Visbreaking of oils

Claim 2

A process for upgrading a substantially liquid hydrocarbon containing feed stream, which also contains metal impurities selected from the group consisting of nickel and vanadium compounds, comprising the step of intimately contacting said feed stream with a carbon monoxide containing gas, at a temperature ranging from about 300° C. to about 550° C. under such reaction conditions as will result in a hydrocarbon containing stream having a reduced level of metal impurities and an increased API 60 gravity, essentially in the absence of a homogeneous or heterogeneous catalyst and essentially in the absence of a second liquid phase which can extract any portion from the hydrocarbon containing feed stream.

Claim 3

A process in accordance with claim 1, wherein the carbon monoxide containing gas also comprises hydrogen.

Claim 4

A process in accordance with claim 1, wherein the carbon monoxide containing gas also comprises hydrogen and hydrogen sulfide.

Claim 5

A process in accordance with claim 1 wherein the substantially liquid hydrocarbon containing feed stream has an API 60 gravity ranging from about 4 to about 30, the vanadium content in said feed stream ranges from about 10 to about 1000 ppm, and the nickel content in said feed stream ranges from about 5 to about 500 ppm.

Claim 6

A process in accordance with claim 2 wherein the substantially liquid hydrocarbon containing feed stream has an API 60 gravity ranging from about 4 to about 30, its vanadium content ranges from about 10 to about 1000 ppm, and its nickel content ranges from about 5 to about 500 ppm.

Claim 7

A process in accordance with claim 3 wherein the substantially liquid hydrocarbon containing feed stream has an API 60 gravity ranging from about 4 to about 30, its vanadium content ranges from about 10 to about 1000 ppm, and its nickel content ranges from about 5 to about 500 ppm.

Claim 8

A process in accordance with claim 1 wherein said reaction conditions comprise a total gas pressure ranging from about 100 psig to about 10,000 psig.

Claim 9

A process in accordance with claim 2 wherein the volume ratio of carbon monoxide to hydrogen ranges from about 1:50 to about 200:1, and said reaction conditions comprise a total gas pressure ranging from about 100 psig to about 10,000 psig.

Claim 10

A process in accordance with claim 3, wherein the volume ratio of carbon monoxide to hydrogen ranges from about 1:50 to about 200:1, the volume ratio of carbon monoxide to hydrogen sulfide ranges from about 1:20 to about 500:1, and said reaction conditions comprise a total gas pressure ranging from about 100 psig to about 10,000 psig.

Claim 11

A process in accordance with claim 4 wherein said reaction conditions comprise a reaction temperature ranging from about 380° C. to about 450° C., a total pressure ranging from about 400 psig to about 5,000 psig, and a reaction time ranging from about 5 minutes to about 5 hours.

Claim 12

A process in accordance with claim 5 wherein the volume ratio of carbon monoxide to hydrogen ranges from about 1:10 to about 10:1, and the said reaction conditions comprise a reaction temperature ranging from about 380° C. to about 450° C., a total pressure ranging from about 400 psig to about 5,000 psig, and a reaction time ranging from about 5 minutes to about 5 hours.

Claim 13

A process in accordance with claim 6 wherein the volume ratio of carbon monoxide to hydrogen ranges from about 1:10 to about 10:1, the volume ratio of carbon monoxide to hydrogen sulfide ranges from about 1:5 to about 10:1 and the said reaction conditions comprise a reaction temperature ranging from about 380° C. to about 450° C., a total pressure ranging from about 400 psig to about 5,000 psig, and a reaction time ranging from about 5 minutes to about 5 hours.

Claim 14

A process in accordance with claim 1, wherein at least a portion of said metal impurities is converted to a precipitate, comprising the additional step of separating said precipitate from the liquid hydrocarbon stream having a reduced metal content and increased API 60 gravity.

Claim 15

A process in accordance with claim 13, wherein said separating step comprises distillation.

Claim 16

A process in accordance with claim 13, wherein said separating step comprises filtration.

Claim 17

A process in accordance with claim 14, wherein at least one heavy hydrocarbon-containing fraction resulting from said distillation is catalytically hydrotreated so as to produce a further purified hydrocarbon containing stream.

Claim 18

A process in accordance with claim 14, wherein at least one heavy hydrocarbon-containing fraction is catalytically cracked so as to convert at least a portion of said fraction to hydrocarbons of lower molecular weight.

Claim 19

A process in accordance with claim 16 wherein said further purified hydrocarbon containing stream is catalytically cracked so as to convert at least a portion of said stream to hydrocarbons of lower molecular weight.

Claim 20

A process comprising the step of (A) intimately contacting a substantially liquid hydrocarbon feed stream, which also contains metal impurities selected from the group consisting of nickel and vanadium compounds, with a carbon monoxide containing gas, at a temperature ranging from about 300° C. to about 550° C. under such reaction conditions as will result in a hydrocarbon containing stream having a reduced level of metal impurities and an increased API 60 gravity, essentially in the absence of a homogeneous or heterogeneous catalyst and essentially in the absence of a second liquid phase which can extract any portion from the hydrocarbon containing feed stream, wherein at least a portion of said metal impurities is converted to a precipitate dispersed in the liquid portion of said hydrocarbon containing stream.

Claim 21

A process comprising the step of (A) intimately contacting a substantially liquid hydrocarbon feed stream, which also contains metal impurities selected from the group consisting of nickel and vanadium compounds, with a carbon monoxide containing gas, at a temperature ranging from about 300° C. to about 550° C. under such reaction conditions as will result in a hydrocarbon containing stream having a reduced level of metal impurities and an increased API 60 gravity, essentially in the absence of a homogeneous or heterogeneous catalyst and essentially in the absence of a second liquid phase which can extract any portion from the hydrocarbon containing feed stream, wherein at least a portion of said metal impurities is converted to a precipitate dispersed in the liquid portion of said hydrocarbon containing stream.

Claim 22

A process in accordance with claim 19 further comprising the steps of (B) separating at least one liquid hydrocarbon-containing fraction being substantially free of solids from said hydrocarbon containing stream having a reduced level of metal impurities and an increased API 60 gravity; and (C) catalytically cracking said fraction so as to convert at least a portion of said fraction to hydrocarbons of lower molecular weight.