Predicting Mixing Volumes in Serial Transport in Pipelines

Author:

Rachid F. B. Freitas1,de Araujo J. H. Carneiro1,Baptista R. M.2

Affiliation:

1. Universidade Federal Fluminense, Nitero´i, RJ, 24210-240, Brazil

2. Research and Development Center, Petrobras-Petro´leo Brasileiro S.A., Rio de Janeiro, RJ, 21949-900, Brazil

Abstract

This paper presents a model for predicting the contaminated mixing volume arising in pipeline batch transfers without physical separators. The proposed technique represents an improvement over the existing methods since it takes into account time-dependent flow rates and accurate concentration-varying axial dispersion coefficients. The governing equation of the model forms a nonlinear boundary-value problem that is solved by a finite element method coupled to the Newton’s method. A comparison among the theoretical predictions of this method, a field test, and other classical procedures show that the proposed method exhibits the best estimate over the whole range of admissible concentrations investigated.

Publisher

ASME International

Subject

Mechanical Engineering

Reference26 articles.

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2. Benke, H., and Gravert, W., 1989, “Process analysers for optimisation of reinjection of contaminated product in product pipelines,” Oil Gas European Magazine, 1, pp. 42–44.

3. Aunicky, Z. , 1970, “The longitudinal mixing of liquids flowing successively in pipelines,” Can. J. Chem. Eng., 48, pp. 12–16.

4. Austin, J. E., and Palfrey, J. R., 1964, “Mixing of miscible but dissimilar liquids in a serial flow in a pipeline,” Proc. Inst. Mech. Eng., 178, Part 1, No. 15, pp. 377–395.

5. Levenspiel, O., 1958, “How much mixing occurs between batches?,” Pipe Line Industry, May, pp. 51–54.

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