US2012131847A1PendingUtilityA1
Low sulfur tall oil fatty acid
Individually held — no corporate assignee on recordPriority: Aug 15, 2005Filed: Feb 9, 2012Published: May 31, 2012
Est. expiryAug 15, 2025(expired)· nominal 20-yr term from priority
C10G 2300/1014C10L 1/1888C10G 25/00C10L 1/02C10L 1/2381Y02P30/20Y02W30/74C10G 2300/44C11B 13/00C10G 2300/202
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Claims
Abstract
The invention relates to tall oil fatty acid compositions having low sulfur content, as well as methods of using and making the same.
Claims
exact text as granted — not AI-modified1 - 4 . (canceled)
5 . A method of making a low sulfur composition, comprising contacting and/or stirring a high sulfur composition comprising:
from 85 to 99.9% by weight of at least one saturated or unsaturated, monocarboxylic aliphatic hydrocarbon having a linear, branched, and/or cyclic chain of from 8 to 24 carbon atoms, a dimer thereof, a trimer thereof, or mixtures thereof; from 0.1 to 15% by weight of at least one cyclic fatty acid compound selected from the group consisting of natural resin-based acids obtained from residues of distillation of natural oils, amine carboxylates and ester and nitrile compounds of these acids; and greater than 25 ppm of sulfur
with an adsorbent having an average pore size of from 10 to 250 angstroms to form a low sulfur composition having less than or equal to 25 ppm of sulfur.
6 . The method according to claim 5 , wherein the high sulfur composition comprises greater than or equal to 30 ppm of sulfur.
7 . The method according to claim 5 , wherein the high sulfur composition comprises greater than or equal to 40 ppm of sulfur.
8 . The method according to claim 5 , wherein the adsorbent comprises at least one member selected from the group consisting of activated carbon containing compound, silica, alumina, clay, acid-activated clay, and diatomaceous earth.
9 . The method according to claim 5 , wherein the adsorbent has an average pore size of from 40 to 100 angstroms.
10 . The method according to claim 5 , wherein the adsorbent has an average pore size of from 50 to 75 angstroms.
11 . The method according to claim 5 , wherein the adsorbent is at least one adsorbent selected from the group consisting of silica and clay.
12 . The method according to claim 5 , wherein the adsorbent is at least one acid-activated clay.
13 . The method according to claim 5 , further comprising distilling the high sulfur composition prior to the contacting step.
14 . The method according to claim 13 , wherein the high sulfur composition comprises greater than or equal to 40 ppm of sulfur prior to said distilling step.
15 . The method according to claim 13 , wherein the high sulfur composition comprises greater than or equal to 60 ppm of sulfur prior to said distilling step.
16 . The method according to claim 13 , wherein the distilling is performed by a short-path distillation column.
17 . The method according to claim 16 , wherein the short-path distillation column is a wiped film evaporator.
18 . The method according to claim 13 , wherein the distilling is performed by a continuous column, a continuous fractionation distillation column, or a combination thereof.
19 - 30 . (canceled)
31 . A low sulfur composition prepared according to the method of claim 5 .
32 . The low sulfur composition of claim 31 , comprising less than or equal to 20 ppm of sulfur.
33 . The low sulfur composition of claim 31 , comprising less than or equal to 15 ppm of sulfur.Join the waitlist — get patent alerts
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