Method and system for recovering coal fines from pipe line coal slurry

A method of recovering coal fines from pipeline coal slurry for combustion purposes, comprising:

• primary dewatering of said pipeline coal slurry via centrifugation to separate the coarse particles larger than about 400 mesh from the pipeline coal slurry and leaving a centrate having a suspension of less than about 15% suspended solids of coal fines smaller than about 400 mesh in water;
• blending a portion of said pipeline slurry into said centrate to produce a blend of about 10-30% by volume of said pipeline slurry to about 90-70% by volume of said centrate;
• filtering the water from said blend on a belt press to separate said blend into a combustible blend cake having more than about 50% solids and a filtrate having a suspended solids concentration of greater than 70 mg/l;
• clarifying said filtrate in a settling tank to separate said filtrate into an effluent having a suspended solids content of less than 70 mg/l and an underflow having a suspended solids content of greater than about 2,000 mg/l;
• and
• adding said underflow to said blend to recover the underflow solids in said belt press.

A method of dewatering primary pipeline coal slurry to recover for combustion substantially all of the suspended particles in said primary slurry and also recover the water in which said particles were suspended in substantially clean condition, comprising:

• dewatering said primary slurry on a primary dewatering device to produce a combustible coal cake having about 20% water and a secondary slurry having a water content in the range of 85%-95%;
• blending a portion of said primary slurry into said secondary slurry to produce a blend having a range of proportions from 1:1 to 1:4 by weight of suspended solids from said slurries;
• dewatering said blend on a secondary dewatering apparatus to produce a coal cake having a water content of less than 50%, and a secondary filtrate having a solids content of less than 1%;
• clarifying said secondary filtrate to produce an effluent having a solids content of less than 70 mg/l and an underflow having a solids content of greater than 10% solids;
• and
• mixing said clarifier underflow with said blend prior to dewatering said blend on said secondary dewatering apparatus to recover the solids content of said underflow.