Process for recovering and upgrading hydrocarbons from oil shale

Claim 2

In a method for recovering hydrocarbons from oil shale by contacting the oil shale solids with water at a high temperature and under a super-atmospheric pressure, the improvement which comprises recovering the maximum yield of liquid hydrocarbons from said oil shale solids and upgrading the recovered liquid hydrocarbons by removing said liquid hydrocarbons from said oil shale solids and cracking, desulfurizing, and demetalating said liquid hydrocarbons by contacting said oil shale solids in the presence of an acidic or oxidative catalytic substance with a water-containing fluid under super-atmospheric pressure, at a temperature in the range of from at least 705° F., the critical temperature of water, to about 900° F., in the absence of externally supplied hydrogen, said catalytic substance being molecular oxygen, carbon dioxide, a metal bisulfate, a metal bisulfite, or a compound which reacts in situ to form a metal bisulfate or a metal bisulfite, wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.15 gram per milliliter and serves as an effective solvent for the removed liquid hydrocarbons; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for the removed liquid hydrocarbons and to thereby form separate phases.

Claim 3

The improved method of claim 1, which method comprises simultaneously removing the liquid hydrocarbons from the oil shale solids and cracking, desulfurizing, and demetalating said liquid hydrocarbons.

Claim 4

The method of claim 1, which method comprises removing the liquid hydrocarbons from the oil shale solids and subsequently cracking, desulfurizing, and demetalating said liquid hydrocarbons.

Claim 5

The improved method of claim 1 wherein said substance is sodium bisulfate.

Claim 6

The improved method of claim 1 wherein said substance is carbon dioxide.

Claim 7

In a method for recovering hydrocarbons from oil shale solids by contacting the oil shale solids with water at a high temperature and under a super-atmospheric pressure, the improvement which comprises recovering the maximum yield of liquid hydrocarbons from said oil shale solids and upgrading the recovered liquid hydrocarbons by removing said liquid hydrocarbons from said oil shale solids and cracking, desulfurizing, and demetalating said liquid hydrocarbons by contacting said oil shale solids in the presence of at least 10 psia of molecular oxygen with a water-containing fluid under super-atmospheric pressure, at a temperature in the range of from at least 705° F., the critical temperature of water, to about 900° F., in the absence of externally supplied hydrogen, wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.15 gram per milliliter and serves as an effective solvent for the removed liquid hydrocarbons; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for the removed liquid hydrocarbons and to thereby form separate phases.

Claim 8

In a method for recovering hydrocarbons from oil shale solids by contacting the oil shale solids with water at a high temperature and under a super-atmospheric pressure, the improvement which comprises recovering the maximum yield of liquid hydrocarbons from said oil shale solids and upgrading the recovered liquid hydrocarbons by removing said liquid hydrocarbons from said oil shale solids and cracking, desulfurizing, and demetalating said liquid hydrocarbons by contacting said oil shale solids in the presence of at least 10 psia of molecular oxygen with a water-containing fluid under super-atmospheric pressure, at a temperature in the range of from at least 705° F., the critical temperature of water, to about 900° F., in the absence of externally supplied hydrogen, wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.15 gram per milliliter and serves as an effective solvent for the removed liquid hydrocarbons; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for the removed liquid hydrocarbons and to thereby form separate phases.

Claim 9

The method of claim 6 wherein said contacting of said oil shale solids with said water-containing fluid is carried out in the presence of at least 15 psia of molecular oxygen.

Claim 10

The method of claim 6 wherein the source of said molecular oxygen is air.

Claim 11

In a method for recovering hydrocarbons from oil shale solids by contacting the oil shale solids with water at a high temperature and under a super-atmospheric pressure, the improvement which comprises recovering the maximum yield of liquid hydrocarbons from said oil shale solids and upgrading the recovered liquid hydrocarbons by removing said liquid hydrocarbons from said oil shale solids and cracking, desulfurizing, and demetalating said liquid hydrocarbons by contacting said oil shale solids in the presence of a material selected from the group consisting of metal bisulfate, metal bisufite, and a compound which reacts in situ to form said metal bisulfate or said metal bisulfite, said compound being sulfur trioxide or sulfur dioxide, with a water-containing fluid under super-atmospheric pressure, at a temperature in the range of from at least 705° F., the critical temperature of water, to about 900° F., in the absence of externally supplied hydrogen, wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.15 gram per milliliter and serves as an effective solvent for the removed liquid hydrocarbons; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for the removed liquid hydrocarbons and to thereby form separate phases.

Claim 12

In a method for recovering hydrocarbons from oil shale solids by contacting the oil shale solids with water at a high temperature and under a super-atmospheric pressure, the improvement which comprises recovering the maximum yield of liquid hydrocarbons from said oil shale solids and upgrading the recovered liquid hydrocarbons by removing said liquid hydrocarbons from said oil shale solids and cracking, desulfurizing, and demetalating said liquid hydrocarbons by contacting said oil shale solids in the presence of a material selected from the group consisting of metal bisulfate, metal bisufite, and a compound which reacts in situ to form said metal bisulfate or said metal bisulfite, said compound being sulfur trioxide or sulfur dioxide, with a water-containing fluid under super-atmospheric pressure, at a temperature in the range of from at least 705° F., the critical temperature of water, to about 900° F., in the absence of externally supplied hydrogen, wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.15 gram per milliliter and serves as an effective solvent for the removed liquid hydrocarbons; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for the removed liquid hydrocarbons and to thereby form separate phases.

Claim 13

The method of claim 9 wherein said metal bisulfate is the bisulfate of an alkali metal and said metal bisulfite is the bisulfite of an alkali metal.

Claim 14

The method of claim 9 wherein said contacting of the oil shale solids with a water-containing fluid is carried out in the presence of sodium bisulfate or a compound which reacts in situ to form sodium bisulfate, said compound being sulfur trioxide or sulfur dioxide, said sulfur dioxide reacting with oxygen to form sulfur trioxide.

Claim 15

The method of claim 9 wherein said metal bisulfate is sodium bisulfate and said metal bisulfite is sodium bisulfite.

Claim 16

The method of claim 10 wherein said metal bisulfate is sodium bisulfate and said metal bisulfite is sodium bisulfite.

Claim 17

The method of claim 9 wherein said compound is sulfur dioxide.