FRICTION FACTOR FOR WATER FLOW THROUGH PACKED BEDS OF SPHERICAL AND NON-SPHERICAL PARTICLES
|
|
- Elijah Stokes
- 5 years ago
- Views:
Transcription
1 SCIENTIFIC PAPER FRICTION FACTOR FOR WATER FLOW THROUGH PACKED BEDS OF SPHERICAL AND NON-SPHERICAL PARTICLES Tatjana Kaluđerović Radoičić 1*, Nevenka Bošković-Vragolović 1, Radmila Garić-Grulović, Mihal Đuriš and Željko Grbavčić 1 1 Faculty o Technology and Metallurgy, University o Belgrade, Karnegijeva 4, Belgrade, Serbia, IChTM - Deartment or Catalysis and Chemical Engineering, University o Belgrade, Njegoseva 1, Belgrade, Serbia ceived vised Acceted * Corresonding author. Tel.: ; ax: address: tanjak@tm.bg.ac.rs (T. Kaluđerović Radoičić).
2 Abstract The aim o this work was the exerimental evaluation o dierent riction actor correlations or water low through acked beds o sherical and non-sherical articles at ambient temerature. The exeriments were erormed by measuring the ressure dro across the bed. Packed beds made o monosized glass sherical articles o seven dierent diameters were used, as well as beds made o 16 ractions o quartz iltration sand obtained by sieving (olydiserse non-sherical articles). The range o bed voidages was , while the range o bed article ynolds numbers was rom 0.3 to 86 or sherical articles and rom 0.1 to 50 or non-sherical articles. The obtained results were comared using a number o available literature correlations. In order to imrove the correlation results or sherical articles, a new simle equation was roosed in the orm o Ergun`s equation, with modiied coeicients. The new correlation had mean absolute deviation between exerimental and calculated values o ressure dro o 9.04%. For non-sherical quartz iltration sand articles the best it was obtained using Ergun`s equation, with mean absolute deviation o 10.36%. Surace-volume diameter (d SV ) necessary or correlating the data or iltration sand articles was calculated based on correlations or d V =(d m ) and =(d m ) rom our revious aer [7]. Keywords: ressure dro, acked bed, sherical articles, quartz iltration sand, nonsherical articles Highlights Exerimental evaluation o ressure dro correlations in acked beds was conducted Pressure dro across beds o sherical and non-sherical articles was measured Sherical glass articles and quartz iltration sand were used as acking material Correlations in the orm o Ergun equation gave the best results The coeicients in Ergun equation are system-seciic
3 3 Introduction Packed beds o articles ermit a widesread means o contact between luid and solid hases and are used in many dierent industrial rocesses. Some examles o their alication include iltration rocesses, ion-exchange, catalytic reactions, heat transer, gas scrubbing, grain drying and others. The shae and size o articles that make u the bed are chosen or the characteristics o the seciic rocess. The article size and shae always aim at high rocess eectiveness, so a wide range o articles are used. In some alications, like in down-low granular ilters, olydiserse natural materials are used as articulate hase. When natural materials are used, the shae o the articles is irregular and their size alls into some granulometric interval. Dierently shaed articles ack with dierent degrees o bed voidage, which results in dierent ressure dro across the bed. The ressure dro through the acked bed is one o the most imortant arameters to be known or the adequate design o the rocess as well as or the estimation o the caital and oerating costs and sizing the ums or ans required to orce the luid through the bed. The ressure gradient through acked beds has been studied extensively and a large number o correlations were roosed [1-17]. The most widely used equation or ressure dro calculation was roosed by Ergun [1]: P ( 1 ) - = 150 H 3 ( 1 ) U U 3 d d (1) The riction actor introduced by Ergun is: P d - H U 3 1 () According to Eqs. (1) and (), Ergun`s equation or riction actor is: (3)
4 where d U (1 ) (4) 4 For sherical articles, d is the diameter o the articles that constitute the acked bed, while or non-sherical articles d is usually taken to be the surace-volume diameter d sv [18, 19]. By analogy, all o the correlations roosed or sherical articles can be used or non-sherical articles using surace-volume diameter. Note that article shericity is deined as: d SV dv where d V reresents the volume diameter o the article. (5) The other literature correlations or riction actor in acked beds o sherical and nonsherical articles are shown in Table 1. Note that some authors used dierent orms or riction actor and ynolds number with resect to Erguns deinitions o and Table 1. Table 1, as shown in The overview o the ressure dro correlations or sherical articles shown in Table 1 is given in our revious aer [0], together with the exerimental data or the riction actor or air low through acked beds o sherical glass articles at ambient and elevated temeratures. The main conclusion o this study was that the overall best it o all our exerimental data is given by Ergun`s [1] correlation, with mean absolute deviation o 10.90% [0]. Some authors roosed riction actor correlations or non-sherical articles which included article shericity directly into the equations (Table 1) [14-17]. Allen et al. [14] reviewed the use o dierent correlations or ressure dro through acked beds o sherical and non-sherical articles. They have shown that the article shae, arrangement, acking method as well as surace roughness inluence the ressure dro signiicantly. The authors also conducted ressure dro measurements in air-articles system, using randomly acked beds o smooth and rough glass sheres, wooden cubes, wooden cylinders, acorns (ellisoids), mixed smooth sheres o dierent sizes and rounded and crushed rock with equivalent diameters rom 10.5 to 4.4 mm. The range o numbers was Based on their exerimental work, they roosed the correlation or non-sherical articles reresented by Eq.(18), Table 1.
5 Nemec and Levec [15] investigated single-hase low through acked bed reactors in 5 the range o numbers o 10< <500 with dense and loose acking o dierent uniormly sized sherical and non-sherical articles (glass and Al O 3 sheres, Al O 3 cylinders and rings as well as Ni-Mo trilobes and quadralobes) in the size range o mm. The luid used in their exeriments was nitrogen at 10 bars. The authors concluded that Ergun`s equation reresents a good aroximation o the luid low through the acked bed o sherical articles in the investigated range, while it under redicts the ressure dro over non-sherical articles under the same conditions. For non-sherical articles they roosed a new correlation which includes the articles shericity, given by Eq.(19), Table 1. Singh et al. [16] investigated the ressure dro o air low through acked bed solar energy storage system having large sized elements o dierent shaes (sheres and cubes) with d V = mm in the range o V numbers rom 157 to 674 and shericities rom 0.55 to 1. The correlation the authors roosed is given by Eq. (0), Table 1. Ozahi et al. [17] investigated the ressure dro in air-article systems, with article size 6 19 mm, and the range o shericity o 0.55 to 1. The range o V numbers in their exeriments was The correlation or riction actor they roosed is given by Eq. (1), Table 1. Several authors 9-13, 1 investigated the inluence o D c /d on ressure dro in acked beds o articles with a general conclusion that the eect o D c /d is negligible or D c /d >10. In addition, some recent studies investigated the ossibility to extend the use o Ergun`s equation to the olydiserse articles systems taking into account the article size distribution [, 3]. Flow through orous media was also studied in the ield o hydrology and or dierent alications in civil engineering. The exerimental results obtained were used to validate the semi-emirical relations or non-darcy low [4, 5, 6]. The resent study was conducted in order to investigate the otimal choice o riction actor correlation or calculating the ressure dro or water low through acked beds o sherical and non-sherical articles. The exerimental evaluation o literature correlations was conducted by measuring the ressure dro across acked beds o dierent acking and or dierent water low rates. The sherical articles used were monosized glass beads, while the non-sherical material used was olydiserse quartz iltration sand. The values o the equivalent diameter and the shericity o the quartz sand articles needed or the calculations were
6 6 obtained by using the correlations or volume diameter and shericity as a unction o mean sieve diameter roosed in our revious aer [7]. These correlations were derived or olydiserse ractions o quartz iltration sand with sieve diameters in the interval d m =0.359 to.415 mm [7]: d V d () d m (3) where d V and d m are in mm. m Exerimental aaratus The exeriments were erormed in the water-article system schematically shown in Fig. 1. The acked bed column () was used or ressure dro measurements. It was equied with a distributor and the calming section (e) in order to ensure the uniorm low o water through the bed. The uwards water low was induced using a um (b) and the low rate was measured using an electromagnetic low meter (d). The acked bed bulk temerature was measured using the temerature indicator (TI). The ressure dro in acked beds o dierent articles was measured using iezometers (h). The exeriments were erormed with two tyes o articles: glass sherical articles and olydiserse quartz iltration sand non-sherical articles, as shown in Fig.. The luid used was deaerated water at a nearly constant temerature o 0 C. In each run, water temerature was recorded and water density and viscosity were calculated. The article characteristics and range o the exerimental conditions are summarized in Table. Seven kinds o mono-sized sherical glass articles were used. The exeriments with glass sherical articles were conducted in two cylindrical columns: irst column o the diameter o 40 mm was used or mm articles and the second column o the diameter o 6 mm or mm articles. The ratio o the column diameter to the article diameter (geometric asect ratio) in the exeriments was between 10.0 and As the wall eects were not studied exerimentally in this aer, it should be noted that the literature on the range o geometric asect ratio in which the wall eects are negligible is somewhat divided. Generally, the wall eects are considered negligible at D c /d ratios less than 10, but there are some researchers who ound wall eects to be signiicant at D c /d ratios as high as 15-0 [10,1]. As in the case o some o our exeriments the D c /d ratios were in that range, the
7 existence o wall eects can not be excluded. The measurements o the ressure dro in the beds o non-sherical articles were conducted using 16 ractions o quartz iltration sand obtained rom the comany Kaolin - Valjevo. The raw material was irst washed by luidization to eliminate ine dust, then dried and sieved through a number o standard sieves with sieve oenings ranging rom.830 to 0.97 mm. The obtained ractions had the sieve diameters in the interval o dm = (ds,n + ds,n+1)/ = to.415 mm and the ratio between the two successive sieve sizes dr =ds,n/ds,n + 1 was in the interval 1.13 to 1.715, where ds,n is the size o the oening o the sieve through which the article had assed and ds,n+1 is the size o the oening o the sieve on which the article was retained, as shown in Table. A total o 3 runs were conducted (7 with sherical articles and 16 with non-sherical articles) and a total o 75 data oints were collected (511 or sherical and 14 or nonsherical articles). Bed article ynolds number, 7 varied between 0.3 and 86 or sherical articles and between 0.1 and 50 or non-sherical articles. All o the water suericial velocities used in the exeriments were below the minimum luidization velocity or the resective articles. The velocities were in the range o U mf, where U mf reresents minimum luidization velocity. Fig. 1. Fig.. Table. sults and discussion The results o the riction actor vs. obtained by the exerimental measurements o ressure dro are shown in Figs. 3 and 4 or sherical and non-sherical articles, resectively. The comarison between the exerimental results and the selected literature correlations is given in Table 3 and in Figs. 5 and 6. The literature correlations or sherical articles shown in Table 1 were tested or all the exerimental data. The suracevolume diameter and the shericity needed or the calculations or non-sherical articles were obtained using the correlations rom our revious aer [7] or quartz iltration sand (Eqs. () and (3)). For quartz iltration sand beds, the literature correlations seciically deined or non-sherical articles were also tested: Allen et al. [14], Nemec and Levec [15],
8 8 Singh et al. [16] and Ozahi et al. [17] correlations. Fig. 3. Fig. 4. Table 3. The mean absolute deviation between the measured values o the ressure gradient and the values obtained rom the literature correlations were calculated according to the ollowing equation: N 1 ( P / H ) calc ( P / H ) measured (4) N ( P / H 1 ) measured where N is the number o data oints, (ΔP/H) calc and (ΔP/H) measured are the calculated and the measured ressure gradients. As can be seen rom Table 3, the best it o our exerimental data or ressure dro in beds o sherical articles was obtained using Cheng [9] correlation, with mean absolute deviation o 10.89%. The correlations o Macdonald et al. [] and Montillet et al. [4] also gave very good results in itting our exerimental data with mean errors o 1.18 and 13.13%, resectively. A number o other correlations tested gave results with mean absolute deviation in the range o 16-0%. It should be noted that Hicks [6] correlation gave the mean error o 50.19% or sherical articles and 84.34% or non-sherical articles. The reason or such a large error is that the range o numbers in this aer was below 183, while the seciied range o alicability o Hicks correlation is >500. The correlations with mean absolute deviation between exerimental and correlated ressure dro less than 0% or beds o sherical articles are shown in Fig. 5. The correlations shown in Fig. 5 were calculated or D c /d = 5 and bed orosity o = 0.40 (the mean values in our exeriments) in order to be able to show the correlations with direct deendence on as lines. Fig. 5. Comared to the data o our revious aer [0], in which air-sherical articles system was investigated, the results are in the similar range or Macdonald et al. [] (1%) and Cheng [9] (11 and 1%) correlations, which gave very good results at ambient temerature both or air-articles and water-articles systems. On the other hand, the correlations o Ergun [1], Tallmadge [7], ichelt [11], Gibilaro et al. [3], Einseld and
9 9 Schnitzlein [10] and Zhavoronkov et al. [1] erormed better in air-articles system, while the correlation o Montillet et al. [4] erormed better in water-articles systems. In order to imrove the correlation results or sherical articles, a new simle equation is roosed in the orm o Ergun`s equation, with modiied coeicient: (5) The mean absolute deviation between the values calculated rom Eq. (5) and the exerimental data is 9.04%. The new correlation is shown in comarison to the exerimental data in Fig. 3. For non-sherical articles (quartz iltration sand), the best it o the exerimental data was obtained using Ergun`s equation [1], with mean absolute deviation o 10.36%. The correlations o ichelt [11], Tallmadge [7] and Einseld and Schnitzlein [10] also gave very good results in itting the exerimental data with mean errors o 10.64%, 11.19% and 11.31%, resectively. The correlations with mean absolute deviation o ressure dro less than 0% or quartz iltration sand acked beds are shown in Fig. 6. The correlations shown in Fig. 6 were calculated or D c /d =73 and bed orosity o = 0.40 (the mean values in our exeriments) in order to be able to show the correlations with direct deendence on as lines. Fig. 6. The correlations secially derived or non-sherical articles gave very oor results in correlating our exerimental data. The mean absolute deviations or these correlations were in the range o 59.40% to 85.%. The reason or this is that the correlations o Allen et al. [14], Sing et al. [16] and Ozahi et al. [17] were derived rom exeriments in systems in which the articles were o large diameters (6 0 mm equivalent diameters) and the numbers were larger than 75, while in our system, the numbers o non-sherical articles were smaller than 5. Allen et al. [14] and Singh et al. [16] correlations were derived or acked bed solar energy storage systems with article materials being wooden cubes, crushed rock, concrete and masonry bricks. On the other hand, the correlation o Nemec and Levec [15] was derived or the articles in the range o mm, but in the high ressure system (5 0 bar). The very oor erormance o the correlations derived or the non-sherical articles in our quartz sand acked beds emhasizes the act that the riction actor in acked beds strongly deends on other variables besides the shericity o the articles. It can be concluded that the
10 10 riction actor is very system seciic and that it deends on article shae and size, voidage, arrangement, acking method as well as surace roughness. It is interesting to note that almost all o the correlations that gave good results in correlating our exerimental data both or sherical and non-sherical articles were in the orm o Ergun`s equation, i.e. reresented a modiication o this equation with dierent coeicients. From this act it can be concluded that the orm o Ergun`s equation with two added terms describing viscous and inertial eects is adequate or reresenting the riction actor in acked beds. However, the coeicients in the equation are very system-seciic and care should be taken when choosing the adequate equation or ressure dro calculation or the seciic urose. The correlation chosen or the seciic system should be obtained rom the data in the similar range o exerimental conditions as the system it is intended to be alied to. Conclusions The resent study was conducted in order to investigate the otimal choice o riction actor correlation or water low through acked bed o articles. The best it o exerimental data or sherical articles was obtained using Cheng [9] correlation (mean absolute deviation o 10.89%). Ergun`s equation [1] gave better results in correlating the data or non-sherical articles with mean absolute deviation o 10.36% comared to 19.8% or sherical glass articles. Ergun`s equation was modiied in order to imrove the it or sherical articles and a new correlation was roosed. The mean absolute deviation between the exerimental data and the roosed correlation is 9.04%. The correlations secially derived or non-sherical articles gave very oor results in correlating our exerimental data robably because they were derived or systems with much larger articles acked in a dierent arrangement. Most o the correlations that gave good results in correlating exerimental data both or sherical and or non-sherical articles were in the orm o Ergun`s equation with modiied coeicients, thus showing that the orm o Ergun`s equation with two added terms describing viscous and inertial eects is adequate or reresenting the riction actor in acked beds. However, the coeicients in the equation are very system-seciic.
11 11 Acknowledgment Financial suort o the Serbian Ministry o Education and Science (Project ON170) is grateully acknowledged.
12 1 Nomenclature a A b c d m d d s d SV d s,n d s,n+1 d V D c emirical coeicient in Eq. (6), dimensionless area o a article emirical coeicient in Eq. (6), dimensionless emirical coeicient in Eq. (6), dimensionless article sieve diameter acked bed article diameter sieve oening article surace-volume diameter the size o the oening o the sieve through which the article had assed the size o the oening o the sieve on which the article was retained article volume diameter column diameter A riction actor deined according to Eq. (18) o riction actor deined according to Eq. (1) S riction actor deined according to Eq. (0) riction actor deined according to Eq. () modiied riction actor deined according to Eq. (7) H P P P bed height ressure bed ressure dro, Pa dimensionless bed ressure dro, Eq.(1) =( Ud )/μ article ynolds number =( Ud )/(μ(1-ε)) bed article ynolds number V article ynolds number deined according to Eq. (0) V bed article ynolds number deined according to Eq. (1) A bed article ynolds number deined according to Eq. (18) U U mf V suericial luid velocity minimum luidization velocity (suericial) volume o a article
13 13 Greek letters voidage μ luid viscosity ρ ρ σ Ψ luid density article density mean absolute deviation article shericity, dimensionless Subscrits luid mf minimum luidization article
14 14 REFERENCES 1. S.S. Ergun, Chem. Eng. Prog. 48 (195) F. Macdonald, M. S. El-Sayed, K. Mow, F. A. L. Dullien, Ind. Eng. Chem. Fundam. 18 (1979) L. G. Gibilaro, R. Di Felice, S. P. Waldram, Chem. Eng. Sci. 40 (1985) A. Montillet, E. Akkari, J. Comiti, Chem. Eng. Process. 46 (007) H. Watanabe, Inte. J.Eng.Fluid Mech. (1989) R.E. Hicks, Ind. Eng. Chem. Fundam. 9 (1970) J.A. Tallmadge, AIChE J. 16 (1970) J. Lee, K. Ogawa, J. Chem. Eng. Jn. 7 (1994) N.S. Cheng, Powder Technol. 10 (011) B. Eiseld, K. Schnitzlein, Chem. Eng. Sci. 56 (001) W. ichelt, Chem. Ing. Tech. 44 (197) N.M. Zhavoronkov, M.E. Aerov, N.N. Umnik, J. Phys. Chem. 3 (1949) (in Russian). 13. R.C. Raichura, Ex. Heat Transer 1 (1999) K.G. Allen, T.W. von Backström, D.G. Kröger, Powder Technol. 46 (013) D. Nemec, J. Levec, Chem. Eng. Sci. 60 (005) R.Singh, R.P. Saini, J.S. Saini, Sol. Energy 80 (006) E.Ozahi, M.Y.Gundogdu, M.Ö. Carinlioglu, Adv. Powder Technol. 19 (008) D. Geldart, Powder Technol. 60 (1990) W.-C. Yang, in Handbook o Fluidization and Fluid-article Systems, W.-C. Yang, Marcel Dekker, New York, (003). 0. R. Pešić, T. Kaluđerović Radoičić, N. Bošković-Vragolović, Z. Arsenijević, Ž. Grbavčić, Chem. Ind. Chem. Eng. Q., 014, DOI:10.98/CICEQ P. 1. R. Di Felice, L.G. Gibilaro, Chem. Eng. Sci. 59 (004) M. Mayerhoer, J. Govaerts, N. Parmentier, H. Jeanmart, L. Helsen, Powder Technol. 05 (011) A. Luckos, J.R. Bunt, Fuel 90 (011) M. Sedghi-Asl, R. Hassan, J. Hydrol. Eng. 49 (011) K. N. Moutsooulos, I. N. Paasyros, V. A. Tsihrintzis. J. Hydrol. 374 (009) M. B. Salahi, M. Sedghi-Asl, M. Parvizi, J. Hydrol. Eng. (015) T. Kaluđerović Radoičić, M.Đuriš, R.Garić-Grulović, Z.Arsenijević, Ž.Grbavčić, Powder Technol. 54 (014)
15 15 Figure cations Fig. 1 Schematic diagram o the exerimental system (a-reservoir; b-um; c-valve; d- electromagnetic low meter; e-calming section; -column; g-overlow; h-iezometers; TItemerature indicator) Fig. Some o the articles used in the exeriments Fig. 3. vs. or sherical articles Fig. 4. vs. or non-sherical articles Fig. 5. Comarison o exerimental data o vs. articles with chosen correlations or sherical Fig. 6. Comarison o exerimental data o vs. with chosen correlations or nonsherical articles
16 Tables Table 1 Some imortant literature correlations or riction actor in acked beds erence Friction actor Eq. number range Sherical articles Ergun [1] (3) 1< < Macdonald et al. [] (6) - Gibilaro et al. [3] 18 (1 ) Note: 3 /( 1 ) (7) - Montillet et al. [4] Kuerten, re. in [5] Hicks 6 Tallmadge 7 Table 1 - continued 0. 1 D c = a d a=0.061 (<0.39), a=0.050 ((>.39); For (D c /d )>50 term (D c /d ) 0. =. 5 (1 ) 1 6 = (1 ) (10) = (1 ) 4. (1 ) 1/6 = 3 3 (8) 10< < D c /d (9) 0.1< < < <610 4 (11) 0.1< <10 5
17 17 erence Friction actor Eq. number range Lee and Ogawa (1 ) n = where n (1) 1< <10 5 Cheng [9] AM B M c D d M M d D D A c c M d D D.. B c c / (13a) (13) - Eiseld and Schnitzlein [10] 154 M M B M by Eq.(13a), ) D / d (. B c (14) 0.01< <
18 Table 1 - continued erence Friction actor Eq. number range ichelt [11] 150 M M B M by Eq.(13a), B. 5 d / D c (15) - 18 Zhavoronkov et al. [1] A 1. B A B 1 D / d ( 1 ) c 1 (16) - Raichura [13] AM B M M by Eq.(13a) 103 A 6 ( 1 ) 80 ( d M 1. 8 B ( d / Dc ) M 1 / Dc ) (17) -
19 Table 1 - continued erence Friction actor Eq. number range Non-sherical articles 3 P 1 V a b A = < < 3000 H c U A 1 A A Coeicients a, b and c deend on article tye and acking structure. Allen et al.[14] U Note: V V d (18) SV A 4, (1 ) A A 6 Nemec and Levec [15] Singh et al. [16] Ozahi et al. [17] 3 3 A, A / 4/3 (19) S Note: P d - V H U UdV V, v ex[ (log ) ] 3/ (1 ), / (1 ) * 3 P d V 76 = 1.76 O - L 1 V Note: * 1 P P / UdV U, V, (1 ) V S V /, o (0) (1) 10< < < V < < V <7773
20 Table. Particle characteristics and the range o the exerimental conditions d or d m mm d s,n+1 d s,n D c mm mm mm kg/m 3 cm/s Sherical articles Non-sherical articles U
21 1 Table 3. Comarison o exerimental data or riction actor with dierent correlations rom the literature σ (%) erence Sherical articles Non-sherical articles Ergun [1] a Macdonald et al.[] a Gibilaro et al. [3] a Montillet et al. [4] a Kuerten, re. in [5] a Hicks [6] a Tallmadge [7] a Lee and Ogawa [8] a Cheng [9] a Eiseld and Schnitzlein [10] a Raichura [13] a ichelt [11] a Zhavoronkov et al.[1] a Allen et al.[14] b Nemec and Levec [15] 63.5 c Singh et al.[16] 85. Ozahi et al.[17] This aer (Eq.(5)) 9.04 a-using d SV ; b-using coeicients or crushed rock, d SV =4.4 mm; c-using coeicients or cylindrical articles
22 Figures Figure 1.
23 Figure. 3
24 Figure 3. 4
25 Figure 4. 5
26 Figure 5. 6
27 Figure 6. 7
Real Flows (continued)
al Flows (continued) So ar we have talked about internal lows ideal lows (Poiseuille low in a tube) real lows (turbulent low in a tube) Strategy or handling real lows: How did we arrive at correlations?
More informationThe Derivation of a Drag Coefficient Formula from Velocity-Voidage Correlations
1 The Derivation o a Drag Coeicient Formula rom Velocity-Voidage Correlations By M. Syamlal EG&G, T.S.W.V, Inc. P.O. Box 880 Morgantown, West Virginia 6507-0880 T.J. O Brien U.S. Department o Energy Morgantown
More informationMinimum Fluidization Velocities of Binary- Solid Mixtures: Model Comparison
Vol:4, No:3, 00 Minimum Fluidization Velocities of Binary- Solid Mixtures: Model Comarison Mohammad Asif International Science Index, Chemical and Molecular Engineering Vol:4, No:3, 00 waset.org/publication/5950
More informationForces Acting on Single Particles in a Fluid
Micro- and Nanoarticle Technology orces Acting on Single Particles in a luid Dr. K. Wegner - Lecture 6.0.019 6. March 019 Particle Science and Technology Particle ormation action Crystallization Preciitation
More informationME 437/ME 537 PARTICLE TRANSPORT, DEPOSITION AND REMOVAL. Goodarz Ahmadi
ME 437/ME 537 PARTICLE TRANSPORT, DEPOSITION AND REMOVAL Goodarz Ahmadi Deartment o Mechanical and Aeronautical Engineering Clarkson University Potsdam, NY 13699-575 1 Air ollution and smog. Particle trajectories
More informationCheng, N. S., and Law, A. W. K. (2003). Exponential formula for computing effective viscosity. Powder Technology. 129(1-3),
THIS PAPER SHOULD BE CITED AS Cheng, N. S., and Law, A. W. K. (2003). Exonential ormula or comuting eective viscosity. Powder Technology. 129(1-3), 156 160. EXPONENTIAL FORMULA FOR COMPUTING EFFECTIVE
More informationEXPERIMENTAL STRATEGY FOR THE DETERMINATION OF HEAT TRANSFER COEFFICIENTS IN PEBBLE-BEDS COOLED BY FLUORIDE SALTS
EXPERIMENTAL STRATEGY FOR THE DETERMINATION OF HEAT TRANSFER COEFFICIENTS IN PEBBLE-BEDS COOLED BY FLUORIDE SALTS L. Huddar, P. F. Peterson Deartment o Nuclear Engineering, University o Caliornia, Berkeley,
More informationGeneralized deposition model of tiny solid particle immersed in turbulent flow
International Journal o Sustainable and Green Energy 04; 3(6-): 7-4 Published online February, 05 (htt://www.scienceublishinggrou.com/j/ijrse) doi: 0.648/j.ijrse.s.0403060. Generalized deosition model
More informationSimulation Of Vertical Gas-Solid Flow: Comparison Of Correlations For Particle-Wall Friction And Drag Coefficient
International Journal of ChemTech search CODEN( USA): IJCRGG ISSN : 0974-4290 Vol.4, No.4, 1314-1321, Oct-Dec 2012 Simulation Of Vertical Gas-Solid Flow: Comarison Of Correlations For article-wall Friction
More informationMHD Flow and Heat Transfer of a Dusty Nanofluid over a Stretching Surface in a Porous Medium
Jordan Journal o Civil Engineering, Volume 11, No. 1, 017 MHD Flow and Heat Transer o a Dusty Nanoluid over a Stretching Surace in a Porous Medium Sandee, N. 1) and Saleem, S. ) 1) Proessor, VIT University,
More informationComputational Acoustic Attenuation Performance of Helicoidal Resonators Comparable to Experiment
Comutational Acoustic Attenuation Perormance o Helicoidal Resonators Comarable to Exeriment PhD. Eng. Wojciech LAPKA Poznan University o Technology Institute o Alied Mechanics Division o Vibroacoustics
More informationCOMSOL in a New Tensorial Formulation of Non-Isothermal Poroelasticity
Excert rom the Proceedings o the COMSOL Conerence 009 oston COMSOL in a New Tensorial Formulation o Non-Isothermal Poroelasticity Mario-César Suárez A. *, 1 and Fernando Samaniego. 1 Faculty o Sciences
More informationEvaluation of Different Modelling Methods Used for Erosion Prediction
Paer No. 11005 Evaluation o Dierent Modelling Methods Used or Erosion Prediction MYSARA EISSA MOHYALDIN 1, NOAMAN ELKHATIB 2, MOKHTAR CHE ISMAIL 3 1 College o Petroleum Eng. And Tech. Sudan University
More informationCONVECTIVE HEAT TRANSFER CHARACTERISTICS OF NANOFLUIDS. Convective heat transfer analysis of nanofluid flowing inside a
Chapter 4 CONVECTIVE HEAT TRANSFER CHARACTERISTICS OF NANOFLUIDS Convective heat transer analysis o nanoluid lowing inside a straight tube o circular cross-section under laminar and turbulent conditions
More informationLift forces on a cylindrical particle in plane Poiseuille flow of shear thinning fluids
Lit orces on a cylindrical article in lane Poiseuille low o shear thinning luids J. Wang and D. D. Joseh Deartment o Aerosace Engineering and Mechanics, University o Minnesota, Aril 3 Abstract Lit orces
More informationChapter 1 Fundamentals
Chater Fundamentals. Overview of Thermodynamics Industrial Revolution brought in large scale automation of many tedious tasks which were earlier being erformed through manual or animal labour. Inventors
More informationHomogeneous and Inhomogeneous Model for Flow and Heat Transfer in Porous Materials as High Temperature Solar Air Receivers
Excert from the roceedings of the COMSOL Conference 1 aris Homogeneous and Inhomogeneous Model for Flow and Heat ransfer in orous Materials as High emerature Solar Air Receivers Olena Smirnova 1 *, homas
More informationANALYSIS OF ULTRA LOW CYCLE FATIGUE PROBLEMS WITH THE BARCELONA PLASTIC DAMAGE MODEL
XII International Conerence on Comutational Plasticity. Fundamentals and Alications COMPLAS XII E. Oñate, D.R.J. Owen, D. Peric and B. Suárez (Eds) ANALYSIS OF ULTRA LOW CYCLE FATIGUE PROBLEMS WITH THE
More informationFree convection of nanoliquids in an enclosure with sinusoidal heating
IOP Conerence Series: Materials Science and Engineering PAPER OPEN ACCESS Free convection o nanoliquids in an enclosure with sinusoidal heating To cite this article: S. Sivasanaran et al 018 IOP Con. Ser.:
More informationITB J. Eng. Sci. Vol. 41, No. 1, 2009,
ITB J. Eng. Sci. Vol. 41, No. 1, 2009, 65-76 65 ressure Drop Correlation Covering Dilute to Dense Regimes o Solid article-gas Flow in a Vertical Conveying ipe Y. Bindar, N.A. Sutrisniningrum & D. Santiani
More informationEXPERIMENTAL STUDY OF PARAMETERS INFLUENCING THE PICKUP VELOCITY IN PNEUMATIC CONVEYING SYSTEMS
Coyright 009 by ABCM EXPERIMENTAL STDY OF PARAMETERS INFLENCING THE PICKP VELOCITY IN PNEMATIC CONVEYING SYSTEMS Luiz Moreira Gomes, luizmg@ufa.br. André Luiz Amarante Mesquita, andream@ufa.br Lab. de
More informationInterference Drag Between Cylindrical Particles in Stokes Flow
Eng. & Tech. Journal,Vol.7, No.8,009 Intererence rag Between ylindrical r. Abbas H. Sulaymon* & r. Sawsan A. M. Mohammed* Abstract Received on: /6/008 Acceted on:5/3/009 In this study, the intererence
More informationBi-power law correlations for sediment transport in pressure driven channel flows
Bi-ower law correlations or sediment transort in ressure driven channel lows J. ang, D. D. Joseh Deartment o Aerosace Engineering and Mechanics, University o Minnesota, Minneaolis, MN 55455 N. A. Patankar
More informationSeparation of Heterogeneous Solid Fluid Mixtures IX. Filtration theory with new flowing models through packed beds
Searation of Heterogeneous Solid Fluid Mixtures IX. Filtration theory with new flowing models through acked beds TIBERIU DINU DANCIU* EMIL DANCIU University Politehnica of Bucharest Chemical and Biochemical
More informationTwo-phase simulation of nanofluid in a heat exchanger in turbulent flow regime
Euroean Online Journal o Natural and Social Sciences 2014; www.euroean-science.com Vol.3, No.3 Secial Issue on Environmental, Agricultural, and Energy Science ISSN 1805-3602 Two-hase simulation o nanoluid
More informationAvailable online at ScienceDirect. Procedia Engineering 102 (2015 )
Available online at www.sciencedirect.com ScienceDirect Procedia Engineering 102 (2015 ) 1366 1372 The 7th World Congress on Particle Technology (WCPT7) Numerical Modelling o ESP or Design Otimization
More informationNumerical Simulations of Methane Aromatization with and without a Ceramic Hydrogen Separation Membrane
Numerical Simulations o Methane Aromatization with and without a Ceramic ydrogen Searation Membrane Zuoan Li*, Christian ølseth, Selene ernandez Moreudo, and eidar augsrud University o Oslo, Deartment
More informationUltrasonic Peeling. The Bauman Moscow State Technical University, Russia,
V. M. Gorshkova Ultrasonic Peeling The Bauman Moscow State Technical University, ussia, v_gorshkova@mail.ru ABSTACT The article suggests a mathematical descrition o eeling by ultrasound technologies. INTODUCTION
More informationDynamics and Heat and Mass Transfer of Liquid-Droplet Cloud in the Emergency Discharge of Aviation Fuel into the Atmosphere
Dynamics and Heat and Mass Transer o Liquid-Drolet Cloud in the Emergency Discharge o Aviation Fuel into the Atmoshere Evgeny Maslov 1,,*, Amgalan Badmaev, and Irina Zharova 1 1 National Research Tomsk
More informationHeat Transfer Modeling using ANSYS FLUENT
Lecture 7 Heat raner in Porou Media 14.5 Releae Heat raner Modeling uing ANSYS FLUEN 2013 ANSYS, Inc. March 28, 2013 1 Releae 14.5 Agenda Introduction Porou Media Characterization he Rereentative Elementary
More informationComparison of electron-plasmon scattering effect on low-field electron mobility in ZnO and SiC
Arican Journal o Mathematics and Comuter Science Research Vol. (9),. 189-195, October, 9 Available online at htt://www.academicjournals.org/ajmcsr ISSN 6-971 9 Academic Journals Full Length Research Paer
More informationChapter 3 Weight estimation - 2 Lecture 7 Topics
Chater-3 Chater 3 eight estimation - 2 ecture 7 Toics 3.5 Estimation o uel raction ( / 0 ) 3.5.1 Mission roile 3.5.2 eight ractions or various segments o mission 3.5.3 Fuel raction or warm u, taxing and
More informationMODELING AND SIMULATION OF REFORMER AUTO- THERMAL REACTOR IN AMMONIA UNIT
Peet trool lleeuum & Cooaal ll IISSN 337-77 Available online at www.vuru.sk/c Petroleum & Coal 9 (), 6-7, 7 MODELING AND SIMULATION OF REFORMER AUTO- THERMAL REACTOR IN AMMONIA UNIT Kayvan Khorsand *,
More informationAnalysis of Non-Thermal Equilibrium in Porous Media
Analysis o Non-Thermal Equilibrium in Porous Media A. Nouri-Borujerdi, M. Nazari 1 School o Mechanical Engineering, Shari University o Technology P.O Box 11365-9567, Tehran, Iran E-mail: anouri@shari.edu
More informationNatural Convection and Entropy Generation in Partially Heated Porous Wavy Cavity Saturated by a Nanofluid
Proceedings o the 5 th International Conerence o Fluid Flow, Heat and Mass Transer (FFHMT'18) Niagara Falls, Canada June 7 9, 2018 Paer No. 123 DOI: 10.11159/hmt18.123 Natural Convection and Entroy Generation
More informationWhen water (fluid) flows in a pipe, for example from point A to point B, pressure drop will occur due to the energy losses (major and minor losses).
PRESSURE DROP AND OSSES IN PIPE When water (luid) lows in a pipe, or example rom point A to point B, pressure drop will occur due to the energy losses (major and minor losses). A B Bernoulli equation:
More informationParameters characterising the pulsing flow for cocurrent flow of gas and foaming liquid in a pressurised tricklebed
Parameters characterising the ulsing flow for cocurrent flow of gas and foaming liquid in a ressurised tricklebed reactor Proceedings of Euroean Congress of Chemical Engineering (ECCE-6) Coenhagen, 16-
More informationMHD Heat and Mass Transfer Forced Convection Flow Along a Stretching Sheet with Heat Generation, Radiation and Viscous Dissipation
Dhaka Univ. J. Sci. 59(): -8, (July) MHD Heat and Mass Transer Forced onvection Flo Along a Stretching Sheet ith Heat Generation, Radiation and Viscous Dissiation M. A. Samad, Sajid Ahmed and Md. Motaleb
More informationModeling Volume Changes in Porous Electrodes
Journal of The Electrochemical Society, 53 A79-A86 2006 003-465/2005/53/A79/8/$20.00 The Electrochemical Society, Inc. Modeling olume Changes in Porous Electrodes Parthasarathy M. Gomadam*,a,z John W.
More informationDetermination of Pressure Losses in Hydraulic Pipeline Systems by Considering Temperature and Pressure
Paer received: 7.10.008 UDC 61.64 Paer acceted: 0.04.009 Determination of Pressure Losses in Hydraulic Pieline Systems by Considering Temerature and Pressure Vladimir Savi 1,* - Darko Kneževi - Darko Lovrec
More informationOE4625 Dredge Pumps and Slurry Transport. Vaclav Matousek October 13, 2004
OE465 Vaclav Matousek October 13, 004 1 Dredge Vermelding Pumps onderdeel and Slurry organisatie Transport OE465 Vaclav Matousek October 13, 004 Dredge Vermelding Pumps onderdeel and Slurry organisatie
More informationAn Improved Expression for a Classical Type of Explicit Approximation of the Colebrook White Equation with Only One Internal Iteration
International Journal o Hydraulic Engineering 06, 5(): 9-3 DOI: 0.593/j.ijhe.06050.03 An Improved Expression or a Classical Type o Explicit Approximation o the Colebrook White Equation with Only One Internal
More informationNanofluids for Heat Transfer Enhancement-A Review. E.K. Goharshadi*, H. Ahmadzadeh, S. Samiee and M. Hadadian
Review article Phys. Chem. Res., Vol. 1, No. 1, 1-33, June 2013. Nanoluids or Heat Transer Enhancement-A Review E.K. Goharshadi*, H. Ahmadzadeh, S. Samiee and M. Hadadian Deartment o Chemistry, Ferdowsi
More informationThermodynamic entropy generation model for metal fatigue failure
Thermodynamic entroy generation model or metal atigue ailure Hossein Salimi a, Mohammad Pourgol-Mohammad *a, Mojtaba Yazdani a a Sahand University o Technology, Tabriz, Iran Abstract: Fatigue damage is
More informationEffective conductivity in a lattice model for binary disordered media with complex distributions of grain sizes
hys. stat. sol. b 36, 65-633 003 Effective conductivity in a lattice model for binary disordered media with comlex distributions of grain sizes R. PIASECKI Institute of Chemistry, University of Oole, Oleska
More informationPreliminary Uncertainty Estimation of the Pressure Distortion Coefficient of a Pressure. Balance by FEM Calculations
Preliminary Uncertainty Estimation of the Pressure Distortion Coefficient of a Pressure Balance by FEM Calculations G. Molinar*, M. Bergoglio*, G. Mosso*,G. Buonanno**, M. Dell Isola** * Istituto di Metrologia
More informationVELOCITY PROFILE OF ENTRAINED AIR IN FREE FALLING PARTICLE PLUMES
VELOCITY PROFILE OF ENTRAINED AIR IN FREE FALLING PARTICLE PLUMES ZQ Liu 1,*, XJ Li 1, PQ Lu 1, TH Zou 1, BY Lu 1 1 Faculty of Mechanical Engineering, Tianjin University of Commerce, Tianjin, 300134, China
More informationResearch on differences and correlation between tensile, compression and flexural moduli of cement stabilized macadam
Research on dierences and correlation between tensile, comression and lexural moduli o cement stabilized macadam Yi Yang School o Traic and Transortation, Changsha University o Science & Technology, Hunan
More informationEffect of geometry on flow structure and pressure drop in pneumatic conveying of solids along horizontal ducts
Journal of Scientific LAÍN & Industrial SOMMERFELD Research: PNEUMATIC CONVEYING OF SOLIDS ALONG HORIZONTAL DUCTS Vol. 70, February 011,. 19-134 19 Effect of geometry on flow structure and ressure dro
More informationPNEUMATIC/HYDRAULIC CONVEYING Ron Zevenhoven ÅA Thermal and Flow Engineering
6 luid and Particulate Systems 424521 /2018 LUIDISATION PNEUMATIC/HYDRAULIC CONVEYING Ron Zevenhoven ÅA Thermal and low Engineering ron.zevenhoven@abo.fi 6.1 luidised beds (Bs) : basic features RoNz 2
More informationA compression line for soils with evolving particle and pore size distributions due to particle crushing
Russell, A. R. (2011) Géotechnique Letters 1, 5 9, htt://dx.doi.org/10.1680/geolett.10.00003 A comression line for soils with evolving article and ore size distributions due to article crushing A. R. RUSSELL*
More informationNON-SIMILAR SOLUTIONS FOR NATURAL CONVECTION FROM A MOVING VERTICAL PLATE WITH A CONVECTIVE THERMAL BOUNDARY CONDITION
NON-SIMILAR SOLUTIONS FOR NATURAL CONVECTION FROM A MOVING VERTICAL PLATE WITH A CONVECTIVE THERMAL BOUNDARY CONDITION by Asterios Pantokratoras School o Engineering, Democritus University o Thrace, 67100
More informationSpecific velocity and Re effects
Seciic velocity and Re eects Content: Seciic velocity and turbomachines geometry Seciic diameter Cordier diram Exercise Reynolds number eects. Seciic velocity and turbomachines geometry For a given um,
More informationModeling and Simulation a Catalytic Fixed Bed Reactor to Produce Ethyl Benzene from Ethanol
Journal of Physical Chemistry and Electrochemistry Vol. No.3 (20) 55-6 Journal of Physical Chemistry and Electrochemistry Islamic Azad University Marvdasht ranch Journal homeage: htt://journals.miau.ac.ir/je
More informationSTUDY ON OIL FILM CHARACTERISTICS OF SLIPPER WITHIN AXIAL PISTON PUMP UNDER DIFFERENT WORKING CONDITION
STUDY ON OIL FILM CHAACTEISTICS OF SLIPPE WITHIN AXIAL PISTON PUMP UNDE DIFFEENT WOKING CONDITION Yi Sun, Jihai-Jiang. Harbin Institute o Technology, School o Mechtrionics Engineering, China ABSTACT In
More informationProblem set 6 for Quantum Field Theory course
Problem set 6 or Quantum Field Theory course 2018.03.13. Toics covered Scattering cross-section and decay rate Yukawa theory and Yukawa otential Scattering in external electromagnetic ield, Rutherord ormula
More informationFactor Analysis of Convective Heat Transfer for a Horizontal Tube in the Turbulent Flow Region Using Artificial Neural Network
COMPUTATIONAL METHODS IN ENGINEERING AND SCIENCE EPMESC X, Aug. -3, 6, Sanya, Hainan,China 6 Tsinghua University ess & Sringer-Verlag Factor Analysis of Convective Heat Transfer for a Horizontal Tube in
More informationScaling Multiple Point Statistics for Non-Stationary Geostatistical Modeling
Scaling Multile Point Statistics or Non-Stationary Geostatistical Modeling Julián M. Ortiz, Steven Lyster and Clayton V. Deutsch Centre or Comutational Geostatistics Deartment o Civil & Environmental Engineering
More informationKuldeep Rawat*, Ayushman Srivastav* *Assistant Professor, Shivalik College of Engineering, Dehradun.
International Journal o Scientiic & Engineering search, Volume 7, Issue 12, December-16 348 ISSN 2229-18 NUMERICAL INVESTIGATION OF HEAT TRANSFER ENHANCEMENT OVER RECTANGULAR PERFORATED FIN Abstract Kuldeep
More informationBuoyancy Driven Heat Transfer of Water-Based CuO Nanofluids in a Tilted Enclosure with a Heat Conducting Solid Cylinder on its Center
July 4-6 2012 London U.K. Buoyancy Driven Heat Transer o Water-Based CuO Nanoluids in a Tilted Enclosure with a Heat Conducting Solid Cylinder on its Center Ahmet Cihan Kamil Kahveci and Çiğdem Susantez
More informationComputational Analysis of Nanofluid Flow in Microchannels with Applications to Micro-heat Sinks and Bio-MEMS
ABSTRACT LI, JIE. Comutational Analysis o Nanoluid Flow in Microchannels with Alications to Micro-heat Sinks and Bio-MEMS. (Under the direction o Proessor C. Kleinstreuer.) Nanoluids, i.e., dilute susensions
More informationGas-side mass transfer coefficient of a laboratory column equipped with one sieve tray
Gas-side mass transer coeicient o a laoratory column equipped with one sieve tray Zhivko Ivanov, Zhelcho Steanov, Bogdan Bogdanov Astract: The inluence o plate geometry on the characteristics o luid low
More informationA MIXED CONTROL CHART ADAPTED TO THE TRUNCATED LIFE TEST BASED ON THE WEIBULL DISTRIBUTION
O P E R A T I O N S R E S E A R C H A N D D E C I S I O N S No. 27 DOI:.5277/ord73 Nasrullah KHAN Muhammad ASLAM 2 Kyung-Jun KIM 3 Chi-Hyuck JUN 4 A MIXED CONTROL CHART ADAPTED TO THE TRUNCATED LIFE TEST
More informationMahmood Bazmi*, Seyed Hassan Hashemabadi*,, and Mahmood Bayat**
Korean J. Chem. Eng., 28(6), 1340-1346 (2011) DOI: 10.1007/s11814-010-0525-8 INVITED REVIEW PAPER Modification of Ergun equation for application in trickle bed reactors randomly packed with trilobe particles
More informationLogistics Optimization Using Hybrid Metaheuristic Approach under Very Realistic Conditions
17 th Euroean Symosium on Comuter Aided Process Engineering ESCAPE17 V. Plesu and P.S. Agachi (Editors) 2007 Elsevier B.V. All rights reserved. 1 Logistics Otimization Using Hybrid Metaheuristic Aroach
More informationNUMERICAL ANALYSIS OF FORCED CONVECTION HEAT TRANSFER FROM TWO TANDEM CIRCULAR CYLINDERS EMBEDDED IN A POROUS MEDIUM
THERMAL SCIENCE, Year 2017, Vol. 21, No. 5, pp. 2117-2128 2117 Introduction NUMERICAL ANALYSIS OF FORCED CONVECTION HEAT TRANSFER FROM TWO TANDEM CIRCULAR CYLINDERS EMBEDDED IN A POROUS MEDIUM by Habib-Ollah
More informationEffect of the variable porosity on the heat transfer process in solar air receiver
Engineering Conerences International ECI Digital Archives Sixth International Conerence on Porous Meia an Its Alications in Science, Engineering an Inustry Proceeings 7-5-2016 Eect o the variable orosity
More informationThe Numerical Simulation of Gas Turbine Inlet-Volute Flow Field
World Journal of Mechanics, 013, 3, 30-35 doi:10.436/wjm.013.3403 Published Online July 013 (htt://www.scir.org/journal/wjm) The Numerical Simulation of Gas Turbine Inlet-Volute Flow Field Tao Jiang 1,
More informationANALYTIC APPROXIMATE SOLUTIONS FOR FLUID-FLOW IN THE PRESENCE OF HEAT AND MASS TRANSFER
Kilicman, A., et al.: Analytic Aroximate Solutions for Fluid-Flow in the Presence... THERMAL SCIENCE: Year 8, Vol., Sul.,. S59-S64 S59 ANALYTIC APPROXIMATE SOLUTIONS FOR FLUID-FLOW IN THE PRESENCE OF HEAT
More informationSteady MHD Flow of Nano-Fluids over a Rotating Porous Disk in the Presence of Heat Generation/Absorption: a Numerical Study using PSO
Journal o Alied Fluid Mechanics, Vol., No.,. 87-879, 7. Available online at.jamonline.net, ISSN 75-57, EISSN 75-645. DOI:.8869/acadub.jam.7.4.665 Steady MHD Flo o Nano-Fluids over a Rotating Porous Dis
More informationOn the Fluid Dependence of Rock Compressibility: Biot-Gassmann Refined
Downloaded 0/9/3 to 99.86.4.8. Redistribution subject to SEG license or coyright; see Terms of Use at htt://library.seg.org/ On the luid Deendence of Rock Comressibility: Biot-Gassmann Refined Leon Thomsen,
More informationCFD AS A DESIGN TOOL FOR FLUID POWER COMPONENTS
CFD AS A DESIGN TOOL FOR FLUID POWER COMPONENTS M. BORGHI - M. MILANI Diartimento di Scienze dell Ingegneria Università degli Studi di Modena Via Cami, 213/b 41100 Modena E-mail: borghi@omero.dsi.unimo.it
More informationJournal of System Design and Dynamics
Vol. 5, No. 6, Effects of Stable Nonlinear Normal Modes on Self-Synchronized Phenomena* Hiroki MORI**, Takuo NAGAMINE**, Yukihiro AKAMATSU** and Yuichi SATO** ** Deartment of Mechanical Engineering, Saitama
More informationOptimal Design of Truss Structures Using a Neutrosophic Number Optimization Model under an Indeterminate Environment
Neutrosohic Sets and Systems Vol 14 016 93 University of New Mexico Otimal Design of Truss Structures Using a Neutrosohic Number Otimization Model under an Indeterminate Environment Wenzhong Jiang & Jun
More informationDirac s Hole Theory and the Pauli Principle: Clearing up the Confusion
Adv. Studies Theor. Phys., Vol. 3, 29, no. 9, 323-332 Dirac s Hole Theory and the Pauli Princile: Clearing u the Conusion Dan Solomon Rauland-Borg Cororation 82 W. Central Road Mount Prosect, IL 656, USA
More informationVI. Electrokinetics. Lecture 31: Electrokinetic Energy Conversion
VI. Electrokinetics Lecture 31: Electrokinetic Energy Conversion MIT Student 1 Princiles 1.1 General Theory We have the following equation for the linear electrokinetic resonse of a nanochannel: ( ) (
More informationScattering of a ball by a bat in the limit of small deformation
INVESTIGACIÓN Revista Mexicana de Física 58 01 353 370 AGOSTO 01 Scattering o a all y a at in the limit o small deormation A. Cao Deartamento de Física Teórica, Instituto de Ciernética, Matemática y Física,
More informationPublished in Powder Technology, 2005
Published in Powder Technology, 2005 Prediction of minimum bubbling velocity, fluidization index and range of particulate fluidization for gas solid fluidization in cylindrical and non-cylindrical beds
More informationModelling heat transfer and fluid flow inside a pressure cooker
17 th Euroean Symosium on Comuter Aided Process Engineering ESCAPE17 V. Plesu and P.S. Agachi (Editors) 2007 Elsevier B.V. All rights reserved. 1 Modelling heat transfer and fluid flow inside a ressure
More informationTime Frequency Aggregation Performance Optimization of Power Quality Disturbances Based on Generalized S Transform
Time Frequency Aggregation Perormance Otimization o Power Quality Disturbances Based on Generalized S Transorm Mengda Li Shanghai Dianji University, Shanghai 01306, China limd @ sdju.edu.cn Abstract In
More informationANALYTICAL MODEL FOR THE BYPASS VALVE IN A LOOP HEAT PIPE
ANALYTICAL MODEL FOR THE BYPASS ALE IN A LOOP HEAT PIPE Michel Seetjens & Camilo Rindt Laboratory for Energy Technology Mechanical Engineering Deartment Eindhoven University of Technology The Netherlands
More informationMechanical Engineering Research Journal BUOYANT FLOW OF NANOFLUID FOR HEAT-MASS TRANSFER THROUGH A THIN LAYER
Dept. o Mech. Eng. CUET Published Online March 2015 (http://www.cuet.ac.bd/merj/index.html) Mechanical Engineering Research Journal Vol. 9, pp. 712, 2013 M E R J ISSN: 1990-5491 BUOYANT FLOW OF NANOFLUID
More informationA Semi-Analytical Solution for a Porous Channel Flow of a Non-Newtonian Fluid
Journal o Applied Fluid Mechanics, Vol. 9, No. 6, pp. 77-76, 6. Available online at www.jamonline.net, ISSN 735-357, EISSN 735-3645. A Semi-Analytical Solution or a Porous Channel Flow o a Non-Newtonian
More informationComparison of the Adsorption Characteristics of Expanded Bed Adsorbent with Conventional Chromatographic Adsorbent
Korean J. Chem. Eng., 18(3), 357-362 (2001) Comarison of the Adsortion Characteristics of Exanded Bed Adsorbent with Conventional Chromatograhic Adsorbent Hong-Bo Hu, Shan-Jing Yao, Zi-Qiang Zhu and Byung-Ki
More informationDETERMINISTIC STOCHASTIC SUBSPACE IDENTIFICATION FOR BRIDGES
DEERMINISIC SOCHASIC SBSPACE IDENIFICAION FOR BRIDGES H. hai, V. DeBrunner, L. S. DeBrunner, J. P. Havlicek 2, K. Mish 3, K. Ford 2, A. Medda Deartment o Electrical and Comuter Engineering Florida State
More information#A64 INTEGERS 18 (2018) APPLYING MODULAR ARITHMETIC TO DIOPHANTINE EQUATIONS
#A64 INTEGERS 18 (2018) APPLYING MODULAR ARITHMETIC TO DIOPHANTINE EQUATIONS Ramy F. Taki ElDin Physics and Engineering Mathematics Deartment, Faculty of Engineering, Ain Shams University, Cairo, Egyt
More information4. Multi-phase flow (an introduction...) (lecture 4 of 4)
Introduction to Comutational Fluid Dynamics (icfd) 445.0 E, 5 s See also ÅA course 445 (5 s) Fluid and articulate systems htt://users.abo.i/rzevenho/kursrz.html#fps 4. Multi-hase low (an introduction...)
More informationMODEL-BASED MULTIPLE FAULT DETECTION AND ISOLATION FOR NONLINEAR SYSTEMS
MODEL-BASED MULIPLE FAUL DEECION AND ISOLAION FOR NONLINEAR SYSEMS Ivan Castillo, and homas F. Edgar he University of exas at Austin Austin, X 78712 David Hill Chemstations Houston, X 77009 Abstract A
More informationMathematical Simulation of Bubble Column Slurry Reactor for Direct Dimethyl Ether Synthesis Process from Syngas
World Academy o Science Engineering and Technology International Journal o Chemical Molecular Nuclear Materials and Metallurgical Engineering Vol:4 No:8 1 Mathematical Simulation o Bubble Column Slurry
More information602 ZHANG Zhi and CHEN Li-Rong Vol Gibbs Free Energy From the thermodynamics, the Gibbs free energy of the system can be written as G = U ; TS +
Commun. Theor. Phys. (Beijing, China) 37 (2002) 601{606 c International Academic Publishers Vol. 37, No. 5, May 15, 2002 The 2D Alternative Binary L J System: Solid-Liquid Phase Diagram ZHANG Zhi and CHEN
More informationA Comprehensive Study on a Latent Heat Thermal Energy Storage System and its Feasible Applications in Greenhouses
Iranian Journal of Chemical Engineering Vol. 13, No. 2 (Sring 2016, IAChE A Comrehensive Study on a Latent Heat Thermal Energy Storage System and its Feasible Alications in reenhouses A. Mirahmad 1, S.
More informationExperimental Determination of Flow and Heat Transfer Correlations for Passive Regenerators
Purdue University Purdue e-pubs International Rerigeration and Air Conditioning Conerence School o Mechanical Engineering 20 Exeriental Deterination o Flow and Heat Transer Correlations or Passive Regenerators
More informationEstimation of Probability of Coition on Different Days of a Menstrual Cycle near the Day of Ovulation: An Application of Theory of Markov Chain
Demograhy India (0) ISSN: 0970-X Vol., Issue: &, : 3-39 Research Article stimation o Probability o Coition on Dierent Days o a Menstrual Cycle near the Day o Ovulation: An Alication o Theory o Marov Chain
More informationHigh speed wind tunnels 2.0 Definition of high speed. 2.1 Types of high speed wind tunnels
Module Lectures 6 to 1 High Seed Wind Tunnels Keywords: Blow down wind tunnels, Indraft wind tunnels, suersonic wind tunnels, c-d nozzles, second throat diffuser, shocks, condensation in wind tunnels,
More informationScienceDirect. Heat transfer and fluid transport of supercritical CO 2 in enhanced geothermal system with local thermal non-equilibrium model
Available online at www.sciencedirect.com ScienceDirect Energy Procedia 63 (2014 ) 7644 7650 GHGT-12 Heat transer and luid transport o supercritical CO 2 in enhanced geothermal system with local thermal
More informationHybrid time-frequency domain adaptive filtering algorithm for electrodynamic shaker control
Journal o Engineering and Comuter Innovations Vol. (10),. 191-05, December 011 Available online at htt://www.academicjournals.org/jeci DOI: 10.5897/JECI11.05 ISSN 141-6508 011 Academic Journals Full Length
More informationMagneto-thermal convection of low concentration nanofluids
MATEC Web o Conerences 8, 6 () DOI:./ mateccon/ 86 C Owned by the authors, ublished by EDP Sciences, Magneto-thermal convection o low concentration nanoluids Aleksandra Roszko, Elzbieta Fornalik-Wajs,
More informationENERGY TRANSFORMATION DURING THE PIERCE PROCESS IN THE PRODUCTION OF SEAMLESS PIPES
Acta Metallurgica Slovaca, Vol. 22, 2016, No. 1,. 60-67 60 ENERGY TRANSFORMATION DURING THE PIERCE PROCESS IN THE PRODUCTION OF SEAMLESS PIPES Ladislav Lazić 1)*, Martina Lovrenić - Jugović 1), Željko
More informationINTRODUCING THE SHEAR-CAP MATERIAL CRITERION TO AN ICE RUBBLE LOAD MODEL
Symosium on Ice (26) INTRODUCING THE SHEAR-CAP MATERIAL CRITERION TO AN ICE RUBBLE LOAD MODEL Mohamed O. ElSeify and Thomas G. Brown University of Calgary, Calgary, Canada ABSTRACT Current ice rubble load
More informationSupplementary Information The Interplay of Kinetics and Thermodynamics in the Catalytic Steam Methane Reforming. over Ni/MgO-SiO 2
Sulementary Information The Interlay of inetics and Thermodynamics in the Catalytic Steam Methane Reforming over Ni/Mg-Si Naoi ageyama a, Brigitte R. Devocht b, Atsushi Taagai a, enneth Toch b, Joris W.
More information