Case Study: Metallurgy Selection and Choke Design Incorporating Trim Interchangeability to Cater to the Entire Production Lifecycle of Raageshwari Deep Gas Field
- Charu Bhardwaj (Cairn Oil & Gas, Vedanta Limited) | Vishal Ranjan (Cairn Oil & Gas, Vedanta Limited) | Shailendra Kumar Jetley (Cairn Oil & Gas, Vedanta Limited) | Shobhit Tiwari (Cairn Oil & Gas, Vedanta Limited) | Anirban Ghosh (Cairn Oil & Gas, Vedanta Limited) | Swapnil Sharma (Cairn Oil & Gas, Vedanta Limited) | Avinash Bohra (Cairn Oil & Gas, Vedanta Limited) | Abhishek Kumar (Cairn Oil & Gas, Vedanta Limited) | Abhudai Beohar (Cairn Oil & Gas, Vedanta Limited) | Sidharth Sharma (Cairn Oil & Gas, Vedanta Limited)
- Document ID
- Society of Petroleum Engineers
- SPE Oil and Gas India Conference and Exhibition, 9-11 April, Mumbai, India
- Publication Date
- Document Type
- Conference Paper
- 2019. Society of Petroleum Engineers
- 2 Well completion, 4.1.2 Separation and Treating, 3 Production and Well Operations, 4 Facilities Design, Construction and Operation, 5.8.1 Tight Gas, 5.8.8 Gas-condensate reservoirs, 5 Reservoir Desciption & Dynamics, 5.8 Unconventional and Complex Reservoirs, 4.1 Processing Systems and Design, 2.4 Hydraulic Fracturing
- De-bottlenecking, Metallurgy Selection
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The Raageshwari Deep Gas (RDG) field, situated within Barmer Basin in the State of Rajasthan, India, was discovered in 2003. The field is a tight gas condensate reservoir, with excellent gas quality of approximately 80% methane, low CO2 and no H2S. Since the permeability (0.01 - 1 md) is low in this reservoir, hydraulic fracturing is required to get substantial recovery from the wells. The field has been under production since 2010. The development of this field has been carried out in three phases and more than 150 fracturing treatments have been pumped in this reservoir till date to achieve sustained economical production. This paper deals with the lessons learnt and changes implemented in choke design through various development phases of the field.
In the initial phase of field development, chokes with a low Flow Coefficient (Cv) were installed to meet the requirement of controlling the wells at low flow rates and high differential pressure. Later as the surface handling capacity increased, the chokes had to be de-bottlenecked, requiring additional Capex for new chokes. To avoid a similar scenario in the future, a comprehensive approach has been followed to envisage Cv requirement, considering well wise production profiles and surface handling capacities throughout the life of field. Since a single trim can't operate over the complete life-cycle of a well, trim interchangeability has been included in the choke design such that low and high Cv trims are interchangeable.
Pre-mature failures of trims were observed in initial phase and a root cause analysis was done to ascertain the reason. Based on the analysis, trim metallurgy has been changed from Tungsten Carbide to ASTM A276 Specific Stainless Steel Grade 440C. Trims with newly selected mettalurgy have been installed in the existing chokes.
The introduction of trim interchangeability has saved MMUSD 0.3 in the future Opex as the requirement of procuring altogether new chokes for late life period of wells is avoided. Initially failures in the trim bodies were observed as early as two months of commissioning but with the change in metallurgy zero failures have been observed with operational life of chokes being higher than four years. This has avoided significant downtime on wells and expenditure on regular trim changeovers.
Although Tungsten Carbide is one of the most common materials used for constructing trims world over, there could be specific cases where-in other metallurgy may add better value. The workflow followed in this paper will help select a suitable metallurgy and can impart a significant value to the industry.
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