Evaporative fuel vapor emission control systems
An evaporative emission control canister system comprises an initial adsorbent volume having an effective incremental adsorption capacity at 25° C. of greater than 35 grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane, and at least one subsequent adsorbent volume having an effective incremental adsorption capacity at 25° C. of less than 35 grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane, an effective butane working capacity (BWC) of less than 3 g/dL, and a g-total BWC of between 2 grams and 6 grams. The evaporative emission control canister system has a two-day diurnal breathing loss (DBL) emissions of no more than 20 mg at no more than 210 liters of purge applied after the 40 g/hr butane loading step.
1. An evaporative emission control canister system, including one or more canisters comprising fuel port and a vent port,
wherein the one or more canisters include an adsorbent volume adjacent to the fuel port, and a plurality of subsequent adsorbent volumes upstream of the vent port,
wherein the plurality of subsequent adsorbent volumes have an effective incremental adsorption capacity at 25° C. of less than 35 grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane, and at least one of (i) an effective butane working capacity (BWC) of from about 1.6 to about 3 g/dL, or (ii) an effective butane working capacity (BWC) of from about 1.6 to about 3 g/dL and a g-total BWC of from 0.8-6 grams.
2. The evaporative emission control canister system of claim 1 , wherein the plurality of subsequent adsorbent volumes comprises a first nominal adsorbent volume, at least one additional nominal adsorbent volume, and an air gap, void or a spacer in between the first nominal adsorbent volume and the at least one additional nominal adsorbent volume.
3. The evaporative emission control canister system of claim 1 , wherein the evaporative emission control canister system further includes a hybrid combustion engine.
4. The evaporative emission control canister system of claim 1 , wherein the evaporative emission control canister system has a two-day diurnal breathing loss (DBL) of no more than 20 mg at (a) no more than 210 liters of purge applied after a 40 g/hr butane loading step or (b) no more than 100 bed volumes (BV) of purge applied after a 40 g/hr butane loading step as determined by the 2012 California Bleed Emissions Test Procedure (BETP).
5. The evaporative emission control canister system of claim 1 , wherein the evaporative emission control canister system has a two-day diurnal breathing loss (DBL) of no more than 20 mg at between 75-210 L of purge applied after a 40 g/hr butane loading step as determined by the 2012 California Bleed Emissions Test Procedure (BETP).
6. The evaporative emission control canister system of claim 1 , wherein the evaporative emission control canister system has a two-day diurnal breathing loss (DBL) of no more than 20 mg at between 50-100 BV of purge applied after a 40 g/hr butane loading step as determined by the 2012 California Bleed Emissions Test Procedure (BETP).
7. The evaporative emission control canister system of claim 1 , wherein the evaporative emission control system further includes at least one heat input unit for heating one or more adsorbent volumes.
8. The evaporative emission control canister system of claim 1 , wherein the adsorbent volume near the fuel port, plurality of adsorbent volumes near the vent port or both includes an adsorbent selected from the group consisting of activated carbon, carbon charcoal, zeolites, clays, porous polymers, porous alumina, porous silica, molecular sieves, kaolin, titania, ceria, and combinations thereof.
9. The evaporative emission control canister system of claim 8 , wherein the adsorbent is selected from the group consisting of activated carbon, carbon charcoal, and combinations thereof.
10. The evaporative emission control canister system of claim 9 , wherein the activated carbon is derived from a material including a member selected from the group consisting of wood, wood dust, wood flour, cotton linters, peat, coal, coconut, lignite, carbohydrates, petroleum pitch, petroleum coke, coal tar pitch, fruit pits, fruit stones, nut shells, nut pits, sawdust, palm, vegetables, synthetic polymer, natural polymer, lignocellulosic material, and combinations thereof.
11. The evaporative emission control canister system of claim 1 , wherein the plurality of subsequent adsorbent volumes is in the form of a honeycomb.
12. The evaporative emission control canister system of claim 1 , wherein the plurality of subsequent adsorbent volumes include a volumetric diluent between nominal volumes.
13. The evaporative emission control canister system of claim 12 , wherein the volumetric diluent includes a member selected from the group consisting of inert spacer particles, trapped air spaces, foams, fibers, screens, and combinations thereof.
14. The canister system of claim 1 , wherein at least one of the plurality of subsequent adsorbent volumes have an effective incremental adsorption capacity at 25° C. of 24 or less grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane.
15. The evaporative emission control canister system of claim 1 , wherein at least one of the plurality of subsequent adsorbent volumes have an effective incremental adsorption capacity at 25° C. of 16 or less grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane.
16. The evaporative emission control canister system of claim 7 , wherein the at least one heat input unit includes at least one of an internal resistive element, external resistive element, or heat input unit associated with the adsorbent.
17. An evaporative emission control canister system, including one or more canisters comprising:
an upstream adsorbent volume having an effective incremental adsorption capacity at 25° C. of greater than 35 grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane; and
a plurality of downstream nominal adsorbent volumes comprising at least one of air gaps, voids, or other volumes between the nominal adsorbent volumes, wherein the plurality of downstream nominal adsorbent volumes have an effective incremental adsorption capacity at 25° C. of less than 35 grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane, and at least one of (i) an effective butane working capacity (BWC) of 1.6-3 g/dL or (ii) an effective butane working capacity (BWC) of 1.6-3 g/dL, and a g-total BWC of from 0.8-6 grams,
wherein the upstream adsorbent volume, the plurality of downstream nominal adsorbent volumes, and air gaps, voids, or other volumes are located within a single canister, or in separate canisters that are connected to permit sequential contact by fuel vapor.
18. The evaporative emission control canister system of claim 17 , wherein the evaporative emission control canister system further includes a hybrid combustion engine.
19. The evaporative emission control canister system of claim 17 , wherein the evaporative emission control canister system has a two-day diurnal breathing loss (DBL) of no more than 20 mg at (a) no more than 210 liters of purge applied after a 40 g/hr butane loading step or (b) no more than 100 bed volumes (BV) of purge applied after a 40 g/hr butane loading step as determined by the 2012 California Bleed Emissions Test Procedure (BETP).
20. The evaporative emission control canister system of claim 17 , wherein the evaporative emission control canister system has a two-day diurnal breathing loss (DBL) of no more than 20 mg at between 75-210 L of purge applied after a 40 g/hr butane loading step as determined by the 2012 California Bleed Emissions Test Procedure (BETP).