Japanese
close

FI (list display)

  • C10G1/00
    		•  Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal (mechanical winning of oil from oil-shales, oil-sand, or the like B03B) HB CC 4H129
  • C10G1/00@A
    		•  Liquefaction of oil shale, oil sand etc. HB CC 4H129
  • C10G1/00@B
    		•  Liquefaction of wastes, city refuse (liquefaction of waste rubber, waste plastic R 1/10) (incineration of waste R F 23 G; heat exchange R F 28; sludge treatment R C 02 F 11/00; generation of gas from solid substances R C 10 J) HB CC 4H129
  • C10G1/00@C
    		•  Liquefaction of plants ( carbon) HB CC 4H129
  • C10G1/00@D
    		•  Liquefaction of coal HB CC 4H129
  • C10G1/00@E
    		•  .Pre-treatment, preparation of slurry HB CC 4H129
  • C10G1/00@F
    		•  ..Dehydration, drying (dehydration of slurry) HB CC 4H129
  • C10G1/00@G
    		•  ..Heating, preheating HB CC 4H129
  • C10G1/00@H
    		•  .Liquefaction reaction (liquefaction through distillation, dry distillation R 1/02, extraction of solvents R 1/04, F864decomposition R 1/06 to 1/08) HB CC 4H129
  • C10G1/00@J
    		•  .Separation refining of liquefaction reaction products ( solid/liquid separation, deliming) ( from extraction, hydrogenetive decomposition) HB CC 4H129
  • C10G1/00@K
    		•  ..CFFC method HB CC 4H129
  • C10G1/00@Z
    		•  Others HB CC 4H129
  • C10G1/02
    		•  .by distillation HB CC 4H129
  • C10G1/04
    		•  .by extraction HB CC 4H129
  • C10G1/04@A
    		•  Characterized by the solvent used HB CC 4H129
  • C10G1/04@B
    		•  .Extraction of supercritical gas HB CC 4H129
  • C10G1/04@C
    		•  .Water HB CC 4H129
  • C10G1/04@Z
    		•  Others (reaction devices R 1/06 G to H) HB CC 4H129
  • C10G1/06
    		•  .by destructive hydrogenation HB CC 4H129
  • C10G1/06@A
    		•  Solvents HB CC 4H129
  • C10G1/06@B
    		•  .Hydrogenative solvents HB CC 4H129
  • C10G1/06@C
    		•  ..EDS method HB CC 4H129
  • C10G1/06@D
    		•  Catalysts HB CC 4H129
  • C10G1/06@E
    		•  .Containing Iron HB CC 4H129
  • C10G1/06@F
    		•  Reductive has HB CC 4H129
  • C10G1/06@G
    		•  Reaction devices (catalyst moving type, boiling floor type reactor R 1/08) HB CC 4H129
  • C10G1/06@H
    		•  .Squeezing in material slurry to reactors, extraction of reaction products HB CC 4H129
  • C10G1/06@Z
    		•  Others HB CC 4H129
  • C10G1/08
    		•  ..with moving catalysts HB CC 4H129
  • C10G1/10
    		•  .from rubber or rubber waste HB CC 4H129
    TOP