19 research outputs found
Vibration Characteristic Analysis of Pressure Fluctuating Attenuator with Circular Elastic Sheets for Linear-Driving Pump
Aiming at the problem of pipeline vibration caused by fluids in linear-driving pump pipeline system, this paper proposed a vibration reduction method based on a pressure-fluctuating attenuator with circular elastic sheets. Firstly, a new type of pressure-fluctuating attenuator was proposed, and its working principle and frequency characteristics were analyzed. Secondly, the mathematical model of the developed attenuator was established in combination with the dynamic characteristic equations of the pipeline. Besides, the effect of relevant parameters on attenuation performance was investigated through simulation. The size and material of the circular elastic sheet were screened according to the pressure fluctuating frequency of the linear-driving pump under the rated conditions. The prototype of the pressure-fluctuating attenuator was fabricated, and the performance of the prototype in the pipeline was tested. The experimental results show that the pressure-fluctuating attenuator with circular elastic sheets has a good suppression effect on the pulsating pressure of the linear-driving pump under the rated conditions
Research on Semi-Active Vibration Control of Pipeline Based on Magneto-Rheological Damper
This paper proposes a scheme to control the low-frequency vibration of pipelines by using magneto-rheological (MR) vibration reduction technology. The state equation and the transfer function of the pipeline system are established, and its stability and the sinusoidal excitation response are analyzed. The prototype of MR damper is developed. The dynamic characteristics of MR damper are tested and the double-sigmoid model of MR damper is established. The two-state control, Proportion Integration Differentiation (PID) control and sliding-mode-variable-structure (SMVS) control methods of pipeline vibration using MR damper are analyzed comparatively, and the vibration control laws are deduced. The simulation analyses are carried out to predict the control effect of different pipeline vibration control algorithms. The verification tests through a semi-active measurement and control platform are carried out, and the feasibility and applicability of different pipeline vibration control strategies are analyzed. The test results show that the three kinds of pipeline vibration control methods based on MR damper can effectively control the pipeline vibration. Especially, SMVS control has the best vibration control effect, the pipeline amplitude drop and the acceleration drop can reach 22.31 dB and 16.34 dB respectively, while the amplitude attenuation rate and the acceleration attenuation rate can reach 92.34% and 84.77%, respectively
A Thermodynamic Model for the Solubility Prediction of Barite, Calcite, Gypsum, and Anhydrite, and the Association Constant Estimation of CaSO<sub>4</sub><sup>(0)</sup> Ion Pair up to 250 °C and 22000 psi
Mineral
solubility predictions are critical for estimating scaling
risks at conditions of high temperature, pressure, and ionic strength
(IS) in mixed electrolytes which occur in various industrial processes.
On the basis of the Pitzer theory, this study establishes a thermodynamic
model to predict the solubilities and scaling risks of barite, calcite,
gypsum, and anhydrite under these extreme conditions. This study combines
the related equilibrium constants, virial coefficients, and the solubilities
of these minerals from 0 °C to 250 °C, from 14.7 psi to
22000 psi, with up to 6 mol NaCl/kg H<sub>2</sub>O with or without
mixed electrolytes to determine the temperature and pressure dependences
of the following virial coefficients for Ca<sup>2+</sup>–SO<sub>4</sub><sup>2–</sup>, Ba<sup>2+</sup>–SO<sub>4</sub><sup>2–</sup>, Ba<sup>2+</sup>–Cl<sup>–</sup>, Na<sup>+</sup>–SO<sub>4</sub><sup>2–</sup>, and Ca<sup>2+</sup>–Br<sup>–</sup> binary interactions used in
the Pitzer theory. Using these virial coefficients, the solubilities
of these four minerals can be accurately predicted with no apparent
temperature, pressure, or IS bias in solutions under the extreme conditions.
The association constants (<i>K</i><sub>assoc</sub>) for
CaSO<sub>4</sub><sup>(0)</sup> ion pairs calculated from the β<sub>CaSO<sub>4</sub></sub><sup>(2)</sup> values derived in the model match well with experimental measurements
at 25 °C and 1 atm, and show similar temperature and pressure
dependence with those calculated from the Fuoss ion pair association
theory and those listed in SOLMINEQ. 88
Mineral precipitation kinetics : assessing the effect of hydrostatic pressure and its implication on the nucleation mechanism
Sulfate minerals
(barite, anhydrite, and celestite) can be a technological
hindrance as a result of scale formation especially for operations
where seawater injection is involved. The effect of pH, temperature,
and saturation index (SI) on sulfate mineral nucleation and growth
are fairly well-known, but the influence of pressure on the nucleation
kinetics has attracted no attention. Here we show that nucleation
kinetics of barite, anhydrite, and celestite is highly dependent on
hydrostatic pressure applied even under constant thermodynamic driving
force, that is, at the same supersaturation level. Activation parameters
of barite nucleation kinetics were calculated, and measured values
are in agreement with literature. The negative activation volume measured
suggests that barite nucleation from hydrated Ba<sup>2+</sup> and
SO<sub>4</sub><sup>2–</sup> ions is coupled to an overall volume
decrease, albeit a large volume increase due to dehydration is expected.
The results indicate that nucleation is not controlled by desolvation
of solvated precursor Ba<sup>2+</sup> and SO<sub>4</sub><sup>2–</sup> ions but rather by an intrinsic volume collapse in the rate-determining
step of the nucleation and crystal growth processes. The activation
parameters measured in this study indirectly support previous findings
of formation of hydrated barite precursor before formation of crystalline
barite particles
Development and Application of a New Theoretical Model for Additive Impacts on Mineral Crystallization
Additives
play an important role in crystallization controls in
both natural and industrial processes. Due to the lack of theoretical
understanding of how additives work, the use and design of additives
in various disciplines are mostly conducted empirically. This study
has developed a new theoretical model to predict the additive impacts
on crystallization based on the classical nucleation theory and regular
solution theory. The new model assumes that additives can impact the
nucleus partial molar volume and the apparent saturation status of
the crystallization minerals. These two impacts were parametrized
to be proportional to additive concentrations and vary with inhibitors.
As a practical example, this new model has been used to predict barite
induction times without inhibitors from 4 to 250 °C and in the
presence of eight different scale inhibitors from 4 to 90 °C.
The predicted induction times showed close agreement with the experimental
data published previously or produced in this study. Such agreement
indicates that this new theoretical model can be widely adopted in
various disciplines to evaluate mineral formation kinetics, elucidate
mechanisms of additive impacts, predict minimum effective dosage (MED)
of additives, and guide the design of new additives, to mention a
few
Calcite and Barite Solubility Measurements in Mixed Electrolyte Solutions and Development of a Comprehensive Model for Water-Mineral-Gas Equilibrium of the Na-K-Mg-Ca-Ba-Sr-Cl-SO<sub>4</sub>‑CO<sub>3</sub>‑HCO<sub>3</sub>‑CO<sub>2</sub>(aq)‑H<sub>2</sub>O System up to 250 °C and 1500 bar
Calcite and barite are two of the
most common scale minerals that occur in various geochemical and industrial
processes. Their solubility predictions at extreme conditions (e.g.,
up to 250 °C and 1500 bar) in the presence of mixed electrolytes
are hindered by the lack of experimental data and thermodynamic model.
In this study, calcite solubility in the presence of high Na<sub>2</sub>SO<sub>4</sub> (i.e., 0.0407 m Na<sub>2</sub>SO<sub>4</sub>) and
barite solubility in a synthetic brine at up to 250 °C and 1500
bar were measured using our high-temperature high-pressure geothermal
apparatus. Using this set of experimental data and other thermodynamic
data from a thorough literature review, a comprehensive thermodynamic
model was developed based on the Pitzer theory. In order to generate
a set of Pitzer theory virial coefficients with reliable temperature
and pressure dependencies which are applicable to a typical water
system (i.e., Na-K-Mg-Ca-Ba-Sr-Cl-SO<sub>4</sub>-CO<sub>3</sub>-HCO<sub>3</sub>-CO<sub>2</sub>-H<sub>2</sub>O) that may occur in geochemical
and industrial processes, we simultaneously fit all available mineral
solubility, CO<sub>2</sub> solubility, as well as solution density.
With this model, calcite and barite solubilities can be accurately
predicted under such extreme conditions in the presence of mixed electrolytes.
Furthermore, the 95% confidence intervals of the estimation errors
for solution density predictions are within 4 × 10<sup>–4</sup> g/cm<sup>3</sup>. The relative errors of CO<sub>2</sub> solubility
prediction are within 0.75%. The estimation errors of the saturation
index mean values for gypsum, anhydrite, and celestite are within
±0.1 and that for halite is within ±0.01, most of which
are within experimental uncertainties