Crystal particle adhesion to surfaces in Black Liquor Evaporators

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Crystal particle adhesion to surfaces in Black Liquor Evaporators Yuanzheng Zhu Ph.D. Candidate (ME) Advisor: Dr. Aidun 03/07/2017

Background Black liquor (BL), normally concentrated from 10-15% to 65-80% solid content by falling film evaporators and burned in a recovery boiler to produce energy Performance of evaporator suffers from rapid heat transfer (HT) surface fouling: need cleaning, cause shutdown Process of crystal adhesion to HT surface and scale formation is not well understood Fig1. Pilot experiments at Chalmers University of Technology and simulation [1-3]. [1] Doro, E. O. and C. K. Aidun (2013). "Interfacial waves and the dynamics of backflow in falling liquid films." Journal of Fluid Mechanics 726: 261-284. [2] Aaron Howell, E. D., Cyrus Aidun, Mathias Gourdon, Lennart Vamling (2014). "Black Liquor Falling Film Evaporation: Computational Model and Pilot Experiments." Proceedings of International Chemical Recovery Conference, Tampere,Finland, June 8 13 2014: 389-401. [3] Doro, E. O. (2012). "Computational modeling of falling liquid film free surface evaporation computational modeling of falling liquid. PhD thesis.

Scope of study: induction period Induction: Scaling initiated on HT surfaces. Length of this period varies greatly dependent upon systems. (inorganic salts) Steady Growth: The thickness of the scale grows steadily with simultaneous deposition and removal. (50% organics) Plateau: The rate of removal and deposition becomes equal; deposit thickness remains constant. Fig1. Idealized deposit thickness curve: three periods of development (Bott, 1995)

Why study induction period? Mechanism of scale induction on clean surfaces is a long unresolved problem. Difficult to study via experiment Individual particle transport/ adhesion/ scaling in length scale: micrometer; time scale: milliseconds Economically beneficial to extend the induction period: Thin layer of scale, high HT efficiency Reduce cleaning frequency

Scale induction: two mechanisms Surface nucleation Crystalized from supersaturated solution in the vicinity of the heat transfer surfaces Stable nuclei form directly on surface Particle deposition Crystals formed elsewhere, but transported and attached to the heat transfer surfaces. Process related to fluid flow of falling film

Falling film boundary layer (BL) Velocity profile of BL Within boundary thickness 0.1mm (=100 micron), can be well approximated by a shear flow with constant shear rates. Use 1000, 200, and 50 s -1 as typical high, median, low shear rate in simulation Fig. Velocity profile of falling film boundary layer: (a) turbulence flow with Reynolds number 800 and 2338, shear rate ~1000 s -1 ; (b) laminar flow with Reynolds number <50, shear rate ~200 s -1. (Chen& Gao, 2004)

15µm Simulation setup Numerical model Particle dynamics (SDE) Coupling BD with LBM Case study: example Crystal diameter 2µm Dominant crystal suspension is burkeite (2Na 2 SO 4 Na 2 CO 3 ): 1 10 µm Domain size: 180µm(L)x30µm(W)x15µm(H) 15µm < 100µm = 0.1 mm Total crystals in bulk fluid: 600 Shear rate: 200 s-1 Surface nuclei (roughness): 20/ 5400µm 2 Temp: 400K (~125C) Parametric study Shear rate: 1000, 200, 50 Surface nuclei: 20, 5, 0 (smooth)

Scale forming process: closer look Points deserve notice: Brownian motion caused by thermal fluctuation Particle deposition by contacting with existing nuclei on HT surface/ surface Nuclei initially existed on HT surface Crystals formed in bulk fluid Crystals that adhered on surface

Scale build up: closer look More aggregates around existing nuclei sites

Rapid scale growth at low shear rate Effect of fluid flow Wall shear rate = (50, 200, 1000) s -1 The lower flow rate, the more scale formation More contact time: crystal-crystal, crystal-surface, crystal-nuclei Diffusion dominants convection Weaker drag force from fluid Consistent with experiments[1] [1]Müller-Steinhagen, H., & Branch, C. A. (1997). Heat transfer and heat transfer fouling in Kraft black liquor evaporators. Experimental Thermal and Fluid Science, 14(4), 425 437

Roughness: various number of nuclei Front view & Side view Nuclei density: dense(20), medium(5), smooth(0)

Roughness: various number of nuclei Scale on rough surface tend to grow vertically (form 3D structure); concentrated in certain locations Scale on smooth surface tend to form uniformly

Summary Developed a numerical model to analyze initialization of crystal growth on HT surface A tool to examine effect of different surface characteristics (particles/ surface) on the scale induction rate Take detailed info from lab experiments to make prediction for further validation Effect of surface roughness and fluid flow on the formation and growth of scale