Abstract A coal liquefaction process wherein a feed coal-solvent slurry is preheated in a thoroughly back-mixed preheater zone and then passed to a dissolver zone. Hot hydrogen is introduced to the process downstream from the preheater zone at or in advance of the dissolver zone and exothermic hydrocracking reactions occur in the dissolver zone. A dissolver zone effluent stream is passed through a vapor-liquid separator and separated hot dissolver vapor at process pressure is vented through the preheater zone wherein it is quenched to provide direct transfer to the preheater zone of the exothermic heat generated in the dissolver zone. The preheater zone is continuously vented to provide rapid removal of cooled vapor from the preheater zone and from the process, advantageously leaving an accumulation of liquid in the preheater zone boiling between the temperatures of the vapor-liquid separator and the preheater zone at process pressure. Venting of hot vapor generated in the exothermic dissolver zone through the preheater zone to accomplish direct internal heat exchange within the process requires continuous venting of cooled vapor from the preheater zone independently of removal of slurry from the preheater zone. Such independent venting of the preheating zone is feasible because of the introduction of hydrogen to the process downstream from the preheating zone.
Inventors
👤 Lawrence J. Kirby
👤 Thomas E. Richardson
👤 Bruce K. Schmid
👤 John V. Ward
Bibliographic Details
Application Number—
JurisdictionUS
Data Sourcegoogle_patents
Last Synchronized2026-10-27 12:24
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/06; C10G1/065
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
242 words
A coal liquefaction process comprising passing wet feed coal to a coal predrying zone to remove a portion of the moisture content thereof; passing partially dried feed coal from said predrying zone together with recycle slurry comprising normally solid dissolved coal, liquid coal and mineral residue to a backmixed feed slurry mixing vessel operated at a pressure below process pressure; venting vapor from said feed slurry mixing vessel independently of removal of mixing vessel effluent slurry to release water vapor formed thereon; pressurizing to process pressure mixing vessel effluent slurry and passing said mixing vessel effluent slurry to a preheater vessel to increase the temperature thereof to a level at which at least a portion of the coal dissolves; passing preheater vessel effluent slurry together with hydrogen to a dissolver zone to exothermically hydrocrack normally solid dissolved coal to liquid coal and hydrocarbon gases; passing hot dissolver zone effluent slurry through high temperature vapor-liquid separator means to remove an overhead vapor stream comprising hydrogen, hydrocarbon gases and naphtha from a separator slurry comprising liquid coal and normally solid dissolved coal with suspended mineral residue; recycling a portion of said separator slurry to said mixing vessel; passing said overhead vapor stream at process pressure to said preheater vessel for direct admixture with the slurry therein to quench said overhead vapor stream and heat the slurry therein; and venting vapor from said preheater vessel independently of removal of effluent slurry from said preheater vessel.
Claim 2
Dependent Claim
242 words
A coal liquefaction process comprising passing wet feed coal to a coal predrying zone to remove a portion of the moisture content thereof; passing partially dried feed coal from said predrying zone together with recycle slurry comprising normally solid dissolved coal, liquid coal and mineral residue to a backmixed feed slurry mixing vessel operated at a pressure below process pressure; venting vapor from said feed slurry mixing vessel independently of removal of mixing vessel effluent slurry to release water vapor formed thereon; pressurizing to process pressure mixing vessel effluent slurry and passing said mixing vessel effluent slurry to a preheater vessel to increase the temperature thereof to a level at which at least a portion of the coal dissolves; passing preheater vessel effluent slurry together with hydrogen to a dissolver zone to exothermically hydrocrack normally solid dissolved coal to liquid coal and hydrocarbon gases; passing hot dissolver zone effluent slurry through high temperature vapor-liquid separator means to remove an overhead vapor stream comprising hydrogen, hydrocarbon gases and naphtha from a separator slurry comprising liquid coal and normally solid dissolved coal with suspended mineral residue; recycling a portion of said separator slurry to said mixing vessel; passing said overhead vapor stream at process pressure to said preheater vessel for direct admixture with the slurry therein to quench said overhead vapor stream and heat the slurry therein; and venting vapor from said preheater vessel independently of removal of effluent slurry from said preheater vessel.
Claim 3
Dependent Claim
27 words
The process of claim 1 wherein between about 5 and 90 weight percent of the moisture content of the feed coal is removed in said predrying zone.
Claim 4
Dependent Claim
37 words
The process of claim 1 wherein the temperature of said recycled separator slurry is above the temperature in said mixing vessel; and said recycled separator slurry adds heat to the mixing vessel to dry the coal therein.
Claim 5
Dependent Claim
44 words
The process of claim 1 wherein the temperature of the slurry in said feed slurry mixing vessel is between about 300° and 500° F. and the residence time of the slurry in said feed slurry mixing vessel is between about 5 and 30 minutes.
Claim 6
Dependent Claim
33 words
The process of claim 1 when said quench of said overhead vapor stream in said preheater vessel induces condensation in said preheater vessel and accumulation in said process of hydrogen donor solvent liquid.