Low emission adsorbent and canister system
The present description provides low DBL bleed emission performance properties that allows the design of evaporative fuel emission control systems that are simpler and more compact than those possible by prior art by inclusion of a vent-side volume comprising a parallel passage adsorbent such as a carbon honeycomb with narrow channel width and low cell pitch.
1 . A parallel passage adsorbent volume (PPAV) comprising activated carbon, wherein the PPAV includes an outer surface and a plurality of parallel passages or channels extending therethrough parallel to the outer surface, and wherein the parallel passages or channels are configured to have an average channel hydraulic diameter (t c,Dh ) of less than or equal to 1.25 mm, a hydraulic diameter cell pitch (CP Dh ) of less than or equal to 1.45 mm and, and wherein the PPAV is configured to be incorporated into a vehicle evaporative emission canister system.
2 . The parallel passage adsorbent volume of claim 1 , wherein the average channel hydraulic diameter (t c, Dh ) is less than or equal to 1.20.
3 . The parallel passage adsorbent volume of claim 1 , wherein the hydraulic diameter cell pitch (CP Dh ) is less than or equal to 1.40 mm.
4 . The parallel passage adsorbent volume of claim 1 , wherein the PPAV further comprises at least one of the following: (i) a plurality channel width (t c, avg ) of less than about 1.25 mm; (ii) a plurality channel width cell pitch (CP tc, avg ) of less than about 1.5 mm; (iii) a cell density of from about 285 to about 1000 cpsi; (iv) a cell wall thickness of less than about 0.5 mm; (v) an incremental adsorption capacity between 5% and 50% n-butane at 25 C of less than about 50 g/L; or (vi) a combination thereof.
5 . The parallel passage adsorbent volume of claim 4 , wherein the plurality channel width (t c, avg ) of the PPAV is less than about 1.20 mm.
6 . The parallel passage adsorbent volume of claim 4 , wherein the plurality channel width cell pitch (CP tc, avg ) of the PPAV is less than about 1.40 mm.
7 . The parallel passage adsorbent volume of claim 4 , wherein the cell density is from about 300 to about 900 cpsi.
8 . The parallel passage adsorbent volume of claim 4 , wherein the cell wall thickness of the PPAV is from about 0.1 mm to about 0.5 mm.
9 . The parallel passage adsorbent volume of claim 1 , wherein the PPAV has a BWC of less than about 10 g/dL.
10 . The parallel passage adsorbent volume of claim 9 , wherein the PPAV has a BWC of less than about 9.5 g/dL.
11 . The parallel passage adsorbent volume of claim 4 , wherein the PPAV has an incremental adsorption capacity (IAC) between 5% and 50% n-butane at 25° C. of less than 45 g/L.
12 . The parallel passage adsorbent volume of claim 1 , wherein the PPAV is a honeycomb or cylindrical honeycomb structure.
13 . The parallel passage adsorbent volume of claim 1 , wherein the activated carbon comprises a material derived from at least one 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, or a combination thereof.
14 . A parallel passage adsorbent volume (PPAV) comprising activated carbon, wherein the PPAV includes an outer surface and a plurality of parallel passages or channels extending therethrough parallel to the outer surface, and wherein the parallel passages or channels are configured to have at least one of an average channel hydraulic diameter (t c,Dh ) of less than or equal to 1.25 mm, a hydraulic diameter cell pitch (CP Dh ) of less than or equal to 1.45 mm or a combination thereof, and a butane working capacity (BWC) of less than 10 g/dL.
15 . The parallel passage adsorbent volume of claim 14 , wherein the average channel hydraulic diameter (t c, Dh ) is less than or equal to 1.20.
16 . The parallel passage adsorbent volume of claim 14 , wherein the hydraulic diameter cell pitch (CP Dh ) is less than or equal to 1.40 mm.
17 . The parallel passage adsorbent volume of claim 14 , wherein the PPAV further comprises at least one of the following: (i) a plurality channel width (t c, avg ) of less than about 1.25 mm; (ii) a plurality channel width cell pitch (CP tc , avg) of less than about 1.5 mm; (iii) a cell density of from about 285 to about 1000 cpsi; (iv) a cell wall thickness of less than about 0.5 mm; (v) an incremental adsorption capacity between 5% and 50% n-butane at 25 C of less than about 50 g/L; or (vi) a combination thereof.
18 . The parallel passage adsorbent volume of claim 17 , wherein the plurality channel width (t c, avg ) of the PPAV is less than about 1.20 mm.
19 . The parallel passage adsorbent volume of claim 17 , wherein the plurality channel width cell pitch (CP tc, avg ) of the PPAV is less than about 1.40 mm.
20 . The parallel passage adsorbent volume of claim 17 , wherein the cell density is from about 300 to about 900 cpsi.
21 . The parallel passage adsorbent volume of claim 17 , wherein the cell wall thickness of the PPAV is from about 0.1 mm to about 0.5 mm.
22 . The parallel passage adsorbent volume of claim 17 , wherein the PPAV has a BWC of less than about 9.5 g/dL.
23 . The parallel passage adsorbent volume of claim 17 , wherein the PPAV has an incremental adsorption capacity (IAC) between 5% and 50% n-butane at 25° C. of less than 45 g/L.
24 . The parallel passage adsorbent volume of claim 14 , wherein the PPAV is a honeycomb or cylindrical honeycomb structure.