E501设计规定说明书

E501 设计规定说明书 Heat Exchanger Specification Sheet 1 Company: 2 Location: 3 Service of Unit: Our Reference: 4 Item No.: Your Reference: 5 Date: Rev No.: Job No.: 6 Size 711.2 / 3000 mm Type AES Hor Connected in 1 parallel 1 series 7 Surf/unit(eff.) 70.7 m2 Shells/unit 1 Surf/shell (eff.) 70.7 m2 8 PERFORMANCE OF ONE UNIT 9 Fluid allocation Shell Side Tube Side 10 Fluid name 11 Fluid quantity, Total kg/s 19.9571 3.8427 12 Vapor (In/Out) kg/s 19.9571 19.9571 0 0 13 Liquid kg/s 0 0 3.8427 3.8427 14 Noncondensable kg/s 0 0 15 16 Temperature (In/Out) C 300 294.97 159.2 260 17 Dew / Bubble point C 18 Density (Vap / Liq) kg/m3 17 / / / 920.61 / 913.5 19 Viscosity mPa*s .0199 / / / .9713 / .8447 20 Molecular wt, Vap 18.02 18.02 21 Molecular wt, NC 22 Specific heat kJ/(kg*K) 2.869 / / / .74 / .753 23 Thermal conductivity W/(m*K) .0512 / / / .0817 / .0785 24 Latent heat kJ/kg 25 Pressure (abs) bar 40 39.9732 1.013 .97935 26 Velocity m/s 4.35 .27 27 Pressure drop, allow./calc. bar .25855 .0268 .20684 .03365 28 Fouling resistance (min) m2*K/W .0002 .0015 .00182 Ao based 29 Heat exchanged 289.5 kW MTD corrected 77.14 C 30 Transfer rate, Service 53.1 Dirty 70.2 Clean 81.8 W/(m2*K) 31 CONSTRUCTION OF ONE SHELL Sketch 32 Shell Side Tube Side 33 Design/vac/test pressure:g bar 44.12647 / / 3.44738 / / 34 Design temperature C 337.78 298.89 35 Number passes per shell 1 4 36 Corrosion allowance mm 0 0 37 Connections In mm 1 387.35 / - 1 52.5 / - 38 Size/rating Out 1 387.35 / - 1 52.5 / - 39 ID Intermediate / - / - 40 Tube No. 448 OD 19 Tks- Avg 1.65 mm Length 3000 mm Pitch 25 mm 41 Tube type Plain Material SS 304 Tube pattern 90 42 Shell SS 304 ID 700 OD 730 mm Shell cover SS 304 43 Channel or bonnet SS 304 Channel cover SS 304 44 Tubesheet-stationary SS 304 Tubesheet-floating SS 304 45 Floating head cover SS 304 Impingement protection None 46 Baffle-cross SS 304 Type Unbaffled Cut(%d) Spacing: c/c mm 47 Baffle-long - Seal type Inlet mm 48 Supports-tube U-bend Type 49 Bypass seal Tube-tubesheet joint Exp. 2 grv 50 Expansion joint - Type 51 RhoV2-Inlet nozzle 1687 Bundle entrance 1618 Bundle exit 1798 kg/(m*s2) 52 Gaskets - Shell side Flat Metal Jacket Fibe Tube Side Flat Metal Jacket Fibe 53 Floating head Flat Metal Jacket Fibe 54 Code requirements ASME Code Sec VIII Div 1 TEMA class R - refinery service 55 Weight/Shell 4604.7 Filled with water 5971.4 Bundle 1460.1 kg 56 Remarks 57 58 T1 T2 S1 S2 E501 设计规定说明书 Setting Plan 102 2 Bolts Fixed 51 632 158 102 2 Bolts Sliding 51 632 158 700 I/D15 4035 Overall 2793074451930 3078061257 Pulling Length 2520 T1 T2 S1 S2 A Nozzle Data RefODWallStandardNotes S1406 mm9.5 mm150 ANSI Slip on S2406 mm9.5 mm150 ANSI Slip on T160 mm3.9 mm150 ANSI Slip on T260 mm3.9 mm150 ANSI Slip on Empty 4605 kg Flooded 5971 kg Bundle 1460 kg Weight Summary Internal Volumem?1.31250.2708 PWHT Radiography Number of Passes1 4 Test Pressurebar Corrosion Allowancemm0.0. Full Vacuum Design TemperatureC337.78298.89 Design Pressurebar44.133.45 Design DataUnitsShellChannel Customer Specifications Design Codes ASME Section VIII Div. 1 TEMA R Date: Rev No.: Job No.: Item No.: Your Reference: Service of Unit: Our Reference: Location: Company: RevisionDate 2017/8/9 Dwg.Chk.App. Aspen Shell & Tube Exchanger Setting Plan AES 700 - 3000 Draw ing Number 608608 T2 T1 619619 S1 S2 657 Views on arrow A E501 设计规定说明书 Tube Layout 209.88 mm234.88 mm Company: Location: Service of Unit: Item No.: Tube Layout Aspen Shell & Tube Drawing Number Design Codes ASME Code Sec VIII Div 1 TEMA R - refinery service Customer Specifications RevisionDateDwg.App. 2017/8/9 Shell inside diameter mm700. Front head inside diameter mm700. Outer tube limit mm658.725 Tube number (calcs.)448 Tube number (layout)405 Tube length mm3000. Tube O.D. mm19. Tube pitch mm25. Tube pattern90 Tube passes4 Tie rod number0 Tie rod diameter Sealing strips (pairs)0 Baffle typeUnbaffled Cent