Method of handling ash-rich material in a coal deashing process

Claim 2

A continuous coal deashing process comprising: introducing a feed mixture comprising soluble coal products, insoluble coal products and a solvent into a separation zone, said solvent consisting essentially of at least one subsubstance having a critical temperature below 800 degrees F. selected from the group consisting of aromatic hydrocarbons having a single benzene nucleus and normal boiling points below about 310 degrees F., cycloparaffin hydrocarbons having normal boiling points below about 310 degrees F., open chain mono-olefin hydrocarbons having normal boiling points below about 310 degrees F., open chain saturated hydrocarbons having normal boiling points below about 310 degrees F., mono-, di, and tri-open chain amines containing from about 2-8 carbon atoms, carbocyclic amines having a monocyclic structure containing from about 6-9 carbon atoms, heterocyclic amines containing from about 5-9 carbon atoms, and phenols containing from about 6-9 carbon atoms and their homologs; maintaining said separation zone at a temperature level in the range of from about 400 degrees F. to about 700 degrees F. and a pressure level in the range of from about 700 psig to about 1000 psig to effect a separation of said feed mixture into a light phase and a heavy phase within said separation zone; providing a monitoring system to measure the viscosity of the heavy phase and compare the measured viscosity with a reference viscosity, said measurement being indicative of the physical characteristics of the heavy phase when withdrawn from the separation zone; withdrawing the heavy phase from the separation zone; and transmitting a signal from the monitoring system to activate a selection means which directs the flow of said withdrawn heavy phase to a flash drum when said measured viscosity exceeds said reference viscosity and to an alternate process unit when said measured viscosity is below said reference viscosity.

Claim 3

The process of claim 1 in which the reference viscosity is about 1000 centipoise.

Claim 4

The process of claim 1 in which said alternate process unit is designed to handle semi-solid or fluid materials and is provided with an inner liner that is readily removable when filled with said heavy phase.

Claim 5

A continuous coal deashing process comprising: introducing a feed mixture comprising soluble coal products, insoluble coal products and a solvent into a separation zone, said solvent consisting essentially of at least one subsubstance having a critical temperature below 800 degrees F. selected from the group consisting of aromatic hydrocarbons having a single benzene nucleus and normal boiling points below about 310 degrees F., cycloparaffin hydrocarbons having normal boiling points below about 310 degrees F., open chain mono-olefin hydrocarbons having normal boiling points below about 310 degrees F., open chain saturated hydrocarbons having normal boiling points below about 310 degrees F., mono-, di, and tri-open chain amines containing from about 2-8 carbon atoms, carbocyclic amines having a monocyclic structure containing from about 6-9 carbon atoms, heterocyclic amines containing from about 5-9 carbon atoms, and phenols containing from about 6-9 carbon atoms and their homologs; maintaining said separation zone at a temperature level in the range of from about 400 degrees F. to about 700 degrees F. and a pressure level in the range of from about 700 psig to about 1000 psig to effect a separation of said feed mixture into a light phase and a heavy phase within said separation zone; providing a monitoring system to measure the viscosity of the heavy phase and compare the measured viscosity with a reference viscosity of about 1000 centipoise, said measurement being indicative of the physical characteristics of the heavy phase when withdrawn from the separation zone; withdrawing the heavy phase from the separation zone; and transmitting a signal from the monitoring system to activate a selection means which directs the flow of said withdrawn heavy phase to a flash drum when said measured viscosity exceeds said reference viscosity of about 1000 centipoise and to an alternate process unit when said measured viscosity is below said reference viscosity of about 1000 centipoise.

Claim 6

A continuous coal deashing process comprising: introducing a feed mixture comprising soluble coal products, insoluble coal products and a solvent into a separation zone, said solvent consisting essentially of at least one subsubstance having a critical temperature below 800 degrees F. selected from the group consisting of aromatic hydrocarbons having a single benzene nucleus and normal boiling points below about 310 degrees F., cycloparaffin hydrocarbons having normal boiling points below about 310 degrees F., open chain mono-olefin hydrocarbons having normal boiling points below about 310 degrees F., open chain saturated hydrocarbons having normal boiling points below about 310 degrees F., mono-, di, and tri-open chain amines containing from about 2-8 carbon atoms, carbocyclic amines having a monocyclic structure containing from about 6-9 carbon atoms, heterocyclic amines containing from about 5-9 carbon atoms, and phenols containing from about 6-9 carbon atoms and their homologs; maintaining said separation zone at a temperature level in the range of from about 400 degrees F. to about 700 degrees F. and a pressure level in the range of from about 700 psig to about 1000 psig to effect a separation of said feed mixture into a light phase and a heavy phase within said separation zone; providing a monitoring system to measure the viscosity of the heavy phase and compare the measured viscosity with a reference viscosity of about 1000 centipoise, said measurement being indicative of the physical characteristics of the heavy phase when withdrawn from the separation zone; withdrawing the heavy phase from the separation zone; and transmitting a signal from the monitoring system to activate a selection means which directs the flow of said withdrawn heavy phase to a flash drum when said measured viscosity exceeds said reference viscosity of about 1000 centipoise and to an alternate process unit when said measured viscosity is below said reference viscosity of about 1000 centipoise.