Solids precipitation and polymerization of asphaltenes in coal-derived liquids

Claim 2

A liquid-solids separation process for removal of unconverted coal and ash particulate solids from hydrogenated coal-derived liquids by extended solvent precipitation and settling which process consists essentially of: (a) adding to said coal-derived liquid one selected anti-solvent liquid naphtha fraction derived solely from the coal liquid without further hydrogenation and having a normal boiling range between about 300°-550° F.; (b) mixing said two liquid streams together upstream of a first solids precipitation and settling step maintained at superatmospheric pressure and maintaining the mixture at sufficient temperature and settling time in the settling step to produce polymerization of asphaltenes and substantial precipitation and settling of the solids, so as to provide a clarified overflow liquid portion and an underflow liquid portion having increased solids concentration; (c) withdrawing said overflow liquid portion containing substantially reduced concentration of solids and passing the stream to a second solvent precipitation step maintained at atmospheric pressure and at sufficient temperature to maintain a substantially liquid condition therein; and (d) withdrawing an overflow liquid product stream from said second precipitation step containing less than about 0.1 W % ash.

Claim 3

The process of claim 1, wherein at least a portion of said anti-solvent additive liquid in (a) is derived from said clarified overflow liquid portion, which is pressure-reduced to atmospheric pressure and phase separated, and the resulting overhead stream is recycled as part of the anti-solvent liquid added at (a).

Claim 4

The process of claim 1, wherein the first precipitation step conditions are maintained at 50-200 psig pressure and 500°-600° F. temperature.

Claim 5

The process of claim 1, wherein the additive anti-solvent liquid fraction is derived by fractionation from coal liquid streams and has a Kauri-butanal value between about 40 and 150.

Claim 6

The process of claim 1, wherein the ratio of the added anti-solvent liquid to coal derived liquid to provide the first settler feed liquid is between about 0.5 and 1.5, and the clarified overflow liquid portion contains 0.1 to 1.0 W % unconverted coal and ash solids.

Claim 7

The process of claim 1, wherein the solids concentration in the first settler underflow liquid is maintained between about 30 and 60 W % by varying its withdrawal rate, and the underflow liquid is pressure reduced and flashed to recover light fractions as an overhead product stream.

Claim 8

The process of claim 1, wherein the hydrogenated coal-derived liquid is passed through a centrifugal type liquid-solids separation step for partial removal of particulate solids upstream of step (a), and the centrifugal step underflow liquid stream is then passed to (a) for further removal of solids.

Claim 9

The process of claim 7, wherein the first settler overflow liquid stream is flashed at atmospheric pressure upstream of the second solids settling step to provide a portion of the anti-solvent liquid.

Claim 10

A liquid-solids separation process for removal of unconverted coal and ash particulate solids from hydrogenated coal-derived liquids by extended solvent precipitation, which process consists essentially of: (a) adding to said coal-derived liquid one selected anti-solvent liquid naphtha fraction derived solely by distillation from the coal liquid without further hydrogenation and having a normal boiling range between about 300°-550° F.; (b) mixing said two liquid streams together upstream of a first solids settling step and maintaining the mixture at 50-200 psig pressure and 500°-600° F. temperature and at sufficient settling time in said settling step to produce substantial polymerization of asphaltenes and precipitation and settling of the solids, so as to provide a clarified overflow liquid portion and an underflow liquid portion having increased solids concentration; (c) passing said underflow liquid portion at reduced pressure to a phase separation step to recover a light fraction product stream; (d) withdrawing said clarified overflow liquid portion containing a substantially reduced concentration of unreacted coal and ash solids and passing the liquid to a phase separation step at atmospheric pressure, and passing the resulting underflow liquid to a second solvent precipitation step at sufficient temperature to maintain a substantially liquid state and at atmospheric pressure; (e) withdrawing an overflow liquid product stream from said second precipitation step containing less than about 0.1 W % ash; and (f) withdrawing an underflow liquid stream from said second settling step.

Claim 11

A liquid-solids separation process for removal of unconverted coal and ash particulate solids from hydrogenated coal-derived liquids by extended solvent precipitation, which process consists essentially of: (a) adding to said coal-derived liquid one selected anti-solvent liquid naphtha fraction derived solely by distillation from the coal liquid without further hydrogenation and having a normal boiling range between about 300°-550° F.; (b) mixing said two liquid streams together upstream of a first solids settling step and maintaining the mixture at 50-200 psig pressure and 500°-600° F. temperature and at sufficient settling time in said settling step to produce substantial polymerization of asphaltenes and precipitation and settling of the solids, so as to provide a clarified overflow liquid portion and an underflow liquid portion having increased solids concentration; (c) passing said underflow liquid portion at reduced pressure to a phase separation step to recover a light fraction product stream; (d) withdrawing said clarified overflow liquid portion containing a substantially reduced concentration of unreacted coal and ash solids and passing the liquid to a phase separation step at atmospheric pressure, and passing the resulting underflow liquid to a second solvent precipitation step at sufficient temperature to maintain a substantially liquid state and at atmospheric pressure; (e) withdrawing an overflow liquid product stream from said second precipitation step containing less than about 0.1 W % ash; and (f) withdrawing an underflow liquid stream from said second settling step.

Claim 12

A liquid-solids separation process for removal of unconverted coal and ash particulate solids from hydrogenated coal-derived liquids by extended solvent precipitation and settling which process consists essential of: (a) passing a hydrogenated coal-derived stream to a centrifugal type liquid-solids separation step to provide overflow and underflow liquid streams, and recycling the overflow stream to the hydrogenation step; (b) adding to said separation step underflow liquid stream a selected naphtha anti-solvent liquid fraction derived solely from the coal-liquid without further hydrogenation and having a normal boiling range between about 400°-650° F.; (c) passing the resulting liquid mixture to a solids settling step maintained at atmospheric pressure and at sufficient temperature to maintain the mixture in substantially liquid condition, and providing sufficient settling time therein to produce substantial polymerization of asphaltenes and precipitation of the solids, so as to provide a clarified overflow liquid portion and an underflow liquid portion containing increased solids concentration; (d) withdrawing the clarified overflow liquid stream containing less than about 0.1 W % ash as liquid product; and (e) withdrawing the underflow liquid product stream.

Claim 13

A liquid-solids separation process for removal of unconverted coal and ash particulate solids from hydrogenated coal-derived liquids by extended solvent precipitation and settling which process consists essential of: (a) passing a hydrogenated coal-derived stream to a centrifugal type liquid-solids separation step to provide overflow and underflow liquid streams, and recycling the overflow stream to the hydrogenation step; (b) adding to said separation step underflow liquid stream a selected naphtha anti-solvent liquid fraction derived solely from the coal-liquid without further hydrogenation and having a normal boiling range between about 400°-650° F.; (c) passing the resulting liquid mixture to a solids settling step maintained at atmospheric pressure and at sufficient temperature to maintain the mixture in substantially liquid condition, and providing sufficient settling time therein to produce substantial polymerization of asphaltenes and precipitation of the solids, so as to provide a clarified overflow liquid portion and an underflow liquid portion containing increased solids concentration; (d) withdrawing the clarified overflow liquid stream containing less than about 0.1 W % ash as liquid product; and (e) withdrawing the underflow liquid product stream.

Claim 14

The process of claim 10, wherein the anti-solvent additive liquid is derived by fractionation of a light coal-derived liquid stream.

Claim 15

The process of claim 10, wherein the solids settling step temperature in step (c) is in the range of 400°-600° F., and internal rake means is used for providing movement and preventing excessive settling of the bottoms stream.

Claim 16

The process of claim 10, wherein the additive anti-solvent liquid fraction is derived by fractionation from a coal liquid atream and has a Kauri-butanol value between about 40 and 150.

Claim 17

The process of claim 10, wherein the ratio of the added anti-solvent liquid to separator underflow liquid to provide the settler feed liquid is between about 0.5 and 1.5, the solids settling time in the settling step is at least 8 hours, and the settler overflow liquid product contains 0.1 to 1.0 W % unconverted coal and ash solids.

Claim 18

The process of claim 10, wherein the settler underflow liquid stream is flashed at sub-atmospheric pressure in a vacuum distillation step, from which an overhead stream is withdrawn as product and bottoms liquid stream is withdrawn.

Claim 19

The process of claim 10, wherein the liquid mixture passed to settling step (c) is introduced near the center of a settler vessel, and the clarified overflow liquid is withdrawn from near the periphery of said vessel.