Union Oil Company of California

Roland O Dhondt

Roland F Deering

George D Cheadle

Don C Jennings

Thomas A Seesee

A solids feeder and method for transporting particulate solids from an elevated solids feed reservoir and introducing the solids upwardly into the bottom of a solids upflow vessel. The feeder includes a stationary feed cylinder axially aligned with a bottom solids inlet of the upflow vessel and fitted with a vertically reciprocatable piston which alternately (1) retracts to allow the feed cylinder to receive solids from the feed reservoir by gravity flow through a feed chute and (2) extends to displace the solids upwardly into the upflow vessel. Horizontally reciprocatable slide plates prevent backflow of solids during the filling of the feed cylinder.

Apparatus and method for introducing solids into a solids upflow vessel

A method for introducing particulate solids upwardly through a bottom solids inlet of a solids upflow vessel wherein after full extension of a piston to displace solids from a feed cylinder into the solids upflow vessel, the piston is partially retracted to 'relax' the bed of solids in the solids upflow vessel. The bed relaxation step reduces the piston-to-solids pressure during the pumping stroke as well as substantially reducing the solids loading pressure on the device used to prevent backflow of solids from the upflow vessel during refilling of the feed cylinder.

Method for introducing solids into a solids upflow vessel

Crushed oil shale is segregated into a major portion of relatively large particles and a minor portion of 'fines,' such as will pass through 1/8-inch screen openings. The large particles are subjected to retorting in an upflowing bed in countercurrent contact with a downflowing hot eduction gas, while the fines are fed onto and controllably transported across the hot planar surface of a free-standing truncated cone of spent shale at the top of the retort.

Shale retorting process and apparatus

Crushed oil shale is segregated into a major portion of relatively large particles and a minor portion of 'fines' which will pass through screen openings up to about 1/4 inch in size. The large particles are subjected to retorting as an upflowing moving bed in countercurrent contact with downflowing hot eduction gas, while the fines are retorted by controlled distribution over the hot upper surface of the bed of retorted large particles.

Crushed oil shale is subjected to eduction in a solids-upflow or -downflow retort in contact with a preheated counter-currently flowing eduction gas comprising a recycled portion of the retort make gases. The problem of shale particle agglomeration is avoided by correlating the eduction gas flow rate and temperature so as to insure that the 750.degree.-850.degree. F shale temperature interval in the retort is maintained at a level sufficiently high in the retort that the total shale, or 'rock' pressure bearing down on said interval is insufficient to bring about agglomeration. It is found that the problem of agglomeration is critical to the 750.degree.-850.degree. F temperature range, and that there is a definite correlation between the oil assay of the raw shale and the permissible rock pressure which the shale particles in this temperature range can withstand without undergoing agglomeration. Provision is made for shifting the 750.degree.-850.degree. F zone upwardly or downwardly in the retort.

Shale retorting process

In a continuous, solids upflow, gas downflow shale retorting process carried out at superatmospheric pressures, hydrostatic sealing means are provided at the shale inlet and retorted shale outlet ends of the retort, thereby avoiding the need for mechanical sealing means, lock vessels, etc. The raw shale is fed into the retort through a standing reservoir of product oil, or preferably a light fraction thereof, and the retorted shale is discharged from the retort through a water quenching zone and seal, in the lower portion of which is maintained a sufficient hydrostatic head of water to prevent the discharge therethrough of retort gases. Steam generated in the quench zone, containing some entrained hydrocarbonaceous matter, is treated in a multistage cooling and condensing manner for gas cleanup and for recovery of heat and an oil-free water condensate for recycle to the water sealing and quench zones.

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Long Beach, CA, United States of America

Roland O Dhondt