Two-stage centrifugal dedusting process

Claim 2

A process for dedusting particulate laden heavy oil derived from solid hydrocarbon-containing material, comprising the steps of: introducing solid hydrocarbon-containing material into a retort; introducing solid heat carrier material into said retort; retorting said solid hydrocarbon-containing material by contacting said solid hydrocarbon-containing material with said solid heat carrier material at a retorting temperature to liberate a mixture of hydrocarbons and entrained particulates of dust ranging in size from less than one micron to 1000 microns derived from said solid hydrocarbon-containing material; separating a heavy oil fraction laden with said particulates of dust from said mixture; heating said heavy oil fraction laden with said particulates of dust to a viscosity of less than 5 centistokes; feeding said heated fraction to a first centrifuge; centrifuging said heated fraction in said first centrifuge into a dedusted first stream of normally liquid heavy oil containing less than 1% by weight of said particulates and a first particulate laden residual stream containing a substantially higher concentration of said particulates then said oil fraction; injecting light oil derived from said solid hydrocarbon-containing material into said first centrifuge to enhance removal of said first particulate laden residual stream from said first centrifuge; feeding said first particulate laden residual stream injected with said light oil at a viscosity of less than 5 centistokes to a second centrifuge; centrifuging said first particulate laden residual stream injected with said light oil in said second centrifuge into a dedusted second stream of normally liquid oil including light oil containing less than 1% by weight of said particulates and a second particulate laden residual stream containing a substantially higher concentration of said particulates than said first particulate laden residual stream; heating said second particulate laden residual stream to vaporize said light oil and form a third particulate dust laden residual stream containing a higher concentration of said particulates than said second particulate dust laden residual stream; feeding said third particulate dust laden stream to a lift pipe; injecting air into said lift pipe to combust heavy oil contained in said third particulate dust laden stream and fluidize, entrain and propel said third particulate laden residual stream to a separation bin; and conveying said combusted third particulate laden residual stream to said retort to provide at least a portion of said solid heat carrier material.

Claim 3

A process in accordance with claim 1 wherein said hydrocarbon-containing material is selected from the group consisting of oil shale, tar sand, coal, lignite, peat and uintaite.

Claim 4

A process in accordance with claim 1 further including: removing retorted hydrocarbon-containing material from said retort; feeding said retorted hydrocarbon-containing material into said lift pipe; combusting, fluidizing, entraining and propelling said retorted hydrocarbon-containing material along with said third particulate laden residual stream upwardly in said lift pipe to said separation bin; and conveying said combusted, retorted, hydrocarbon-containing material along with said combusted, third particulate laden residual stream to said retort.

Claim 5

A process in accordance with claim 1 further including mixing said heavy oil fraction in a first vessel before said heavy oil fraction is fed to said first centrifuge.

Claim 6

A process in accordance with claim 4 wherein said heavy oil fraction is heated in said first vessel.

Claim 7

A process in accordance with claim 4 wherein said mixed heavy oil fraction is discharged from said first vessel and a portion of said discharged, heavy oil fraction is recirculated back to said first vessel.

Claim 8

A process in accordance with claim 6 wherein said discharged heavy oil fraction is heated before being recirculated back to said first vessel.

Claim 9

A process in accordance with claim 1 wherein said first particulate laden residual stream injected with said light oil is fed to a second vessel before being fed to said second centrifuge.

Claim 10

A process in accordance with claim 8 wherein said first particulate laden residual stream injected with light oil is mixed in said second vessel.

Claim 11

A process in accordance with claim 8 wherein said first particulate laden residual stream injected with light oil is heated in said second vessel.

Claim 12

A process in accordance with claim 8 wherein some of said light oil is vaporized in and removed from said second vessel.

Claim 13

A process in accordance with claim 8 wherein said first particulate laden residual stream is discharged from said second vessel and a portion of said discharged first particulate laden residual stream is recirculated back to said second vessel.

Claim 14

A process in accordance with claim 12 wherein said discharged first particulate laden residual stream is heated before being recirculated to said second vessel.

Claim 15

A process in accordance with claim 1 wherein said dedusted first stream is mixed with said dedusted second stream.

Claim 16

A process in accordance with claim 14 wherein said mixed dedusted streams are cooled.

Claim 17

A process in accordance with claim 1 wherein said heavy oil fraction is heated to a viscosity less than 2 centistokes before being fed to said first centrifuge.

Claim 18

A process in accordance with claim 1 wherein said first particulate laden residual stream injected with said light oil is fed at a viscosity of less than 2 centistokes to said second centrifuge.

Claim 19

A process in accordance with claim 1 wherein said dedusted streams each contain less than 0.3% by weight of said particulates.

Claim 20

A process for dedusting heavy shale oil, comprising the steps of: mixing dust laden heavy shale oil consisting of normally liquid heavy shale oil having a boiling point over 600° F. and from 25% to 50% by weight of entrained particulates of shale dust ranging in size from less than 1 micron to 1000 microns, in a first vessel to enhance uniform suspension of said shale dust; pumping a portion of said mixed dust laden heavy shale oil back to said first vessel to further enhance uniform suspension of said shale dust; heating said dust laden heavy shale oil to a temperature from 500° F. to 600° F. at atmospheric pressure to decrease the viscosity of said dust laden heavy shale oil to less than 5 centistokes; pumping said heated dust laden heavy shale oil to a first centrifuge; centrifuging said heated dust laden heavy shale oil in said first centrifuge into a dedusted first stream consisting of normally liquid heavy shale oil and less than 1% by weight of said shale dust and a first dust laden residual stream consisting of from 25% to 40% by weight of normally liquid heavy shale oil and from 60% to 75% by weight of said shale dust; injecting light shale oil into said first centrifuge to flush said first dust laden residual stream out of said first centrifuge; feeding said first dust laden residual stream to a second vessel; mixing said first dust laden residual stream in said second vessel to enhance uniform suspension of said shale dust in said first dust laden residual stream; pumping a portion of said mixed residual stream back to said second vessel to further enhance uniform suspension of said shale dust; maintaining said mixed residual stream at a viscosity of less than 5 centistokes; pumping said mixed residual stream to a second centrifuge; centrifuging said residual stream in said second centrifuge into a dedusted second stream of normally liquid heavy shale oil diluted with light shale oil and less than 1% by weight of said shale dust and a second dust laden residual stream consisting of from 25% to 40% by weight of normally liquid heavy shale oil diluted with light shale oil and 60% to 75% by weight of said shale dust; feeding said second dust laden residual stream to a dryer; heating said second dust laden residual stream in said dryer to at least about 500° F. to vaporize said light shale oil and form a third dust laden residual stream consisting of from 10% to 20% by weight normally liquid heavy shale oil and from 80% to 90% by weight of said shale dust; removing said light shale oil vapors from said dryer; conveying said third dust laden residual stream to a lift pipe; combusting said normally liquid heavy shale oil in said third particulate laden residual stream in said lift pipe leaving a spent stream; conveying said spent stream to a retort; and retorting raw oil shale in said retort by mixing solid heat carrier material containing said spent stream with said raw oil shale in said retort.

Claim 21

A process for dedusting heavy shale oil, comprising the steps of: mixing dust laden heavy shale oil consisting of normally liquid heavy shale oil having a boiling point over 600° F. and from 25% to 50% by weight of entrained particulates of shale dust ranging in size from less than 1 micron to 1000 microns, in a first vessel to enhance uniform suspension of said shale dust; pumping a portion of said mixed dust laden heavy shale oil back to said first vessel to further enhance uniform suspension of said shale dust; heating said dust laden heavy shale oil to a temperature from 500° F. to 600° F. at atmospheric pressure to decrease the viscosity of said dust laden heavy shale oil to less than 5 centistokes; pumping said heated dust laden heavy shale oil to a first centrifuge; centrifuging said heated dust laden heavy shale oil in said first centrifuge into a dedusted first stream consisting of normally liquid heavy shale oil and less than 1% by weight of said shale dust and a first dust laden residual stream consisting of from 25% to 40% by weight of normally liquid heavy shale oil and from 60% to 75% by weight of said shale dust; injecting light shale oil into said first centrifuge to flush said first dust laden residual stream out of said first centrifuge; feeding said first dust laden residual stream to a second vessel; mixing said first dust laden residual stream in said second vessel to enhance uniform suspension of said shale dust in said first dust laden residual stream; pumping a portion of said mixed residual stream back to said second vessel to further enhance uniform suspension of said shale dust; maintaining said mixed residual stream at a viscosity of less than 5 centistokes; pumping said mixed residual stream to a second centrifuge; centrifuging said residual stream in said second centrifuge into a dedusted second stream of normally liquid heavy shale oil diluted with light shale oil and less than 1% by weight of said shale dust and a second dust laden residual stream consisting of from 25% to 40% by weight of normally liquid heavy shale oil diluted with light shale oil and 60% to 75% by weight of said shale dust; feeding said second dust laden residual stream to a dryer; heating said second dust laden residual stream in said dryer to at least about 500° F. to vaporize said light shale oil and form a third dust laden residual stream consisting of from 10% to 20% by weight normally liquid heavy shale oil and from 80% to 90% by weight of said shale dust; removing said light shale oil vapors from said dryer; conveying said third dust laden residual stream to a lift pipe; combusting said normally liquid heavy shale oil in said third particulate laden residual stream in said lift pipe leaving a spent stream; conveying said spent stream to a retort; and retorting raw oil shale in said retort by mixing solid heat carrier material containing said spent stream with said raw oil shale in said retort.

Claim 22

A process in accordance with claim 19 wherein said first dust laden residual stream consists of 30% by weight of normally liquid heavy shale oil and 70% by weight of said shale dust.

Claim 23

A process in accordance with claim 19 wherein said second dust laden residual stream consists of 30% by weight of said normally liquid heavy shale oil diluted with light shale oil and 70% by weight of said shale dust.

Claim 24

A process in accordance with claim 19 wherein said shale oil is heated to a temperature from 100° F. to 300° F. before being pumped to said second centrifuge.

Claim 25

A process in accordance with claim 19 wherein said shale oil is heated to about 250° F. before being pumped to said second centrifuge.

Claim 26

A process in accordance with claim 19 wherein said dedusted streams contain from 80% to 95% by weight of said heavy shale oil from said dust laden heavy shale oil.

Claim 27

A process in accordance with claim 19 wherein said dedusted streams contain at least 90% by weight of said heavy shale oil from said dust laden heavy oil.

Claim 28

A process in accordance with claim 19 wherein said dedusted streams each contain less than 0.3% by weight of said shale dust.

Claim 29

A process for producing and dedusting shale oil, comprising the steps of: introducing raw oil shale into a retort; introducing solid heat carrier material containing spent oil shale and a spent stream into said retort at a temperature from 1000° F. to 1400° F.; retorting said raw oil shale by mixing said raw oil shale with said solid heat carrier material in said retort at a retorting temperature from 850° F. to 1000° F. to liberate a mixture of hydrocarbons and entrained particulates of shale dust selected from the group consisting of raw oil shale, retorted oil shale and spent oil shale, said shale dust ranging in size from less than one micron to 1000 microns; separating a light oil fraction and a 15% to 35% by weight, particulate laden heavy oil fraction consisting of normally liquid heavy shale oil having a boiling point over 600° F. and from 25% to 50% by weight of said entrained particulates of shale dust; mixing said particulate laden heavy oil fraction in a first vessel to enhance uniform suspension of said shale dust; pumping a portion of said mixed fraction back to said first vessel to further enhance uniform suspension of said shale dust; heating said particulate laden heavy oil fraction to a temperature from 500° F. to 600° F. at atmospheric pressure to decrease the viscosity of said particulate laden heavy oil fraction to less than 5 centistokes; pumping said heated fraction to a first centrifuge; centrifuging said heating fraction in said first centrifuge into a dedusted first stream consisting of normally liquid heavy shale oil and less than 1% by weight of said shale dust and a first particulate laden residual stream consisting of from 25% to 40% by weight of normally liquid heavy shale oil and from 60% to 75% by weight of said shale dust; injecting light shale oil derived from said light oil fraction into said first centrifuge to flush said first particulate laden residual stream out of said first centrifuge; feeding said first particulate laden residual stream admixed with said light shale oil at a temperature from 500° F. to 600° F. to a second vessel; vaporizing some of said light shale oil from said admixture; mixing said admixture in said second vessel to enhance uniform suspension of said shale dust in said admixture; removing said light shale oil vapors from said admixture in said second vessel leaving a residue consisting of normally liquid heavy shale oil diluted with normally liquid light shale oil; pumping a portion of said residue back to said second vessel to further enhance uniform suspension of said shale dust in said admixture; maintaining a viscosity of less than 5 centistokes in said residue; pumping said residue to a second centrifuge; centrifuging said residue in said second centrifuge into a dedusted second stream consisting of normally liquid heavy shale oil diluted with said light shale oil and less than 1% by weight of said shale dust and a second particulate laden residual stream consisting of from 25% to 40% by weight of normally liquid heavy shale oil diluted with said light shale oil and from 60% to 75% by weight of said shale dust; feeding said second particulate laden residual stream to a dryer; heating said second particulate laden residual stream in said dryer to at least about 500° F. to vaporize said light shale oil and form a third particulate laden residual stream consisting of from 10% to 20% by weight normally liquid heavy shale oil and from 80% to 90% by weight of said shale dust; removing said light shale oil vapors from said dryer; conveying said third particulate laden residual stream to a lift pipe; combusting said heavy shale oil in said third particulate laden residual stream in said lift pipe to leave a spent stream; and conveying said spent stream to said retort to provide at least a portion of said solid heat carrier material.

Claim 30

A process for producing and dedusting shale oil, comprising the steps of: introducing raw oil shale into a retort; introducing solid heat carrier material containing spent oil shale and a spent stream into said retort at a temperature from 1000° F. to 1400° F.; retorting said raw oil shale by mixing said raw oil shale with said solid heat carrier material in said retort at a retorting temperature from 850° F. to 1000° F. to liberate a mixture of hydrocarbons and entrained particulates of shale dust selected from the group consisting of raw oil shale, retorted oil shale and spent oil shale, said shale dust ranging in size from less than one micron to 1000 microns; separating a light oil fraction and a 15% to 35% by weight, particulate laden heavy oil fraction consisting of normally liquid heavy shale oil having a boiling point over 600° F. and from 25% to 50% by weight of said entrained particulates of shale dust; mixing said particulate laden heavy oil fraction in a first vessel to enhance uniform suspension of said shale dust; pumping a portion of said mixed fraction back to said first vessel to further enhance uniform suspension of said shale dust; heating said particulate laden heavy oil fraction to a temperature from 500° F. to 600° F. at atmospheric pressure to decrease the viscosity of said particulate laden heavy oil fraction to less than 5 centistokes; pumping said heated fraction to a first centrifuge; centrifuging said heating fraction in said first centrifuge into a dedusted first stream consisting of normally liquid heavy shale oil and less than 1% by weight of said shale dust and a first particulate laden residual stream consisting of from 25% to 40% by weight of normally liquid heavy shale oil and from 60% to 75% by weight of said shale dust; injecting light shale oil derived from said light oil fraction into said first centrifuge to flush said first particulate laden residual stream out of said first centrifuge; feeding said first particulate laden residual stream admixed with said light shale oil at a temperature from 500° F. to 600° F. to a second vessel; vaporizing some of said light shale oil from said admixture; mixing said admixture in said second vessel to enhance uniform suspension of said shale dust in said admixture; removing said light shale oil vapors from said admixture in said second vessel leaving a residue consisting of normally liquid heavy shale oil diluted with normally liquid light shale oil; pumping a portion of said residue back to said second vessel to further enhance uniform suspension of said shale dust in said admixture; maintaining a viscosity of less than 5 centistokes in said residue; pumping said residue to a second centrifuge; centrifuging said residue in said second centrifuge into a dedusted second stream consisting of normally liquid heavy shale oil diluted with said light shale oil and less than 1% by weight of said shale dust and a second particulate laden residual stream consisting of from 25% to 40% by weight of normally liquid heavy shale oil diluted with said light shale oil and from 60% to 75% by weight of said shale dust; feeding said second particulate laden residual stream to a dryer; heating said second particulate laden residual stream in said dryer to at least about 500° F. to vaporize said light shale oil and form a third particulate laden residual stream consisting of from 10% to 20% by weight normally liquid heavy shale oil and from 80% to 90% by weight of said shale dust; removing said light shale oil vapors from said dryer; conveying said third particulate laden residual stream to a lift pipe; combusting said heavy shale oil in said third particulate laden residual stream in said lift pipe to leave a spent stream; and conveying said spent stream to said retort to provide at least a portion of said solid heat carrier material.

Claim 31

A process in accordance with claim 27 wherein said retorting temperature is from 900° F. to 960° F.

Claim 32

A process in accordance with claim 27 wherein said solid heat carrier material is introduced into said retort at a temperature from 1200° F. to 1300° F.

Claim 33

A process in accordance with claim 27 wherein said first particulate laden residual stream consists of 30% by weight of normally liquid heavy shale oil and 70% by weight of said shale dust.

Claim 34

A process in accordance with claim 27 wherein said second particulate laden residual stream consists of 30% by weight of said normally liquid heavy shale oil diluted with said light shale oil and 70% by weight of said shale dust.

Claim 35

A process in accordance with claim 27 wherein said shale oil is heated to a temperature from 100° F. to 300° F. before being pumped to said second centrifuge.

Claim 36

A process in accordance with claim 27 wherein said shale oil is heated to about 250° F. before being pumped to said second centrifuge.

Claim 37

A process in accordance with claim 27 wherein from 80% to 90% by weight of said normally liquid heavy shale oil from said particulate laden heavy oil fraction is dedusted and recovered in said dedusted streams.

Claim 38

A process in accordance with claim 27 wherein at least 90% by weight of said normally liquid heavy shale oil from said particulate laden heavy oil fraction is dedusted and recovered in said dedusted streams.

Claim 39

A process in accordance with claim 35 wherein said dedusted streams each contain less than 0.3% by weight of said shale dust.