Significant production rate decline and a few ESP failures were observed in the Mangala field, onshore India, due to scaling. Scale inhibitor squeeze treatments were required to arrest the production decline and prevent additional ESP failures. The Mangala crude oil is extremely waxy, with a wax appearance temperature (WAT) of 62 o C and a reservoir temperature of 65 o C. This meant that prior to chemical application, fluids would have to be pre-heated to prevent wax formation and potential damage to the near wellbore area. The produced water chemistry included iron concentrations in the region of 5 -15 mg/l, which was related to the presence of significant quantity of siderite within the formation and which could have resulted in potential formation damage due to iron dissolution when applying pre-selected acid-phosphonate inhibitors. Additionally, the two main producing formations FM3 and FM 4 are produced from long horizontal wells completed with stand-alone screens. Chemical placement in the wells therefore proved to be a significant challenge, and treatments were designed to achieve placement across the water producing zones. This paper describes the squeeze chemical selection for minimisation of formation damage risks associated with treatments in this particularly challenging case study, with WAT close to reservoir temperature and the presence of reactive iron minerals. The impact that these factors had on both chemical performance and on the potential applicability of the selected chemicals is discussed. The paper also discusses pre-conditioning treatments pumped in these wells to regain productivity. The work also demonstrates how a combination of laboratory testing and treatment modelling has been used to minimise the potential for formation damage while at the same time maximising chemical treatment of the water producing zones. The detailed mineralogy and heterogeneity of the reservoir formations, the impact of production conditions and elevated iron on the performance of the selected chemicals are all described as well as the selection of alternative generic chemicals which were not poisoned by the increased iron. Initial field treatments have been conducted and preliminary results will also be presented which concur with the chemical qualification and treatment design
Overview of Mangala FieldThe onshore Mangala field is located in the north-west part of India in the Barmer Basin (Figure 1). The field was discovered in January 2004. The main reservoir unit in Mangala field is the Fatehgarh group, which is a very high quality quartzose sandstone reservoir, with high net to gross, high porosity and multi-Darcy permeability. The Fatehgarh sand has been subdivided into the Lower Fatehgarh formation dominated by well-connected sheet flood and braided channel sands, and the Upper Fatehgarh formation dominated by sinuous, meandering, fluvial channel sands. Five reservoir units are recognized, named FM1-FM5 from the top downwards. FM1 and FM2 comprise the Upper Fatehgarh formation and FM3, FM4 and FM5 form ...