Figures & data
Figure 2. Critical deposition zone in front of porous media and its reduction with the filtration time.
![Figure 2. Critical deposition zone in front of porous media and its reduction with the filtration time.](/cms/asset/3a02724e-4a43-41d9-a7c7-e5a20c6bdb20/tjen_a_1186293_f0002_oc.jpg)
Figure 3. Designed cross-flow filtration and mud cake buildup simulator set-up. Filtration cell and O-ring along with sealant is depicted at the top right of the picture. At the bottom right of the picture, mud cake formed after circulation is illustrated; (a) Fresh drilling fluid mud cake, (b) MWCNTs fluid mud cake, (c) nano-SiO2 fluid mud cake and (d) nano CaCO3 fluid mud cake.
![Figure 3. Designed cross-flow filtration and mud cake buildup simulator set-up. Filtration cell and O-ring along with sealant is depicted at the top right of the picture. At the bottom right of the picture, mud cake formed after circulation is illustrated; (a) Fresh drilling fluid mud cake, (b) MWCNTs fluid mud cake, (c) nano-SiO2 fluid mud cake and (d) nano CaCO3 fluid mud cake.](/cms/asset/2fc4a795-e1cc-4675-b133-f97f13a5164a/tjen_a_1186293_f0003_oc.jpg)
Table 1. Drilling fluid samples characteristics.
Table 2. Solid particles characteristics obtained by DLS and literature.
Table 3. Deposition and erosion intensity indexes measured for solid particles.
Figure 6. Aggregated structure of nanoparticles in drilling fluids proposed by fractal dimension analysis.
![Figure 6. Aggregated structure of nanoparticles in drilling fluids proposed by fractal dimension analysis.](/cms/asset/250e25d5-391a-427d-9296-89afa3180a5c/tjen_a_1186293_f0006_oc.jpg)
Figure 7. FESEM images taken from mud cake after dynamic filtration test. (a) fresh mud cake with bentonite particles, (b) nano-SiO2 mud cake, (c) nano-CaCO3 mud cake and (d) MWCNTs mud cake.
![Figure 7. FESEM images taken from mud cake after dynamic filtration test. (a) fresh mud cake with bentonite particles, (b) nano-SiO2 mud cake, (c) nano-CaCO3 mud cake and (d) MWCNTs mud cake.](/cms/asset/72da8fb1-6327-4857-aff0-5723ee79e4f5/tjen_a_1186293_f0007_oc.jpg)
Figure 8. Filtration rate reduction during test and dynamic equilibrium achievement for four drilling fluid samples at horizontal and vertical position. (a) Fresh mud, (b) nano-SiO2 mud, (c) nano-CaCO3 mud and (d) MWCNTs mud.
![Figure 8. Filtration rate reduction during test and dynamic equilibrium achievement for four drilling fluid samples at horizontal and vertical position. (a) Fresh mud, (b) nano-SiO2 mud, (c) nano-CaCO3 mud and (d) MWCNTs mud.](/cms/asset/9732ac6d-5eb7-41c5-a118-d58067537e3a/tjen_a_1186293_f0008_oc.jpg)
Table 4. Vertical force ∑Fy, particle depositional acceleration ay and possible depositional volume Vc exerted on bentonite computed by model for fresh mud at different inclinations.
Table 5. Vertical force ∑Fy, particle depositional acceleration ay and possible depositional volume Vc exerted on particles computed by model for nano-SiO2 mud at different inclinations.
Table 6. Vertical force ∑Fy, particle depositional acceleration ay and possible depositional volume Vc exerted on particles computed by model for nano-CaCO3 mud at different inclinations.
Table 7. Vertical force ∑Fy, particle depositional acceleration ay and possible depositional volume Vc exerted on particles computed by model for nano-MWCNTs mud at different inclinations.
Table 8. Erosion parameters (vertical force ∑Fy, shear stress τ, critical shear stress τcr and mud cake surface occupied by particle Sp) exerted on aggregated particles on the cake surface for four drilling fluid samples.
Table 9. Mud cake thickness, hc, weight ratio of nanoparticle and bentonite on the cake, Mr, comparison between model and experimental outputs after 300 sec circulation for studied drilling fluids.