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    • 3. 发明专利
    • MANUFACTURE OF COALLHEAVY OIL MIXED FUEL
    • JPS55135196A
    • 1980-10-21
    • JP4275679
    • 1979-04-09
    • MITSUI SHIPBUILDING ENGDENGEN KAIHATSU KK
    • NAKABAYASHI KIYOUSHIMATSUURA HIKOOSUGINO YUTAKASATOU KATSUMINAGATA KENICHIKATOU HIROICHI
    • C10L1/32
    • PURPOSE:To obtain a coal-heavy oil mixed fuel free of sedimentation of coal particles during storage, by the procedure in which pulverized coal and heated heavy oil are continuously supplied into a container turning at high speed while controlling the revolving number of the container, the amount of coal to supply, and the amount of heavy oil to supply in a manner to satisfy respective relations. CONSTITUTION:The raw material coal 1 is charged into the pulverizer 3 by the conveyer 2 and then the pulverized coal is supplied to the high-speed rotary container 14. On the other hand, the heavy oil 13 is supplied through the heater 11 from the oil tank 9 by the oil pump 10 into the container 14, where the revolving number of the cotainer 14, the amount of coal to supply, and the amount of heavy oil to supply are controlled so as to satisfy the relatioship of the formula (G is gravity in the centrifugal force field, t is average staying time in the centrifugal force field, g is the acceleration of gravity, and t is max. storage period). Thus, air and moisture are removed in the centrifugal force field, the coal of a grain size, sedimenting in the centrifugal force field, is restored to the pulverizer 3 again, and only coal of a grain size, not sedimenting in the centrifugal force field, is mixed with the heavy oil to obtain the subject mixed fuel.
    • 5. 发明专利
    • MANUFACUTURE OF FORMED COKE
    • JPS58104986A
    • 1983-06-22
    • JP20580181
    • 1981-12-18
    • MITSUI SHIPBUILDING ENG
    • KATOU HIROICHISATOU KATSUMI
    • C10B57/04C10L5/10C10L9/00
    • PURPOSE:To obtain a formed coke of improved quality and productivity, with the advantage of using high-ash caking coal, etc., by blending a caking coal and a non- or sparingly caking coal, carrying out grinding followed by adding a binder to make an aggregate, separating ash particles, then adding the binder and hot water to carry out forming. CONSTITUTION:For example, a caking coal 1 is blended with a non- or sparingly caking coal 2, the resulting blend being ground to obtain a blend coal 9, which is then incorporated wth a binder 12 to perform a kneading followed by adding a liquid medium 23 immiscible with said binder to agitate in the tank 26. Thus, only caking coal particles and non- or sparingly caking coal ones are made into an aggregate through the binder 12, while the ash particles being separated as a suspension in the medium 23. Further, using a screen 31, said aggregate and the ash particle suspension are separated from each other as an unfiltered recovered coal 28 and as a filtered waste liquid 29, respectively. The resulting aggregate is incorporated with a new batch of the binder 12 and a hot water 13 to carry out a kneading, then forming under presure, thus obtaining the objective formed coke 17. EFFECT:Capable of simply incorporating the ash particle elimination procedure into the existing process.
    • 9. 发明专利
    • DEASHING METHOD OF COAL-OIL MIXTURE FUEL
    • JPS56166298A
    • 1981-12-21
    • JP7033180
    • 1980-05-27
    • MITSUI SHIPBUILDING ENG
    • NAGATA KENICHIKATOU HIROICHI
    • C10L1/32
    • PURPOSE:To take ash particles from a fuel with water efficiently, by dispersing a mixed fuel of finely pulverized coal with an oil, e.g. heavy oil, (COM fuel) in water at a high temperature into drops with agitation. CONSTITUTION:N2 gas at the top 50 of a pressure vessel 4 at a temperature of 100-300 deg.C and a pressure of atmospheric one to 88kg/cm is passed through a conduit 51 and a pump 52, and the moisture is adjusted by waterdrops fed from a water tank 13 and jetted from a moisture conditioning nozzle. The N2 gas is then injected from an injection inlet 56 to form gas bubbles, which rise in a parallel cylinder 28 and an enlarged conical pipe 29 of an inner cylinder 11 in a container 4 while collecting an ash in a COM fuel with the moisture contained therein. The gas bubbles disappear in the interface 61 between the liquid and the N2 gas; however, ash particles near the interface 61 are pushed near the inner wall of the container 4 by centrifugal blades 57 and settle in the water along the inner wall by the aggregation and disappearance of the fine gas bubbled. The settled particles are then expelled from a delivery outlet 16 as a slurry with the water.