Maximum electrostatic charge of powder in pipe flow

Abstract In dry powder process, particles collide against each other and onto wall, and normally, electrostatic charge is generated. Such a process is called trioelectrification or tribo-/contact-/impact-charging of particles. In this paper, the amount of maximum (or saturated or equilibrium) charge on a particle in a powder flow of a pneumatic conveyer with a metal pipe was discussed. A theoretical discussion involving the space charge effect with the basis of ‘charge relaxation model,’ in which the maximum charge is limited to cause gas break down, is shown. The result showed two regions in which the space charge does not affect on, and dominates the amount of the charge. The charge was proportional to the particle size raised to the power 1.5 in the region of no space charge effect, whilst power 3 in the other region of the space charge dominant. Empirically a well approximated analytical formula was found, for all over the range including these two regions. The maximum charge as a function of particle size, pipe size, and volume fraction of the powder, was given as: q / C = 1.10 × 10 - 4 ( d p / m ) 3 { ϕ ( D / m ) } 2 + { 17.1 ( d p / m ) 1.5 } . A comparison showed that the theory gives a certain overestimation to the data cited from literatures. Additional discussions were given in details.

[1]  Masaharu Nifuku,et al.  A study on the static electrification of powders during pneumatic transportation and the ignition of dust cloud , 2003 .

[2]  Hideo Yamamoto,et al.  Impact charging of particulate materials , 2006 .

[3]  Mojtaba Ghadiri,et al.  Analysis of pulsating electric signals generated in gas–solids pipe flow , 2008 .

[4]  Shuji Matsusaka,et al.  Bipolar charge distribution of a mixture of particles with different electrostatic characteristics in gas–solids pipe flow , 2003 .

[5]  A. Gajewski Measuring the charging tendency of polysterene particles in pneumatic conveyance , 1989 .

[6]  Hideo Yamamoto,et al.  Impact charging experiments with single particles of hundred micrometre size , 2003 .

[7]  Hideo Yamamoto,et al.  The Electrostatic Force Between a Charged Dielectric Particle and a Conducting Plane , 1997 .

[8]  S. Nieh,et al.  Effects of humidity, conveying velocity, and particle size on electrostatic charges of glass beads in a gaseous suspension flow , 1988 .

[9]  Hideo Yamamoto,et al.  Charge Transfer between a Single Polymer Particle and a Metal Plate due to Impact , 1987 .

[10]  Shuji Matsusaka,et al.  Electrostatic charge distribution of particles in gas–solids pipe flow , 2002 .

[11]  Shuji Matsusaka,et al.  Control of electrostatic charge on particles by impact charging , 2007 .

[12]  Hideo Yamamoto,et al.  Charge relaxation process dominates contact charging of a particle in atmospheric conditions , 1995 .

[13]  Tatsushi Matsuyama,et al.  Charge transfer between a polymer particle and a metal plate due to impact , 1992, Conference Record of the 1992 IEEE Industry Applications Society Annual Meeting.

[14]  Sampuran Singh,et al.  Electrostatic Charging Characteristics of Polyethylene Powder During Pneumatic Conveying , 1985, IEEE Transactions on Industry Applications.

[15]  Hideo Yamamoto,et al.  Characterizing the Electrostatic Charging of Polymer Particles by Impact Charging Experiments , 1994 .

[16]  Hideo Yamamoto,et al.  Charge-relaxation process dominates contact charging of a particle in atmospheric condition: II. The general model , 1997 .