scholarly journals Sulfate Removal From Water Produced During CO2 Enhanced Oil Recovery, Coal-Bed Methane Recovery, and Mining Operations Using Anion Exchange Resins

2015 ◽  
Vol 2015 (2) ◽  
pp. 1-10
Author(s):  
Cole Duckworth ◽  
Charles J Werth ◽  
Seyed A Destgheib ◽  
Chad Knutson
2012 ◽  
Author(s):  
Chad Knutson ◽  
Seyed A. Dastgheib ◽  
Yaning Yang ◽  
Ali Ashraf ◽  
Cole Duckworth ◽  
...  

1978 ◽  
Vol 18 (03) ◽  
pp. 207-218 ◽  
Author(s):  
D.R. Zornes ◽  
G.P. Willhite ◽  
M.J. Michnick

Abstract The separation of petroleum mono- and disulfonates on an anion-exchange column using high-pressure liquid chromatography (HPLC) was investigated as a method /or the determination of sulfonate concentrations in aqueous or hydrocarbon solutions. Quantitative analysis o/ brine (3,000 ppm) or hexane solutions containing 500 to 5,000 ppm ppm) or hexane solutions containing 500 to 5,000 ppm of unfractionated Witco TRS 10-80 Petronate was possible to a precision of 2 percent. Extending the possible to a precision of 2 percent. Extending the method to solutions containing TRS 10-80 sulfonates with altered mono- and di-ratios was accomplished by deriving ultraviolet (UV) response factors /or the average mono- and disulfonates present in the original TRS 10-80. Application of the HPLC technique with monoand disulfonate response factors was demonstrated by analysis of sulfonate concentrations in both phases in a series of two-phase hexane-brine phases in a series of two-phase hexane-brine systems. Trends in the distribution coefficients were identified readily. Preferential partitioning of the mono- and disulfonates between the hydrocarbon and brine phases was indicated by changes in the ratio of the mono- and disulfonate areas on the chromatographs. The HPLC technique gave information on the sulfonate composition that was not obtained by traditional wet-lab methods. Introduction Surfactant concentration is an important parameter in the evaluation of surfactants used in oil recovery processes. Unfortunately, quantative analysis of processes. Unfortunately, quantative analysis of surfactants commonly used in enhanced oil recovery processes is difficult because these often are processes is difficult because these often are complex mixtures of anionic surfactant molecules. Commercially available petroleum sulfonates not only contain a range of molecular weights but also vary in percentage of mono-, di- and polysulfonated molecules. Numerous analytical techniques have been presented in the literature to determine anionic presented in the literature to determine anionic surfactants in water and oil. The two-phase titration technique, introduced by Epton in 1946, was modified and used to determine petroleum sulfonates. Disadvantages of the Epton titration method includethe average equivalent weight of the anionic surfactant must be known;it cannot differentiate between mono-, di-, and polysulfonated molecules;experimental evidence polysulfonated molecules; (3) experimental evidence indicates the method is not stoichiometric for low molecular-weight sulfonates and there is limited knowledge of be stoichiometry for polysulfonated molecules; andit is not automated easily. The Epton titration method has been used because no other good analytical techniques exist. Recent developments in HPLC and in ion-exchange resin offer the possibility of improved analytical techniques to determine petroleum sulfonates. Traditionally, the chromatographic separation of aromatic sulfonates by ion-exchange has been difficult because of excessive noncoulombic adsorption on polystyrene-type, anion-exchange resins. Successful separation of low molecular-weight aromatic sulfonates on a quaternized polyalkeneamine, anion-exchange resin was reported by Stehl. Development of pellicular anion-exchange resins with a quaternary alkylamine bonded to an inert nonpermeable core further reduced the anionic adsorption of aromatic sulfonate molecules and extended the range of application. Schmit and Singh reposed separations of naphthalene-sulfonic-acid dye intermediates on pellicular anion-exchange resin. Suffridge reported pellicular anion-exchange resin. Suffridge reported separation of a petroleum sulfonate into its monoand disulfonate constituents on a pellicular anion-exchange resin using a linear ionic-strength gradient. SPEJ P. 207


2012 ◽  
Vol 616-618 ◽  
pp. 1591-1594
Author(s):  
Feng Shan Han ◽  
Li Song

The reduction of greenhouse gases emission is a growing concern of many countries. The geological storage of is useful and effective approaches to reduce emission. The oil and natural gas industries have long commercial practice of gas injection, enhanced oil recovery ( -EOR). Because coal seam has strong absorption capacity for ,the coal seam can be used as geological storage reservoirs, and coal seam has such characteristics that coal seam is preference for absorption and postponement for absorption, injection into coal seam can enhanced coal bed methane recovery, -ECBM, is a new energy generated by methane from injection into coal seam, and is beneficial complement of the energy , injection into coal seam can not only reduce greenhouse gases emission and but also enhance coal bed methane recovery, which is very significance to environment protection and energy sustainable development in china.


Energy ◽  
2004 ◽  
Vol 29 (9-10) ◽  
pp. 1611-1621 ◽  
Author(s):  
F. van Bergen ◽  
J. Gale ◽  
K.J. Damen ◽  
A.F.B. Wildenborg

1999 ◽  
Vol 40 (9) ◽  
pp. 207-214 ◽  
Author(s):  
J.-P. Croué ◽  
D. Violleau ◽  
C. Bodaire ◽  
B. Legube

The objective of this work was to compare the affinity of well characterized NOM fractions isolated from two surface waters with strong (gel matrix and macroporous matrix) and weak anion exchange resins (AER) using batch experiment conditions. The structural characterization of the fraction of NOM has shown that the higher the hydrophilic character, the lower the C/O atomic ratio, the lower the SUVA, the lower the aromatic carbon content and the lower the molecular weight. In general (not always), strong AER was more efficient to remove DOC than weak AER. For the same water source (Suwannee River), the higher the molecular weight of the NOM fraction, the lower the affinity with AER. Increasing the ionic strength favored the removal of the hydrophobic NOM fraction (“salting out” effect) while increasing the pH apparently reduced the removal of the hydrophilic NOM fraction. Results were discussed in terms of size exclusion, adsorption, anion exchange and also hydrophobic/hydrophilic repulsion.


2020 ◽  
pp. 039139882094773
Author(s):  
Karin Strobl ◽  
Stephan Harm ◽  
Ute Fichtinger ◽  
Claudia Schildböck ◽  
Jens Hartmann

Introduction: Heparin and citrate are commonly used anticoagulants in membrane/adsorption based extracorporeal liver support systems. However, anion exchange resins employed for the removal of negatively charged target molecules including bilirubin may also deplete these anticoagulants due to their negative charge. The aim of this study was to evaluate the adsorption of citrate by anion exchange resins and the impact on extracorporeal Ca2+ concentrations. Methods: Liver support treatments were simulated in vitro. Citrate and Ca2+ concentrations were measured pre and post albumin filter as well as pre and post adsorbents. In addition, batch experiments were performed to quantify citrate adsorption. Results: Pre albumin filter target Ca2+ concentrations were reached well with only minor deviations. Citrate was adsorbed by anion exchange resins, resulting in a higher Ca2+ concentration downstream of the adsorbent cartridges during the first hour of treatment. Conclusions: The anion exchange resin depletes citrate, leading to an increased Ca2+ concentration in the extracorporeal circuit, which may cause an increased risk of clotting during the first hour of treatment. An increase of citrate infusion during the first hour of treatment should therefore be considered to compensate for the adsorption of citrate.


2009 ◽  
Vol 1 (1) ◽  
pp. 81-89 ◽  
Author(s):  
Wang Zuo-tang ◽  
Wang Guo-xiong ◽  
Rudolph V. ◽  
Diniz da Costa J. C. ◽  
Huang Pei-ming ◽  
...  

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