Precipitation of Calcium Carbonate (CaCO
3
) in Water−
Monoethylene Glycol Solutions
P. D. Natsi, S. G. Rokidi, and P. G. Koutsoukos*
Department of Chemical Engineering, University of Patras and FORTH ICEHT, Patras, GR 26500, Greece
*S Supporting Information
ABSTRACT: The influence of monoethylene glycol (MEG) on the precipitation process of calcium carbonate at constant
supersaturation, 25 °C, and pH 8.5 was investigated. MEG aqueous solutions supersaturated with respect to all calcium
carbonate polymorphs were used since they are often encountered in oil production processes where they are used as a hydrate
inhibitor. Both seeded and unseeded experiments were done in aqueous supersaturated calcium carbonate solutions containing
MEG over the concentration range 0−80% v/v. The presence of MEG affected the induction times and the subsequent rates of
precipitation in unseeded, spontaneous precipitation of calcium carbonate. At low values of the supersaturation ratio (SR
calcite
=
77.62−15 135.61 or σ
calcite
= 7.81−122) and for MEG concentrations in the range 30−80% v/v, the solutions were stable for 4
days. At lower than 30% v/v MEG concentrations, calcium carbonate precipitation took place past induction periods between
160 and 500 min. The morphological examination of the precipitates showed that in the presence of low MEG concentrations
(10−20% v/v) the precursor vaterite was stabilized. The homogeneous nucleation and growth of calcium carbonate in the
absence and in the presence of MEG was also investigated by the inoculation of stable supersaturated solutions with quartz and
calcite seed crystals. In both cases nucleation and growth of calcium carbonate was significantly reduced with increasing MEG
concentration in the solutions.
■
INTRODUCTION
Calcium carbonate (CaCO
3
) is a sparingly soluble salt,
encountered in three distinct polymorphs, calcite, aragonite,
and vaterite. Two more hydrated forms of calcium carbonate the
hexahydrate (ikaite) and monohydrate are also known to form
in addition to amorphous calcium carbonate (ACC).
1,2
The first
mineral phase forming is the least stable, transforming to a more
stable phase possibly through a dissolution−precipitation
process.
3
The polymorphic phases and the hydrates of calcium
carbonate, are encountered in biological mineralization, in
geological and industrial processes and have been the subject of
numerous investigations over the past decades.
4,5
A large
number of studies have been concerned with the mechanism of
calcium carbonate nucleation and growth in aqueous super-
saturated solutions.
5−8
Of particular importance is scale
formation in the production processes of fossil fuels and natural
gas. In this case oil and gas is produced from subsurface
reservoirs the walls of which have been permeated with water,
gas, and oil or combinations of these fluids. It is believed that the
rocks of oil and gas reservoirs were saturated with water before
the intrusion of oil and gas. As a result, there is always a portion
of water left, known as connate water.
9
The composition of this
and other water used in the oil production process is enriched in
hardness metal anions and carbonic species providing aqueous
environment favorable for the formation of a number of
sparingly soluble salts including carbonates.
10−12
The formation
of these salts in drilling and production equipment increases
operational costs as treatment processes are necessary to
minimize losses. Another significant scaling problem however
is the corresponding to the formation of gas hydrates because of
the presence of hydrocarbons C1−C4, CO
2
, and H
2
S.
13
For this
reason MEG is most often used in oil and gas production as an
efficient thermodynamic inhibitor at various concentrations
Received: August 29, 2018
Revised: November 21, 2018
Accepted: March 5, 2019
Published: March 5, 2019
Article
pubs.acs.org/IECR
Cite This: Ind. Eng. Chem. Res. XXXX, XXX, XXX-XXX
© XXXX American Chemical Society A DOI: 10.1021/acs.iecr.8b04180
Ind. Eng. Chem. Res. XXXX, XXX, XXX−XXX
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