Surfactant Analysis & Adsorption on Carbonate Minerals Kun Ma, Yezi Dong, Leyu Cui, Yu Bian, Maura Puerto, Sibani Lisa Biswal and George J. Hirasaki Department of Chemical & Biomolecular Engineering Rice University, Houston, TX 04/26/2011 Outline ★ Surfactant analysis - Potentiometric titration - High performance liquid chromatography ★ Adsorption on carbonate minerals - Dolomite and carbonate sand - Ionic and nonionic surfactants - Simulation of transport of a finite slug List of surfactants in this study Trade name (Manufacturer) Chemical name Acronym (in this study) Agent X-3153-026 (Stepan) sodium (C1618) alpha olefin sulfonate AOS 1618 Petrostep S-2A (Stepan) sodium (C1518) Internal olefin sulfonate IOS 1518 Steol CS-330 (Stepan) sodium laureth sulfate, 3 moles EO CS 330 -- (Arcos) hexadecyltrimethylammonium bromide CTAB -- (Sigma-Aldrich) dodecyltrimethylammonium bromide DTAB -- (Sigma-Aldrich) hexadecylpyridinium chloride CPC Amphosol CS-50 (Stepan) cocamidopropyl hydroxysultaine CS 50 Mackam LAB (Rhodia) lauryl and myristyl betaines LAB Mackam CB-35 (Rhodia) coco betaines CB Tergitol 15-S-30 (Dow) secondary alcohol ethoxylate, 31 EO 15-S-30 Potentiometric titration • For anionic surfactants (such as AOS 1618): -- An ion selective electrode (ISE, pHoenix, Cat. No. SUR1502) is used for aqueous titration; -- TEGO ® trant A100 (~10-3 mol/L) is used as the titrant; -- Serial diluted SDS solution is used to calibrate the titrant. Titration curves of SDS by hyamine and TEGO High Performance Liquid Chromatography Column Guard Column Storage Solution Mobile phase pH Temperature Pressure Typical Flow Rate Injection Volume Dionex Acclaim Surfactant, 4.6 ×250mm (P/N 063203) Dionex Acclaim Surfactant, 4.6 ×10mm (P/N 069701) Acetonitril/0.1%Acetic Acid or Acetonitril/100mM NH4OAc at v/v 80/20 ACN/DI or Methanol/DI, 0%-100% organic in mobile phase 2.5-7.5 <60oC <5500 psi 0.8-2.0 mL/min 5-50 µL Analysis of zwitterionic surfactants Cocamidopropyl hydroxysultaine brine surfactant 0.435% AMPHOSOL CS-50 in Brine; Injection: 25 µL; Column Temperature: 25°C; Mobile Phase: 100mM Ammonium Acetate(pH5.5)/CAN, linear gradient: 75/25-25/75 in 20 minutes; Flow rate: 1 ml/min; ELSD setting: 60°C, 3.5 Bar. Successful separation of high-salinity brine and surfactants Carbonate minerals for static adsorption • Carbonate sand (limestone): 20/40 mesh, purchased from Franklin Minerals, Nolanville TX, BET surface area 0.29 m2/gram. • Dolomite powder: 200+ mesh, purchased from Vital Earth / Carl Pool, BET surface area 0.97 m2/gram. • Equilibration time for static adsorption experiments at room temperature: 24 hours. • Synthetic brine: NaCl 182.31 g/L, CaCl2 58.33 g/L, MgCl2.6H2O 25.62 g/L. Carbonate sand vs. dolomite powder AOS1618 static adsorption in DI water Carbonate 20/40 Dolomite powder 2 1.8 Adsorption (mg/m^2) 1.6 1.4 1.2 1 0.8 0.6 0.4 0.2 0 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 Equilibrium surfactant concentration (wt%) 0.16 0.18 Comparison of anionics Comparison of cationics Comparison of zwitterionics Adsorption of TERGITOL 15-S-30 Adsorption plateaus anionics cationics nonionics zwitterionics Surfactant adsorption model Assumptions: 1. Surfactant is present in aqueous phase, but not in gaseous phase; 2. Surfactant adsorption can be described with a Langmuir-type isotherm. ( C sw S w C sg S g ) [ K sw t x (S w C sw x C ss s a s s , max (1 ) ) K sg C sw 1 C sw C ss t x (S g ( C sw u w C sg u g ) x C sg x )] Static adsorption of anionic surfactant on dolomite AOS1618 static adsorption on dolomite (0%Na2CO3, 0%NaCl) Experimental data Fit by Langmuir isotherm 2 s 2 Surface excess (mg/m ) 1.8 s , max 1.6 1.4 C sw 1 C sw s , max 1 . 688 1.2 1 12 . 2 L / g 0.8 0.6 0.4 0.2 0 0 0.2 0.4 0.6 0.8 1 Residual concentration (g/L) 1.2 1.4 1.6 mg / m 2 Propagation of a finite slug (0.5 PV) CONCENTRATION CONCENTRATIONPROFILE PROFILE PROFILEat atatttDDt=10 =0.1 =0.2 =0.3 =0.4 =0.5 =0.6 =0.7 =0.8 =0.9 =1.1 =1.2 =1.3 =1.4 =1.5 =1 =2 =3 =4 =5 CONCENTRATION D DIMENSIONLESS CONCENTRATION CONCENTRATION DIMENSIONLESS 1.2 FD(NX=1000) FD(NX=1000) MOC MOC 1 0.8 0.6 0.4 0.4 0.2 0.2 00 00 0.1 0.1 0.2 0.2 Surfactant: AOS1618, 0.2% wt Mineral: dolomite powder No dispersion 0.7 0.6 0.5 0.4 0.3 0.3 0.4 0.5 0.6 0.7 DISTANCE DIMENSIONLESS DIMENSIONLESS DISTANCE 0.8 0.8 0.9 0.9 11 Effluent of a finite slug (0.5 PV) EFFLUENT CONCENTRATION HISTORY DIMENSIONLESS EFFLUENT HISTORY 1 FD(NX=1000) MOC 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 0 2 4 Surfactant: AOS1618, 0.2% wt Mineral: dolomite powder 6 8 10 12 DIMENSIONLESS TIME 14 16 18 20 Conclusions ★ Ethoxylated anionic surfactant CS 330 has lower adsorption than AOS 1618 or IOS 1518 on dolomite in DI water at room temperature. ★ The nonionic surfactant Tergitol 15-S-30 shows the lowest adsorption on dolomite in DI water at room temperature among all the surfactants measured so far. ★ For the cationic surfactant DTAB, the adsorption plateau is close to that of CS 330 on dolomite in DI water at room temperature; however, other cationics exhibit high adsorption, and a possible reason is that room temperature is close to the temperature of phase transition (Kraft temperature). ★ The zwitterionic surfactants CS-50 and LB have high adsorption in both DI water and synthetic brine. Acknowledgment This work was financially supported by ADNOC, ADCO, ZADCO, ADMA-OPCO and PI, U.A.E. Analysis of zwitterionic surfactants Lauryl betaine HPLC profile of MACKAM LAB (0.21 wt% lauryl betaine) and MACKAM CB-35 (0.21 wt% lauryl betaine) with an ELSD detector. MACKAM CB-35 contains cetyl betaine while MACKAM LAB does not Analysis of nonionic surfactants 0.2% Tergitol 15-S-30 in Brine; Injection: 50 µL; Column Temperature: 25°C; Mobile Phase: 100mM Ammonium Acetate(pH5.5)/CAN, linear gradient: 75/2525/75 in 20 minutes; Flow rate: 1 ml/min; ELSD setting: 60°C, 3.5 Bar. Carbonate sand vs. dolomite powder AOS1618 static adsorption in DI water Carbonate 20/40 Dolomite powder 2.4 2.2 2 Adsorption (mg/g) 1.8 1.6 1.4 1.2 1 0.8 0.6 0.4 0.2 0 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 Equilibrium surfactant concentration (wt%) 0.16 0.18 Effect of carbonate / bicarbonate ions Adsorption of MACKAM LAB Future work ★ Continue current work in synthetic brine; ★ Potential determining ions for adsorption reduction; ★ Adsorption at elevated temperatures; ★ Evaluation of other foaming surfactants.