Republic of Latvia
Cabinet
Regulation No. 294 Adopted 17 May 2016
|
Procedures for Calculating Savings
of Primary Energy Produced by Cogeneration Plants
Issued pursuant to
Section 46, Paragraph five of the Energy Law
1. The Regulation prescribes the procedures by which savings
of primary energy produced by cogeneration plants shall be
calculated.
2. The values which are used for the calculation of
electricity produced in cogeneration, shall be determined on the
basis of the expected or actual operation of the installation
under normal conditions of use. In relation to micro-cogeneration
installations such calculations may be based on approved
values.
3. The amount of electricity produced in cogeneration during
the time period for the settlement of accounts which is left
after utilisation of electricity for the needs of the
cogeneration plant, shall be determined as follows:
3.1. the total actual efficiency coefficient of energy
production for the cogeneration plant shall be calculated
(
), using the following
formula:
 |
, where |
- is the amount of electricity
produced in cogeneration installations installed in a
cogeneration plant during the period of time for the settlement
of accounts which is determined according to the readings of the
meters at the generator output (MWh);
- is the amount of the useful
thermal energy produced in cogeneration installations installed
in a cogeneration plant during the period of time for the
settlement of accounts (MWh);
- is the amount of fuel consumed
in cogeneration installations installed in a cogeneration plant
during the period of time for the settlement of accounts
(MWh);
3.2. it shall be assumed that the amount of electricity
produced in cogeneration remaining after utilisation of
electricity for the needs of the cogeneration plant is equal to
the amount of electricity exported to the electricity grid during
the period of time for the settlement of accounts, if one of the
following conditions is conformed to:
3.2.1. the total actual efficiency coefficient of energy
production for the cogeneration plant in which the technology
referred to in Sub-paragraph 4.1 or 4.3 of this Regulation is
used, is 80 % or more;
3.2.2. the total actual efficiency coefficient of energy
production for the cogeneration plant in which any of the
technologies referred to in Sub-paragraph 4.2, 4.4, 4.5, 4.6,
4.7, 4.8, 4.9, 4.10 or 4.11 of this Regulation is used, is 75 %
or more;
3.3. if the calculated total actual efficiency coefficient of
the cogeneration plant is less than the values referred to in
Sub-paragraph 3.2.1 or 3.2.2 of this Regulation, the amount of
electricity produced in cogeneration remaining after utilisation
for the needs of the cogeneration plant
shall be calculated, using the following
formula:
 |
, where |
- is the amount of the useful
thermal energy produced in cogeneration installations installed
in a cogeneration plant during the period of time for the
settlement of accounts (MWh);
α - is the proportion between the electricity produced
in cogeneration and useful thermal energy which, using the data
of the technical passport of the relevant installation, is
calculated when the installation is fully operating in
cogeneration. If such data are not available, the abovementioned
value shall be determined depending on the cogeneration
technology used (Annex 1).
4. Savings of primary energy in cogeneration plants which
consist of the cogeneration installation and one or several
boilers for production of thermal energy or only from a
cogeneration installation and which concurrently produce
electricity and useful thermal energy, shall be calculated for
one or several of the following production technologies:
4.1. a combined cycle gas turbine with heat recovery;
4.2. a steam backpressure turbine;
4.3. a steam condensing extraction turbine with a steam
discharge pipeline for heat supply;
4.4. a gas turbine with heat recovery;
4.5. an internal combustion engine;
4.6. a micro-turbine;
4.7. Stirling engines;
4.8. fuel cells;
4.9. steam engines;
4.10. organic Rankine cycle;
4.11. other technologies or combinations thereof if by using
them it is possible to produce electricity and useful thermal
energy concurrently.
5. The values which are used for the calculation of
cogeneration efficiency and savings of primary energy, shall be
determined on the basis of foreseeable or actual operation of the
installation under normal conditions of use. In relation to
micro-cogeneration installations the savings of primary energy
may be calculated on the basis of approved data.
6. In order to determine the efficiency of a cogeneration
plant, the primary energy savings (PES) which are obtained when
the cogeneration plant produces energy in cogeneration, shall be
calculated. The following formula shall be used for the
calculations:
 |
, where |
- is the electric efficiency
coefficient of cogeneration installations installed in a
cogeneration plant within a certain period of time which is
calculated using the formula referred to in Paragraph 7 of this
Regulation;
- is the heat efficiency
coefficient of cogeneration installations installed in a
cogeneration plant within a certain period of time which is
calculated using the formula referred to in Paragraph 8 of this
Regulation;
- is the efficiency coefficient
for an individual production of thermal energy depending on the
type of fuel used (Annex 2);
- is the efficiency coefficient
for an individual production of thermal energy depending on the
type of fuel used (if firewood or biogas is used in a
cogeneration plant,
shall be assumed), which is calculated using the
following formula:
 |
, where |
- is the harmonised efficiency
coefficient with a climate correction for an individual
production of electricity depending on the fuel used and the year
in which the cogeneration plant was put into service (Annex
2);
- is the own consumption
coefficient of a cogeneration plant which is calculated by
dividing the annual amount of electricity consumed by a
cogeneration plant with the annual amount of electricity produced
in a cogeneration plant;
- is the correction coefficient
for avoided grid losses in relation to electricity that is
consumed in a cogeneration plant (Annex 3);
- is the correction coefficient
for avoided grid losses in relation to electricity that is
transferred into the grid (Annex 3).
7. The electrical efficiency coefficient
of cogeneration installations installed in a
cogeneration plant within a certain period of time which is not
less than four months, shall be calculated, using the following
formula:
 |
, where |
- is the amount of electricity
produced in cogeneration installations installed in a
cogeneration plant within the relevant period of time which is
not less than four months (MWh);
B - is the total amount of fuel consumed for the
production of electricity and useful thermal energy in the
cogeneration installations installed in a cogeneration plant
within the relevant period of time which is not less than four
months (MWh).
8. The heat efficiency coefficient
of cogeneration installations installed in a
cogeneration plant within a certain period of time which is not
less than four months, shall be calculated, using the following
formula:
 |
, where |
- is the amount of the useful
thermal energy produced in cogeneration installations installed
in a cogeneration plant within the relevant period of time which
is not less than four months (MWh);
B - is the total amount of fuel consumed for the
production of electricity and useful thermal energy in the
cogeneration installations installed in a cogeneration plant
within the relevant period of time which is not less than four
months (MWh).
Informative Reference to the
European Union Directive
This Regulation contains legal norms arising from Directive
2012/27/EU of the European Parliament and of the Council of 25
October 2012 on energy efficiency, amending Directives
2009/125/EC and 2010/30/EU and repealing Directives 2004/8/EC and
2006/32/EC.
Prime Minister Māris Kučinskis
Deputy Prime Minister,
Minister for Economics Arvils Ašeradens
Annex 1
Cabinet
Regulation No. 294
17 May 2016
Proportion between Electricity
Produced in Cogeneration and Useful Thermal Energy for Different
Cogeneration Technologies
No. |
Cogeneration technology |
Energy and
heat proportion α |
1. |
Combined cycle gas turbine with
heat recovery |
0.95 |
2. |
Steam condensing extraction
turbine with a steam discharge pipeline for heat supply |
0.45 |
3. |
Steam backpressure
turbine |
0.45 |
4. |
Gas turbine with heat
recovery |
0.55 |
5. |
Internal combustion
engine |
0.75 |
Deputy Prime Minister,
Minister for Economics Arvils Ašeradens
Annex 2
Cabinet
Regulation No. 294
17 May 2016
Efficiency Coefficients
I. Harmonised
efficiency reference values with climate correction for
individual production of electricity
Table 1
Fuel |
Category |
Type of fuel |
The year of the
putting into service of a cogeneration plant |
2012 and earlier |
2012-2015 |
2016 and later |
Solid fuel |
S1 |
Hard coal, including
anthracite, bituminous coal, sub-bituminous coal, coke,
semicoke, petroleum coke |
0.442 |
0.442 |
0.442 |
S2 |
Lignite, lignite briquettes,
shale oil |
0.418 |
0.418 |
0.418 |
S3 |
Peat, peat briquettes |
0.390 |
0.390 |
0.390 |
S4 |
Dry biomass, including wood
pellets and briquettes, dried woodchips, clean wood residues,
nutshells and olive and other stones |
0.330 |
0.330 |
0.370 |
S5 |
Other solid biomass,
including solid biomass of all types which is not listed in
Category S4, as well as black and brown liquor |
0.250 |
0.250 |
0.300 |
S6 |
Municipal and industrial
waste (non-renewable) and renewable/biologically degradable
waste |
0.250 |
0.250 |
0.250 |
Liquid fuel |
L7 |
Heavy fuel oil, gas oil,
diesel oil, other oil products |
0.442 |
0.442 |
0.442 |
L8 |
Biofuels, including
biomethanol, bioethanol, biobutanol, biodiesel and other
biofuels |
0.442 |
0.442 |
0.442 |
L9 |
Liquid waste, including
biologically degradable waste and non-renewable waste
(including pyrolysis oil, melted fat, fat, and spent
grain) |
0.250 |
0.250 |
0.290 |
Gaseous fuel |
G10 |
Natural gas, LPG, LNG and
biomethane |
0.533 |
0.533 |
0.538 |
G11 |
Refinery gas, hydrogen and
synthesis gas |
0.450 |
0.450 |
0.450 |
G12 |
Biogas which has been
obtained from anaerobic digestion, waste landfill and sewage
treatment |
0.428 |
0.428 |
0.428 |
G13 |
Coke gas, blast furnace gas,
mining gas and other recoverable gases (except refinery
gas) |
0.358 |
0.358 |
0.358 |
Other |
O14 |
Waste heat (including exhaust
gases of high temperature processes, products of exothermic
chemical reaction) |
- |
- |
0.300 |
O15 |
Nuclear energy |
- |
- |
0.300 |
O16 |
Solar energy |
- |
- |
0.300 |
O17 |
Geothermal energy |
- |
- |
0.300 |
O18 |
Other fuel which is not
referred to in this Table |
- |
- |
0.300 |
II. Efficiency
Coefficients for Separate Production of Thermal Energy
Table 2
Fuel |
Category |
Type of fuel |
Type of use of
thermal energy |
Hot water |
Vapour* |
Direct use of waste
gases** |
Solid fuel |
S1 |
Hard coal, including
anthracite, bituminous coal, sub-bituminous coal, coke,
semicoke, petroleum coke |
0.88 |
0.83 |
0.80 |
S2 |
Lignite, lignite briquettes,
shale oil |
0.86 |
0.81 |
0.78 |
S3 |
Peat, peat briquettes |
0.86 |
0.81 |
0.78 |
S4 |
Dry biomass, including wood
pellets and briquettes, dried woodchips, clean wood residues,
nutshells and olive and other stones |
0.86 |
0.81 |
0.78 |
S5 |
Other solid biomass,
including solid biomass of all types which is not listed in
Category S4, as well as black and brown liquor |
0.80 |
0.75 |
0.72 |
S6 |
Municipal and industrial
waste (non-renewable) and renewable/biologically degradable
waste |
0.80 |
0.75 |
0.72 |
Liquid fuel |
L7 |
Heavy fuel oil, gas oil,
diesel oil, other oil products |
0.85 |
0.80 |
0.77 |
L8 |
Biofuels, including
biomethanol, bioethanol, biobutanol, biodiesel and other
biofuels |
0.85 |
0.80 |
0.77 |
L9 |
Liquid waste, including
biologically degradable waste and non-renewable waste
(including pyrolysis oil, melted fat, fat, and spent
grain) |
0.75 |
0.70 |
0.67 |
Gaseous fuel |
G10 |
Natural gas, LPG, LNG and
biomethane |
0.92 |
0.87 |
0.84 |
G11 |
Refinery gas, hydrogen and
synthesis gas |
0.90 |
0.85 |
0.82 |
G12 |
Biogas which has been
obtained from anaerobic digestion, waste landfill and sewage
treatment |
0.80 |
0.75 |
0.72 |
G13 |
Coke gas, blast furnace gas,
mining gas and other recoverable gases (except refinery
gas) |
0.80 |
0.75 |
0.72 |
Other |
O14 |
Waste heat (including exhaust
gases of high temperature processes, products of exothermic
chemical reaction) |
0.92 |
0.87 |
- |
O15 |
Nuclear energy |
0.92 |
0.87 |
- |
O16 |
Solar energy |
0.92 |
0.87 |
- |
O17 |
Geothermal energy |
0.92 |
0.87 |
- |
O18 |
Other fuel which is not
referred to in this Table |
0.92 |
0.87 |
- |
Notes.
1. * These values must be used by units which operate with
vapour and have been put into operation after 31 December 2015.
If such units, upon calculating the efficiency coefficient for
individual production of thermal energy, do not take into account
recovery of condensate, then the values indicated in the Table in
case of vapour must be increased by 5 per cent by volume.
2. ** Such values must be used, if the temperature of waste
gases is 250°C or higher.
Deputy Prime Minister,
Minister for Economics Arvils Ašeradens
Annex 3
Cabinet
Regulation No. 294
17 May 2016
Correction Factors z for Avoided
Grid Losses that are Applicable to the Calculation of Efficiency
Coefficient for Separate Production of Electricity
Voltage in the grid to which a
cogeneration plant is connected |
For electricity exported to
the grid |
For electricity consumed in a
cogeneration plant |
345 kV or higher |
1 |
0.976 |
From 200 up to 345 kV (not
included) |
0.972 |
0.963 |
From 100 up to 200 kV (not
included) |
0.963 |
0.951 |
From 50 up to 100 kV (not
included) |
0.952 |
0.936 |
From 12 up to 50 kV (not
included) |
0.935 |
0.914 |
From 0.45 up to 12 kV (not
included) |
0.918 |
0.891 |
Less than 0.45 kV |
0.888 |
0.851 |
Deputy Prime Minister,
Minister for Economics Arvils Ašeradens
Translation © 2017 Valsts valodas centrs (State
Language Centre)