M-DEV0468: Deviation for determining the baseline efficiencies of heat generator and heat engine
|Submitted by||DNV (23 Feb 2012)|
|Project activity||Punta Pereira biomass power plant|
ACM0006 ver. 11: Consolidated methodology for electricity and heat generation from biomass residues
|Title/subject of deviation||Deviation for determining the baseline efficiencies of heat generator and heat engine|
|PDD||PDD (2442 KB)|
The deviation requested is related to the way the efficiencies of heat generators and heat-to-power ratio of the heat engines are determined in the baseline. Punta Pereira is a greenfield pulp mill project and the baseline defined in the PDD is: “conventional self-sufficient pulp mill, without surplus power generation capacity”.
For the Punta Pereira baseline determination the efficiency of two equipment, the pulp mill recovery boiler and the turbo generator, should be determined. The deviation of each parameter is described in the sections below:
Efficiency of the turbo generator:
According to Step 1.5 “Determine the efficiencies of heat generators, and efficiencies and heat-to-power ratio of heat engines” of the methodology ACM0006 (version 11.1) only Option 1: “Default values should be chosen” is applicable to the project. This option automatically refers to Option F: “Use a default value” of the “Tool to determine the baseline of thermal or electric energy generation system” (version 1).
Table 1 of the referred tool is related to heat generating equipment and is consequently not applicable to the turbo generator. In this case the “Tool to determine the baseline of thermal or electric energy generation system” (version 1) refers to the Annex I: “Default efficiency factors for power plant” of the “Tool to calculate de emission factor for an electricity system” (version 2.2.0), however this Annex only presents efficiencies for fossil fuel power plants (coal, oil and natural gas).
Returning to the “Tool to determine the baseline of thermal or electric energy generation system” (verison 1), in situations where a specific technology in not include in the table the maximum default efficiency of 100% may be used, as a simple approach.
The value given for efficiency (100%) is impossible to be achieved according to thermodynamical principles. The most efficient heat engine cycle is the Carnot cycle, which consists in an ideal and reversible cycle with two isothermal processes and two adiabatic processes. According to the second law of thermodynamics, Carnot Cycle is given by:
FORMULA 1: PLEASE REFER TO ANNEX 1
Notice that 100% efficiency is impossible as it would require a TL equal to zero Kelvin (-273°C) and a TH near infinite.
Despite that, turbines efficiencies also vary according to the applied technology, the inlet steam conditions, steam extractions and its output conditions.
Considering the presented above the maximum theoretical turbo generator efficiency for the project activity was calculated based on the following configuration:
- one back-pressure turbine with capacity of 116 MW,
- inlet steam of 717 tonnes/h at 83 Bar and 478°C
- one steam medium-pressure extraction of 273 tonnes/h at 12.5 Bar and 200°C
- one steam low-pressure extraction of 444 tonnes/h at 5.3 Bar and 164°C
- outlet flow to the feed water of 717 tonnes/h at 120°C
The turbine efficiency is given by the theoretical formula 1, presented above. In the project case there are two steam extractions that must be considered in the calculation, resulting in:
FORMULA 2: PLEASE REFER TO ANNEX 1
At the present case and considering the steam conditions as presented above: hHP = hin = 3 342 kJ/kg, hMP = 2 854 kJ/kg, hLP = 2 687 kJ/kg and hfw = 502 kJ/kg. The flows inside the turbine, mHP-MP and mMP-LP will be 717 tonnes/h and 444 (=717-273) tonnes/h, respectively.
Thus applying those values to formula 2, results:
FORMULA 3: PLEASE REFER TO ANNEX 1
Considering 100% of isentropic efficiency in order to reflect a maximum theoretical value, the calculated efficiency power-to-heat ratio of the turbo generator results in the efficiency (0.2082), when divided by 3.6 to convert to MWh/GJ this results in 0.05784 MWh/GJ.
Therefore the suggested project specific efficiency for the turbo generator is the maximum isoentropic efficiency of the turbine. In DNV opinion this value can be considered conservative and realistic.
Also when compared to the baseline efficiency of similar pulp mill CDM projects: Nueva Aldea: 0.04525 MWh/GJ (UNFCCC n°0258); Valdivia: 0.04235 MWh/GJ (UNFCCC n°1787); Fray Bentos: 0.03746 MWh/GJ (UNFCCC n°1493)1, the proposed value for the turbo generator of Punta Pereira project is the highest, assuring conservativeness at the baseline.
Efficiency of the pulp mill recovery boiler:
According to Step 1.5 of the methodology ACM0006 (version 11.1) only Option 1: “Default values should be chosen” is applicable to the project. This option automatically refers to Option F: “Use a default value” of the “Tool to determine the baseline of thermal or electric energy generation system” (version 1). At Table 1: “Default baseline efficiency for different technologies” only fossil fuel boilers (natural gas, oil and coal) are listed, and there is no option that could be chosen in order to represent the technology used at a pulp mill recovery boiler.
In cases where no options of Table 1 are applicable the “Tool to determine the baseline of thermal or electric energy generation system” (version 1) indicates the maximum default efficiency of 100% should be used, as a simple and conservative approach.
However if the efficiency of 100% was used in the recovery boiler, once the amount of biomass residues is fixed, the steam production would increase and consequently more heat would be generated in the baseline. This excess of steam would, not be used in the process and would have to be discarded. On the other hand, if a larger turbine was selected in the baseline, more energy would be generated and theoretically, there would be an electricity surplus; consequently the concept of the baseline would be corrupted and the project would not be in line with the common practice of the industry.
Using an efficiency of 100% in the baseline it would not allow the project baseline to be classified as “conventional self-sufficient pulp mill, without surplus power generation capacity”, which is the industry common practice.
The suggested project specific efficiency for the recovery boiler was determined as the optimal point for the power plant operation (Case 22.214.171.124 of ACM0006). On the next steps the optimal point for operation, where the balance of biomass-based heat equals the remaining demand for process heat, is presented and justified as the most conservative option:
FORMULA 4: PLEASE REFER TO ANNEX 1
And also the electricity generation balance using fossil fuels equals to zero:
FORMULA 5: PLEASE REFER TO ANNEX 1
Below are the scenarios with different efficiencies were simulated according ACM006 steps:
TABLE 1: PLEASE REFER TO ANNEX 1
The efficiency with lower emission (76.2%) is the point where equations 4 and 5 are satisfied.
Values below 76.2%:
For values below the proposed efficiency, the process heat demand would not be achieved using only the biomass residues and fossil fuel would have to be used in order to generate the necessary heat. In this condition the baseline emissions would be higher due to increase in heat generated with fossil fuel in the recovery boiler. (Case 126.96.36.199 of ACM0006).
Values above 76.2%:
For values above the proposed efficiency, baseline emissions would be slightly higher due to the increase in heat generated with fossil fuel in the recovery boiler due to technical constrains (start-up and shut-down). According to page 32 of ACM0006 version 11.1 for the consumption of fuel due to technical constraints, the project participants shall: “(i) clearly identify the fossil fuel type and quantity required due to this technical constraint; (ii) add the identified quantity to the parameter FFBL,HG,y; (iii) determine the heat generation from this quantity of fossil fuel based on the efficiency of the heat generator; and (iv) add the calculated heat generation to the parameter HGBL,BR,y”.
Therefore applying formula 14 of ACM0006 for the fossil fuel:
FORMULA 6: PLEASE REFER TO ANNEX 1
Therefore, the heat generated (HGBL,FF) is directly proportional to the baseline efficiency (ηBL,HG) and as presented in Table 1 above, the higher the efficiency, higher would be the emission reductions.
In the Punta Pereira project the baseline is defined as “conventional self-sufficient pulp mill, without surplus power generation capacity”. The size of the pulp mill was defined based on its processing capacity and this value is limited to 1,300,000 ADt/year (air dry tonnes). The recovery boiler and turbo generator were designed based on the total amount of biomass available and on specific operational conditions of the pulp mill. Therefore it is DNV opinion that the default values available in the methodology ACM0006 (version 11.1) are not applicable to the Punta Pereira project.
The presented deviation is proposing project specific values for the efficiencies of the turbo generator and the pulp recovery boiler.
DNV considers that the default values available to determine the efficiency of the turbo generator and the pulp recovery boiler in accordance to the methodology ACM0006 (version 11.1) and respective tools are not sufficient or applicable to the Punta Pereira project.
It is DNV opinion that the baseline efficiencies should be conservative and comply with the pulp and paper industry in the relevant geographical region defined for the Punta Pereira project.
In order to reflect the project conditions and also to be represent a conservative and realistic baseline, project specific efficiencies for the turbo generator and the recovery boiler should be used in the baseline. Thus, being project specific efficiencies, it does not require an amendment to the approved methodology, once an amendment should be applicable to all projects classified under the methodology ACM0006.
Two scenarios were simulated in order to calculate the impact of the deviation on the estimates of the emission reductions:
Scenario 1 - Efficiencies of the turbo generator:
Considering that there is no applicable efficiency value for biomass steam turbines in the approved methodology and respective tools, it is not possible to evaluate the impact of the deviation in this scenario (green field projects).
Although the proposed turbo generator efficiency was already shown to be more conservative than the average efficiency of similar pulp mill CDM projects. The average efficiency of Nueva Aldea, Valdivia and Fray Bentos equals to 0.04169 MWh/GJ, which is 28% lower than the proposed value (0.05784 MWh/GJ).
Scenario 2 – Efficiencies of the recovery boiler:
Using the 76.2% efficiency instead of the 100% efficiency for the recovery boiler the emission reductions would decrease in 99 tCO2 per year. This is due to the decrease in the heat generation in the recoveryboiler from fuel oil utilization, as explained above in this document.
Project participants are aware that the impact in emission reductions between the proposed (76.2%) and default value (100%) are very low and represents 0.09% of the annual emission reduction. However their main argument is about the conservativeness of the baseline (self-sufficient heat and power generation pulp mill). A baseline boiler with 100% efficiency would generate surplus of heat and power, which is not the common practice of the pulp and paper industry and, consequently does not reflect a conservative baseline scenario.
|Annexes||Annex 1 - Deviation request formatted (637 KB)|
|Annex 2 Recovery Boiler Efficiency (242 KB)|
|Annex 3 Generator Efficiency (234 KB)|
|Annex 4 GHG emissions (305 KB)|
|Link to the documentation made available at validation stage||Link to relevant documentation|
|Signed form||Signed form (480 KB)|
This request for deviation has been accepted.
The Chairs have accepted the request for deviation to allow use of actual, credible and realistic values of efficiency of turbo-generator and the pulp recovery boiler in the baseline, instead of use of default values (100%) as required by the methodology and the referenced applicable tools.
|Current status||30 Apr 2012 - Deviation accepted|
23 Feb 2012 -
22 Mar 2012 - Successfully passed the Completeness Check
12 Apr 2012 - Awaiting EB decision