Water Content of Sour Hydrocarbon Systems

1963 ◽  
Vol 3 (04) ◽  
pp. 293-297 ◽  
Author(s):  
J. Lukacs ◽  
D.B. Robinson

Abstract A knowledge of the equilibrium water content of hydrocarbon systems under pressure is important to the national gas industry. The information available on the solubility of water in hydrocarbon, hydrogen sulfide, and carbon dioxide systems is reviewed in this paper and the influence of the more important variables such as temperature, pressure and molecular structure on solubility in liquids and gases is discussed. A suitable chromatographic technique bas been developed for determining low concentrations of water. Tailing of the water peaks bas been eliminated by adding water to the carrier gas stream The method is applicable for both gas or liquid samples and is effective in the presence of hydrogen sulfide. The experimental study of water solubility in methane-hydrogen sulfide systems at a temperature of 16F has shown that the presence o/ hydrogen sulfide causes only a modest increase in water content at pressures up to 1,400 psia. Theoretical considerations and data on pure hydrogen sulfide and carbon dioxide suggest that the effect of both these compounds will be greater at higher pressures and in the liquid phase. Introduction Before transporting or processing natural gases and gas condensates, it is usually necessary to dry them using suitable dehydration equipment. The design and operation of this equipment requires a knowledge of the amount of water present in the fluid at the reservoir and operating conditions. This is influenced by temperature, pressure and composition, particularly when certain nonhydrocarbon components are present. Field experience indicates that hydrogen sulfide and carbon dioxide, for example, alter the usual water solubility relationships appreciably. However, an extensive search of the literature does not reveal any quantitative data on such systems. For sweet natural gases, generalized empirical correlations such as the one proposed by Katz, et al, can be used to predict water solubility with confidence at most temperatures and pressures of interest. However, existing theoretical relationships do not permit a calculation of the deviation from these curves when polar substances like hydrogen sulfide are present in the system. Thus one must resort to an experimental approach to obtain the necessary information. The fact that laboratory experimental methods frequently involve the use of mercury which reacts with hydrogen sulfide in the presence of water, and that hydrogen sulfide interferes with many chemical reactions specific for water has contributed to the difficulty of studying water solubility in systems containing hydrogen sulfide. In this investigation the water content of a limited member of methane-hydrogen sulfide mixtures was determined using a special technique with gas chromatography. REVIEW OF PUBLISHED DATA Experimentally determined water solubility data have been reported for methane, ethane, propane, n-butane, 1-butene, hydrogen sulfide and carbon dioxide. These studies report the effect of pressure, temperature and molecular structure on water solubility in single component gases and liquids. SPEJ P. 293^

1971 ◽  
Vol 11 (03) ◽  
pp. 272-276 ◽  
Author(s):  
Jack G. Roof

Abstract The solubility of sulfur in hydrogen sulfide has been determined by an absolute method at 21 combinations of pressure and temperature within the range of 1,020 to 4,520 psia and 110 deg. to 230 deg. F. respectively. Results, which appear to be consistent within about 2 percent, show the solubility to increase with pressure along an isotherm but to pass through maxima along isobars. Where direct comparison can be made, our values differ drastically from published results at lower pressures and are in serious disagreement at higher pressures. The solubility of sulfur in carbon disulfide is reported for pressures from 1,020 to 5,020 psia at 150 deg. F. No published data were found for direct comparison. Both the solubility of sulfur and the density of saturated solutions decrease with increasing pressure at this temperature. Introduction Difficulties in production arise when a fluid containing a high content of hydrogen sulfide occurs in a reservoir in which elemental sulfur is present Changes in pressure and temperature present Changes in pressure and temperature can cause deposition of dissolved sulfur from hydrogen sulfide-rich fluids in both the formation and the production tubing. The first step in a study of this problem is to determine the solubility of sulfur in pure hydrogen sulfide under conditions of interest in production. This report presents results of one such study. Values published in the literature generally appear to be grossly in error. In some approaches to repairing the damage caused by sulfur plugging of formation and tubing, carbon disulfide is used as a solvent. Experiments were run at a typical temperature of 150 deg. F and elevated pressure to obtain basic data on the solubility of sulfur in carbon disulfide. SOLUBILITY OF SULFUR IN HYDROGEN SULFIDE EQUIPMENT AND MATERIALS Except for the items described, the equipment used in this study was of the type commonly found in a high-pressure laboratory. A schematic sketch of the equipment is show in Fig. 1. The equilibrium vessel was a thin-walled Teflon bag machined from solid bar stock to the shape indicated in Fig. 1. The bag, of a design suggested by R. H. Arntson, Shell Development Co., was approximately 2.25 in. OD and 5.9 in. long, with a wall thickness of 0.045 in. A split ring around the upper flange pulled the tapered neck of the bag snugly onto the projecting cone of the pressure vessel to seal against the mercury surrounding the bag. Two-way Valve B was used to shut off the pressure vessel from the crossline between Valves pressure vessel from the crossline between Valves A and C. Valve B was designed to have minimal dead volume below the Teflon washer packing. Sulfur was caught for weighing in a special glass trap, also shown in Fig. 1. This vessel was made of 35-mm OD pyrex Tubing and was about 7.5 in. in length. Each end terminated in precision-ground 0.25-in. tubing to accept Swagelok fittings. Each chamber included a coarse glass frit at its downstream end and was loosely filled with glass wool. Pressure was measured on a Heise gauge, which had been calibrated against an Aminco dead-weight gauge. Uncertainties in pressure should seldom exceed 5 psia. The pressure differential across the wall of the Teflon bag fell within this uncertainty in pressure. Temperature in the pressure vessel was measured by a tubular iron-constantan thermocouple inserted into a small hole in the bottom of the vessel. Emf of the couple was measured on a Rubicon potentiometer. The thermocouple had been calibrated potentiometer. The thermocouple had been calibrated against a platinum resistance thermometer. Uncertainties in temperature probably were not greater than 1 deg. F. A Thermotrol was used to control the temperature of the air thermostat. Both the precipitated sulfur and the carbon disulfide were Baker's Analyzed grade. SPEJ P. 272


Catalysts ◽  
2018 ◽  
Vol 8 (10) ◽  
pp. 441 ◽  
Author(s):  
Ren-Jun Kang ◽  
Yong-Song Chen

When the fuel supplied to a high-temperature proton exchange membrane fuel cell (HT-PEMFC) is produced by hydrocarbon formation, hydrogen sulfide (H2S) may appear, resulting in decreased cell performance and durability. To study the effects of H2S on the performance and durability of the HT-PEMFC, a series of experiments was conducted. In the first step, the effects of polyvinylidene fluoride (PVDF) and platinum loading on cell performance were investigated and discussed under pure hydrogen operation conditions. Optimal PVDF and platinum compositions in the catalyst layer are suggested. Then, the effect of H2S on membrane electrode assembly (MEA) performance with various platinum loadings was investigated by supplying hydrogen containing 5.2 ppm of H2S to the anode of the MEA. An electrochemical impedance spectroscope was employed to measure the impedance of the MEAs under various operating conditions. Finally, degradation of the MEA when supplied with hydrogen containing 5.2 ppm of H2S was analyzed and discussed. The results suggest that the performance of an MEA with 0.7 mg Pt cm−2 and 10% PVDF can be recovered by supplying pure hydrogen. The rate of voltage decrease is around 300 μV h−1 in the presence of H2S.


1960 ◽  
Vol 219 (01) ◽  
pp. 54-60 ◽  
Author(s):  
D.B. Robinson ◽  
C.A. Macrygeorgos ◽  
G.W. Govier

2015 ◽  
Vol 15 (1) ◽  
pp. 72
Author(s):  
Allan N. Soriano ◽  
Adonis P. Adornado ◽  
Angelica A. Pajinag ◽  
Diana Joy F. Acosta ◽  
Niel M. Averion ◽  
...  

The paper evaluates the performance of the nine selected alkanolamines, namely, monoethanolamine (MEA), diethanolamine (DEA), monomethylethanolamine (MMEA), aminoethylethanolamine (AEEA), diisopropanolamine (DIPA), triethanolamine (TEA), dimethylethanolamine (DMEA), N-methyldiethanolamine (MDEA), and piperazine (PZ) for post-combustion capture of pure hydrogen sulfide (H2S) and mixtures of hydrogen sulfide and carbon dioxide (CO2) at different solvent mass flows: 500, 750, and 1000 kg/h using Aspen Plus® Version 7.2. The objective of the paper is to select the best chemical absorbent for each different criterion: percent H2S removal, percent H2S solvent carrying capacity, percent H2S retained in the lean solvent, percent CO2 and H2S removal, percent CO2 and H2S solvent carrying capacity, percent CO2 and H2S retained in the lean solvent. Based from the obtained results, piperazine is an absorbent that has a good potential for use as a single amine or in mixtures with other amines for capture of pure H2S and mixtures of H2S and CO2.


2021 ◽  
Vol 937 (4) ◽  
pp. 042085
Author(s):  
N Mukhutdinov ◽  
I Khalismatov ◽  
N Akramova ◽  
R Zakirov ◽  
A Zakirov ◽  
...  

Abstract The results of long-term studies of natural gases in the Bukhara-Khiva oil and gas region of Uzbekistan are summarized. The results of studying the composition of gases in hydrocarbon deposits generated by OM of continental (terrigenous deposits of the Cretaceous and Middle Jurassic) and marine (carbonate Jurassic) facies are presented. Regularities of changes in individual constituents of gases (hydrocarbons, hydrogen sulfide, carbon dioxide, nitrogen, etc.) with depth are considered; the influence exerted on the composition of gases by various factors and, above all, those of them, which, in the opinion of most researchers, are the main ones. The revealed patterns are used for predictive assessment of the distribution of various constituents of natural gases in the study area.


1975 ◽  
Vol 15 (03) ◽  
pp. 227-233 ◽  
Author(s):  
F.W. Schremp ◽  
G.R. Roberson

Abstract Laboratory tests showed that properly welded X-60 pipeline steel was not susceptible to environmental failure in supercritical carbon dioxide (CO2); and corrosion rates were less than 0.02 mils penetration per year (MPY). Other tests showed penetration per year (MPY). Other tests showed nonmetallic seals to be susceptible to damage. Seals constructed from Teflon, nylon, semi-rigid polyurethanes and ethylene-propylene rubber were polyurethanes and ethylene-propylene rubber were acceptable. Thin-film coatings and centrifugally cast cement also were acceptable pipe linings. Introduction Operation of the SACROC carbon dioxide-miscible secondary recovery project involves gathering, pipelining, and injecting more than 200,000,000 pipelining, and injecting more than 200,000,000 scf/D of carbon dioxide (CO2) into selected wells at a pressure of 2,400 psia. Waste CO2 is collected at approximately ambient conditions from four natural gas stripping stations. Thirteen compressors, totaling nearly 75,000 hp, are used to compress the gas to 2,000 to 2,400 psia. The gas is transported 232 miles in a 16- and 12-in. diameter pipeline to the Kelly-Snyder field, Scurry County, pipeline to the Kelly-Snyder field, Scurry County, Tex., where an additional 6,500 hp is used further to compress and to inject the gas at 2400 psia. Composition of the waste CO2 varies at each of the four stripping stations. The gas may contain 3 to 15 percent light hydrocarbons (chiefly methane), with up to 300 ppm hydrogen sulfide and a water content up to saturation. According to pipeline specifications, the mixed high-pressure gas contains at least 90 mol percent CO2 with the balance consisting of C1-C6 hydrocarbons. The mixed gas also contains less than 50 ppm water vapor and less dean 300 ppm hydrogen sulfide. In service, the line temperature varies from 45 to 120 degrees F. Before construction, it was necessary to know how supercritical CO2 would affect welded X-60 pipeline steel and other materials that might be used pipeline steel and other materials that might be used in the system. Laboratory tests were made after a literature search failed to produce the needed information. APPARATUS The apparatus used to simulate SACROC CO2 pipeline conditions is shown in Fig. 1, which shows pipeline conditions is shown in Fig. 1, which shows that the CO2 charging system consists of a source of CO2, a molecular sieve desiccator, a Sprague compressor unit, and an accumulator. Compressed CO2 is stored in the accumulator at 3,500 psig and nitrogen is used to maintain the pressure. When needed, hydrocarbon gas also can be supplied separately to the accumulator. Compressed CO2 at 2,000 psig is supplied from the accumulator to each of the three test cells via a regulator and check valves, V-37 and V-38. Test Cell 1 has a separate pump to circulate the CO2. Test Cells 2 and 3 are connected in series with a second circulating pump. Pump velocities can be varied but usually are set to develop a lineal flow rate of 30 to 40 in./min in the test cells. Test Cells 1 and 2 are equipped with Panametrics hygrometer probes to monitor the water content. probes to monitor the water content. The test cells also have connections to inject H2S and water and to sample the gas composition. Hydrogen sulfide content is monitored with Kitagawa detector tubes (0.01 to 0.17 volume percent). Test temperature is maintained at 72 2 degrees F. Heating mantles (not shown) can be attached to the cells to maintain a temperature of 130 degrees 2 degrees F when needed. WELDED X-60 PIPELINE STEEL TESTS The purpose of these tests was to determine the effect of simulated SACROC CO2 pipeline conditions on field-welded X-60 steel. Six manufacturers were contacted and from each were obtained samples of pipe that were at least 12 in. in diameter and with pipe that were at least 12 in. in diameter and with a minimum wall thickness of 0.344 in. Compositions of the pipe samples appear in Table 1. SPEJ P. 227


2018 ◽  
Vol 2 (2) ◽  
Author(s):  
SULASMI ANGGO

The Analysis of physical chemical from dara shells (Anadara granosa) origin from Kayutanyo, kab. Banggai, has been conducted.Dara shell meat is sleaned and dried and after that powered with blender. Determine % rendement, water bonding capacity and index water solubility with Anderson method, coarse fat content with gravimetric method and carbohydrate method with “bye difference” decrease method.The result of analysis showed rendement value is 24,35%, water bonding capacity is 1,6248 gram/ml, index water solubility is 0,202 gram/ml, water content is 79,0045%, total dust content is 1,072%, coarse protein content is 2,25%, coarse fat content is 8,47%, carbohydrate content is 9,2035%. Keyword : Dara shells, (Anadara granosa), analysis physical chemical


Nutrients ◽  
2021 ◽  
Vol 13 (5) ◽  
pp. 1519
Author(s):  
Alessandra Berry ◽  
Barbara Collacchi ◽  
Roberta Masella ◽  
Rosaria Varì ◽  
Francesca Cirulli

Due to the global increase in lifespan, the proportion of people showing cognitive impairment is expected to grow exponentially. As target-specific drugs capable of tackling dementia are lagging behind, the focus of preclinical and clinical research has recently shifted towards natural products. Curcumin, one of the best investigated botanical constituents in the biomedical literature, has been receiving increased interest due to its unique molecular structure, which targets inflammatory and antioxidant pathways. These pathways have been shown to be critical for neurodegenerative disorders such as Alzheimer’s disease and more in general for cognitive decline. Despite the substantial preclinical literature on the potential biomedical effects of curcumin, its relatively low bioavailability, poor water solubility and rapid metabolism/excretion have hampered clinical trials, resulting in mixed and inconclusive findings. In this review, we highlight current knowledge on the potential effects of this natural compound on cognition. Furthermore, we focus on new strategies to overcome current limitations in its use and improve its efficacy, with attention also on gender-driven differences.


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