Abstract

<p>This study investigates the means of deferring the breakthrough of injected N2 and alleviating the impact of such on production rates and specifications as well as minimizing the required changes to the gas processing facilities. This aimed at assisting the ongoing efforts to transfer the Cantarell experience to Abu Dhabi, where large amounts of N2 gas will be generated and injected into a large gas condensate reservoir to partially substitute the recycling of lean gas. This will bring forward the opportunity to exploit lean gas by securing base load supplies before the start of reservoir blowdown, compared to the peak shaving approach currently practiced. Managing N2 breakthrough starts by better understanding the pattern at which N2 injection spreads into the gas accumulation. Based on the findings of initial subsurface and plant simulations carried out in 2008, N2 breakthrough in Abu Dhabi might be possibly deferred by segmenting the reservoir into a rich N2 region and lean N2 region. The approach assumes no thief zones will be faced and no channeling of N2 injected between the two regions is taking place. N2 is injected in the north region of the reservoir. The production of that region will be segregated and fed to a gas processing plant of lower NGL (natural gas liquid) recovery, which essentially takes longer time to start suffering the deterioration of residue gas (gas mixture resulted after separating NGL) quality. The residue gas use can be limited to re-injection where the effect of below specification LHV (Low Heat Value) would not be an issue. The rest of the reservoir feeds another gas processing plant of higher NGL recovery level from which an amount of residue gas equivalent to that of the injected N2 will be rerouted to the sales network. This scenario will significantly delay as well as downsize the requirement of a N2 rejection plant. There is technical and certainly economical advantage of deferring the installation of costly N2 rejection units. Such a requirement can be entirely eliminated if the sales gas specification can be relaxed considering blending with other gas streams of higher LHV, and in collaboration with gas customers, i.e. assessing their capability to tolerate feedstock of lower specifications. It must be noted that such school of thinking may not necessarily be eventually embraced. The chosen scenario will also depend on the final configuration, i.e., wells grouping and gas gathering, of the ongoing project.</p>

Highlights

  • Abu Dhabi is witnessing a significant increase in demand for gas needed for pressure maintenance in oil reservoirs as well as for gas cycling in gas condensate reservoirs

  • Natural gas substitution with non-hydrocarbon gases, has the potential to free up substantial volumes of natural gas currently being used for gas injection

  • For the All Field Scenario, the residue gas LHV falls below specification sooner in the High NGL Recovery Plant of more significance in terms of liquids production, and N2 Rejection is required earlier than the Isolated Scenario and at a larger capacity as well

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Summary

Introduction

Abu Dhabi is witnessing a significant increase in demand for gas needed for pressure maintenance in oil reservoirs as well as for gas cycling in gas condensate reservoirs. It must be noted that such analysis was made at an early stage of Abu Dhabi’s N2 injection project, based on the data and knowledge available by end of 2008 Several deterministic factors such as the distribution of the trunk lines from the north and south zones of the reservoir to the High or Low NGL Recovery Plants, impacting the simulation runs, may have been modified altering the N2 concentration in the feed streams. Even in this latter hypothetical assumption, rejected N2 should be injected at some reservoir to create a value, as the idea of venting N2, which was bought or generated at a cost, would not be acceptable As it would be expected, plant simulation has shown that as the N2 content of the feed gas to both plants increases, the product gas LHV and both NGL and Condensate production rates decrease.

Findings
Discussion of findings
Conclusions and Recommendations
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