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<< "A0 = " << a0 << " P&L = " << pl << " Final = " << a0 + pl << " IM = " << imargin << " MM = " << mmargin << endl; // Reports individual trades cout << "INDIVIDUAL TRADES" << endl; for(Trades::size_type i = 0; i < ts.size(); i++) { cout << (unsigned int)i << " (" << (unsigned int)ts[i].entryIndex() << "," << (unsigned int)ts[i].exitIndex() << ")" << " P&L=" << ts[i].pl() << " SIZE=" << ts[i].entrySize() << " P&L/SIZE=" << ts[i].plPerUnit() << " EQ=" << ts[i].equityChange() << " COST=" << ts[i].totalCost() << endl; } // Reports statistics of trades cout << "STATISTICS OF TRADES" << endl; cout << "Total P&L = " << total_pl_alg(ts) << endl; cout << "Total P&L/unit = " << total_pl_unit_alg(ts) << endl; cout << "Gross profit = " << gross_profit_alg(ts) << endl; cout << "Gross profit/unit = " << gross_profit_unit_alg(ts) << endl; cout << "Gross loss = " << gross_loss_alg(ts) << endl; cout << "Gross loss/unit = " << gross_loss_unit_alg(ts) << endl; cout << "Total number of trades = " << (unsigned int)ts.size() << endl; cout << "Number of winning trades = "

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Purpose: This script step switches the current layout to Find mode, enabling you to execute Find requests (which is the same as choosing View Find Mode or pressing +F/Ctrl+F). Options: Specify Find requests, Pause Select Specify Find requests to start each Find request with the criteria that were in effect when the script was created. If you prefer to start the Find request from scratch, leave this option unchecked. If additional steps follow Enter Find Mode, you should also select the Pause option assuming you want users to have an opportunity to modify the Find requests. See also: Perform Find, Enter Browse Mode, Enter Preview Mode

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, 78, 1040 1052 Roussinova, V, S M Kresta, and R J Weetman 2001 Low frequency macroinstabilities in a stirred tank: scale-up and prediction based on large eddy simulations, presented at the 18th Biennial North American Mixing Conference, Pocono Manor, PA, June Shih, T-H, W W Liou, A Shabbir, and J Zhu (1995) A new k eddy-viscosity model for high Reynolds number turbulent ows: model development and validation, Comput Fluids, 24, 227 238 Syamlal, M, W Rogers, and T J O Brien (1993) MIFX Documentation, Vol 1, Theory Guide, DOE/METC-9411004, NTIS/DE9400087, National Technical Information Service, Spring eld, VA Tanguy, P A, F Thibault, C Dubois, and A Ait-Kadi (1999) Mixing hydrodynamics in a double planetary mixer, Chem Eng Res Des, 77(4), 318 324 Tipnis, S K, W R Penney, and J B Fasano (1993).

This polynomial is called the weight enumerator. 0 The weight enumerator is (essentially) the z-transform of the weight distribution sequence.

Use this and u = u'+ f in (12.20); relate the coefficient of N N to the fermion mass and the coefficients of 7r. 7r and u 2 to the meson masses [see (2.41) and (2.46)]; this yields (12.35).

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An experimental investigation to determine a scale-up method for fast competitive parallel reactions in agitated vessels, presented at the AIChE Annual Meeting, St Louis, MO Versteeg, H K, and W Malalasekera (1995) An Introduction to Computational Fluid Dynamics: The Finite Volume Method, Longman Scienti c & Technical, Harlow, Essex, England Weetman, R J (1997) Automated sliding Mesh CFD computations for uidfoil impellers, Proc 9th European Conference on Mixing, Paris Wyman, N (nd) CFD review, http://wwwcfdreviewcom Yakhot, V, and S A Orszag (1986) Renormalization group analysis of turbulence: I Basic theory, J Sci Comput, 1, 1 51 Zalc, J M, E S Szalai, F J Muzzio, and S Jaffer (2002) Characterization of ow and mixing in an SMX static mixer, AIChE J 48(3), 427 436 Zhou, G, P A Tanguy, and C.

5-14

Calculating the hazard requires thinking carefully about the population at risk at each point in time. At any given tenure, the population at risk for the 365-day hazard probability is all customers whose tenure is exactly 365. Calculating this population for any given date, such as Feb 14, 2006, is easy:

energy intensity or power per unit mass viscosity continuous phase viscosity dispersed phase viscosity viscosity calculated at wall temperature interfacial or surface tension

Dubois (2000) Power consumption in a double planetary mixer with non-newtonian and viscoelastic materials, Chem Eng Res 78(3), 445 453..

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