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32 PEFTEC 2017 - Show Preview


the purge stage and extraction of a mixture of standards and additional compounds, including organo sulphides and organo thiolates (mercaptides) and extraction from other matrices including naphtha and crude oils must be undertaken.


References


(1) Wilhelm, S.M., Liang, L and Kirchgessner, D. (2006). Energy Fuels 20, pp 180-186


(2) Spiric, Z. and Mashyanov, N.R. (2000). Fresenius J Anal Chem, 366 pp 429-432.


(3) Lang, D., Gardner, M., and Holmes, J. (2012). http://www. mercurynetwork.org.uk/wp-content/uploads/2009/09/IKIMP-Oil- and-Gas-2012-Final-Report.pdf


Table 1: Recoveries of a selection of inorganic and organic mercury standards with serial extraction using L-cysteine, saturated NaCl and the UOP-938 stipu- lated solution of 100 mg/L NaCl.


In Conclusion


The use of a fi ne sintered frit during the purge stage reduces signifi cantly the time needed to remove all elemental mercury. It also decreases the proportion of any (CH3


)2 Hg present that would


be desorbed and thus improves the accuracy of quantifi cation of both the elemental and non-ionic organic mercury species in a condensate sample.


The study to date has shown that L-cysteine (1% v/v) exhibits far greater effi cacy than NaCl (100 mg/L) for extraction of soluble ionic mercury species from condensate. Indeed, even with mercury concentrations that exceeded the UOP 938-10 limit (in some cases) and with an extraction/contact time of just 10 minutes (from the fi rst serial extraction), the L-cysteine extraction effi ciency for all inorganic and organic ionic mercury species


tested, except Hg2 SO4 , exceeded 85%. Where time permits,


employing an optimised serial extraction with L-cysteine is likely to be the best approach for on-site mercury speciation.


The relatively poor extraction effi ciency of 100 mg/L NaCl excludes it from being the aqueous solution of choice for Qa3 on-site applications. It must also surely cast some doubt upon the effi ciency of UOP 938-10, certainly in samples where Hg2 C2


SO4 H5 HgCl are present.


If accurate, on-site speciation and quantifi cation of mercury species in the oil and gas industry is to be achieved so that fully effective mercury removal systems are employed and mercury partitioning within the hydrocarbon processing system is fully understood, then a robust method is required. Thus, further studies involving the optimisation of the parameters during


and


(4) Wilhelm, S.M., Liang, L., Cussen, D. and Kirchgessner, D. A (2007). Environ Sci Technol, 41 (13), pp 4509-4514.


(5) Carnell, P.J.H., Row V.A. and McKenna, R. (2007). http://www. ivt.ntnu.no/ept/fag/tep4215/innhold/LNG%20Conferences/2007/ fscommand/PO_08_Row_s.pdf


(6) Harfoushian J. (2013). SPE, 166220.


(7) Kirby M. and Baker S. (2017). Poster presented at: 13th International Conference on Mercury as a Global Pollutant, July 16 – 21 2017, Providence, Rhode Island, USA.


(8) Rahman, G.M.M., Fahrenholz T.M., Kingston H.M.S, Pamuku M., Hwang J.D. and Young L.A (2010). Spectroscopy, 25(1) pp 36 – 45.


(9) Bouyssiere, B., Baco, F., Savary, L and Lobiñski, R. (2002). Journal of Chromatography A, 976 pp 431–439.


(10) Gaulier, F., Gibert, A., Walls, D., Langford, M., Baker, S., Baudot, A., Porcheron, F. and Lienemann, C-P. (2015). Fuel Processing Technology, 131 pp 254–261.


Author Details Stuart Baker, Matthew Kirby, Matthew Bower, David Walls and Mark Andrew, Qa³ Ltd • Unit 3, The Calvert Centre, Woodmancott, Winchester, Hampshire, SO21 3BN, UK Tel: + 44 (0) 1256 397390 • Email: enquiries@qa3.co.uk • Web: www.qa3.co.uk


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