Purification of an oil-containing liquid using a surface treated permeable inorganic membrane

Claim 2

A process for purifying an oil-containing liquid to remove aqueous and solid impurities which comprises: (a) maintaining an oil-containing liquid within a temperature range of from just above the freezing point of the liquid to just below its boiling point; (b) passing said liquid through a permeable inorganic membrane comprising a metal selected from the group consisting of Sc, Y, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu, Ag, Au, Zn, Cd, Hg, B, Al, Ga, In, Tl, Ge, Sn, Pb, As, Sb, Bi, elements in the lanthanide series and the actinide series, mixtures thereof, mixtures of Groups IIa (Be, Mg, Ca, Sr and Ba) and VIb (Se and Te), and a ceramic selected from the group consisting of an oxide, sulfide, boride, carbide, or nitride of one or more of said metals which has been previously treated by contacting the membrane with an organic reactant selected from the group consisting of a phosphonic acid, a phosphinic acid, a monocarboxylic acid, a dicarboxylic acid, a boronic acid, a phosphoric acid ester and a precursor which decomposes upon contact with said inorganic membrane to from one of said organic reactants to form a layer of said organic reactant thereon; and (c) maintaining a pressure on said oil-containing liquid within a range of form about 2 psig to about 1200 psig as said liquid passes through said treated inorganic membrane.

Claim 3

The process of claim 1 wherein said permeable inorganic membrane has been treated to form a hydrophobic layer of said organic reactant thereon.

Claim 4

The process of claim 1 wherein said permeable inorganic membrane has been treated to form a monomolecular layer of said organic reactant thereon.

Claim 5

The process of claim 3 wherein said treated permeable inorganic membrane has a pore size, after treatment, within a range of from about 35 Å up to about 15 microns.

Claim 6

The process of claim 3 wherein said oil-containing liquid is maintained within a temperature range of from about 0° C. to about 500° C. as it is passed through said treated inorganic membrane.

Claim 7

The process of claim 3 which includes the further steps of: (d) interrupting said passing of said oil-containing liquid through said treated membrane; and (e) physically purging said treated membrane to remove solids from said membrane.

Claim 8

The process of claim 6 wherein said step of physically purging said treated membrane to remove solids further comprises backflushing said treated membrane.

Claim 9

The process of claim 3 which includes the further steps of: (d) interrupting said passing of said oil-containing liquid through said treated membrane; and (e) physically purging said treated membrane to remove organic deposits from said membrane.

Claim 10

The process of claim 3 which includes the further steps of: (d) interrupting said passing of said oil-containing liquid through said treated membrane; and (e) contacting said treated membrane with one or more chemicals capable of removing solids from said membrane.

Claim 11

The process of claim 1 which further comprises contacting said treated membrane with one or more chemicals selected from the group consisting of one or more acids, one or more bases, one or more organic solvents or surfactants, one or more chelating agents, and mixtures of the same.

Claim 12

The process of claim 9 wherein said step of contacting said treated membrane with one or more chemicals capable of removing solids from said membrane further comprises contacting said treated membrane with an acidic or basic chemical having a pH ranging from 1 to 14.

Claim 13

The process of claim 3 wherein said treated permeable inorganic membrane comprises a permeable material selected from the group consisting of a metal, a ceramic, a metal coated ceramic and a ceramic coated metal.

Claim 14

The process of claim 12 wherein said metal, metal coated ceramic, or ceramic coated metal comprises a metal selected from the group consisting of Sc, Y, Ti, Zr, Hf, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu, Ag, Au, Zn, Cd, Hg, B, Al, Ga, In, Tl, Ge, Sn, Pb, As, Sb, Bi, elements in the lanthanide series and the actinide series, mixtures thereof, and mixtures of Groups IIa (Be, Mg, Ca, Sr and Ba) and VIb (Se and Te).

Claim 15

The process of claim 12 wherein said ceramic, metal coated ceramic, or ceramic coated metal comprises a ceramic selected from the group consisting of an oxide, sulfide, boride, carbide, or nitride of a metal selected from the group consisting of Sc, Y, Ti, Zr, Hf, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu, Ag, Au, Zn, Cd, Hg, B, Al, Ga, In, Tl, Ge, Sn, Pb, As, Sb, Bi, elements in the lanthanide series and the actinide series, mixtures thereof, and mixtures of Groups IIa (Be, Mg, Ca, Sr and Ba) and VIb (Se and Te).

Claim 16

The process of claim 12 wherein said treated permeable inorganic membrane comprises a metal inorganic membrane material selected from the group consisting of Ti, Ta, W, Al, Sn, Zn, Co, Zr, Fe, Cr-Ni-Fe stainless steel alloys, Ni, Cr, Ru, Os, Rh, Ir, Pd, Pt, Ag and Au.

Claim 17

The process of claim 12 wherein said treated permeable inorganic membrane comprises a metal oxide/hydroxide inorganic membrane material selected from the group consisting of aluminum oxide, iron oxide, titanium oxide, zirconium oxide and a zeolite.

Claim 18

The process of claim 16 wherein said treated permeable inorganic membrane comprises a metal oxide/hydroxide inorganic membrane material selected from the group consisting of aluminum oxide and zirconium oxide.

Claim 19

The process of claim 3 wherein said treated permeable inorganic membrane has been treated with one or more phosphonic acids having the formula RPO(OH) 2 , where R may comprise a 1-30 carbon-containing group selected from the group consisting of aliphatic hydrocarbons, aromatic hydrocarbons, aldehydes, ketones, amines, amides, thioamides, imides, lactams, anilines, pyridines, piperidines, carbohydrates, thiocyanates, esters, lactones, ethers, alkenes, alkynes, alcohols, nitriles, oximes, organosilicones, ureas, thioureas, perfluoro organic groups, perchloro organic groups, perbromo organic groups and combinations of these groups.

Claim 20

The process of claim 18 wherein said phosphonic acid molecule may also include one or more inorganic groups substituted thereon selected from the group consisting of halogens, nitrates, phosphates, phosphinates, phosphinites, phosphonates and quaternary ammonium salts.

Claim 21

The process of claim 3 wherein said treated permeable inorganic membrane has been treated with one or more phosphinic acids having the formula RR'PO(OH), where R' may be hydrogen and both R and R' may each be comprised of a 1-30 carbon-containing group selected from the group consisting of aliphatic hydrocarbons, aromatic hydrocarbons, aldehydes, ketones, amines, amides, thioamides, imides, lactams, anilines, pyridines, piperidines, carbohydrates, thiocyanates, esters, lactones, ethers, alkenes, alkynes, alcohols, nitriles, oximes, organosilicones, ureas, thioureas, perfluoro organic groups, perchloro organic groups, perbromo organic groups and combinations of these groups.

Claim 22

The process of claim 20 wherein said phosphinic acid molecule may also include one or more inorganic groups substituted thereon selected from the group consisting of halogens, nitrates, phosphates, phosphinates, phosphinites, phosphonates and quaternary ammonium salts.

Claim 23

The process of claim 3 wherein said treated permeable inorganic membrane has been treated with one or more carboxylic acids selected from the group consisting of: (a) one or more monocarboxylic acids having the formula R"(COOH); (b) one or more dicarboxylic acids having the formula R"(COOH) 2 ; and (c) mixtures of the same; where R" may comprise a 2-30 carbon-containing group selected from the group consisting of aliphatic hydrocarbons, aromatic hydrocarbons, aldehydes, ketones, amines, amides, thioamides, imides, lactams, anilines, pyridines, piperidines, carbohydrates, thiocyanates, esters, lactones, ethers, alkenes, alkynes, alcohols, nitriles, oximes, organosilicones, ureas, thioureas, perfluoro organic groups, perchloro organic groups, perbromo organic groups and combinations of these groups.

Claim 24

The process of claim 22 wherein said carboxylic acid molecule may also include one or more inorganic groups substituted thereon selected from the group consisting of halogens, nitrates, phosphates, phosphinates, phosphinites, phosphonates and quaternary ammonium salts.

Claim 25

The process of claim 3 wherein said treated permeable inorganic membrane has been treated with one or more boronic acids having the formula RB(OH) 2 , where R may comprise a 1-30 carbon-containing group selected from the group consisting of aliphatic hydrocarbons, aromatic hydrocarbons, aldehydes, ketones, amines, amides, thioamides, imides, lactams, anilines, pyridines, piperidines, carbohydrates, thiocyanates, esters, lactones, ethers, alkenes, alkynes, alcohols, nitriles, oximes, organosilicones, ureas, thioureas, perfluoro organic groups, perchloro organic groups, perbromo organic groups and combinations of these groups.

Claim 26

The process of claim 24 wherein said boronic acid molecule may also include one or more inorganic groups substituted thereon selected from the group consisting of halogens, nitrates, phosphates, phosphinates, phosphinites, phosphonates and quaternary ammonium salts.

Claim 27

The process of claim 3 wherein said treated permeable inorganic membrane has been treated with a phosphoric acid ester selected from the group consisting of: (a) one or more phosphoric acid esters having the formula (RO)PO(OH) 2 ; (b) one or more phosphoric acid diesters having the formula (RO)(R'O)PO(OH); and (c) mixtures of the same; where R or R' may each comprise a 1-30 carbon-containing group selected from the group consisting of aliphatic hydrocarbons, aromatic hydrocarbons, aldehydes, ketones, amines, amides, thioamides, imides, lactams, anilines, pyridines, piperidines, carbohydrates, thiocyanates, esters, lactones, ethers, alkenes, alkynes, alcohols, nitriles, oximes, organosilicones, ureas, thioureas, perfluoro organic groups, perchloro organic groups, perbromo organic groups and combinations of these groups.

Claim 28

The process of claim 26 wherein said phosphoric acid ester molecule may also include one or more inorganic groups substituted thereon selected from the group consisting of halogens, nitrates, phosphates, phosphinates, phosphinites, phosphonates and quaternary ammonium salts.

Claim 29

A process for purifying an oil-containing liquid to remove aqueous and solid impurities which comprises: (a) heating said oil-containing liquid to a temperature range of from about 0° C. to about 500° C. and maintaining said liquid within said temperature range during said process; (b) passing said liquid through an inorganic membrane comprising aluminum oxide or zirconium oxide, said membrane having been previously treated by contact with an organic reactant selected from the group consisting of a phosphonic acid, a phosphinic acid, a monocarboxylic acid, a dicarboxylic acid, a boronic acid, a phosphoric acid ester, and a precursor which decomposes upon contact with said inorganic membrane to form one of said organic reactants to form a monomolecular layer of said organic reactant thereon whereby said treated inorganic membrane has a pore size, after treatment, within a range of from about 5 Å to about 1000 microns; and (c) maintaining a pressure on said oil-containing liquid within a range of from about 2 psig to about 1200 psig as said liquid passes through said treated inorganic membrane.

Claim 30

A process for purifying an oil-containing liquid to remove aqueous and solid impurities which comprises: (a) heating said oil-containing liquid to a temperature range of from about 0° C. to about 500° C. and maintaining said liquid within said temperature range during said process; (b) passing said liquid through an inorganic membrane comprising aluminum oxide or zirconium oxide, said membrane having been previously treated by contact with an organic reactant selected from the group consisting of a phosphonic acid, a phosphinic acid, a monocarboxylic acid, a dicarboxylic acid, a boronic acid, a phosphoric acid ester, and a precursor which decomposes upon contact with said inorganic membrane to form one of said organic reactants to form a monomolecular layer of said organic reactant thereon whereby said treated inorganic membrane has a pore size, after treatment, within a range of from about 5 Å to about 1000 microns; and (c) maintaining a pressure on said oil-containing liquid within a range of from about 2 psig to about 1200 psig as said liquid passes through said treated inorganic membrane.

Claim 31

The process of claim 28 which includes the further steps of: (a) interrupting said passing of said oil-containing liquid through said treated membrane; and (b) physically purging said treated membrane to remove solids from said membrane.

Claim 32

The process of claim 28 which includes the further step of: (a) interrupting said passing of said oil-containing liquid through said treated membrane; and (b) contacting said treated membrane with one or more chemicals capable of removing solids from said membrane.

Claim 33

A process for purifying an oil-containing liquid to remove aqueous and solid impurities which comprises: (a) heating said oil-containing liquid to a temperature range of from about 0° C. to about 500° C. and maintaining said liquid within said temperature range during said process; (b) passing said liquid through a permeable inorganic membrane comprising a metal selected from the group consisting of Sc, Y, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu, Ag, Au, Zn, Cd, Hg, B, Al, Ga, In, Tl, Ge, Sn, Pb, As, Sb, Bi, elements in the lanthanide series and the actinide series, mixtures thereof, mixtures of Groups IIa (Be, Mg, Ca, Sr and Ba) and VIb (Se and Te), and a ceramic selected from the group consisting of an oxide, sulfide, boride, carbide, or nitride of one or more of said metals, said membrane having been previously treated by contact with an organic reactant selected from the group consisting of a phosphonic acid, a phosphinic acid, a monocarboxylic acid, a dicarboxylic acid, a boronic acid, a phosphoric acid ester and a precursor which decomposes upon contact with said inorganic membrane to form a monomolecular layer of said organic reactant thereon, said inorganic membrane having a pore size of about 5 Å to 1000 microns; (c) maintaining a pressure on said oil-containing liquid within a range of from about 2 psig to about 1200 psig as said liquid passes through said treated inorganic membrane; (d) interrupting said passing of said oil-containing liquid through said treated membrane; and (e) removing solids from said membrane.

Claim 34

A process for purifying an oil-containing liquid to remove aqueous and solid impurities which comprises: (a) heating said oil-containing liquid to a temperature range of from about 0° C. to about 500° C. and maintaining said liquid within said temperature range during said process; (b) passing said liquid through a permeable inorganic membrane comprising a metal selected from the group consisting of Sc, Y, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu, Ag, Au, Zn, Cd, Hg, B, Al, Ga, In, Tl, Ge, Sn, Pb, As, Sb, Bi, elements in the lanthanide series and the actinide series, mixtures thereof, mixtures of Groups IIa (Be, Mg, Ca, Sr and Ba) and VIb (Se and Te), and a ceramic selected from the group consisting of an oxide, sulfide, boride, carbide, or nitride of one or more of said metals, said membrane having been previously treated by contact with an organic reactant selected from the group consisting of a phosphonic acid, a phosphinic acid, a monocarboxylic acid, a dicarboxylic acid, a boronic acid, a phosphoric acid ester and a precursor which decomposes upon contact with said inorganic membrane to form a monomolecular layer of said organic reactant thereon, said inorganic membrane having a pore size of about 5 Å to 1000 microns; (c) maintaining a pressure on said oil-containing liquid within a range of from about 2 psig to about 1200 psig as said liquid passes through said treated inorganic membrane; (d) interrupting said passing of said oil-containing liquid through said treated membrane; and (e) removing solids from said membrane.