Abstract Improvements in a process for reforming coal by subjecting a mixed slurry containing a hydrocarbon solvent and coal fines to hydrogenation reaction under high temperature and pressure conditions, gas-liquid separation, and distillation to obtain a solvent-refined coal, the improvements comprising: maintaining the reaction temperature and total reaction pressure within a hydrogenation reactor at 400° to 500° C. and 50 to 200 atms., and controlling the residence time distribution of reactants, excepting gaseous reactants, in the hydrogenation reaction zone to have an average residence time longer than 17 minutes, and to keep the quantity of the reactants which have a residence time shorter than 10 minutes in a proportion less than 20% by weight of the reactants.
In a process for reforming coal by subjecting a mixed slurry containing a hydrocarbon solvent and coal fines to hydrogenation reaction under high temperature and pressure conditions, gas-liquid separation, and distillation to obtain a solvent-refined coal, the improvement comprising: maintaining the reaction temperature and total reaction pressure within a hydrogenation reactor at 400° to 500° C. and 50 to 200 atms., and controlling the residence time distribution of reactants, excepting gaseous reactants, in the hydrogenation reaction zone to have an average residence time longer than 17 minutes, and to keep the quantity of said reactants which have a residence time shorter than 10 minutes in a proportion less than 20% by weight of said reactants.
Claim 2
Dependent Claim
115 words
In a process for reforming coal by subjecting a mixed slurry containing a hydrocarbon solvent and coal fines to hydrogenation reaction under high temperature and pressure conditions, gas-liquid separation, and distillation to obtain a solvent-refined coal, the improvement comprising: maintaining the reaction temperature and total reaction pressure within a hydrogenation reactor at 400° to 500° C. and 50 to 200 atms., and controlling the residence time distribution of reactants, excepting gaseous reactants, in the hydrogenation reaction zone to have an average residence time longer than 17 minutes, and to keep the quantity of said reactants which have a residence time shorter than 10 minutes in a proportion less than 20% by weight of said reactants.
Claim 3
Dependent Claim
22 words
The improvement of claim 1, wherein the product mixture resulting from said hydrogenation reaction is for use in a metallurgical carbonaceous material.
Claim 4
Dependent Claim
28 words
The improvement of claim 1, wherein the product mixture resulting from said hydrogenation reaction is further subjected to deashing and secondary hydrogenation reaction to produce a liquid product.