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1 A Akzo 12y26.doc
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12 Example of sun shade mat: ECO-MAT Power consumption of air-conditioner is saved by 10%. Picture of air-conditioner with ECO-MAT Comparison of consumed power of air-conditioner No use of ECO-MAT Use of ECO-MAT Current Source: Hour
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14 Fig.2-5 Relationship between cooling water temperature and steam consumption of booster Source: The new oil and fat technology, Mr. E. Bornardini, Publishing house Technologie, Rome
15 Fig. 2-1 Flow-sheet and flow-rate of Cooling Tower (CR-II) (1) 8/19 Result of Measuring 1) Motor current of fan Rated current (A) Actual current (A) Load factor (%) ) Motor current of feed pump 504G G G G80.4 Rated current (A) Actual current (A) 106 Standby (?) Load factor (%) ) Flow rate of cooling water (Total,19 August) Rated=930m3/h, Actual=664 (Inlet line), 678 (Outlet line) Av.671? Load factor=actual / Rated = 72%?, (can not measure on 22 August) 4) Temperature of water Wet bulb temp. Outlet line Inlet line Water in tower ~ ~ ~32.5 Deference degc degc
16 Fig. 2-2 Flow-sheet and flow-rate of Cooling tower CR-III Rated current (A) Actual current (A) Load factor (%) ) Motor current of water feed pump 503G30 503G31 503G32 503G33 Rated current (A) Actual current (A) Load factor (%) Valve opening 50% 50% 100% 100% 3) Flow rate of cooling water (Total,19 August) Rated flow-rate=934m3/h, Actual flow-rate=cannot measure (Pipe diameter is too large.) 4) Temperature of WaterdegC Measuring Wet Bulb Temp. Outlet Line Inlet Line Water temp. in Tower date 19 August ~ ~ ~34.9 Difference 7.5~ ~3.6 ( 5.5~7.9 against WB ) 22 August ~ ~ ~33.8 Difference 3.3~ ~4.3 (2.8~6.8 against WB )
17 Fig. 2-3 Flow-sheet and operation data of Section 400 Vacuum System 11 bar 920 kg/h 26 kg/h bar 48 kg/h No.1 No.2 400D5 Distillation CW 32 CW 33.4 Column CW CW D Post Distillation Steam Consumption (Booster Ejector) Designed Value: 994kg/h Actual Value: 1,150 kg/h (116% against Designed Value) Water Temperature of Surface Condenser (No.1) Designed: Inlet 32 deg C Outlet 36 deg C Actual : Inlet deg C Outlet 34.4~35 deg C Water Flow Rate in Surface Condenser (No.1) Designed: 196 m3/h Actual : can not measure
18 Fig. 2-4 Flow-sheet and operation data of Section 403 Vacuum System E5 1bar 56 Dryer Distillation Column Post Distillation 403E10 Steam Consumption ( Booster Ejector) Designed Value : 1,180 kg/h Actual Value : bar 790kg/h E12A CW 36.7 CW CW bar 403E12B CW 37.2 Temperature of Surface Condenser (E12A) Designed Value : inlet 33 deg C outlet 38 deg C Actual Value : inlet deg C outlet deg C Water Flow Rate of Surface Condenser (E12A,12B) Designed Value : 155 m3/h E12A 22 m3/h E12B Actual Value : can not measure
19 Cooling tower No. 1 Factory name: Company A Date of measurement: 2005/8/22 Each * mark indicates a measured value
20 Cooling tower No. 4 Factory name: Company A Date of measurement: 2005/8/19 Each * mark indicates a measured value
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22 Cooling tower No. CR-2 Factory name: Company A Date of measurement: 2005/8/19 Each * mark indicates a measured value
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24 Cooling tower No. CR-3 Factory name: Company A Date of measurement: 2005/8/19 Each * mark indicates a measured value
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26 Air compressor and compressed air line Factory name: Company A Date of measurement: 2005/8/22 Each * mark indicates a measured value No. Unit Compressor No.1 No.2 No.3 1 Measuring time 9:25 2 Specifications 3 Motor power 4 Rated capacity m3/min * 5 suction air temperature degc * 6 Discharge air pressure Mpa Discharge air temperature degc * 8 Motor current on load A * 9 Motor current or power at no-load A, kw * 10 Full load time min * 11 No-load time min 12 Dryer input air pressure Mpa Air receiver pressure Mpa Header pressure Mpa User * 16 Air pressure at 502/503 C/V 3 bar * 17 Air pressure at section 802 C/V & blow * 18 Air pressure at 504 C/V * 19 Air pressure at CR II C/V * 20 Air pressure at CR III C/V 21 Air pressure at CR 2 Blow 4-5 bar 22 Air pressure at CR 1 Packer 3 bar 23 Air pressure at CR IV C/V & blow Note: C/V = Control valve
27 Steam generation Fuel Temperature, Oxygen % Sampling nozzle Exhaust gas Surface temperature Feed water volume, temperaqture
28 No Item Unit DATA Remarks Measuring time min 32 1 Rated capacity t/h 2.0 Specification 2 Boiler load factor % 3 * Feed water temperature degc Specific gravity of water kg/l Amount of feed water L/h Amount of feed water kg/h Enthalpy of feed water kj/kg * Drum steam pressure M Pa Enthalpy of steam kj/kg 2,785 Steam table 12 * Fuel gas temperature degc Fuel gas pressure in gage kpa Amount of fuel gas m3s/h Amount of fuel gas m3n/h Lower calorific value of fuel gas kj/m3s 38, Lower calorific value of fuel gas kj/m3n 40, * Exhaust gas temperature degc At the outlet of boiler 20 * Oxygen concentration of exhaust gas % 1.20 Min. 0.3% - Max. 2.5% 21 CO concentration of exhaust gas ppm Max. 447ppm 22 Excess air ratio * Outside air temperature degc Exhaust gas loss kj/m3n 4,005 [28]*[29]*([19]-[23]) 25 Theoretical air volume m3n/m3n *[18]/ Actual air volume m3n/m3n Specific heat of combustion air kj/m3nc Theoretical dry exhaust gas volume m3n/m3n *[18]/ Actual dry exhaust gas volume m3n/m3n Specific heat of exhaust gas kj/m3nc Blow loss 0 33 * Surface temperature deg C * Surface area (2.22m dia*3.6ml) m Radiation loss from surface kj/m3n Convection loss from surface kj/m3n Dissipation loss from surface kj/m3n Boiler efficiency (Indirect method) % 89.9
29 Calculation sheet of economizer of High pressure boiler Feed water temperature degc Feed water temperature (Outlet of economizer) degc Specific gravity of water kg/l 1.0 Amount of feed water kg/h Amount of feed water kg/m3n 15.7 Enthalpy of feed water kj/kg
30 Exhaust gas Steam Temperature, generation Oxygen % Sampling nozzle Surface temperature Fuel consumption Feed water volume, temperature
31 Boiler efficiencies according to the heat input/output method Factory name: Company A Boiler No. Middle pressure No.5 Date of measurement: 2005/8/19 Each * mark indicates a measured value No. Item Unit DATA Remarks 1 Measuring time min 32 2 Rated capacity t/h 15.0 Specification 3 Boiler load factor % * Feed water temperature deg C * Drum steam pressure M Pa Enthalpy of steam kj/kg 2792 Steam table 7 * Fuel gas temperature deg C 34 8 * Fuel gas pressure in gage kpa Amount of fuel gas (Reading of meter) m3/h Amount of fuel gas m3s/h Amount of fuel gas m3n/h Lower calorific value of fuel gas kj/m3s 38, Lower calorific value of fuel gas kj/m3n 40, * Exhaust gas temperature deg C At the outlet of boiler 15 * Oxygen concentration of exhaust gas % 1.90 Min. 1.6% - Max. 2.5% 16 * CO concentration of exhaust gas ppm 1.3 Max. 5ppm 17 Excess air ratio * Outside air temperature deg C Exhaust gas loss kj/m3n 3,560 [23]*[24]*([14]-[18]) 20 Theoretical air volume m3n/m3n *HL/ Actual air volume m3n/m3n Specific heat of combustion air kj/m3n-c Theoretical dry exhaust gas volume m3n/m3n *HL/ Actual dry exhaust gas volume m3n/m3n Specific heat of exhaust gas kj/m3n-c Blow loss 0 27 * Surface temperature deg C * Surface area (3.3m dia * 5.8mL) m Radiation loss from surface kj/m3n Convection loss from surface kj/m3n Dissipation loss from surface kj/m3n Boiler efficiency (Indirect method) % ([19]+[31])/[20]*100
32 Calculation sheet of air preheater of Boiler No #NAME?
33 Calculation sheet of economizer of Boiler of 31.8 t/h Feed water temperature degc Feed water temperature (Outlet of economizer) degc Specific gravity of water kg/l 1.0 Amount of feed water kg/h Amount of feed water kg/m3n 11.3 Enthalpy of feed water kj/kg Drum steam pressure M Pa
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35 Thermal image of insulation 62.4 C >281.0 C SP01 SP02 SP03 SP04 SP05
36 53.9 C >281.0 C SP01 SP02 SP03 SP04 SP05
37 SP01 SP02 SP03 >281.0 C 53.9 C
38 53.9 C >281.0 C SP01 SP02 SP03 SP04 SP05
39 46.2 C >281.0 C SP01 SP02 SP03 SP04 SP05
40 No. Area Equipment name Steam pressure (Mpa) Steam trap type Inspection results Remarks CR4001/0/TD 0.3 Disk Good 91 o C 2 CR4003/0/TD 0.3 Disk Leak 93 o C 3 CR403/0/TD 0.3 Disk Good 97 o C 4 CR4083/5/IB 1.3 Bucket Leak 141 o C L14 5 CR4047/5/IB 1.3 Bucket Good 135 o C 6 CR4060/5/TD 0.3 Disk Low Temperature 79 o C 8 CR2 CR201/1/IB 0.3 Bucket Good 89 o C 9 CR202/1/IB 1.3 Bucket Leak 115 o C L15 10 CR203/1/IB 1.3 Bucket Low Temperature 54 o C Valve Closed 11 CR204/1/TD 0.3 Disk Good 87 o C 12 CR205/1/TD 0.3 Disk Low Temperature 82 o C 13 CR206/1/TD 0.3 Disk Low Temperature 83 o C 14 CR207/1/TD 0.3 Disk Low Temperature 64 o C 15 CR201/2/TD 0.3 Disk Low Temperature 85 o C 16 CR202/2/TD 0.3 Disk Low Temperature 66 o C 18 CR3 CR3001/1/TD 0.3 Disk Good 86 o C 19 CR3002/1/F 1.3 Float Low Temperature 73 o C 20 CR3003/1/F 0.3 Float Good 112 o C 21 CR3004/1/F 0.3 Float Good 104 o C 22 CR3005/1/F 0.3 Float Blocked 89 o C 23 CR3006/1/F 0.4 Float Good 92 o C 24 CR3007/1/TD 1.3 Disk Good 140 o C 26 CR3001/2/F 1.3 Float Good 148 o C 27 CR3002/2/TD 1.3 Disk Leak 148 o C S01 28 CR3003/2/F 1.3 Float Good 153 o C 29 CR3004/2/TD 0.3 Disk Leak 107 o C S04 31 CR3001/3/TD 1.3 Disk Blowing 144 o C 32 CR3002/3/TD 1.3 Disk Blowing 145 o C 33 CR3003/3/TD 1.3 Disk Leak 141 o C M10 34 CR3004/3/TD 0.3 Disk Blocked 32 o C 35 CR3005/3/TD 1.3 Disk Good 142 o C Inspection results Quantity Good 13 Low 8 temperature Leaking 6 Blowing 2 In the ejector of CR3 Blocked 2 Total 31
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17 Fig.2-1 Relationship between cooling water temperature and steam consumption of booster Source: The new oil and fat technology, Mr. E. Bornardini, Publishing house Technologie, Rome Note:
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