Abstract

Wax deposition and gelation of waxy crude oil in production pipelines are detrimental to crude oil transportation from offshore fields. A waxy crude oil forms intra-gel voids in pipelines under cooling mode, particularly below the pour point temperature. Consequently, intrusion of non-reacting gas into production pipelines has become a promising method to lessen the restart pressure required and clear the clogged gel. A trial-and-error method is currently employed to determine the required restart pressure and restart time in response to injected gas volume. However, this method is not always accurate and requires expert knowledge. In this study, predictive models based on an Artificial Neural Network (ANN) and multilinear regression are developed to predict restart pressure and time as a function of seabed temperature and non-reacting gas injected volume. The models’ outcomes are compared against experimental results available from the literature. The empirical models predicted the response variables with an absolute error of below 5% compared to the experimental studies. Thus, such models would allow accurate estimation of restart pressure, thereby improving transportation efficiency in offshore fields.

Highlights

  • The production of waxy crude oil at offshore fields has increased due to new oil field discoveries and depletion of onshore fields

  • The ambient temperature is a central factor in ensuring smooth production and transportation of waxy crude oil from these fields

  • The fluid experiences a high pour point temperature, which is usually higher than the ambient temperature

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Summary

Introduction

The production of waxy crude oil at offshore fields has increased due to new oil field discoveries and depletion of onshore fields. The ambient temperature is a central factor in ensuring smooth production and transportation of waxy crude oil from these fields. Waxy crude oil usually contains high paraffin waxes up to 50% [1,2]. Wax precipitation usually takes place when the pressure and temperature of waxy crude oil drop to the point of onset of crystallization [5,6,7]. Waxy crude oil gel exhibits yield stress that increases with further cooling and precipitation of waxes [12,13,14,15]. Laboratory investigation showed that temperature history, shear history, ageing, and composition were the four factors affecting the yield strength of waxy crude oil [16]

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