0

4—transfer correction see s6 1

Tài liệu Hướng dẫn-Nâng cao Win2003-phần 4 - DNS Zone Transfer pdf

Tài liệu Hướng dẫn-Nâng cao Win2003-phần 4 - DNS Zone Transfer pdf

Hệ điều hành

... Host PC 01 PC02 e Trong Reverse Lookup Zones → Vào 19 2 .16 8.4.x kiểm tra thấy có Pointer IP PC 01 PC02 72 Phiên Bản Thử Nghiệm – Lưu Hành Nội Bộ III Thực hiện: Cấu hình DNS Zone Tranfer PC 01 a Trong ... Nghiệm – Lưu Hành Nội Bộ 71 b Trong cửa sổ New Host nhập vào thông số sau: Name: PC 01 IP Address: Địa IP PC 01 (vd: 19 2 .16 8.4.23) → Đánh dấu chọn vào ô Create associated pointer (PTR) record → Add Host ... Bộ 75 f Trong cửa sổ Master DNS Servers → Nhập địa IP PC 01 vào ô IP Address → Add → Next → Finish → Kiểm tra 19 2 .16 8.4.x có Pointer PC 01 PC02 * Ngoài ra, ta làm gia tăng tính Security cách cho...
  • 8
  • 572
  • 3
Báo cáo khoa học: Receptor- and calcium-dependent induced inositol 1,4,5-trisphosphate increases in PC12h cells as shown by fluorescence resonance energy transfer imaging pot

Báo cáo khoa học: Receptor- and calcium-dependent induced inositol 1,4,5-trisphosphate increases in PC12h cells as shown by fluorescence resonance energy transfer imaging pot

Báo cáo khoa học

... transfer J Biol Chem 276, 15 337 15 344 10 Vicentini LM, Ambrosini A, Di Virgilio F, Pozzan T & Meldolesi J (19 85) Muscarinic receptor-induced phos- 515 6 16 17 18 19 20 21 22 23 phoinositide hydrolysis ... 11 12 Acknowledgements This work was supported by Grant-in-Aid 10 214 204 for Scientific Research on Priority Areas (B) on ‘Regulation of Neural Transduction by Glial Cells’, Grant-in-Aid 15 08 210 1 ... criticism of the manuscript 13 14 15 References Berridge MJ, Lipp P & Bootman MD (2000) The versatility and universality of calcium signalling Nat Rev Mol Cell Biol 1, 11 – 21 Carafoli E (2002) Calcium...
  • 11
  • 419
  • 0
Heat Transfer Engineering Applications Part 4 potx

Heat Transfer Engineering Applications Part 4 potx

Kĩ thuật Viễn thông

... Volkov, A & Klaumünzer, S (19 95) Model of track formation, Physical Review B 51( 18): 12 107 12 115 URL: http://link.aps.org/doi /10 .11 03/PhysRevB. 51. 1 210 7 Sands, D (2 011 ) Pulsed laser heating and ... shaped embedded Au nanoparticles, Applied Physics Letters 94 (11 ): 11 310 7 URL: http://link.aip.org/link/APPLAB/v94/i 11/ p 113 107/s1&Agg=doi 84 14 Heat Transfer - Engineering Applications Will-be-set-by-IN-TECH ... Effects and Defects in Solids 16 2(7): 5 01 513 URL: http://www.informaworld.com/openurl?genre=article&doi =10 .10 80 /10 42 015 07 014 72 2 21& magic=crossref||D404A21C5BB053405B1A640AFFD44AE3 Lin, Z & Zhigilei,...
  • 30
  • 460
  • 0
Mass Transfer in Chemical Engineering Processes Part 4 pot

Mass Transfer in Chemical Engineering Processes Part 4 pot

Kĩ thuật Viễn thông

... Transfer, 19 87; (30): 10 51- 1060 Shen, C.M ; Worek, W.M., 19 92 The Effect of Wall Conduction on the Performance of Regenerative Heat Exchangers, Energy, 19 92, (17 ),pp .11 99 -12 13 Sphaier, C.M.; Worek, ... Cowling (19 70)[9] The model was then further matured through the work of Jenkins and Savage (19 83) [10 ], Lun et al (19 84) [18 ], Ding and Gidaspow (19 90) [11 ], Gidaspow et al (19 92)[8], and Gidaspow (19 94) [12 ] ... balances W   Y  Yw  t * T1  Tw  T  x * Tw t * (8) (9)  T  Tw    Y  Yw  (10 ) With 2  2  C wr H f T1 Q H T1 (11 ) (12 ) Equation (12 ) represents the heat of adsoprtion,...
  • 25
  • 684
  • 0
Convection and Conduction Heat Transfer Part 4 pdf

Convection and Conduction Heat Transfer Part 4 pdf

Kĩ thuật Viễn thông

... 0 .16 5 0.247 0.329 0. 412 0.494 0.576 0.659 0.7 41 0.824 0.906 0.988 1. 0 71 1 .15 3 1. 235 (a) 0. 018 0.035 0.053 0.0 71 0.088 0 .10 6 0 .12 4 0 .14 1 0 .15 9 0 .17 7 0 .19 4 0. 212 0.230 0.247 0.265 (b) 0.004 0. 011 ... cooling, J.Heat Transfer 11 0 (19 88) 10 97 11 11 [5] C K Cha and Y Jaluria, Recirculating mixed convection flow for energy extraction, Int j Heat Mass Transfer 27 .18 01- 1 810 11 984) [6] J Imberger’and ... steady state regime (figure 11 .b.) 30 30 Legend: 25 Nu _ Galerkin Collocation 20 20 Nu Legend: 25 Galerkin Collocation 15 15 10 10 5 10 z/R 15 20 (a) 10 z/R 15 20 (b) Fig 11 Heat transfer comparison...
  • 30
  • 517
  • 0
Developments in Heat Transfer Part 4 doc

Developments in Heat Transfer Part 4 doc

Kĩ thuật Viễn thông

... and vertical pipe (Holman, 19 81) In case of horizontal pipe, 0.53 · 10 · 10 (8) 0 .13 · 10 · 10 (9) · 10 · 10 (10 ) And in case of vertical pipe, 0.59 0 .1 · 10 · 10 (11 ) Where Prf is Prantl number ... (4×2.66GHz) 26000 Mesh resolution (estimated) Ra = 2 10 9 : 64 14 4× 318 Ra = 10 10 : 12 8 19 0×462 time step Ra = 2 10 9 : 1. 27 10 -3 Ra = 10 10 : 6.25 10 -4 Computer: Nec-Sx5 vectorial parallel machine ... constant, J s-1m-2K-4 free molecular heat conductivity at 0°C, J s-1m-1K -1 heat conductivity of the water vapour at ambient pressure, J s-1m-1K -1 heat conductivity of the glass, J s-1m-1K -1 heat conductivity...
  • 40
  • 415
  • 0
Heat and Mass Transfer Modeling and Simulation Part 4 docx

Heat and Mass Transfer Modeling and Simulation Part 4 docx

Kĩ thuật Viễn thông

... fact Fig 11 illustrates its distribution over the fin region 2.5 0 .1 0 .18 1. 5 0.2 0 .1 16 16 16 14 0.2 0.2 0.5 16 0.2 y* 0 .1 22 0 16 0 -1 0.2 0 .1 -0.5 0.2 -1. 5 -2.5 -2.5 0.2 16 0 .1 0 .18 -2 0.2 ... of FLUENT3.2 rSR  49 710 00T 3.0257 exp(  C5 C3 99.937 1. 62 61 1.3396 )C1 (1  ) C2 RT KSR ,C C1C2 rDE  207600T 1. 1274 exp(  C C3 12 1.5 71 1 .12 74 )C1 (1  ) RT KDE ,C C1 (1) (2) In this study, ... Simulation 2.5 0 .15 0 .1 0 .1 0 .1 0.05 0 .15 0 0.0 0.5 y* 0.05 1 0.2 0 .1 0.05 1. 5 0.2 -1 0 .1 -0.5 0.05 -1. 5 -2 -2.5 -2.5 -2 0 .1 0 .1 -1. 5 0 .1 -1 -0.5 x* 0.5 1. 5 2.5 Fig 10 b Fin temperature distribution...
  • 20
  • 460
  • 0
Heat Transfer Engineering Applications Part 4 pot

Heat Transfer Engineering Applications Part 4 pot

Kĩ thuật Viễn thông

... Volkov, A & Klaumünzer, S (19 95) Model of track formation, Physical Review B 51( 18): 12 107 12 115 URL: http://link.aps.org/doi /10 .11 03/PhysRevB. 51. 1 210 7 Sands, D (2 011 ) Pulsed laser heating and ... shaped embedded Au nanoparticles, Applied Physics Letters 94 (11 ): 11 310 7 URL: http://link.aip.org/link/APPLAB/v94/i 11/ p 113 107/s1&Agg=doi 84 14 Heat Transfer - Engineering Applications Will-be-set-by-IN-TECH ... Effects and Defects in Solids 16 2(7): 5 01 513 URL: http://www.informaworld.com/openurl?genre=article&doi =10 .10 80 /10 42 015 07 014 72 2 21& magic=crossref||D404A21C5BB053405B1A640AFFD44AE3 Lin, Z & Zhigilei,...
  • 30
  • 361
  • 0
Evaporation Condensation and Heat transfer Part 4 pot

Evaporation Condensation and Heat transfer Part 4 pot

Kĩ thuật Viễn thông

... 10 00 WATER ITERM 6Mb ITERM 12 ITERM 30MF 10 0 10 10 0 ΔT, K Fig Heat transfer coefficient for water and water-iterm oil mixtures 10 0000 q, W/m2 WATER OIL WATER-OIL 10 20 30 10 000 10 ΔT, K 10 0 10 00 ... εol =12 %; OCW - q=37 kW/m2, εol =15 %); b) 2500 2250 τ = 70 T sr,m , oC α , W/m K 2750 10 6 τlim 65 q=67,9 kW/m2 εo =12 % p=748mmHg α ΔΤ Tsr,m 10 4 2000 17 50 10 2 60 55 50 15 00 45 12 50 τ = 40 10 00 10 0 ... 5000 εo 17 % 15 % 14 % 11 % 9% 7% 6% 4% 2% 4500 4000 3500 3000 τlim 2500 2000 15 00 10 00 500 0 10 20 30 40 50 60 70 80 90 10 0 τ, Fig 17 Run-time of heat transfer coefficient; water-iterm oil 12 mixtures...
  • 40
  • 286
  • 0
Advanced Topics in Mass Transfer Part 4 ppt

Advanced Topics in Mass Transfer Part 4 ppt

Kĩ thuật Viễn thông

... 19 72) Re = 3 .1 ⋅ 10 − ⋅ 10 Re = 3 .1 ⋅ 10 − ⋅ 10 Solid particles suspended in agitated vessel with baffles 0.33 ⎛d ⎞ Sh = 10 .68 ⋅ 10 Re0 .15 Sc 0.08 ⎜ s ⎟ ⎝d⎠ Re = 6.3 ⋅ 10 − 3.3 ⋅ 10 Solid-liquid ... Transfer, Vol 49, 15 01- 1 515 ISSN 0 017 -9 310 Noordsij, P & Rotte, J.W (19 67) Mass transfer coefficients to a rotating and to a vibrating sphere Chemical Engineering Science, Vol 22, 14 75 -14 81, ISSN 0009-2509 ... Sh∗ Sh∗ = Sh ρ ∗ Emax ⇒ Sh ∗ = ( 0 .17 N exp ( −0 .12 N ) ) Re Sc ( + 0 .11 Re ) 9.35 N exp ( 1. 21 N ) )( + 0.0 21 Re )( + 0.255 Re ) ( 0.33 rec 1. 37 0.33 0.22 rec 1. 25 rec 0.95 rec (54) The graphical...
  • 40
  • 329
  • 0
Heat Transfer Mathematical Modelling Numerical Methods and Information Technology Part 4 potx

Heat Transfer Mathematical Modelling Numerical Methods and Information Technology Part 4 potx

Kĩ thuật Viễn thông

... Residue 10 11 12 13 14 15 16 17 10 00 10 00 2 2 2 10 00 2 10 00 10 00 10 00 1. 99 × 10 −3 8.90 × 10 −4 1. 05 × 10 −3 8.64 × 10 −4 9 .18 × 10 −4 1. 66 × 10 −4 1. 54 × 10 −4 4.57 × 10 −4 6. 41 × 10 −5 1. 91 × 10 −3 1. 21 × 10 −4 ... 10 −5 2.46 × 10 −4 6 .19 × 10 −3 2.85 × 10 −4 3.07 × 10 −3 1. 31 × 10 −3 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 1. 51 0.46 0.33 2.28 0.53 3. 31 0.57 1. 73 1. 66 ... 1. 66 1. 59 1. 15 0.34 0.90 5.47 0.25 0.78 0.37 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 10 00 1. 51 0.48 0.33 2.28 0.52 3.32 0.59 1. 65 1. 78 1. 66 1. 27 0.34 1. 05...
  • 40
  • 362
  • 0
Heat Transfer Theoretical Analysis Experimental Investigations Systems Part 4 pptx

Heat Transfer Theoretical Analysis Experimental Investigations Systems Part 4 pptx

Kĩ thuật Viễn thông

... plate SU-8 Air Thermal Conductivity (W/mK) at 300K 14 8 16 1 34 16 1. 38 1. 4 0 .15 0 .16 0.2* 0.026 Thermal Expansion (ppm/K) at 300K 2.6 19 .2 2.4 0.8 10 .3 2.8 62.5 62 52* Coefficient Data can be found ... are expected 12 9 Microchannel Heat Transfer 206.9 Re = 6.5 H = 34.7μm 17 2.4 Pressure (kPa) Pure Water KCl = 10 -4M KCl = 10 -2M Re = 15 .6 13 7.9 Pure Water KCl = 10 -4M KCl = 10 -2M 10 3.4 Re = 25 ... plates channel in the entry region (Naito, 19 84) can be expressed as follows: Nux = 0.4 610 43Gz1 (1 + 6.35257 Gz 1 − 33.4079Gz 1 + 419 .15 8Gz −3 − 15 37.84Gz−2 ) (8-42) Comparison of the correlation...
  • 40
  • 238
  • 0
Mass Transfer in Multiphase Systems and its Applications Part 4 pot

Mass Transfer in Multiphase Systems and its Applications Part 4 pot

Kĩ thuật Viễn thông

... Systems 14 3 14 3 Run 11 1 Run 11 2 Run 11 3 Run 11 4 Run 11 5 L (m) data 0 0,5 1, 5 -ln(χ ∗) * Fig Effect of the kinetic coefficient on the flotation yield, Simulations with χ R = 0.225 , kd up = (Run 11 1), ... ; wog ∈ ; X ∈ No Impeller A b c m1 m2 ±Δ, % Exp point Rushton turbine (RT) 0.0 31 0.43 0. 515 -18 6,67 11 .9 21 6.8 10 0 Smith turbine (CD 6) ... ; PG-L-S/VL ∈ ; wog ∈ ; X ∈ No Configuration of impellers A B C m ±Δ, % lower upper Rushton Turbine A 315 0 .10 3 0.409 0.695 4 .10 ...
  • 40
  • 422
  • 0
Convection and Conduction Heat Transfer Part 4 doc

Convection and Conduction Heat Transfer Part 4 doc

Kĩ thuật Viễn thông

... 0 .16 5 0.247 0.329 0. 412 0.494 0.576 0.659 0.7 41 0.824 0.906 0.988 1. 0 71 1 .15 3 1. 235 (a) 0. 018 0.035 0.053 0.0 71 0.088 0 .10 6 0 .12 4 0 .14 1 0 .15 9 0 .17 7 0 .19 4 0. 212 0.230 0.247 0.265 (b) 0.004 0. 011 ... cooling, J.Heat Transfer 11 0 (19 88) 10 97 11 11 [5] C K Cha and Y Jaluria, Recirculating mixed convection flow for energy extraction, Int j Heat Mass Transfer 27 .18 01- 1 810 11 984) [6] J Imberger’and ... steady state regime (figure 11 .b.) 30 30 Legend: 25 Nu _ Galerkin Collocation 20 20 Nu Legend: 25 Galerkin Collocation 15 15 10 10 5 10 z/R 15 20 (a) 10 z/R 15 20 (b) Fig 11 Heat transfer comparison...
  • 30
  • 334
  • 0
Heat Transfer Theoretical Analysis Experimental Investigations and Industrial Systems part 4 pot

Heat Transfer Theoretical Analysis Experimental Investigations and Industrial Systems part 4 pot

Kĩ thuật Viễn thông

... plate SU-8 Air Thermal Conductivity (W/mK) at 300K 14 8 16 1 34 16 1. 38 1. 4 0 .15 0 .16 0.2* 0.026 Thermal Expansion (ppm/K) at 300K 2.6 19 .2 2.4 0.8 10 .3 2.8 62.5 62 52* Coefficient Data can be found ... are expected 12 9 Microchannel Heat Transfer 206.9 Re = 6.5 H = 34.7μm 17 2.4 Pressure (kPa) Pure Water KCl = 10 -4M KCl = 10 -2M Re = 15 .6 13 7.9 Pure Water KCl = 10 -4M KCl = 10 -2M 10 3.4 Re = 25 ... plates channel in the entry region (Naito, 19 84) can be expressed as follows: Nux = 0.4 610 43Gz1 (1 + 6.35257 Gz 1 − 33.4079Gz 1 + 419 .15 8Gz −3 − 15 37.84Gz−2 ) (8-42) Comparison of the correlation...
  • 40
  • 236
  • 0
Heat Transfer Handbook part 4 ppt

Heat Transfer Handbook part 4 ppt

Điện - Điện tử

... ρV dR1 + R1 ˆ ˆ ρVVn dS1 Lines: 10 01 to 10 42 ——— (1. 66) ∂ ∂t ∂ ∂t ˆ ˆ ρVx Vn dS1 R1 (1. 67a) ˆ ˆ ρVy Vn dS1 (1. 67b) ˆ ˆ ρVx Vn dS1 ˆ ρVx dR1 = Fx − (1. 67c) S1 ˆ ρVy dR1 = Fy − R1 S1 ˆ ρVz dR1 = ... 21 / 2nd Proofs / Heat Transfer Handbook / Bejan 0.42567pt PgVar ——— Normal Page PgEnds: TEX S1 or, by rearrangement of terms, ∂ ∂t [ 21] , ( 21) [ 21] , ( 21) 22 10 11 12 13 14 15 16 17 18 19 20 21 ... MOMENTUM AND THE MOMENTUM THEOREM 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 S2 S1 a 21 c b Figure 1. 7 Regions bounded by control...
  • 10
  • 313
  • 0
Turbocharge your GMAT sentence correction guide part 4 pot

Turbocharge your GMAT sentence correction guide part 4 pot

Kỹ năng nói tiếng Anh

... typically used in a restaurant setting www.manhattanreview.com c 19 99 - 2008 Manhattan Review Sentence Correction Guide – Grammar Review 1. 7 16 Verb A class of words that serve to indicate the occurrence ... therefore found in (1) Clauses beginning with if, as if, though, as though and www.manhattanreview.com c 19 99 - 2008 Manhattan Review Sentence Correction Guide – Grammar Review 19 (2) After verbs ... dancing Conditional: would dance www.manhattanreview.com c 19 99 - 2008 Manhattan Review Sentence Correction Guide – Grammar Review 18 Common Irregular Verbs Infinitive Participle Part Participle...
  • 7
  • 268
  • 0
Kỹ thuật truyền số liệu : ATM Asynchronous Transfer Mode part 4 doc

Kỹ thuật truyền số liệu : ATM Asynchronous Transfer Mode part 4 doc

Cao đẳng - Đại học

... cell • • • • • • 622.08Mbps 15 5.52Mbps 51. 84Mbps 25.6Mbps Lớp vật lý sở cell Lớp vật lý sở SDH Data Communication and Computer Networks ©2007, Dr Dinh Duc Anh Vu 31 dce 2007 Lớp vật lý sở cell ... Dinh Duc Anh Vu 35 dce 2007 Lớp vật lý sở SDH • Áp đặt cấu trúc dòng ATM – e.g for 15 5.52Mbps – Dùng khung STM -1 (STS-3) – Có thể mang loại tải ATM STM • Các kết nối đặt biệt chuyển mạch dùng kênh...
  • 9
  • 410
  • 1
A HEAT TRANSFER TEXTBOOK - THIRD EDITION Episode 1 Part 4 potx

A HEAT TRANSFER TEXTBOOK - THIRD EDITION Episode 1 Part 4 potx

Kĩ thuật Viễn thông

... and approximation: 4 Qnet = A1 F1–2 σ T1 − T2 2 2 = A1 F1–2 σ (T1 + T2 )(T1 − T2 ) = A1 F1–2 σ 2 (T1 + T2 ) (T1 + T2 ) (T1 − T2 ) = 2Tm + (∆T )2 /2 =2Tm =∆T A1 4σ Tm F1–2 ∆T (2.28) ≡hrad 2Tm or ... §2.4 U (W/m2 K) 0.3−2 0.5−6 0.3−5 1. 2−4 ∼ 6† As low as 45 As high as 600 60−550 60−340 11 0−2, 000 11 0−8, 500 350−780 500 1, 900 800 1, 400 1, 500−5, 000 1, 500 10 , 000 Main heat loss is by infiltration ... 58 .1 s heff A (18 .44) (1. 33 × 10 −4 ) From eqn (1. 22) with T0 = 72.3◦ C Tresistor = 35.0 + (72.3 − 35.0)e−t/58 .1 ◦ C Ninety-five percent of the total temperature drop has occured when t = 3T = 17 4...
  • 25
  • 367
  • 0

Xem thêm