Separation media and methods especially useful for separating water-hydrocarbon emulsions having low interfacial tensions
Abstract
Separation media, separation modules and methods are provided for separating water from a water and hydrocarbon emulsion and include a fibrous nonwoven coalescence layer for receiving the water and hydrocarbon emulsion and coalescing the water present therein as a discontinuous phase to achieve coalesced water droplets having a size of 1 mm or greater, and a fibrous nonwoven drop retention layer downstream of the coalescence layer having a high BET surface area of at least 90 m 2 /g or greater sufficient to retain the size of the coalesced water droplets to allow separation thereof from the hydrocarbon.
Claims
exact text as granted — not AI-modified1 . Separation media for separating water from a water and hydrocarbon emulsion comprising:
a fibrous nonwoven coalescence layer for receiving the water and hydrocarbon emulsion and coalescing the water present therein as a discontinuous phase to achieve coalesced water droplets having a size of 1 mm or greater; and a fibrous nonwoven drop retention layer downstream of the coalescence layer having a high BET surface area of at least 90 m 2 /g or greater sufficient to retain the size of the coalesced water droplets to allow separation thereof from the hydrocarbon.
2 . The separation media of claim 1 , wherein the drop retention layer has a high BET surface area of at least 95 m 2 /g or greater.
3 . The separation media of claim 1 , wherein the drop retention layer has a high BET surface area of at least 100 m 2 /g or greater.
4 . The separation media of claim 1 , wherein the drop retention layer comprises a mixture of fibers having a high BET surface area and fibers having a low BET surface area.
5 . The separation media of claim 1 , wherein the drop retention layer comprises a resin binder.
6 . The separation media of claim 1 , wherein the resin binder includes a polar chemical group.
7 . The separation media of claim 1 , which further comprises at least one additional layer adjacent to one of the coalescence and drop retention layers.
8 . The separation media of claim 7 , wherein the at least one additional layer is positioned between the coalescence and drop retention layers.
9 . The separation media of claim 7 , wherein the at least one additional layer is positioned upstream of the coalescence layer.
10 . The separation media of claim 7 , wherein the at least one additional layer is positioned downstream of the drop retention layer.
11 . A separation module for separating water from a water and hydrocarbon emulsion comprising a housing having an inlet for the emulsion and respective outlets for water and dewatered hydrocarbon, and a separation media according to claim 1 within the housing.
12 . A method for separating water from a water and hydrocarbon emulsion comprising:
(a) passing a water and hydrocarbon emulsion through a fibrous nonwoven coalescence layer so as to coalesce the water present therein as a discontinuous phase to achieve coalesced water droplets having a size of 1 mm or greater; and (b) passing the hydrocarbon and coalesced water droplets through a downstream droplet retention layer having a high BET surface area of at least 90 m 2 /g or greater sufficient to retain the size of the coalesced water droplets; and (c) separating the coalesced water droplets from the hydrocarbon.
13 . The method of claim 12 , wherein the hydrocarbon has an interfacial tension (γ) of less than 25 dynes/cm.
14 . The method of claim 13 , wherein the hydrocarbon is a liquid fuel which comprises a surfactant.
15 . The method of claim 14 , wherein the liquid fuel is a fuel which comprises biodiesel.
16 . The method of claim 12 , wherein step (a) is practiced so that at least 90 wt. % of the water in the emulsion is coalesced into water droplets having a droplet size of 1 mm or greater.
17 . The method of claim 16 , wherein step (b) is practiced so that the coalesced water droplets retain a droplet size of 1 mm or greater.
18 . The method of claim 12 , wherein step (c) is practiced by allowing the water droplets to separate from the hydrocarbon by a density difference therebetween.Join the waitlist — get patent alerts
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