Molten salt hydroconversion process

{
  "publication_number": "US4092236A",
  "country": "US",
  "kind": "A",
  "title": "Molten salt hydroconversion process",
  "abstract": "Hydrocarbonaceous materials such as petroleum residuums, coal, lignite or the like are introduced into a molten salt bath maintained in a reaction zone at elevated temperature and pressure. Hydrogen also is introduced into the reaction zone in an amount sufficient to provide a pressure in the reaction zone within the range of from about 30 to 400 atmospheres. The hydrocarbonaceous material is reacted for a time sufficient to produce cracked products including a major amount of liquid and a minor amount of gaseous and solid products of enriched hydrogen content. The molten salt bath comprises at least one alkali metal hydroxide which preferably is sodium hydroxide. Substantially all of the sulfur and ash constituents of the hydrocarbonaceous material are retained in the molten salt. When the hydrocarbonaceous material is a normally solid material such as coal, it advantageously is crushed and slurried in an organic hydrogen donor solvent prior to its introduction into the molten salt bath.",
  "claims": [
    "1. A process for hydrocracking coal comprising: introducing coal into a molten sale bath maintained in a reaction zone at a temperature of from about 350° to about 550° C; introducing hydrogen into the reaction zone an amount sufficient to provide a pressure in the reaction zone within the range of from about 30 to 500 atmospheres; and reacting said coal for a time sufficient to produce cracked products including liquid, gaseous and solid products of enriched hydrogen content, said molten salt bath comprising a major amount of at least one alkali metal hydroxide.",
    "2. The process of claim 1 wherein said coal is ground and slurried in an organic hydrogen donor solvent prior to being introduced into said molten salt bath.",
    "3. The process of claim 1 wherein said coal contains ash and sulfur constituents and said cracked gaseous and liquid products are substantially free of ash and sulfur.",
    "4. The process of claim 3 wherein said molten salt bath includes a minor amount of an alkali metal carbonate and up to about 15 wt.% of an alkali metal sulfide.",
    "5. The process of claim 1 wherein said molten salt bath is maintained in a reaction zone at a temperature of from about 400° to 500° C and said hydrogen is introduced in an amount sufficient to provide pressure in a reaction zone within the range of from about 50 to 300 atmospheres.",
    "6. The process of claim 5 wherein said alkali metal is sodium.",
    "7. A process for hydrocracking coal comprising introducing a mixture of an ash and sulfur-containing coal and an organic hydrogen donor solvent into a molten salt bath, maintained in a reaction zone at a temperature of from about 400° to 500° C; introducing hydrogen into the reaction zone in an amount sufficient to provide a pressure in the reaction zone within the range of from about 50 to 300 atmospheres; and reacting the coal for a time sufficient to produce cracked products including liquid, gaseous and solid products of an enriched hydrogen content and substantially free of ash and sulfur, said molten salt bath comprising a major amount of an alkali metal hydroxide, a minor amount of an alkali metal carbonate, and up to about 15 wt.% of an alkali metal sulfide.",
    "8. The process of claim 7 wherein said alkali metal is sodium."
  ],
  "cpc": [
    "C10G 47/02",
    "C10G 1/065",
    "C10G 1/086"
  ],
  "assignees": [
    "ROCKWELL INTERNATIONAL CORP"
  ],
  "filing_date": "1976-08-30",
  "publication_date": "1978-05-30",
  "grant_date": "1978-05-30",
  "priority_date": "1976-08-30",
  "application_number": "US-71873176-A",
  "family_id": "24887270",
  "citations": [
    "US2768935A",
    "US3677932A",
    "US3679577A",
    "US3708270A",
    "US3745109A",
    "US3779722A",
    "US3966582A",
    "US4003823A"
  ]
}