 in aqueous (2-DIPA) solution was found to be faster than that in the other aqueous and non-aqueous tertiary amines studied and was also are higher than in aqueous Methyldiethanolamine (MDEA), an amine considered the industry standard.
摘要测定了CO2与叔胺[2-(二异丙基)乙醇(2- dipa)， N, N, N '， N ' -四(2-羟丙基)乙二胺(THPEDA)，三[2-(2-甲氧基乙氧基)乙基]胺(TMEEA)在水体系和甲醇体系中反应N-(2-羟乙基)苯胺(2- hean)]的准一级速率常数(k0)。测量范围为(298.15 ~ 323.15)K，使用止流技术，浓度范围为(200 ~ 1100)mol/m3。用碱催化机理将得到的水与非水体系的数据进行了关联，并计算了二级反应速率常数k2 (m3mol−1s−1)。研究发现，CO2在水(2-DIPA)溶液中的反应速度比研究的其他水和非水叔胺中的反应速度快，也高于水甲基二乙醇胺(MDEA)，一种被认为是行业标准的胺。
{"title":"Reaction Kinetics of CO2 in Aqueous 2-(Diisopropylamino)ethanol, N,n,n′,n′-tetrakis(2-hydroxypropyl)ethylenediamine, Tris[2-(2-methoxyethoxy) ethyl]amine, and N-(2-hydroxyethyl)aniline Solutions Using the Stopped-Flow Technique","authors":"A. Tagiuri, A. Henni","doi":"10.7569/jnge.2018.692502","DOIUrl":"https://doi.org/10.7569/jnge.2018.692502","url":null,"abstract":"Abstract The observed pseudo first order rate constants (k0) were measured for the reaction between CO2 and tertiary amines such as [2-(Diisopropylamino) ethanol (2-DIPA), N,n,n′,n′-tetrakis(2-hydroxypropyl)ethylenediamine (THPEDA), and Tris[2-(2-methoxyethoxy) ethyl]amine (TMEEA) in aqueous systems, and in methanol for N-(2-hydroxyethyl)aniline (2-HEAN)]. The measurements were performed from (298.15 to 323.15) K using the stopped flow technique, and at concentrations ranging from (200 to1100) mol/m3. The base catalysis mechanism was used to correlate the data obtained for both aqueous and non-aqueous systems, and to calculate the second order reaction rate constants k2 (m3mol−1s−1). The reaction rate of CO2 in aqueous (2-DIPA) solution was found to be faster than that in the other aqueous and non-aqueous tertiary amines studied and was also are higher than in aqueous Methyldiethanolamine (MDEA), an amine considered the industry standard.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"7 1","pages":"39 - 57"},"PeriodicalIF":0.0,"publicationDate":"2018-07-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"86371384","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2018-07-26DOI: 10.7569/jnge.2018.692501
H. Sørensen, Rasmus Risum Boesen, Sukit Leekumjorn, Peter Jørgensen Herslund
Abstract Parameters are presented enabling the Cubic Plus Association (CPA) concept to be applied with the Peng-Robinson equation for petroleum reservoir fluids carrying water and any of the gas hydrate inhibitors, methanol, mono-ethylene-glycol, or tri-ethylene-glycol. The acid gases, CO2 and H2S, are treated as solvating components, which do not self-associate, but cross-associate with water and hydrate inhibitors. Association is not considered for the remaining petroleum reservoir fluid constituents. The presented concept and parameters enable CPA to be used in flow assurance and process simulations on produced reservoir well streams containing water and hydrate inhibitors, while retaining consistency with prior reservoir simulations carried out using the Peng-Robinson equation on the water free reservoir fluid. A comprehensive data material for the mutual solubility of gases and aqueous components and hydrate inhibition is used to determine the pure component parameters and binary interaction parameters for associating components.
{"title":"Peng-Robinson Equation of State Extended to Handle Aqueous Components Using CPA Concept","authors":"H. Sørensen, Rasmus Risum Boesen, Sukit Leekumjorn, Peter Jørgensen Herslund","doi":"10.7569/jnge.2018.692501","DOIUrl":"https://doi.org/10.7569/jnge.2018.692501","url":null,"abstract":"Abstract Parameters are presented enabling the Cubic Plus Association (CPA) concept to be applied with the Peng-Robinson equation for petroleum reservoir fluids carrying water and any of the gas hydrate inhibitors, methanol, mono-ethylene-glycol, or tri-ethylene-glycol. The acid gases, CO2 and H2S, are treated as solvating components, which do not self-associate, but cross-associate with water and hydrate inhibitors. Association is not considered for the remaining petroleum reservoir fluid constituents. The presented concept and parameters enable CPA to be used in flow assurance and process simulations on produced reservoir well streams containing water and hydrate inhibitors, while retaining consistency with prior reservoir simulations carried out using the Peng-Robinson equation on the water free reservoir fluid. A comprehensive data material for the mutual solubility of gases and aqueous components and hydrate inhibition is used to determine the pure component parameters and binary interaction parameters for associating components.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"80 1","pages":"1 - 38"},"PeriodicalIF":0.0,"publicationDate":"2018-07-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"77972321","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2018-07-26DOI: 10.7569/jnge.2018.692503
Seungwoo Lee, R. Marriott
Abstract Both H2S and CO2 (acid gases) are removed during natural gas treatment and, if purified, CO2 fluids can be marketed as a high-pressure product, thereby adding a secondary value to hydrocarbon production. If high-pressure cryogenic separation techniques are used to separate the acid gas components, the CO2 fluid will require further processing before sale. In exploring high-pressure oxidation of H2S in CO2, we first required the solubility of elemental sulfur, S8, within CO2 and a model to calculate the sulfur fugacities over a range of temperatures and pressures. Solubility information allows one to (a) define sulfur dew point conditions within high-pressure recovery processes and (b) provide for fugacity coefficients necessary to calculate high-pressure recovery limits. In this work, the solubilities of elemental sulfur in dense phase CO2 were measured from T = 323.75 to 424.05 K and at p = 10 and 20 MPa. The measured solubilities of elemental sulfur increased with increasing temperature as well as increasing pressure. Two thermodynamic models were tested to correlate the experimental solubility: (i) a previous Virial Equation Model and (ii) a Fluctuation Solution Theory correlation. Both models are self-consistent with the reference vapor pressure at low pressure. Through the comparison of the calculated results, the Fluctuation Solution Theory correlation was found to best fit the experimental data.
{"title":"Solubility of Elemental Sulfur in Dense Phase Carbon Dioxide from T = 324 to 424 K and p = 10 and 20 MPa","authors":"Seungwoo Lee, R. Marriott","doi":"10.7569/jnge.2018.692503","DOIUrl":"https://doi.org/10.7569/jnge.2018.692503","url":null,"abstract":"Abstract Both H2S and CO2 (acid gases) are removed during natural gas treatment and, if purified, CO2 fluids can be marketed as a high-pressure product, thereby adding a secondary value to hydrocarbon production. If high-pressure cryogenic separation techniques are used to separate the acid gas components, the CO2 fluid will require further processing before sale. In exploring high-pressure oxidation of H2S in CO2, we first required the solubility of elemental sulfur, S8, within CO2 and a model to calculate the sulfur fugacities over a range of temperatures and pressures. Solubility information allows one to (a) define sulfur dew point conditions within high-pressure recovery processes and (b) provide for fugacity coefficients necessary to calculate high-pressure recovery limits. In this work, the solubilities of elemental sulfur in dense phase CO2 were measured from T = 323.75 to 424.05 K and at p = 10 and 20 MPa. The measured solubilities of elemental sulfur increased with increasing temperature as well as increasing pressure. Two thermodynamic models were tested to correlate the experimental solubility: (i) a previous Virial Equation Model and (ii) a Fluctuation Solution Theory correlation. Both models are self-consistent with the reference vapor pressure at low pressure. Through the comparison of the calculated results, the Fluctuation Solution Theory correlation was found to best fit the experimental data.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"4 1","pages":"58 - 69"},"PeriodicalIF":0.0,"publicationDate":"2018-07-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"80012107","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2017-12-29DOI: 10.7569/jnge.2017.692509
R. M. Zin, C. Coquelet, A. Valtz, M. I. Abdul Mutalib, K. Sabil
Abstract Mercaptans (RSH) or thiols are odorous substances offensive at low concentration and toxic at higher levels. The presence of mercaptans as pollutants in the environment creates a great threat on water and air safety. In this study, the solubility of mercaptans in water was studied through the use of apparent Henry’s Law constant (H) and infinite dilution activity coefficients (γ∞). These thermodynamic properties are useful for environmental impact studies and engineering design particularly in processes where dilute aqueous systems are involved. The aim of this paper is to develop a new thermodynamic correlation for estimation of apparent Henry’s Law constant (H), infinite dilution activity coefficient (γ∞) and solubility of C1-C4 mercaptans including their isomers in pure water. This correlation was developed based on compiled literature data. New measurements of apparent Henry’s Law constant and infinite dilution activity coefficients of methyl mercaptan and ethyl mercaptan in water were carried out to validate the developed correlation. Validation with new measurement data showed a good consistency with low differences (less than 5%) for majority of the data. Additionally, heat of absorption of various mercaptans in pure water was discussed based on temperature influence, Henry Law Constants and solubility.
{"title":"A New Thermodynamic Correlation for Apparent Henry’s Law Constants, Infinite Dilution Activity Coefficient and Solubility of Mercaptans in Pure Water","authors":"R. M. Zin, C. Coquelet, A. Valtz, M. I. Abdul Mutalib, K. Sabil","doi":"10.7569/jnge.2017.692509","DOIUrl":"https://doi.org/10.7569/jnge.2017.692509","url":null,"abstract":"Abstract Mercaptans (RSH) or thiols are odorous substances offensive at low concentration and toxic at higher levels. The presence of mercaptans as pollutants in the environment creates a great threat on water and air safety. In this study, the solubility of mercaptans in water was studied through the use of apparent Henry’s Law constant (H) and infinite dilution activity coefficients (γ∞). These thermodynamic properties are useful for environmental impact studies and engineering design particularly in processes where dilute aqueous systems are involved. The aim of this paper is to develop a new thermodynamic correlation for estimation of apparent Henry’s Law constant (H), infinite dilution activity coefficient (γ∞) and solubility of C1-C4 mercaptans including their isomers in pure water. This correlation was developed based on compiled literature data. New measurements of apparent Henry’s Law constant and infinite dilution activity coefficients of methyl mercaptan and ethyl mercaptan in water were carried out to validate the developed correlation. Validation with new measurement data showed a good consistency with low differences (less than 5%) for majority of the data. Additionally, heat of absorption of various mercaptans in pure water was discussed based on temperature influence, Henry Law Constants and solubility.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"53 73 1","pages":"148 - 170"},"PeriodicalIF":0.0,"publicationDate":"2017-12-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"87679275","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2017-12-29DOI: 10.7569/jnge.2017.692507
F. Jou, A. E. Mather
Abstract The solubility of ethane has been measured in 3 M solutions of alkanolamines at 75 °C. The solutions also contained various loadings of H2S. Partial pressures of ethane varied up to 6880 kPa. The effect of the hydrogen sulfide on the solubility of ethane is highly non-linear.
{"title":"Effect of H2S on the Solubility of Ethane in Alkanolamine Solutions","authors":"F. Jou, A. E. Mather","doi":"10.7569/jnge.2017.692507","DOIUrl":"https://doi.org/10.7569/jnge.2017.692507","url":null,"abstract":"Abstract The solubility of ethane has been measured in 3 M solutions of alkanolamines at 75 °C. The solutions also contained various loadings of H2S. Partial pressures of ethane varied up to 6880 kPa. The effect of the hydrogen sulfide on the solubility of ethane is highly non-linear.","PeriodicalId":22694,"journal":{"name":"The Journal of Natural Gas Engineering","volume":"8 1","pages":"143 - 147"},"PeriodicalIF":0.0,"publicationDate":"2017-12-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"87672572","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
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