scholarly journals The Influence of Various Vibration Frequency on Barium Sulfate Scale Formation Of Vibrated Piping System In The Presence Citric Acid

2018 ◽  
Vol 953 ◽  
pp. 012247
Author(s):  
N Karaman ◽  
W Mangestiyono ◽  
S Muryanto ◽  
J Jamari ◽  
A P Bayuseno
2018 ◽  
Vol 31 ◽  
pp. 01001
Author(s):  
W. Mangestiyono ◽  
J. Jamari ◽  
S. Muryanto ◽  
A. P. Bayuseno

Vibration in many industries commonly generated by the operation mechanical equipment such as extruder, mixer, blower, compressor, turbine, generator etc. Vibration propagates into the floor and attacks the pipe around those mechanical equipment. In this paper, the influence of vibration in a pipe on the CaSO4scale formation was investigated to understand the effect of vibration on the kinetics, mass of scale, crystal phases and crystal polymorph. To generate vibration force, mechanical equipment was prepared consisted of electrical motor, crankshaft, connecting rod and a vibration table at where test pipe section mounted. Deposition rate increased significantly when the vibration affected to the system i.e. 0.5997 and 1.6705 gr/hr for vibration frequency 4.00 and 8.00 Hz. The addition 10.00 ppm of citric acid declined the deposition rate of 8 Hz experiment from 3.4599 gr/hr to 2.2865 gr/hr.


Author(s):  
Yi Jia ◽  
Reinaldo E. Madeira ◽  
Frederick Just-Agosto

This paper presents the formulation of a finite element model and vibration frequency analysis of a fluid filled pipe having variable cross sections. The finite element method with consideration of Coriolis force developed in [1] was adopted for frequency analysis of a pipe in this study. The stiffness matrix, the c-matrix (Coriolis force) and mass (for dynamic analysis) matrix that contain all parameters of the fluids properties and flow conditions have been developed. The numerical model was employed to simulate the dynamic performance of the piping system with the specific configurations for an application. A critical relationship between the natural frequencies and pipe geometry has been established. The results of frequencies analysis of the piping system gave us an insight whether a resonance frequency might occur.


2019 ◽  
Vol 13 ◽  
pp. 299-304
Author(s):  
Sutomo Sutomo ◽  
Stefanus Muryanto ◽  
Wiji Mangestiono ◽  
Jamari Jamari ◽  
Athanasius Priharyoto Bayuseno

2009 ◽  
Vol 6 (2) ◽  
pp. JAI102049
Author(s):  
S. W. Dean ◽  
Hosni M. Ezuber

2010 ◽  
Vol 61 (9) ◽  
pp. 2267-2272 ◽  
Author(s):  
J. Kim ◽  
T. I. Yoon

The formation of inorganic fouling on MF membrane was investigated in membrane bioreactor (MBR) treating industrial wastewater. Membrane autopsy works using microscopic techniques and surface analysis were carried out at the completion of pilot-scale operation to analyze foulant materials extensively. Scaling occurred on the membrane surface significantly in the MBR treating calcium-rich wastewater (LSI > 2.0). Our experiments showed that the coverage of the membrane surface by the inorganic fouling consisted mostly of calcium while the internal fouling within membrane pores due to the scale formation was almost negligible. Most of calcium was rejected on the MF membrane surface as scale formation of calcium carbonate (>90% as rejection). The sequence sodium hypochlorite-citric acid for the removal of membrane scale was more effective than the sequence citric acid-sodium hypochlorite cleaning. It appeared that the structure of organic compounds combined with calcium became loose by the addition of the sodium hypochlorite, thereby releasing calcium more easily from the membrane by applying the acid cleaning agent.


1975 ◽  
Vol 15 (06) ◽  
pp. 509-516 ◽  
Author(s):  
G.H. Nancollas ◽  
S.T. Liu

Abstract The kinetics of crystallization and dissolution of barium sulfate seed crystals were investigated conductimetrically. Growth is characterized by an initial surge caused by secondary nucleation, followed by a rate that is proportional to The square of the supersaturation. Studies were made using seed material of differing morphology; in all cases, the crystallization was surface controlled. A surface reaction also appears to be rate-determining for the corresponding dissolution process, but the over-all rate constant is considerably greater than that for growth. Crystallization and dissolution were studied in the presence of potential phosphonate and polyphosphate scaling inhibitors phosphonate and polyphosphate scaling inhibitors in some cases, both processes were markedly inhibited. The incorporation of the antiscalant into the developing crystals may pose problems in down-hole application. Introduction The state of knowledge of adsorption and desorption phenomena and of reactions at the solid-liquid interfaces under wellbore conditions is extremely limited. Consequently, the procedures used for eliminating scale by the chemical treatment of surface waters that are frequently injected into an oil-bearing formation are often based on empirical considerations. In the absence of knowledge of the mechanism of scale formation and its inhibition, the choice of additive is usually made on the basis of the results of spontaneous precipitation experiments made in the laboratory. precipitation experiments made in the laboratory. Although attempts are made to reproduce such experimental data, extreme sensitivity to factors such as the methods used to mix reagents, rates of stirring, and concentrations of reactants make it impossible to do so. Also, it is difficult to avoid heterogeneous nucleation in such systems, and this process also may be influenced by the presence of the additive. Interpretations of the course of the precipitation reactions solely in terms of the precipitation reactions solely in terms of the thermodynamic solubility products of the precipitating minerals also is questionable. Such precipitating minerals also is questionable. Such treatments assume that, at all stages of the scaling process, the systems are effectively at equilibrium process, the systems are effectively at equilibrium and are amenable to treatment using experimental solubility products. It has been shown that kinetic factors often are considerably more important in determining the course of a precipitation process. Thus, in the case of calcium phosphate crystal growth, an amorphous precursor is formed rapidly at the beginning of the reaction and undergoes a slow transformation to the thermodynamically stable phase, hydroxyapatite. Significant changes with phase, hydroxyapatite. Significant changes with time are observed in such factors as chemical composition, crystallinity, and the specific surface areas of the solid phases. The nature of the initially precipitated phases and the course of the subsequent precipitated phases and the course of the subsequent crystal growth reaction is markedly dependent not only on the degree of supersaturation of the solution, but also on the ionic strength of the solution and the type of neutral or inert electrolyte present. Simple equilibrium solubility studies reveal nothing of these factors that may be important in determining whether scale will form in the field. Not only is the growth of crystals important for studies of scale formation, but a knowledge of the mechanism of the reverse process, dissolution, also is essential if the results of laboratory experiments are to be used to predict the behavior in actual scaling situations. At first, the growth and dissolution of crystals may be considered to be exactly reciprocal processes. The dissolution process usually has been considered to be a simple process usually has been considered to be a simple diffusion-controlled process, with the transport of lattice ions away from the crystal surface as the slow step in the reaction. in terms of diffusion following Fick's law, the rate of reaction would be expected to be proportional to the subsaturation, mo - m, where m is the molar concentration of electrolyte in the solution and mo is the equilibrium (solubility) value. Although a number of salts follow this kinetic path, there is now appreciable evidence that the dissolution of many slightly soluble salts is controlled by a process other than film diffusion of the crystal lattice ions. Whereas scale inhibitors would be expected to have little influence on a dissolution process that depends on the diffusion of crystal lattice ions away from the surface, a surface-controlled process may be markedly retarded in their presence. SPEJ P. 509


2018 ◽  
Vol 159 ◽  
pp. 01056
Author(s):  
Waleed Ali ◽  
Wahyu Putranto ◽  
Stefanus Muryanto ◽  
Athanasius Bayuseno

Barium sulfate (BaSO4) with fine sizes is important for many applications. Barium Sulfate (BaSO4) is suitable for applications as diverse as whiteness, inertness and high density. Many different approaches have been reported for the preparation of nanoparticles BaSO4 including the addition of different additives. Aims of this study to synthesize barium sulfate (BaSO4) from natrium sulfate and barium chloride with the modification of the mixing speed, temperature and additive concentration variations. This study conducted in Diponegoro University Laboratorium. The sample were characterized by a number of different methodologies, including XRD and SEM-EDS. The higher the temperature of the mass of the crust that formed more and more. The results showed a temperature of 40°C was obtained crust mass greater than at 30°C. The addition of the additive citric acid to 20 ppm does not have enough influence to lower the formation of crust mass. From the SEM image, it is clear that the particle size is less than 10 μm.


2017 ◽  
Vol 23 (12) ◽  
pp. 12243-12246
Author(s):  
N Karaman ◽  
J Jamari ◽  
A. P Bayuseno ◽  
S Muryanto

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