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Commission Regulation (EU) 2018/1832 of 5 November 2018 amending Directive 2007/46/EC of the European Parliament and of the Council, Commission Regulation (EC) No 692/2008 and Commission Regulation (EU) 2017/1151 for the purpose of improving the emission type approval tests and procedures for light passenger and commercial vehicles, including those for in-service conformity and real-driving emissions and introducing devices for monitoring the consumption of fuel and electric energy (Text with EEA relevance)
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This Annex provides the method to determine the levels of evaporative emission from light-duty vehicles in a repeatable and reproducible manner designed to be representative of real world vehicle operation.
For the purposes of this Annex, the following definitions shall apply:
BWC | Butane working capacity |
PF | Permeability factor |
APF | Assigned permeability factor |
OVC-HEV | Off-vehicle charging hybrid electric vehicle |
NOVC-HEV | Not off-vehicle charging hybrid electric vehicle |
WLTC | Worldwide light-duty test cycle |
REESS | Rechargeable electric energy storage system |
Fuel tank system material and construction;
Vapour hose material, fuel line material and connection technique;
Sealed tank or non-sealed tank system;
Fuel tank relief valve setting (air ingestion and relief);
Canister butane working capacity (BWC300) within a 10 per cent range of the highest value (for canisters with the same type of charcoal, the volume of charcoal shall be within 10 per cent of that for which the BWC300 was determined);
Purge control system (for example, type of valve, purge control strategy).
Each of the evaporative emission families defined in paragraph 5.5.1. shall be attributed a unique identifier of the following format:
EV-nnnnnnnnnnnnnnn-WMI-x
Where:
nnnnnnnnnnnnnnn is a string with a maximum of fifteen characters, restricted to using the characters 0-9, A-Z and the underscore character ‘_’.
WMI (world manufacturer identifier) is a code that identifies the manufacturer in a unique manner defined in ISO 3780:2009.
x shall be set to ‘1’ or ‘0’ in accordance with the following provisions:
With the agreement of the approval authority and the owner of the WMI, the number shall be set to ‘1’ where a vehicle family is defined for the purpose of covering vehicles of:
a single manufacturer with one single WMI code;
a manufacturer with several WMI codes, but only in cases when one WMI code is to be used;
more than one manufacturer, but only in cases when one WMI code is to be used.
In the cases (i), (ii) and (iii), the family identifier code shall consist of one unique string of n-characters and one unique WMI code followed by ‘1’.
With the agreement of the approval authority, the number shall be set to ‘0’ in the case that a vehicle family is defined based on the same criteria as the corresponding vehicle family defined in accordance with point (a), but the manufacturer chooses to use a different WMI. In this case the family identifier code shall consist of the same string of n-characters as the one determined for the vehicle family defined in accordance with point (a) and a unique WMI code which shall be different from any of the WMI codes used under case (a), followed by ‘0’.
The limit value shall be that specified in Table 3 of Annex I to Regulation (EC) No 715/2007.
This Annex describes the procedure for the Type 4 test which determines the evaporative emission of vehicles.
The vehicle shall be in good mechanical condition and have been run-in and driven at least 3 000 km before the test. For the purpose of the determination of evaporative emissions, the mileage and the age of the vehicle used for certification shall be included in all relevant test reports. The evaporative emission control system shall be connected and functioning correctly during the run-in period. A carbon canister aged in accordance with the procedure described in paragraph 5.1. of this Appendix shall be used.
The chassis dynamometer shall meet the requirements of paragraph 2. of Sub-Annex 5 of Annex XXI.
The evaporative emission measurement enclosure shall meet the requirements of paragraph 4.2. of Annex 7 of UN/ECE Regulation No 83.
The analytical systems shall meet the requirements of paragraph 4.3. of Annex 7 of UN/ECE Regulation No 83. Continuous measuring of hydrocarbons is not mandatory unless the fixed volume type enclosure is used.
The temperature recording shall meet the requirements of paragraph 4.5. of Annex 7 of UN/ECE Regulation No 83.
The pressure recording shall meet the requirements of paragraph 4.6. of Annex 7 of UN/ECE Regulation No 83, except that the accuracy and resolution of the pressure recording system defined in paragraph 4.6.2. of Annex 7 of UN/ECE Regulation No 83 shall be:
Accuracy: ± 0,3 kPa
Resolution: 0,025 kPa
The fans shall meet the requirements of paragraph 4.7. of Annex 7 of UN/ECE Regulation No 83, except that the capacity of the blowers shall be 0,1 to 0,5 m3/sec instead of 0,1 to 0,5 m3/min.
The gases shall meet the requirements of paragraph 4.8. of Annex 7 of UN/ECE Regulation No 83.
The additional equipment shall meet the requirements of paragraph 4.9. of Annex 7 of UN/ECE Regulation No 83.
The auxiliary canister should be identical to the main canister but not necessarily aged. The connection tube to the vehicle canister shall be as short as possible. The auxiliary canister shall be fully-purged with dry air prior to loading.
The canister weighing scale shall have an accuracy of ±0,02 g.
Before performing the hot soak and diurnal losses sequences, the canister shall be aged in accordance with the procedure described in Figure VI.1.
The canister shall be cycled between temperatures from – 15 °C to 60 °C in a dedicated temperature enclosure with 30 minutes of stabilisation at – 15 °C and 60 °C. Each cycle shall last 210 minutes (see Figure VI.2).
The temperature gradient shall be as close as possible to 1 °C/min. No forced air flow should pass through the canister.
The cycle shall be repeated 50 times consecutively. In total, this procedure lasts 175 hours.
Following the temperature ageing procedure, the canister shall be shaken vertically with the canister mounted as per its orientation in the vehicle with an overall Grms > 1,5 m/sec2 with a frequency of 30 ± 10 Hz. The test shall last 12 hours.
The canister shall be loaded to 2 gram breakthrough. As an alternative, loading shall be deemed to be completed when the hydrocarbon concentration level at the vent outlet reaches 3 000 ppm.
Density at 15 °C;
Vapour pressure;
Distillation (70 °C, 100 °C, 150 °C);
Hydrocarbon analysis (olefins, aromatics, benzene only);
Oxygen content;
Ethanol content.
The stabilised canister shall be loaded to 2 gram breakthrough and subsequently purged a minimum of 5 times. Loading shall be performed with a mixture composed of 50 per cent butane and 50 per cent nitrogen by volume at a rate of 40 grams butane per hour.
Purging shall be performed in accordance with paragraph 5.1.3.1.2. of this Appendix.
The BWC shall be included in all relevant test reports after each loading.
BWC300 shall be calculated as the average of the last 5 BWCs.
Type of activated carbon;
Loading rate;
Fuel specifications.
Within 6 to 36 hours, the rig with the fuel tank system shall be placed in an enclosure. The last 6 hours of this period shall be at an ambient temperature of 20 °C ± 2 °C. In the enclosure, a diurnal procedure shall be performed over the first 24-hour period of the procedure described in paragraph 6.5.9. of this Appendix. The fuel vapour in the tank shall be vented to the outside of the enclosure to eliminate the possibility of the tank venting emissions being counted as permeation. The HC emissions shall be measured and the value shall be included in all relevant test reports as HC3W.
Within 6 to 36 hours, the rig with the fuel tank system shall be placed in an enclosure. The last 6 hours of this period shall be at an ambient temperature of 20 °C ± 2 °C. In the enclosure, a diurnal procedure shall be performed over a first period of 24 hours of the procedure described in accordance with paragraph 6.5.9. of this Appendix. The fuel tank system shall be vented to the outside of the enclosure to eliminate the possibility of the tank venting emissions being counted as permeation. The HC emissions shall be measured and the value shall be included in all relevant test reports in this case as HC20W.
PF = HC20w – HC3W
A full description of the fuel tank system tested, including information on the type of tank tested, whether the tank is metal, monolayer non-metal or multilayer, and which types of materials are used for the tank and other parts of the fuel tank system;
The weekly mean temperatures at which the ageing was performed;
The HC measured at week 3 (HC3W);
The HC measured at week 20 (HC20W);
The resulting permeability factor (PF).
APF multilayer/metal tank = 120 mg /24 h
Where the manufacturer chooses to use an APF, the manufacturer shall provide the approval authority with a declaration in which the type of tank is clearly specified as well as a declaration of the type of materials used.
The vehicle shall be prepared in accordance to paragraphs 5.1.1. and 5.1.2. of Annex 7 of UN/ECE Regulation No 83. At the request of the manufacturer and with approval of the approval authority, non-fuel background emission sources (e.g. paint, adhesives, plastics, fuel/vapour lines, tyres, and other rubber or polymer components) may be reduced to typical vehicle background levels before testing (e.g. baking of tyres at temperatures of 50 °C or higher for appropriate periods, baking of the vehicle, draining washer fluid).
For a sealed fuel tank system, the vehicle canisters shall be installed so that access to canisters and connection/disconnection of canisters can be done easily.
The tests included in this Annex shall be performed using the test conditions specific to interpolation family vehicle H with the highest cycle energy demand of all the interpolation families included in the evaporative emission family being considered.
Alternatively, at the request of the approval authority, any cycle energy representative of a vehicle in the family may be used for the test.
The test procedure for non-sealed and sealed tank systems shall be followed in accordance with the flow chart described in Figure VI.4.
The sealed fuel tank systems shall be tested with one of 2 options. One option is to test the vehicle with one continuous procedure. Another option, called the stand-alone procedure, is to test the vehicle with two separate procedures which will allow repeating the dynamometer test and the diurnal tests without repeating the tank depressurisation puff loss overflow test and the depressurisation puff loss measurement.
The fuel tank of the vehicle shall be emptied. This shall be done so as not to abnormally purge or abnormally load the evaporative control devices fitted to the vehicle. Removal of the fuel cap is normally sufficient to achieve this. The fuel tank shall be refilled with reference fuel at a temperature of 18 °C ± 2 °C to 40 ± 2 per cent of its nominal capacity.
Within 5 minutes after completing fuel drain and refill, the vehicle shall be soaked for a minimum of 6 hours and a maximum of 36 hours at 23 °C ± 3 °C.
The vehicle shall be placed on a chassis dynamometer and driven over the following phases of the cycle described in Sub-Annex 1 of Annex XXI:
For Class 1 vehicles: low, medium, low, low, medium, low
For Class 2 and 3 vehicles: low, medium, high, medium.
For OVC-HEVs, the preconditioning drive shall be performed under the charge-sustaining operating condition as defined in paragraph 3.3.6. of Annex XXI. Upon the request of approval authority, any other mode may be used.
Within one hour after the preconditioning drive, the fuel tank of the vehicle shall be emptied. This shall be done so as not to abnormally purge or abnormally load the evaporative control devices fitted to the vehicle. Removal of the fuel cap is normally sufficient to achieve this. The fuel tank shall be refilled with test fuel at a temperature of 18 °C ± 2 °C to 40 ± 2 per cent of its nominal capacity.
Within five minutes of completing fuel drain and refill, the vehicle shall be parked for a minimum of 12 hours and a maximum of 36 hours at 23 °C ± 3 °C.
During soaking, the procedures described in paragraphs 6.5.5.1. and 6.5.5.2. may be performed either in the order of first paragraph 6.5.5.1. followed by paragraph 6.5.5.2. or in the order paragraph 6.5.5.2. followed by paragraph 6.5.5.1. The procedures described in paragraphs 6.5.5.1. and 6.5.5.2. may also be performed simultaneously.
For OVC-HEVs, the REESS shall be fully charged in accordance with the charging requirements described in paragraph 2.2.3. of Appendix 4 to Sub-Annex 8 of Annex XXI.
The canister aged in accordance with the sequence described in paragraph 5.1. of this Appendix shall be loaded to 2 gram breakthrough in accordance with the procedure described in paragraph 5.1.4. of Annex 7 of UN/ECE Regulation No 83.
The test vehicle shall be pushed onto a dynamometer and shall be driven over the cycles described in paragraph 6.5.3.(a) or paragraph 6.5.3.(b) of this Appendix. OVC-HEVs shall be operated in charge-depleting operating condition. The engine shall be subsequently shut off. Exhaust emissions may be sampled during this operation and the results may be used for the purpose of exhaust emission and fuel consumption type approval if this operation meets the requirement described in Sub-Annex 6 or Sub-Annex 8 of Annex XXI.
Within 7 minutes after the dynamometer test and within 2 minutes of the engine being switched off, the hot soak evaporative emissions test shall be performed in accordance with paragraph 5.5. of Annex 7 of UN/ECE Regulation No 83. The hot soak losses shall be calculated in accordance with paragraph 7.1. of this Appendix and included in all relevant test reports as MHS.
After the hot soak evaporative emissions test, the test vehicle shall be soaked for not less than 6 hours and not more than 36 hours between the end of the hot soak test and the start of the diurnal emission test. For at least the last 6 hours of this period the vehicle shall be soaked at 20 °C ± 2 °C.
At the end of each emission sampling period, the hydrocarbon concentration, temperature and barometric pressure shall be measured and used to calculate the diurnal test results using the equation in paragraph 7.1. of this Appendix. The result obtained from the first 24 hours shall be included in all relevant test reports as MD1. The result obtained from the second 24 hours shall be included in all relevant test reports as MD2.
Within one hour after the preconditioning drive, the fuel tank of the vehicle shall be emptied. This shall be done so as not to abnormally purge or abnormally load the evaporative control devices fitted to the vehicle. Removal of the fuel cap is normally sufficient to achieve this, otherwise the canister shall be disconnected. The fuel tank shall be refilled with reference fuel at a temperature of 18 °C ± 2 °C to 15 ± 2 per cent of the tank's nominal capacity.
Within 5 minutes after completing fuel drain and refill, the vehicle shall be soaked for stabilization for 6 to 36 hours at an ambient temperature of 20 °C ± 2 °C.
The tank pressure shall be subsequently released so as not to abnormally raise the inside pressure of the fuel tank. This may be done by opening the fuel cap of the vehicle. Regardless of the method of depressurisation, the vehicle shall be returned to its original condition within 1 minute.
The canister aged in accordance with the sequence described in paragraph 5.1. of this Appendix shall be loaded to 2 gram breakthrough in accordance with the procedure described in paragraph 5.1.6. of Annex 7 of UN/ECE Regulation No 83, and shall be subsequently purged with 25 ± 5 litres per minute with emission laboratory air. The volume of purge air shall not exceed the volume determined in paragraph 6.6.1.5.1. This loading and purging can be done either (a) using an on-board canister at a temperature of 20 °C or optionally 23 °C, or (b) by disconnecting the canister. In both cases, no further relief of the tank pressure is allowed.
The maximum purge amount Volmax shall be determined by the following equation. In the case of OVC-HEVs, the vehicle shall be operated in charge-sustaining operating condition. This determination can also be done at a separate test or during the preconditioning drive.
where:
is the cumulative purge volume rounded to the nearest 0,1 litres measured using a suitable device (e.g. flowmeter connected to the vent of the carbon canister or equivalent) over the cold start preconditioning drive described in the paragraph 6.5.3. of this Appendix, l;
is the manufacturer's nominal fuel tank capacity, l;
is the fuel consumption over the single purge cycle described in paragraph 6.5.3. of this Appendix which may be measured in either warm or cold start condition, l/100 km. For OVC-HEVs and NOVC-HEVs, fuel consumption shall be calculated in accordance with paragraph 4.2.1. of Sub-Annex 8 of Annex XXI;
is the theoretical distance to the nearest 0,1 km of a single purge cycle described in paragraph 6.5.3. of this Appendix, km.
After completing canister loading and purging, the test vehicle shall be moved into an enclosure, either a SHED or an appropriate climatic chamber. It shall be demonstrated that the system is leak-free and the pressurisation is performed in a normal way during the test or by separate test (e.g. by means of pressure sensor on the vehicle). The test vehicle shall be subsequently exposed to the first 11 hours of the ambient temperature profile specified for the diurnal emission test in Appendix 2 to Annex 7 of UN/ECE Regulation No 83 with a maximum deviation of ± 2 °C at any time. The average temperature deviation from the profile, calculated using the absolute value of each measured deviation, shall not exceed ± 1 °C. The ambient temperature shall be measured at least every 10 minutes and included in all relevant test sheets.
The manufacturer shall ensure that the refuelling operation cannot be initiated before the sealed fuel tank system is fully depressurised to a pressure less than 2,5 kPa above ambient pressure in normal vehicle operation and use. At the request of the approval authority, the manufacturer shall provide detailed information or demonstrate proof of operation (e.g. by means of pressure sensor on the vehicle). Any other technical solution may be allowed provided that a safe refuelling operation is ensured and that no excessive emissions are released to the atmosphere before the refuelling device is connected to the vehicle.
Within 15 minutes after the ambient temperature has reached 35 °C as described in paragraph 6.6.1.6. of this Appendix, the chamber shall be sealed and the measurement procedure shall be started.
The hydrocarbon analyser shall be zeroed and spanned, after which the hydrocarbon concentration, temperature and barometric pressure shall be measured to give the initial readings CHCi, Pi and Ti for the sealed tank depressurisation puff loss overflow determination.
The ambient temperature T of the enclosure shall not be less than 25 °C during the measurement procedure.
At the end of the procedure described in paragraph 6.6.1.7.2. of this Appendix, the hydrocarbon concentration in the chamber shall be measured after 60 ± 5 seconds. The temperature and the barometric pressure shall also be measured. These are the final readings CHCf, Pf and Tf for the sealed tank depressurisation puff loss overflow.
The sealed tank puff loss overflow result shall be calculated in accordance with paragraph 7.1. of this Appendix and included in all relevant test reports.
After completing puff loss loading, the vehicle shall be soaked at 23 ± 2 °C for 6 to 36 hours to stabilise the vehicle temperature.
For OVC-HEVs, the REESS shall be fully charged in accordance with the charging requirements described in paragraph 2.2.3. of Appendix 4 to Annex 8 of Annex XXI during the soaking described in paragraph 6.6.1.9. of this Appendix.
The fuel tank of the vehicle shall be drained and filled up to 40 ± 2 per cent of the tank's nominal capacity with reference fuel at a temperature of 18 °C ± 2 °C.
The vehicle shall be subsequently parked for a minimum of 6 hours to a maximum of 36 hours in the soak area at 20 °C ± 2 °C to stabilise the fuel temperature.
The tank pressure shall be subsequently released so as not to abnormally raise the inside pressure of the fuel tank. This may be done by opening the fuel cap of the vehicle. Regardless of the method of depressurisation, the vehicle shall be returned to its original condition within 1 minute. After this action, the vapour storage unit shall be connected again.
The test shall be performed as described in paragraphs 6.6.1.1. to 6.6.1.13. of this Appendix. However, in this case, the ambient temperature described in paragraph 6.5.9.1. of this Appendix shall be replaced by the profile specified in Table VI.1 of this Appendix for the diurnal emission test.
Ambient temperature profile of the alternative sequence for sealed fuel tank system
Time (hours) | Temperature (°C) |
---|---|
0/24 | 20,0 |
1 | 20,4 |
2 | 20,8 |
3 | 21,7 |
4 | 23,9 |
5 | 26,1 |
6 | 28,5 |
7 | 31,4 |
8 | 33,8 |
9 | 35,6 |
10 | 37,1 |
11 | 38,0 |
12 | 37,7 |
13 | 36,4 |
14 | 34,2 |
15 | 31,9 |
16 | 29,9 |
17 | 28,2 |
18 | 26,2 |
19 | 24,7 |
20 | 23,5 |
21 | 22,3 |
22 | 21,0 |
23 | 20,2 |
The test shall be performed as described in paragraphs 6.7.2.1.1. to 6.7.2.1.4. of this Appendix. However, in this case, the ambient temperature described in 6.5.9.1. of this Appendix shall be modified pursuant to the profile specified in Table VI.1 of this Appendix for the diurnal emission test.
The following equation shall be used:
where:
is the mass of hydrocarbons, grams;
is the mass of hydrocarbons exiting the enclosure in the case of fixed volume enclosures for diurnal emission testing, grams;
is the mass of hydrocarbon entering the enclosure in the case of fixed volume enclosures for diurnal emission testing, grams;
is the measured hydrocarbon concentration in the enclosure, ppm volume in C1 equivalent;
is the net enclosure volume corrected for the volume of the vehicle with the windows and the luggage compartment open, m3. If the volume of the vehicle is not known, a volume of 1,42 m3 shall be subtracted;
is the ambient chamber temperature, K;
is the barometric pressure, kPa;
is the hydrogen to carbon ratio
where:
is taken to be 2,33 for puff loss overflow measurement in SHED and diurnal test losses;
is taken to be 2,20 for hot soak losses;
is 1,2 × 10– 4 × (12 + H/C), in (g × K/(m3 × kPa));
is the initial reading;
is the final reading;
The test report shall contain at least the following:
Description of the soak periods, including time and mean temperatures;
Description of aged canister used and reference to exact ageing report;
Mean temperature during the hot soak test;
Measurement during hot soak test, HSL;
Measurement of first diurnal, DL1st day;
Measurement of second diurnal, DL2nd day;
Final evaporative test result, calculated in accordance with paragraph 7. of this Appendix;
Declared fuel tank relief pressure of the system (for sealed tank systems);
Puff loss loading value (in the case of using the stand-alone test described in paragraph 6.7. of this Appendix).’
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