US2007125685A1PendingUtilityA1
Method for removing calcium from crude oil
Est. expiryDec 2, 2025(expired)· nominal 20-yr term from priority
C10G 53/10C10G 53/04C10G 53/02C10G 21/27C10G 21/12C10G 29/20C10G 53/06
48
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Claims
Abstract
Methods for reducing calcium deposition along surfaces in contact with the water phase of a resolved water/oil emulsion are disclosed. High calcium crude oil and the like are contacted with a sequestrant to form a sequestered calcium containing complex that partitions to the water phase in the resolved emulsion. A specifically formulated polymeric deposit control agent is added to the water phase to inhibit calcium deposit formation therein and along surfaces in contact with the water phase.
Claims
exact text as granted — not AI-modified1 . Method for reducing calcium content in a liquid hydrocarbonaceous medium comprising:
a. contacting said liquid hydrocarbonaceous medium with a metal sequestering agent to form a sequestered calcium containing complex; b. contacting said liquid hydrocarbonaceous medium with an aqueous medium to form an emulsion whereby upon resolution of said emulsion at least a portion of said sequestered calcium containing complex remains in said aqueous medium; and c. contacting said aqueous medium with a water soluble or water dispersible polymer having the formula I to inhibit calcium deposit formation therein or along surfaces in contact with said aqueous medium, wherein said polymer has the formula: wherein E is the repeat unit remaining after polymerization of an ethylenically unsaturated compound; R 1 is H or lower (C 1 -C 6 ) alkyl; G is lower (C 1 -C 6 ) alkyl or carbonyl; Q is O or NH; R 2 is lower (C 1 -C 6 ) alkyl; hydroxy lower (C 1 -C 6 ) alkyl, lower (C 1 -C 6 ) alkyl sulfonic acid -(Et-O)— n —-(iPr-O)— n or —(Pr—O—) n wherein n ranges from about 1 to 100 alkyl, and R 3 is H or XZ wherein X is an anionic radical selected from the group consisting of SO 3 , PO 3 or COO; Z is H or hydrogens or any other water soluble cationic moiety which counterbalances the valence of the anionic radical X; F, when present, is a repeat unit having the Formula II: wherein X and Z are the same as in Formula I; R 4 is H or (C 1 -C 6 ) lower alkyl, R 5 is a hydroxy substituted alkyl or alkylene having from 1 to 6 atoms, and XZ may or may not be present; c and d are positive integers, e is a non-negative integer, and j is 0 or 1.
2 . Method as recited in claim 1 wherein from about 1 to 300 ppm of said polymer (I) is brought into contact with said aqueous medium, based on one million parts of said aqueous medium.
3 . Method a recited in claim 2 wherein from about 1 to 100 ppm of said polymer (I) is brought into contact with said aqueous medium.
4 . Method as recited in claim 3 wherein said liquid hydrocarbonaceous medium has a calcium content of greater than about 30 ppm calcium based upon one million parts of said liquid hydrocarbonaceous medium.
5 . Method as recited in claim 4 wherein said liquid hydrocarbonaceous medium is crude oil.
6 . Method as recited in claim 5 wherein said metal sequestering agent is citric acid or salt thereof and wherein said sequestered calcium containing complex is calcium citrate.
7 . Method as recited in claim 6 wherein said polymer I is a member or members selected from the group consisting of
1) AA/AHPSE; 2) AA/APES; 3) AA/AMPS; 4) AA/APES/AHPSE 5) AA/MA/APES 6) AA/AMPS/APES
8 . Method as recited in claim 7 wherein said polymer I is
1) AA/AHPSE; 2) AA/APES; or 3) AA/AMPS
9 . Method as recited in claim 8 wherein said polymer I is AA/AHPSE.
10 . Method as recited in claim 8 wherein said polymer I is AA/APES.
11 . Method as recited in claim 8 wherein said polymer I is AA/AMPS.
12 . Method as recited in claim 8 further comprising contacting said emulsion with an emulsion breaker.
13 . Method as recited in claim 12 further comprising adding a corrosion inhibitor to said liquid hydrocarbonaceous medium or to said aqueous medium.
14 . Method as recited in claim 8 wherein said emulsion is heated to a temperature of about 100° F.-300° F.
15 . Method as recited in claim 14 wherein said resolution of said emulsion is performed in a desalter apparatus.
16 . Method as recited in claim 15 wherein n in Formula I is from 1 to 20 and X in Formula I is selected from Na, K, Ca, and NH 4 .
17 . A method for reducing calcium deposition along surfaces in contact with a water phase formed as a result of resolution of an emulsion in a petroleum refinery desalter of the type wherein crude oil containing calcium therein is contacted with a sequestrant and a water wash to form said emulsion having a sequestered calcium complex in said emulsion, wherein at least a portion of said sequestered calcium complex partitions to said water phase upon said resolution, said method comprising contacting said sequestered calcium complex with a water soluble or water dispersible polymer having the Formula I:
wherein E is the repeat unit remaining after polymerization of an ethylenically unsaturated compound; R 1 is H or lower (C 1 -C 6 ) alkyl; G is lower (C 1 -C 6 ) alkyl or carbonyl; Q is O or NH; R 2 is lower (C 1 -C 6 ) alkyl; hydroxy lower (C 1 -C 6 ) alkyl, lower (C 1 -C 6 ) alkyl sulfonic acid; -(Et-O)— n —(iPr-O)— n or —(Pr—O—) n wherein n ranges from about 1 to 100, and R 3 is H or XZ wherein X is an anionic radical selected from the group consisting of SO 3 , PO 3 or COO; Z is H or hydrogens or any other water soluble cationic moiety which counterbalances the valence of the anionic radical X; F, when present, is a repeat unit having the Formula II:
wherein X and Z are the same as in Formula I. R 4 is H or (C 1 -C 6 ) lower alkyl, R 5 is a hydroxy substituted alkyl or alkylene having from 1 to 6 atoms, and XZ may or may not be present; c and d are positive integers, e is a non-negative integer, and j is 0 or 1.
18 . Method as recited in claim 17 wherein said crude oil comprises about 100 ppm calcium and greater.
19 . Method is recited in claim 18 wherein said sequestrant is citric acid and wherein said sequestered calcium complex is calcium citrate, and wherein about 1 to 300 ppm of said polymer I is added to said water phase based on one million parts of said water phase, said polymer comprising a member or members selected from the group consisting of
1) AA/AHPSE 2) AA/APES 3) AA/AMPS 4) AA/APES/AHPSE 5) AA/MA/APES 6) AA/AMPS/APES
20 . Method as recited in claim 19 wherein said polymer I is
1) AA/AHPSE; 2) AA/APES; or 3) AA/AMPS.
21 . Method as recited in claim 1 wherein said liquid hydrocarbonaceous medium is crude oil produced at an oil production site and wherein said steps (a) through (c) are performed proximate said site.Join the waitlist — get patent alerts
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