The present disclosure relates to hydrocarbon emission control systems. More specifically, the present disclosure relates to substrates coated with hydrocarbon adsorptive coating compositions, air intake systems, and evaporative emission control systems for controlling evaporative emissions of hydrocarbons from motor vehicle engines and fuel systems.

A blow-by gas recirculation device includes: a blow-by gas passage connected to an intake passage; an oil separator provided in the blow-by gas passage; and an adsorption/desorption member which is provided in the intake passage and/or the blow-by gas passage. The intake passage and the blow-by gas passage is located between the oil separator and the compressor of a turbocharger, and the adsorption/desorption member is configured so as to adsorb oil contained in a blow-by gas B and desorb the oil while the diameter of particles of the oil is increased.

A smart multi-modal vehicular air filtration management system including a first filter element and a second filter element disposed in a fresh air housing, wherein the fresh air housing has an inlet and an outlet. Additionally, a third filter element is provided which is disposed in a cabin housing, the cabin housing having one or more inlet. A fluid channel arranged between the fresh air and cabin housing. Finally, a diverter is included which is disposed near an outlet of the fresh air housing, wherein the diverter is configured to cause air to flow through the fresh air housing selectively through one or both of the first filter element and the second filter element.

A cleaning device includes a housing, an air driver, an ozone generator, and a catalyst. The housing defines an internal cavity. The housing has a first portion defining a first chamber of the internal cavity, a second portion defining a second chamber of the internal cavity, and an intermediate portion extending between the first portion and the second portion, and defining an intermediate chamber. The first chamber is connected to an inlet of the housing. The first portion having a first width. The second chamber is connected to an outlet of the housing. The second portion has a second width greater than the first width. The first portion, the intermediate portion, and the second portion are linearly aligned along a longitudinal axis of the housing. The air driver is positioned within the first chamber. The ozone generator is positioned within the intermediate chamber. The catalyst is positioned within the second chamber.

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.

A boil-off management system for a cryotank includes a boil-off conduit which is fluidically connectable to a cryotank via a boil-off valve. The boil-off management system further includes an air feed conduit and a mixing chamber for mixing a first medium (e.g., hydrogen) flowing in through the boil-off conduit with a second medium (e.g., air and/or oxygen) flowing in through the air feed conduit. A catalytic converter is arranged downstream of the mixing chamber and an outlet downstream of the catalytic converter. At least one enrichment apparatus is provided and configured to temporarily increase the proportion of the first medium flowing in through the boil-off conduit in relation to the second medium flowing in through the air feed conduit at the catalytic converter.

Proposed is a system for capturing carbon dioxide and sulfur oxide for ships that can capture carbon dioxide in flue gas using a basic alkaline mixture and use the captured carbon dioxide to capture sulfur oxides in the flue gas. The carbon dioxide and sulfur oxide capture system for ships uses sodium carbonate or sodium hydrogen carbonate prepared from the captured carbon dioxide as a desulfurization agent to capture sulfur oxides in the flue gas discharged from ships, thereby simultaneously producing carbon dioxide and sulfur oxides in one system.

A honeycomb filter includes: a honeycomb structure having porous partition walls disposed so as to surround cells, and plugging portions disposed at any one of ends on the inflow end face and the ends on the outflow end face, of cells. In a cross section perpendicular to an extending direction of the cells, a thickness T1 of the partition walls in a central portion including a center of gravity O of the cross section is 0.17 to 0.32 mm, a thickness T2 of the partition walls in an outer peripheral portion is 70 to 90% of the thickness T1, and the outer peripheral portion extends from an outer peripheral edge of the cross section of honeycomb structure by 6 to 12% of a radius r which is from the center of gravity O of the cross section to the outer peripheral edge.

An inerting fuel tank system comprising a closed tank and any number of flow impingement valves. The flow impingement valve allows uninhibited flow in one direction. In the reverse direction, the fluid flows back into the input flow stream thereby slowing / preventing the fluid flow outward. The flow impingement valve resists reverse flow of fluid out of a fuel tank vent due to sloshing or other flow dynamics.

A honeycomb structure including a honeycomb structure portion made of ceramics having an outer peripheral wall and partition walls disposed inside the outer peripheral wall and partitioning a plurality of cells; and a pair of electrode layers provided on an outer surface of the outer peripheral wall; wherein in a cross-section orthogonal to a direction in which the cells extend, assuming a coordinate value of a center of gravity O is 0, and a coordinate value of an inner peripheral surface of the outer peripheral wall is 1.00 R, an average value P.sub.1A of a porosity (%) of the partition walls in a range of coordinate values of 0 to 0.50 R and an average value P.sub.2A of a porosity (%) of the partition walls in a range of coordinate values of 0.50 R to 1.00 R satisfy a relationship of 1<P.sub.2A/P.sub.1A.