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HomeMy WebLinkAboutNC0003433_Fig 6-13 One Dimension_20160229dc 2 Governing Equation R ac = D axz — v ax c(x, 0) = Cti c(0 t) — �Co 0<t<—to p t > to ac ax (00' t) = 0 _ Cti+(Co —Cti)A(x,t) 0<tto c(x, t) — 51Cj + (Co — Cti) A(x, t) — (Co — Cti) A(x, t — to) t > to } Where: 1 Rx — vt 1 vx Rx + vt A(x,t)=2erfc i +2exp(D)erfc i 2 2(DRt)2 2 2(DRt)' where: c(x,t) = concentration at a distance x from the source area and a time t cl = background concentration co = source concentration v = groundwater velocity (v=ki/n) t = time to = time when source is terminated x = distance from source D = dispersion R = retardation factor erfc = complementary error function exp = exponent 148 RIVER STREET, SUITE 220 GREENVILLE, SOUTH CAROLINA 29601 �%� PHONE 864-421-9999 ✓� ■ ■���� www s nterracor .com DRAWNBY: KBERNIER DATE: FEBRUARY PROJECT MANAGER: C. SUTTELL LAYOUT: FILE PATH: P:\G,ke Energy Progress. 10261103, Cape Fear Ash Basin GW Assessment Pl,,\20. EG_CAP\CAP P,,1 2\Figures FIGURE 6-13 ONE DIMENSIONAL CONVECTIVE -DISPERSIVE SOLUTE TRANSPORT WITH SOURCE TERM AND SORPTION PROPERTIES CAPE FEAR STEAM ELECTRIC PLANT MONCURE, NORTH CAROLINA