A Study of Solubility of Strontium Sulfate

1983 ◽  
Vol 23 (02) ◽  
pp. 292-300 ◽  
Author(s):  
Donald F. Jacques ◽  
Brent I. Bourland

Abstract This paper describes the results of a solubility study of strontium sulfate in sodium chloride brine. A predictive equation for the solubility of strontium sulfate is presented, which is useful for calculating solubility in water containing 0 to 200 g/L (0 to 200 g/dm3) sodium chloride at temperatures from 100 to 300 degrees F (38 to 149 degrees C), with pressures from 100 to 3,000 psig (689 to 20 684 kPa), and total ionic strengths of 0 to 3.43. This paper also describes the experimental technique employed and the special equipment designed for this study. Introduction Strontium sulfate scale formation has become a growing concern in oil-production systems. Until recently, the appearance of strontium in oilfield scales has been primarily in the presence of barium sulfate scale. Almost pure SrSO4 scale now is observed in several production wells around the world. The scale formation is primarily a result of subsurface commingling of waters, which results in a water supersaturated in SrSO4. The literature does not readily provide solubility data that permit prediction of SrSO4 scaling under downhole conditions. Jacques et al. presented the most recent SrSO4 solubility data in 1979. Their work presented a comprehensive literature survey, new solubility data developed in synthetic brine systems from 77 to 212 degrees F (25 to 100 degrees C), and studies of effective SrSO4 scale inhibitors. The study showed that the solubility of SrSO4 increased with increasing ionic strength and decreased with increasing temperature once 104 degrees F (40 degrees C) had been exceeded. A method of predicting SrSO4 precipitation in field brines was suggested on the assumption that solubilities based on pure sodium chloride systems were the limiting thermodynamic case. This model did not provide for pressure effects and it was limited to 212 degrees F (100 degrees C). Some work available at the time indicated slight increases in SrSO4 solubility with pressure, but the study was limited to 95 degrees F (35 degrees C) maximum and low salinity. To predict SrSO4 precipitation and scaling under downhole conditions, solubility data are needed that bracket all possible temperatures, pressures. and salinities of oilfield waters. This study reports the results of new solubility determinations developed under broader test conditions. The results then are combined with the 1979 data 4 to provide a predictive solubility model. Theory To develop data that could be used generally to predict SrSO4 solubility in most oilfield brines, the solubility of SrSO4 was studied in pure synthetic NaCl brines. The salinity, temperature, and pressure ranges used in this study were selected to encompass most oilfield conditions. Minimum Maximum Salinity, g/L, NaCl 0 200Pressure, psig (kPa) 100(689) 3,000 (20 700)Temperature, degrees F 100 (38) 300 (149)( degrees C) To develop the most useful data possible over the ranges of the three variables listed demanding the fewest possible experiments, we used the Box-Behnken experimental design as taught by DuPont. This space-filling design was followed by a second design, a 2 3 factorial, inside the first design. SPEJ P. 292^

2021 ◽  
Author(s):  
Mattoso Marcio de Padua ◽  
Pimenta Maiza Goulart

Abstract The purpose of this article is to present a set of experiences and challenges related to the current Buzios FPSOs and the perspectives offered by these related experiences, which should drive further enhancements for next generations of pre-salt production units. Buzios field is a giant oil discovery located at Brazilian southeast coast and has four production systems already in operation: P-74, P-75, P-76 and P-77. Throughout these projects, Petrobras observed technical and business opportunities that are going to lead improvements for next generation of Buzios field's FPSOs. These include enhancements on high production wells, H2S removal technology, vessel standardization, digital transformation solutions, design procedures improvements and several measures to strength the integration between design, construction, commissioning and operation phases. During the construction, commissioning and startup period of the Buzios’ current installed units, Petrobras identified technical issues that should be addressed in order to add value to the next generation of Buzios’ FPSOs. These experiences point out to the need of technical design improvements and reviews such as: change in technology of H2S removal from solid bed to membranes; a complete analysis of hull capacities and dimensions and standardization of the vessel; and a set of standardization methods and processes to develop the basic design - including aspects of digital transformation. The result was a standard design project called Reference Project ("Projeto de Referência" in Portuguese) that intends to be a reference for new units to be installed in Buzios field. This design also intends to be the basis to other projects in order to allow faster business decisions.


1990 ◽  
Author(s):  
Maria Carmen Moreira Bezerra ◽  
Carlos Nagib Khalil ◽  
Francisca Ferreira Rosario

1955 ◽  
Vol 33 (5) ◽  
pp. 774-786 ◽  
Author(s):  
J. A. Labash ◽  
G. R. Lusby

Solubility data have been obtained at 20 °C. and 60 °C. for the following ternary systems:[Formula: see text]No evidence of the formation of double salts or of solid solutions in the first three systems was obtained. Ammonium sulphite monohydrate does not appear to dehydrate at 60 °C. in solutions saturated with sodium sulphite or ammonium chloride. In the study of the NaCl–NH4Cl–H2O system, the data agree with average values obtained from the literature and some discrepancies in the published data have been noted. In the NaCl–Na2SO3–H2O system some anomalous results can be explained on the basis of the existence of solid solutions of the hydrated and anhydrous forms of sodium sulphite and sodium sulphate.


2011 ◽  
Vol 110-116 ◽  
pp. 2183-2187
Author(s):  
Hua Lin Liu ◽  
Wei Xiong

For rapid production decline, difficult production stability ability in low permeability reservoirs, establishment of effective injection-production system between injection and production wells is proposed to curb production decline. The effectiveness of an injection-production system should contain two aspects, supplementing enough energy to layer on time and overcoming starting pressure gradient. Completely fractured injection-production well arrangement is simplified into an injection-production one-way flow model, and layer pressure calculation formula is derived by separating variables while single-phase flow. Formulas of determining terminal parameters and driving pressure gradient of an effective injection-production system are gained by demanding for time limits on layer pressure and letting production well’s B.H.P (bottom hole pressure) equal or a bit bigger than a minimum pressure. Results show that the efficiency of a completely fractured well arrangement is related to permeability, oil viscosity, reservoir thickness, well spacing, well draining, production rate, and maximum producing pressure drop. The bigger the production rate, the smaller well draining should adopt, and the driving pressure gradient will also become bigger. For a certain reservoir, several sets of effective injection-production systems are possible, and which effective injection-production system is the best should determine by the principle of cost-effective development.


2007 ◽  
Vol 4 (6) ◽  
pp. 100958
Author(s):  
S. W. Dean ◽  
Hosni M. Ezuber

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