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ECH-A
Energy-Saving and Carbon-
Reducing Emulsified Heavy
Crude Oil Equipment

VAST CALIBRE TECHNOLOGY INC.
E- mail:VIGIRA@HOTMAIL.COM
TEL:886955111899(Rep) SKYPE: VIGIRA
Table of Contents
   Use of Heavy Crude Oil and Problems         2
   Related technologies                        3
   Comparison of related technologies          4
   ECH-A Emulsification Device                 5
   ECH-A Performance Test and Comparison 9
   Estimation and Comparison of ECH-A and
    Related Techniques in Their Oil-efficient
    Capacity                                  25
   Water Addition Suggestion for Energy-saving
    Heavy Crude Oil.                          29
                                                    1
Use of Heavy Crude Oil and Problems
   Characteristics and Use of Heavy Crude Oil
     Heavy crude oil is the residues at the bottom of the tower
      left over from processing and cracking of crude oil. Its
      heating value (8,500 ~ 11,000 Kcal/kg) is high, so are its
      bitumen and sulfur content.
     Because heavy crude oil has a high heating value and is
      relatively cheap, it is widely used.
   Problems associated with use of heavy crude oil
     Incomplete burning is likely, which will lead to greater air
      pollution and higher emission indexes (suspension
      particulates SS, SOx, NOx, NO, CO, and tail gas emission
      temperature)
     Because heavy crude oil has greater viscosity and
      repeated heating is thus necessary, bitumen will sediment
      and oil silt will clog the nozzle and pipeline. As such, the
      frequency of cleaning the burner nozzles and the oil tank is
      relatively high, leading to economic losses.
                                                                   2
Related technologies
   Additives in the heavy crude oil:
    To enhance the burning performance of heavy crude oil, additives can be
    pour point depressants, demulsifiers, and bitumen dissipating agents.
   Bottleneck problems
      Compared with the saved fuels, additives are expensive with limited
       benefits.
      Without auxiliary equipment, additives cannot be used separately.
   Average oil-efficient rate after additives costs are deducted:
    8%
   With ECH-A, bottleneck problems are solved.
      There is no need for any additives and it saves on fuels, with numerous
       benefits
      There is no need to add auxiliary equipment. Installation is easy.
      Ratio of water addition can be as high as 40%, depending on the needs.
       With addition of 18.5% of water, the oil-efficient rate is 16.19%.
      Emulsifying water can be replaced by organic industrial waste water. It
       is more eco-friendly.


                                                                              3
Comparison of related technologies
       Related Techniques Use of additives   ECH-A


Comparison Items
1. Cost-saving             Low (below 8%)    High (With addition of 18.5%
(Relatively reduced fuel                     of water, the oil-efficient rate
expenses)                                    is 16.19%)

2. Air pollution           High              High
improvement

3.Stability                High              High


4. Burner and peripheral   High              Low
equipments
5. Overall economic        Low               High
benefit
                                                                           4
ECH-A Emulsification Device
   ECH-A Design Concepts
      Online reconstitution of energy-saving and eco-
       friendly emulsified heavy crude oil.
      Complete emulsification of heavy crude oil + water to
       generate highly-efficient secondary nebulization and
       contribute to complete burning for enhanced oil-
       efficent rate.
      Complete homogenizing emulsification. Storage and
       transportation is possible.
      Complete homogenizing emulsification with stable
       burning conditions.
      Optimized reconstitution ratio can be applied with the
       burning equipment on-site to reflect actual demand.
                                                                5
Appearance of ECH-A




    LxWxH = 2m x 1.5m x 1.8m
                               6
Energy-Saving and Eco-Friendly
    Heavy Crude Oil Process of ECH-A

 Raw material
 heavy crude oil
 (60 – 100%)                                     ECH-A energy-
                                                 saving and eco-   Burning device
                                                 friendly heavy
Water or organic                                 crude oil
industrial waste
water
(0-40%)

                   ECH-A Emulsification Device



                                                                             7
Secondary nebulization of oil mist
in the burning chamber
(Micro-explosion) = The key for
ECH-A to enhance oil-efficient and
reduce emissions of pollutants.


                                     8
ECH-A Performance Test and
Comparison
   Testing Institution
     Research  Developments on Combustion, Science
      and Technology, Department of Mechanical
      Engineering, National Cheng Kung University
   Secondary nebulization water drop distribution
    and analysis
   Comparison of ECH-A and heavy crude oil
     Burning  test
     Air pollution test


                                                      9
Secondary nebulization testing
equipment




                                 10
From ECH-A oil mist to secondary nebulization
(micro-explosion)
      1.   ECH oil mist is heated


      2. When the temperature exceeds 100℃, water
         in the oil mist starts to gasify and the volume
         starts to inflate.


      3. When the water gasifying pressure is greater
         than the tension on the surface of the oil mist,
         the oil mist explodes.



      4. The oil mist explodes to several particles with
          smaller diameters. Their oxygen-absorbing
          capability is enhanced, contributing to the
          burning.
                                                            11
ECH-A Emulsified Heavy Crude Oil –
Water Drop Distribution Analysis
   100 amplification factor     200 amplification factor    400 amplification factor     100 amplification factor     200 amplification factor        400 amplification factor




                                                                                       Figure 4 Distribution Map of Water Drop Diameters in Oil No. F03-25-10B (Test No.
Figure 3 Distribution Map of Water Drop Diameters in Oil No. F03-25-10B (Test No.      M06-21-10B)
M05-15-10B)

                                                                                       Test No.                                            M05-15-10B M06-21-10B
                                                                                       Measured water drop quantity                           200        200
Manufactured Date 03/25/2010 Location: Sanxia, Taipei
Test 1, 05/15/2010 Location: Guiren Campus, National                                   Average diameter (μm)                                      4.96                   5.3
Cheng Kung University                                                                  Standard deviation (μm)                                    3.09                   2.6
Test 2, 06/21/2010 Location: Guiren Campus, National                                   Maximum diameter (μm)                                     19.25                  18.3
Cheng Kung University                                                                  Minimum diameter (μm)                                      1.16                   2.2
                                                                                       Distribution Map of Water Drop                            Fig. 3                 Fig. 4
                                                                                             Diameters
                                                                                                                                                                                 12
Heavy Crude Oil VS. ECH-A Emulsified
 Heavy Crude Oil
 Burning Temperature Test – Testing
 Platform




Figure 2 Photographs of Multiple-Fuel Burning Test Equipment


                                                               Figure 3 Configuration Layout of Temperature Measurements for Horizontal Burners.




                                                                                                                                       13
Heavy Oil VS. ECH-A Emulsified Heavy Crude Oil
  Comparison Table and Statistics of Burning
                Temperatures
Fuel oil         Content %   Water            Minimum       Maximum
                             addition ratio   flame         flame
                             %                temperature   temperature
                                              ℃(R7)         ℃(R7)

Heavy crude      100%        0%               1104          1136
oil



ECH-A            81.5 %      18.5 %           1057          1095
Emulsified oil




                                                                          14
Heavy Crude Oil VS. ECH-A Emulsified Heavy Crude Oil
Comparison Table of Burning Temperatures – Actual
Measurement Record Sheet
      Heavy crude oil              Burning Performance (Oil No. F06-07-10A; Test No.: B06-16-10A)
         Time*(minute )




               Original Data
               6%O2 Modification

               Original Data
               6%O2 Modification

          ECH-A                Burning Performance (Oil No. F06-07-10B; Test No.: B06-16-10B)
         Time*(minute )




               Original Data
               6%O2 Modification
               Original Data
               6%O2 Modification

      *Timing starts after the oil has gone through the pre-burn test for 1 hour.
                                                                                                    15
Heavy Crude Oil VS ECH-A Emulsified
            Heavy Crude Oil
 Comparison Table of Secondary Air Supply

Fuel oil         Content %   Water            Consumption   Secondary air
                             addition ratio   L/Hr          supply
                             %                              M3/hr

Heavy crude      100%        0%               20            210
oil



ECH-A            81.5 %      18.5 %           20            195
Emulsified oil




                                                                       16
Heavy Crude Oil VS ECH-A Emulsified
Heavy Crude Oil
Comparison of Secondary Air Supply – Actual
Measurement Record Sheet
              Heavy crude oil   ECH-A




                                        17
Heavy Crude Oil VS ECH-A Emulsified
           Heavy Crude Oil
 Comparison Table of Burning Efficiency
Fuel oil         Content %   Water            Minimum        Maximum
                             addition ratio   efficiency %   efficiency %
                             %


Heavy crude      100%        0%               84             85
oil



ECH-A            81.5 %      18.5 %           85             86
Emulsified oil




                                                                            18
Heavy Crude Oil VS ECH-A Emulsified Heavy
Crude Oil
Comparison Table of Efficiency and Stability –
Actual Measurement Record Sheet
            Heavy crude oil   ECH-A




                                           19
Heavy Crude Oil VS ECH-A Emulsified
         Heavy Crude Oil
 Comparison Table of Heating Values
 Fuel oil         Heavy crude     Water            Net heating
                  oil content %   addition ratio   value
                                  %                cal/g


 Heavy crude      100%            0%               9711
 oil



 ECH-A            81.5 %          18.5 %           9440
 Emulsified oil




                                                                 20
Heavy Crude Oil VS ECH-A Emulsified Heavy
                   Crude Oil
Comparison Table and Statistics of Heating Values
          Oil No.                Heavy crude oil               ECH-A   Test method
Density@60℉, g/mL
Flash point, ℃
Sulfur content, %
Flow, ℃

Dynamic
viscosity cSt

Total aromatic hydrocarbons, wt%
Water content, vol%
Carbon content, wt%

Hydrogen content, wt%
Nitrogen content, μg%
Net heating value, cal/g
Total heating value, cal/g
Note: “-" in the table means that the analysis was not performed.                    21
#6 Heavy Crude Oil VS ECH-A Emulsified
           Heavy Crude Oil
 Comparison of Air Pollution Emissions




         Air Pollution Emissions Testing Equipment
                                                     22
Heavy Crude Oil VS ECH-A Emulsified
            Heavy Crude Oil
Comparison Table of Air Pollution Emissions
Fuel oil     O2 % max   CO2 % max CO (ppm)   NOx (ppm)   Sox (ppm)
                                  min        max         max



Heavy        6.2        10.9      0          369         199.5
crude oil



ECH-A        6.15       10.5      0          286.6       180.6
Emulsified
oil
Water
Content
18.5%
                                                                 23
Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil
   Comparison Table and Statistics of Air Pollution
                    Emissions
              Burning Performance (Oil No. F06-07-10A; Test No.: B06-16-10A) Heavy crude oil
         Time*(minute )




               Original Data
              6%O2
              Modification
              Original Data
              6%O2
              Modification

               Burning Performance (Oil No. F06-07-10B; Test No.: B06-16-10B)       ECH-A
         Time*(minute )




               Original Data
              6%O2
              Modification
              Original Data
              6%O2
              Modification
                                                                                               24
      *Timing starts after the oil has gone through the pre-burn test for 1 hour.
Estimation and Comparison of
ECH-A and Related Techniques in
   Their Oil-efficient Capacity




                              25
ECH-A Average Oil-efficient Rate Estimate Table                              * Based on Test

Report on 07/09/2010

Example: Water Content of 20%
I. Oil-efficient rate
1. #6 Heavy crude oil total heating value: 10,260 cal/g = 10,260,000 kcal/MT
2. Total heating value of ECH-A (including 18.5% of water) emulsified heavy crude oil
3. For ECH-A emulsified heavy crude oil to reach the total heating value 10,260,000
    kcal/MT, the fuels that need to be used are 10,260,000 kcal/MT /9,986,000 kcal/MT =
    1.027MT = 1,027kg. In other words, to maintain the same heating value when ECH-A
    is used, additional 1,027 – 1,000 kg = 27kg of ECH-A fuel oil that contains 18.5% of
    water needs to be used.
4. Therefore, the oil-saving rate when ECH-A emulsified heavy crude oil is used is 1,000
    kg – (815.0 kg + 27 kg)=158.0kg. In other words, the oil-efficient rate is
    158.0kg/1,000kg=15.8%.
II. Saved expenditure
Suppose the cost for each ton of #6 heavy crude oil is NT 19,528 / MT
5. The cost for each ton of ECH-A emulsified heavy oil is NT 19,528 /MT*0.815(fuel oil) +
    (NT65*0.1850)(Water)+ (NT 2.74kw-h*2.2kw- h)(electricity cost)= NT15,915 + 12.0 +
    7.0 = NT 15,934
6. When ECH-A with an equivalent heating value is used, it is NT 15,934/MT*1.027 MT =
    NT 16365.
7. Saved fuel cost with ECH-A = NT 19,528 –NT 16365 = NT3,163
8. Saved expenditure with ECH-A = NT3,163 / NT 19,528 = 16.19%
   Saved expenditure with water addition ratio of 18.5%= 16.19%.

                                                                                        26
Estimate Table of Average Oil-efficient Rates
for Related Technologies (GFXP)
Example: Water content of 12.85% and emulsifying agent of 0.65%
I. Oil-efficient rate
    #6 Heavy crude oil total heating value: 10,260 cal/g = 10,260,000 kcal/MT
2. Total heating value of GFXP (including 18.5% of water) emulsified heavy crude oil =
    10,162 cal/g =10,162,000kcal/MT
3. For GFXP emulsified heavy crude oil to reach the total heating value 10,627,000
    kcal/MT, the fuels that need to be used are 10, 627,000 kcal/MT / 10,162,000
    kcal/MT = 1.046MT = 1,046kg. In other words, to maintain the same heating value,
    additional 1,046 – 1,000 kg = 46kg of GFXP fuel oil that contains 12.85% of water
    and 0.65% of emulsifying agent needs to be used.
4. Therefore, the oil-saving rate when GFXP emulsified heavy crude oil is used is 1,000
    kg – (865.5 kg + 46 kg)=88.5kg. In other words, the oil-efficient rate is
    88.5kg/1,000kg=8.85%.
II. Saved expenditure
    Suppose the cost for each ton of #6 heavy crude oil is NT 19,528 / MT
5. Cost for each ton of GFXP emulsified heavy crude oil= = NT 19,528 /MT*0.8655 (fuel
    oil) + (NT65*0.1280)(Water)+ (NT29,100*0.0065)(emulsifying agent)(NT 2.74kw-
    h*7.6kw- h)(electricity cost)= NT16,901 + 8.32 + 189.15 + 20.824 = NT 17,119
6. When GFXP with an equivalent heating value is used, it is NT 17,119/MT*1.046 MT =
    NT 17,907.
7. Saved fuel cost with GFXP = NT 19,528 –NT 17,907 = NT1,621
8. Saved expenditure with GFXP = NT1,621 / NT 19,528 = 8.3%
    Saved expenditure with water addition ratio of 18.5%= 8.3%.

                                                                                     27
Comparison Table of ECH-A and Related
    Technologies (GFXP) in Energy-Saving

Energy-saving technology    Oil-efficient rate   Saved expenditure
ECH-A                       15.8%                16.19%
(Water content of 18.5%)


GFXP                         8.85%               8.3%
(Water content of 12.85% and
emulsifying additives of
0.65%)




                                                                     28
Recommended water addition rates for
ECH-A emulsified heavy crude oil used
in different industries
               Industry                    Application    Water addition
                                                              rates
Glass fiber manufacturers, glass
industries, ceramics industries,         Furnaces,       ~20%
cement industries, metallurgical         melting pots,
industries, mining industries,           baking ovens
asphalt factories, power plants
Pharmaceutical industries,
petrochemical industries, dyeing         Steam boilers   ~30%
and finishing industries, printing
and dyeing industries, textiles, dairy
industries, chemical industries, dye
industries
Food industry, hospitals, hotels,    Steam boilers,
swimming pools, public architecture, Hot water boilers   ~40%
general industries

                                                                           29

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Ech a vastcalibre

  • 1. ECH-A Energy-Saving and Carbon- Reducing Emulsified Heavy Crude Oil Equipment VAST CALIBRE TECHNOLOGY INC. E- mail:VIGIRA@HOTMAIL.COM TEL:886955111899(Rep) SKYPE: VIGIRA
  • 2. Table of Contents  Use of Heavy Crude Oil and Problems 2  Related technologies 3  Comparison of related technologies 4  ECH-A Emulsification Device 5  ECH-A Performance Test and Comparison 9  Estimation and Comparison of ECH-A and Related Techniques in Their Oil-efficient Capacity 25  Water Addition Suggestion for Energy-saving Heavy Crude Oil. 29 1
  • 3. Use of Heavy Crude Oil and Problems  Characteristics and Use of Heavy Crude Oil  Heavy crude oil is the residues at the bottom of the tower left over from processing and cracking of crude oil. Its heating value (8,500 ~ 11,000 Kcal/kg) is high, so are its bitumen and sulfur content.  Because heavy crude oil has a high heating value and is relatively cheap, it is widely used.  Problems associated with use of heavy crude oil  Incomplete burning is likely, which will lead to greater air pollution and higher emission indexes (suspension particulates SS, SOx, NOx, NO, CO, and tail gas emission temperature)  Because heavy crude oil has greater viscosity and repeated heating is thus necessary, bitumen will sediment and oil silt will clog the nozzle and pipeline. As such, the frequency of cleaning the burner nozzles and the oil tank is relatively high, leading to economic losses. 2
  • 4. Related technologies  Additives in the heavy crude oil: To enhance the burning performance of heavy crude oil, additives can be pour point depressants, demulsifiers, and bitumen dissipating agents.  Bottleneck problems  Compared with the saved fuels, additives are expensive with limited benefits.  Without auxiliary equipment, additives cannot be used separately.  Average oil-efficient rate after additives costs are deducted: 8%  With ECH-A, bottleneck problems are solved.  There is no need for any additives and it saves on fuels, with numerous benefits  There is no need to add auxiliary equipment. Installation is easy.  Ratio of water addition can be as high as 40%, depending on the needs. With addition of 18.5% of water, the oil-efficient rate is 16.19%.  Emulsifying water can be replaced by organic industrial waste water. It is more eco-friendly. 3
  • 5. Comparison of related technologies Related Techniques Use of additives ECH-A Comparison Items 1. Cost-saving Low (below 8%) High (With addition of 18.5% (Relatively reduced fuel of water, the oil-efficient rate expenses) is 16.19%) 2. Air pollution High High improvement 3.Stability High High 4. Burner and peripheral High Low equipments 5. Overall economic Low High benefit 4
  • 6. ECH-A Emulsification Device  ECH-A Design Concepts  Online reconstitution of energy-saving and eco- friendly emulsified heavy crude oil.  Complete emulsification of heavy crude oil + water to generate highly-efficient secondary nebulization and contribute to complete burning for enhanced oil- efficent rate.  Complete homogenizing emulsification. Storage and transportation is possible.  Complete homogenizing emulsification with stable burning conditions.  Optimized reconstitution ratio can be applied with the burning equipment on-site to reflect actual demand. 5
  • 7. Appearance of ECH-A LxWxH = 2m x 1.5m x 1.8m 6
  • 8. Energy-Saving and Eco-Friendly Heavy Crude Oil Process of ECH-A Raw material heavy crude oil (60 – 100%) ECH-A energy- saving and eco- Burning device friendly heavy Water or organic crude oil industrial waste water (0-40%) ECH-A Emulsification Device 7
  • 9. Secondary nebulization of oil mist in the burning chamber (Micro-explosion) = The key for ECH-A to enhance oil-efficient and reduce emissions of pollutants. 8
  • 10. ECH-A Performance Test and Comparison  Testing Institution  Research Developments on Combustion, Science and Technology, Department of Mechanical Engineering, National Cheng Kung University  Secondary nebulization water drop distribution and analysis  Comparison of ECH-A and heavy crude oil  Burning test  Air pollution test 9
  • 12. From ECH-A oil mist to secondary nebulization (micro-explosion) 1. ECH oil mist is heated 2. When the temperature exceeds 100℃, water in the oil mist starts to gasify and the volume starts to inflate. 3. When the water gasifying pressure is greater than the tension on the surface of the oil mist, the oil mist explodes. 4. The oil mist explodes to several particles with smaller diameters. Their oxygen-absorbing capability is enhanced, contributing to the burning. 11
  • 13. ECH-A Emulsified Heavy Crude Oil – Water Drop Distribution Analysis 100 amplification factor 200 amplification factor 400 amplification factor 100 amplification factor 200 amplification factor 400 amplification factor Figure 4 Distribution Map of Water Drop Diameters in Oil No. F03-25-10B (Test No. Figure 3 Distribution Map of Water Drop Diameters in Oil No. F03-25-10B (Test No. M06-21-10B) M05-15-10B) Test No. M05-15-10B M06-21-10B Measured water drop quantity 200 200 Manufactured Date 03/25/2010 Location: Sanxia, Taipei Test 1, 05/15/2010 Location: Guiren Campus, National Average diameter (μm) 4.96 5.3 Cheng Kung University Standard deviation (μm) 3.09 2.6 Test 2, 06/21/2010 Location: Guiren Campus, National Maximum diameter (μm) 19.25 18.3 Cheng Kung University Minimum diameter (μm) 1.16 2.2 Distribution Map of Water Drop Fig. 3 Fig. 4 Diameters 12
  • 14. Heavy Crude Oil VS. ECH-A Emulsified Heavy Crude Oil Burning Temperature Test – Testing Platform Figure 2 Photographs of Multiple-Fuel Burning Test Equipment Figure 3 Configuration Layout of Temperature Measurements for Horizontal Burners. 13
  • 15. Heavy Oil VS. ECH-A Emulsified Heavy Crude Oil Comparison Table and Statistics of Burning Temperatures Fuel oil Content % Water Minimum Maximum addition ratio flame flame % temperature temperature ℃(R7) ℃(R7) Heavy crude 100% 0% 1104 1136 oil ECH-A 81.5 % 18.5 % 1057 1095 Emulsified oil 14
  • 16. Heavy Crude Oil VS. ECH-A Emulsified Heavy Crude Oil Comparison Table of Burning Temperatures – Actual Measurement Record Sheet Heavy crude oil Burning Performance (Oil No. F06-07-10A; Test No.: B06-16-10A) Time*(minute ) Original Data 6%O2 Modification Original Data 6%O2 Modification ECH-A Burning Performance (Oil No. F06-07-10B; Test No.: B06-16-10B) Time*(minute ) Original Data 6%O2 Modification Original Data 6%O2 Modification *Timing starts after the oil has gone through the pre-burn test for 1 hour. 15
  • 17. Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison Table of Secondary Air Supply Fuel oil Content % Water Consumption Secondary air addition ratio L/Hr supply % M3/hr Heavy crude 100% 0% 20 210 oil ECH-A 81.5 % 18.5 % 20 195 Emulsified oil 16
  • 18. Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison of Secondary Air Supply – Actual Measurement Record Sheet Heavy crude oil ECH-A 17
  • 19. Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison Table of Burning Efficiency Fuel oil Content % Water Minimum Maximum addition ratio efficiency % efficiency % % Heavy crude 100% 0% 84 85 oil ECH-A 81.5 % 18.5 % 85 86 Emulsified oil 18
  • 20. Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison Table of Efficiency and Stability – Actual Measurement Record Sheet Heavy crude oil ECH-A 19
  • 21. Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison Table of Heating Values Fuel oil Heavy crude Water Net heating oil content % addition ratio value % cal/g Heavy crude 100% 0% 9711 oil ECH-A 81.5 % 18.5 % 9440 Emulsified oil 20
  • 22. Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison Table and Statistics of Heating Values Oil No. Heavy crude oil ECH-A Test method Density@60℉, g/mL Flash point, ℃ Sulfur content, % Flow, ℃ Dynamic viscosity cSt Total aromatic hydrocarbons, wt% Water content, vol% Carbon content, wt% Hydrogen content, wt% Nitrogen content, μg% Net heating value, cal/g Total heating value, cal/g Note: “-" in the table means that the analysis was not performed. 21
  • 23. #6 Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison of Air Pollution Emissions Air Pollution Emissions Testing Equipment 22
  • 24. Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison Table of Air Pollution Emissions Fuel oil O2 % max CO2 % max CO (ppm) NOx (ppm) Sox (ppm) min max max Heavy 6.2 10.9 0 369 199.5 crude oil ECH-A 6.15 10.5 0 286.6 180.6 Emulsified oil Water Content 18.5% 23
  • 25. Heavy Crude Oil VS ECH-A Emulsified Heavy Crude Oil Comparison Table and Statistics of Air Pollution Emissions Burning Performance (Oil No. F06-07-10A; Test No.: B06-16-10A) Heavy crude oil Time*(minute ) Original Data 6%O2 Modification Original Data 6%O2 Modification Burning Performance (Oil No. F06-07-10B; Test No.: B06-16-10B) ECH-A Time*(minute ) Original Data 6%O2 Modification Original Data 6%O2 Modification 24 *Timing starts after the oil has gone through the pre-burn test for 1 hour.
  • 26. Estimation and Comparison of ECH-A and Related Techniques in Their Oil-efficient Capacity 25
  • 27. ECH-A Average Oil-efficient Rate Estimate Table * Based on Test Report on 07/09/2010 Example: Water Content of 20% I. Oil-efficient rate 1. #6 Heavy crude oil total heating value: 10,260 cal/g = 10,260,000 kcal/MT 2. Total heating value of ECH-A (including 18.5% of water) emulsified heavy crude oil 3. For ECH-A emulsified heavy crude oil to reach the total heating value 10,260,000 kcal/MT, the fuels that need to be used are 10,260,000 kcal/MT /9,986,000 kcal/MT = 1.027MT = 1,027kg. In other words, to maintain the same heating value when ECH-A is used, additional 1,027 – 1,000 kg = 27kg of ECH-A fuel oil that contains 18.5% of water needs to be used. 4. Therefore, the oil-saving rate when ECH-A emulsified heavy crude oil is used is 1,000 kg – (815.0 kg + 27 kg)=158.0kg. In other words, the oil-efficient rate is 158.0kg/1,000kg=15.8%. II. Saved expenditure Suppose the cost for each ton of #6 heavy crude oil is NT 19,528 / MT 5. The cost for each ton of ECH-A emulsified heavy oil is NT 19,528 /MT*0.815(fuel oil) + (NT65*0.1850)(Water)+ (NT 2.74kw-h*2.2kw- h)(electricity cost)= NT15,915 + 12.0 + 7.0 = NT 15,934 6. When ECH-A with an equivalent heating value is used, it is NT 15,934/MT*1.027 MT = NT 16365. 7. Saved fuel cost with ECH-A = NT 19,528 –NT 16365 = NT3,163 8. Saved expenditure with ECH-A = NT3,163 / NT 19,528 = 16.19% Saved expenditure with water addition ratio of 18.5%= 16.19%. 26
  • 28. Estimate Table of Average Oil-efficient Rates for Related Technologies (GFXP) Example: Water content of 12.85% and emulsifying agent of 0.65% I. Oil-efficient rate #6 Heavy crude oil total heating value: 10,260 cal/g = 10,260,000 kcal/MT 2. Total heating value of GFXP (including 18.5% of water) emulsified heavy crude oil = 10,162 cal/g =10,162,000kcal/MT 3. For GFXP emulsified heavy crude oil to reach the total heating value 10,627,000 kcal/MT, the fuels that need to be used are 10, 627,000 kcal/MT / 10,162,000 kcal/MT = 1.046MT = 1,046kg. In other words, to maintain the same heating value, additional 1,046 – 1,000 kg = 46kg of GFXP fuel oil that contains 12.85% of water and 0.65% of emulsifying agent needs to be used. 4. Therefore, the oil-saving rate when GFXP emulsified heavy crude oil is used is 1,000 kg – (865.5 kg + 46 kg)=88.5kg. In other words, the oil-efficient rate is 88.5kg/1,000kg=8.85%. II. Saved expenditure Suppose the cost for each ton of #6 heavy crude oil is NT 19,528 / MT 5. Cost for each ton of GFXP emulsified heavy crude oil= = NT 19,528 /MT*0.8655 (fuel oil) + (NT65*0.1280)(Water)+ (NT29,100*0.0065)(emulsifying agent)(NT 2.74kw- h*7.6kw- h)(electricity cost)= NT16,901 + 8.32 + 189.15 + 20.824 = NT 17,119 6. When GFXP with an equivalent heating value is used, it is NT 17,119/MT*1.046 MT = NT 17,907. 7. Saved fuel cost with GFXP = NT 19,528 –NT 17,907 = NT1,621 8. Saved expenditure with GFXP = NT1,621 / NT 19,528 = 8.3% Saved expenditure with water addition ratio of 18.5%= 8.3%. 27
  • 29. Comparison Table of ECH-A and Related Technologies (GFXP) in Energy-Saving Energy-saving technology Oil-efficient rate Saved expenditure ECH-A 15.8% 16.19% (Water content of 18.5%) GFXP 8.85% 8.3% (Water content of 12.85% and emulsifying additives of 0.65%) 28
  • 30. Recommended water addition rates for ECH-A emulsified heavy crude oil used in different industries Industry Application Water addition rates Glass fiber manufacturers, glass industries, ceramics industries, Furnaces, ~20% cement industries, metallurgical melting pots, industries, mining industries, baking ovens asphalt factories, power plants Pharmaceutical industries, petrochemical industries, dyeing Steam boilers ~30% and finishing industries, printing and dyeing industries, textiles, dairy industries, chemical industries, dye industries Food industry, hospitals, hotels, Steam boilers, swimming pools, public architecture, Hot water boilers ~40% general industries 29