← Back to Patent Explorer
US3776533A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus for continuous heat processing of ore pellets

Assignee: Dravo Corp
•
Filing: 1970-01-28
•
Granted: 1973-12-04
•
Expires: 1990-01-28
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Apparatus and method for preheating, hardening and reducing ore pellets that provide for envelopment of the pellets in inert particulate material throughout the processing. Green pellets are continuously charged into a fluidized bed of heated particulate material and preheated while being buoyantly moved to a second fluidized bed. The preheated pellets are then buoyantly transported through the second fluidized bed of particulate material, which is at a higher temperature than the first bed, while being hardened. Hardened pellets are directly discharged from the second bed to the upper region of a columnar reactor for random envelopment within a bed of inert particulate material that is heated to a temperature sufficient to reduce the pellets during downward movement through the reactor.

Inventors

  • 👤 J Vlnaty

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 14:34
CPC Classifications
C; C21; C21B; C21B13/00; C21B13/14; C21B13/0046; C21B13/008; C21B13/0086; C22; C22B; C22B1/00; C22B1/14; C22B1/24; C22B1/2413; Y; Y02; Y02P; Y02P10/00; Y02P10/10; Y02P10/134

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 281 words
Apparatus for The continuous heat processing of pellets, characterized by the cushioning of the pellets during preheating and incipient hardening to minimize breakage or attrition, wherein the pellets are enveloped in inert particulate material at all stages of processing comprising: a. a pellet-forming apparatus, b. a first enclosure containing a fluidized bed of solid particles of inert material arranged to continuously receive green pellets and buoyantly move them to a point of discharge with means for maintaining the fluidized bed at an elevated temperature to preheat and dry the pellets as they are carried to the point of discharge, c. a second enclosure containing a fluidized bed similar to the first into which the dry preheated pellets from the first unit are directly discharged, said second enclosure having means for maintaining the fluidized bed at a temperature higher than the first to effect incipient hardening of the pellets, d. means for charging fluidized gas to each of said enclosures so arranged as to direct the movement of the pellets through said enclosures, e. a columnar reactor arranged to continuously receive hardened pellets directly from said second enclosure at its upper end, said reactor having means for continuously supplying highlyheated inert particulate material into the upper end thereof to envelop the pellets as they are discharged into the upper end thereof, and f. means at the bottom of the reactor for continuously removing and separating pellets and particulate material to effect a continuous downward movement of the pellets and particulate material through the column at a controlled rate, g. said apparatus thereby effecting the processing of the pellets continuously while they are randomly enveloped in and separated by hot inert particulate material.
Claim 2
Dependent Claim 281 words
Apparatus for The continuous heat processing of pellets, characterized by the cushioning of the pellets during preheating and incipient hardening to minimize breakage or attrition, wherein the pellets are enveloped in inert particulate material at all stages of processing comprising: a. a pellet-forming apparatus, b. a first enclosure containing a fluidized bed of solid particles of inert material arranged to continuously receive green pellets and buoyantly move them to a point of discharge with means for maintaining the fluidized bed at an elevated temperature to preheat and dry the pellets as they are carried to the point of discharge, c. a second enclosure containing a fluidized bed similar to the first into which the dry preheated pellets from the first unit are directly discharged, said second enclosure having means for maintaining the fluidized bed at a temperature higher than the first to effect incipient hardening of the pellets, d. means for charging fluidized gas to each of said enclosures so arranged as to direct the movement of the pellets through said enclosures, e. a columnar reactor arranged to continuously receive hardened pellets directly from said second enclosure at its upper end, said reactor having means for continuously supplying highlyheated inert particulate material into the upper end thereof to envelop the pellets as they are discharged into the upper end thereof, and f. means at the bottom of the reactor for continuously removing and separating pellets and particulate material to effect a continuous downward movement of the pellets and particulate material through the column at a controlled rate, g. said apparatus thereby effecting the processing of the pellets continuously while they are randomly enveloped in and separated by hot inert particulate material.
Claim 3
Dependent Claim 56 words
Apparatus for the continuous heat-processing of pellets wherein the pellets are enveloped in inert particulate material at all stages of processing as defined in claim 1 including means for separating dried and preheated pellets from said solid particles of inert material discharged from said first enclosure prior to charging of said pellets into said second enclosure.
Claim 4
Dependent Claim 42 words
Apparatus for the continuous heat-processing of pellets wherein the pellets are enveloped in inert particulate material at all stages of processing as defined in claim 2 including means for reheating and returning said separated inert material for recycle to said first enclosure.
Claim 5
Dependent Claim 53 words
Apparatus for continuous heat-processing of pellets wherein the pellets are enveloped in inert particulate material at all stages of processing as defined in claim 2 including means for separating hardened pellets from solid particles of said fluidized bed discharged from the second enclosure prior to envelopment of said pellets in said columnar reactor.
Claim 6
Dependent Claim 49 words
Apparatus for continuous heat-processing of pellets wherein the pellets are enveloped in inert particulate material at all stages of processing as defined in claim 5 including means for reheating and returning said separated solid particles of said fluidized bed of the second enclosure for recycle to said second enclosure.
Claim 7
Dependent Claim 51 words
Apparatus for continuous heat-processing of pellets wherein the pellets are enveloped in inert particulate material at all stages of processing as defined in claim 1 including means for charging a reducing gas to the lower portion of said columnar reactor for countercurrent flow to said movement of pellets and particulate material.
Claim 8
Dependent Claim 48 words
Apparatus for continuous heat processing of pellets wherein the pellets are enveloped in inert particulate material at all stages of processing as defined in claim 1 including means for exhausting gases from said columnar reactor and means for cooling said exhaust gases to remove volatile metals present therein.
Claim 9
Dependent Claim 155 words
Apparatus for use in the manufacture of pellets containing agglomerated mineral particles comprising: a. a pelletizing unit for continuously forming moist green pellets, b. an Enclosure into which the moist green pellets are discharged by gravity, said enclosure containing a fluidized bed of heated finely-divided inert particulate material to cushion the pellets as they gravitate into the enclosure and through which they become randomly distributed, c. means for continuously progressing said bed from one end of the enclosure toward the other while maintaining the bed in a heated condition and discharging the material and pellets from the other end, whereby the pellets are dried and preheated while buoyed in said bed, d. means for separating the preheated and dried pellets from the particulate material upon discharge at said other end, and e. means for heating and recycling the separated particulate material to the end of said enclosure into which the moist green pellets are discharged.
Claim 10
Dependent Claim 155 words
Apparatus for use in the manufacture of pellets containing agglomerated mineral particles comprising: a. a pelletizing unit for continuously forming moist green pellets, b. an Enclosure into which the moist green pellets are discharged by gravity, said enclosure containing a fluidized bed of heated finely-divided inert particulate material to cushion the pellets as they gravitate into the enclosure and through which they become randomly distributed, c. means for continuously progressing said bed from one end of the enclosure toward the other while maintaining the bed in a heated condition and discharging the material and pellets from the other end, whereby the pellets are dried and preheated while buoyed in said bed, d. means for separating the preheated and dried pellets from the particulate material upon discharge at said other end, and e. means for heating and recycling the separated particulate material to the end of said enclosure into which the moist green pellets are discharged.
Claim 11
Dependent Claim 124 words
Apparatus for use in the manufacture of pellets containing agglomerated mineral particles as defined in claim 8 including: a. a second enclosure containing a fluidized bed of heated finely-divided inert particles, b. means for transferring dried and preheated pellets from the first enclosure directly to said second enclosure, c. the fluidized bed of said second enclosure being at a temperature several hundred degrees higher than the fluidized bed in said first enclosure wherein the preheated and dried pellets are continuously enveloped and buoyed in the fluidized bed of the second enclosure in random distribution from the end into which the pellets are transferred from the first enclosure to the other end from which the pellets are discharged to harden the pellets for further processing.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-12-03 1977-06-04 1977-12-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-12-03 1981-06-04 1981-12-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-12-03 1985-06-04 1985-12-04 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag