Calcium Sulfate Scale Formation: A Kinetic Approach

1978 ◽  
Vol 18 (02) ◽  
pp. 133-138 ◽  
Author(s):  
George H. Nancollas ◽  
Atal E. Eralp ◽  
Jasbir S. Gill

Abstract The growth and phase transformation of calcium sulfate dihydrate and hemihydrate crystals were studied at temperatures from 70 to 130 deg. C. At 70 deg. C the second-order rate constant for dihydrate crystal growth did not change by more than 20 percent over a pH range of 3.2 to 9.2. It was also independent of ionic strength up to 2.0M. Growth in stable supersaturated calcium sulfate solution was completely inhibited by 7 x 10-7 M phytic acid for about 24 hours at 70 deg. C. The seeded crystallization of calcium sulfate hemihydrate at temperatures from 90 to 140 deg. C and The phase changes from a- to beta-hemihydrate were investigated by X-ray diffraction, specific surface area analysis, and scanning electron microscopy. Organic phosphonates were found to be effective inhibitors of crystal growth of all the phases at high temperatures. Introduction The phases that form during the crystallization of many sparingly soluble salts evidently are determined much more by kinetic factors than by thermodynamic considerations. Thus, in the case of calcium phosphate crystal growth, an amorphous precursor is formed rapidly at the beginning of the precursor is formed rapidly at the beginning of the reaction and undergoes slow transformation to the thermodynamically stable phase, hydroxyapatite. Significant changes with time are observed in such factors as chemical composition, crystallinity, and specific surface areas of the solid phases. The simple equilibrium studies do not reveal the factors that may be important in determining whether these phases will precipitate in the field. phases will precipitate in the field. The case of calcium sulfate, which is important in desalination, geochemistry, and petroleum engineering, is complicated further by the fact that it can crystalize from aqueous solutions in three forms- dehydrate (CaSO4 - 2H2O), hemihydrate (a-CaSO4 1/2 H2O or beta-CaSO4 - 1/2 H2O), and anhy-drite (CaSO4). These phases may be stable or unstable depending on temperature or ionic strength, and they have decreasing solubilities with increasing temperatures above about 40 deg. C. To understand the formation of these scale minerals, high-temperature laboratory methods must be used for the kinetic studies, allowing both solutions and solid phases to be sampled without spurious temperature effects. The kinetics of transformation of one hydrate to another is particularly important in determining the nature of the scale formed under field conditions as a function of both temperature and background electrolyte concentration. This investigation studied the formation and dissolution of calcium sulfate phases under some typical field conditions. Kinetic investigations were emphasized since these frequently can be used to predict the nature of the phases formed under specific conditions of concentration or temperature. Moreover, unlike the results of spontaneous precipitation experiments, such studies are highly reproducible. The effects of factors such as ionic strength, temperature, supersaturation, and effectiveness of scale inhibitors may be studied quantitatively. In addition, the influence of the nature of the seed crystal phase and morphology on the subsequent growth process can be investigated. The morphology of the crystals comprising scale deposits may be particularly important in determining whether they pack together as hard, destructive scale or remain as a sludge to be swept away by the liquid phase. Seeded-crystal growth processes are better models than are spontaneous processes are better models than are spontaneous precipitation studies for the scale formation reactions precipitation studies for the scale formation reactions in which the solid phase is formed heterogeneously either on a foreign substrate or on crystals of scale already present. The growth rate of calcium sulfate dihydrate seed crystals is independent of the fluid dynamics in the system, suggesting that the rate is not diffusion-controlled but depends on a surface reaction rate. This has particular significance for the formation of scale in the oil well because the scaling rate is expected to be independent of the dynamics of fluid flow at the metal surface. SPEJ P. 133

2014 ◽  
Vol 926-930 ◽  
pp. 210-213
Author(s):  
Bi Jun Luo ◽  
Hai Hong Wu ◽  
Yu Qi Wang ◽  
Qi Zhang

Crystallization kinetics experiment of calcium sulfate dehydrates, which is prepared by bittern under 20°C and 120r/min conditions, is carried out. According to the results of the experimental data, nucleation densityn0of gypsum crystals is proportional to the residence time, and the rate of crystal growth lineGis inversely proportional to the residence time. Meanwhile, the crystallization kinetics formula is derived to be:B0= 5.78×102G0.87.


2005 ◽  
Vol 5 (2) ◽  
pp. 116
Author(s):  
S. Muryanto ◽  
H M Ang

The formation of scales in pipes and on the surfaces of vessels is one of the major problems encountered by the mineral processing industry in Australia and elsewhere. A cursory study revealed that one of the main components of the scales was gypsum or calcium sulfate dihydrate. This paper discusses a typical undergraduate laboratory project to investigate the formation of calcium sulfate dihydrate scale on the surfaces of different types of pipes under isothermal conditions. This laboratory exercise is essentially a crystallization process and is suggested as one of the topics for final-year chemical engineering undergraduate project since it is a very important unit operation in the chemical, mineral, or pharmaceutical industries. Keywords: Calcium sulfate dihydrate, laboratory project, scale formation, and undergraduate curriculum..


1988 ◽  
Vol 66 (6) ◽  
pp. 1529-1536 ◽  
Author(s):  
Zahid Amjad

A seeded crystal growth technique has been used to study the influence of solution pH and temperature ranging from 25 to 50 °C on the performance of polymers of varying functional groups as calcium sulfate dihydrate (CaSO4•2H2O, gypsum) crystal growth inhibitors. Results indicate that at constant temperature and at a constant solution pH, crystallization in the presence of polyacrylic acids is preceded by an initial slow growth reaction, hereafter called induction period, following which crystal growth of gypsum proceeds with a rate close to that in pure supersaturated solution. Results suggest that at a constant pH, polyacrylic acid concentration, molecular weight, and temperature greatly affect the duration of induction period. Kinetic data collected as a function of solution pH in the range 2.5 to 9.0 suggest that solution pH has a marked effect on the induction period. The observed dependence of induction period on solution pH may be explained in terms of the degree of ionization of polyacrylic acid. Among the polymers of varying functional groups studied, i.e. carboxyl, sulfonate, acrylamide, dimethyldiallylammonium, etc., only those polymers having carboxyl group showed marked inhibitory activity for the growth of gypsum crystals.


1974 ◽  
Vol 14 (02) ◽  
pp. 117-126 ◽  
Author(s):  
G.H. Nancollas ◽  
M.M. Reddy

Abstract Reviewed here is the kinetics of crystal growth of sparingly soluble minerals such as calcium carbonate, calcium sulfate, and barium sulfate, which frequently cause scaling problems in oil fields. For all three electrolytes, the crystal growth is surface controlled and follows a second-order rate law with an activation energy for the growth process of 10 to 20 kcal mol(-1). The growth of calcium sulfate seeded crystal above 100 degrees C demonstrates the importance of characterizing polymorphic transformation processes. Phosphonate scale inhibitors show differing modes of Phosphonate scale inhibitors show differing modes of imbibition in systems precipitating CaCO3 and CaSO4. Introduction The formation of crystals of scale-forming, sparingly soluble minerals continues to be a very serious problem for the petroleum engineer. Scaling arises from a specific set of geological, physical, and chemical conditions. Geological factors such as ground water circulation and mineral composition may mediate in scale formation as may physical factors such as pumping rate, well pressure, and the extent of fluid addition to the oil-bearing formation. However, the principal factors regulating scale formation in the oil field are chemical and such investigations can answer many of the problems. For example, scale caused by the addition problems. For example, scale caused by the addition of surface water to an oil-bearing formation can often be eliminated by chemical treatment of the injected water. A more important scaling arises from changes in subsurface mineral solubility due to variations in temperature and pressure under down-hole conditions. The difficulties are compounded by the fact that conditions frequently encountered under down-hole conditions, notably high pressure and high temperature, cannot be readily simulated in the laboratory. Sampling of an aqueous solution brought to the surface for analysis can lead to entirely misleading results owing not only to changes in temperature and pressure, but also to the fact that the solution may be actively depositing scale minerals within the well. In addition, the possible deposition of carbonate scale is dependent possible deposition of carbonate scale is dependent upon the carbon dioxide partial pressure in contact with the solution. The minerals that appear to pose the most serious problems in oilwell scaling are the sulfates of calcium and barium, and calcium carbonate. Calcium sulfate and calcium carbonate have solubility values that decrease with increasing temperature. The higher ambient temperature in the down-hole situation will therefore encourage the formation of scale deposits of these minerals. In the case of calcium sulfate the problem is complicated by the transition between the dehydrate, hemihydrate, and anhydrite phases. These calcium sulfate polymorphs may be stable or unstable under different conditions of temperature or of ionic strength. Barium sulfate presents a particularly serious problem, since it is very insoluble and cannot be dispersed once it has deposited as scale. Numerous studies have been made of the spontaneous precipitation of sparingly soluble minerals from solutions containing concentrations of the crystal lattice ions considerably in excess of the solubility values. Attempts are usually made to use controlled methods of mixing the reagent solutions containing the lattice ions, but it is extremely difficult to obtain reproducible results from such experiments. There are probably no systems that are entirely free from foreign substances or particles that can readily act as sites for the formation of nuclei of the precipitating phase. The attainment of so-called "homogeneous" phase. The attainment of so-called "homogeneous" nucleation conditions is therefore very difficult even when extreme precautions are taken to exclude impurities and foreign particles from the solutions. Experiments are frequently conducted to determine scaling thresholds in the laboratory by mixing solutions of salts containing the lattice ions and observing the appearance of the first precipitate. Such experiments are open to the same objections as those given above, however; moreover, they are frequently carried out in such a manner as to ignore important kinetic factors in the rate of precipitation. Thermodynamic interpretations of the results assume the attainment of equilibrium and involve the thermodynamic solubility products of the precipitating minerals. precipitating minerals. SPEJ P. 117


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