US4793937A
Expired / Lapsed
US
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Method and apparatus for separating contaminants from fluidizable solids
Assignee: AMERICAN TOXIC DISPOSAL PARTNERS A CORP OF ILL
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Filing: 1987-04-10
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Granted: 1988-12-27
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Expires: 2007-04-10
Abstract
Abstract A process and apparatus for treating any fluidizable solid material having an organic contaminant or recoverable material absorbed or adsorbed thereon, particularly a sludge contaminated with polychlorinated biphenyl or other toxic chemicals having a boiling point of at least 110° C. The method and apparatus includes heating the fluidizable solids, using hot turbulent gas at a temperature in the range of 850° to 2,500° F. to vaporize and thereby separate the organic material, for example, the toxic chemicals from the fluidizable solids and to fluidize at least a portion of the solids. The recoverable or contaminant liquid, for example the toxic chemicals, are then further treated to recover or dispose of the separated liquid, such as by condensing the liquid and filtering or decanting it from the condensed water.
Inventors
- 👤 William C. Meenan
- 👤 George D. Sullivan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 16:17
CPC Classifications
B; B09; B09C; B09C1/00; B09C1/06; C; C02; C02F; C02F11/00; C02F11/004; C02F11/12; C02F11/13
Claims Analysis
Total Claims: 28
Claim 1
Independent Claim
85 words
A method for treating a fluidizable solid material contaminated with a polychlorinated biphenyl comprising: fluidizing and heating said material in a drying vessel at a temperature sufficient to enable recovery of substantially all of the polychlorinated biphenyls in a gaseous stream out of said drying vessel, leaving 5 parts per million or less of the polychlorinated biphenyls in the material, thereby separating the polychlorinated biphenyls from the material; and removing said gaseous stream containing said separated polychlorinated biphenyls from said drying vessel for further treatment.
Claim 2
Independent Claim
85 words
A method for treating a fluidizable solid material contaminated with a polychlorinated biphenyl comprising: fluidizing and heating said material in a drying vessel at a temperature sufficient to enable recovery of substantially all of the polychlorinated biphenyls in a gaseous stream out of said drying vessel, leaving 5 parts per million or less of the polychlorinated biphenyls in the material, thereby separating the polychlorinated biphenyls from the material; and removing said gaseous stream containing said separated polychlorinated biphenyls from said drying vessel for further treatment.
Claim 3
Dependent Claim
25 words
The method of claim 1 wherein the material is exposed to a hot gas for a period of about 1 minute to about 1.5 hours.
Claim 4
Dependent Claim
28 words
The method of claim 2 wherein the hot gas vaporizes said polychlorinated biphenyls and entrains a portion of the material, as fine particulates, with said vaporized polychlorinated biphenyls.
Claim 5
Dependent Claim
14 words
The method of claim 3 further including separating the particulates from the polychlorinated biphenyls.
Claim 6
Independent Claim
102 words
A method for treating a fluidized solid material contaminated with a polychlorinated biphenyl comprising: contacting the fluidizable solid material in a separator with hot turbulent gas at a temperature sufficient to enable recovery of substantially all of the polychlorinated biphenyls in a gaseous stream out of said drying vessel, and thereby separate the polychlorinated biphenyl from the material and gaseously entrain a portion of the finer fluidiable solid material in particulate form, leading a dried particulate mass of fluidized solids having about 5 ppm or less of polychlorinated biphenyls; and removing said gaseous stream containing the separated polychlorinated biphenyls from said separator.
Claim 7
Independent Claim
102 words
A method for treating a fluidized solid material contaminated with a polychlorinated biphenyl comprising: contacting the fluidizable solid material in a separator with hot turbulent gas at a temperature sufficient to enable recovery of substantially all of the polychlorinated biphenyls in a gaseous stream out of said drying vessel, and thereby separate the polychlorinated biphenyl from the material and gaseously entrain a portion of the finer fluidiable solid material in particulate form, leading a dried particulate mass of fluidized solids having about 5 ppm or less of polychlorinated biphenyls; and removing said gaseous stream containing the separated polychlorinated biphenyls from said separator.
Claim 8
Dependent Claim
28 words
The method of claim 5 further including conveying the entrained particulate fluidizable solids out of said separator and separating the entrained particulate solids from the vaporized polychlorinated biphenyls.
Claim 9
Dependent Claim
27 words
The method of claim 6 wherein the fluidizable solids are contacted with hot turbulent air and combustion gases at a temperature of 1000° F. to 1800° F.
Claim 10
Dependent Claim
36 words
The method of claim 7 including condensing a portion of the gaseous stream removed from the vaporization chamber to form a condensate and separating a substantial portion of the condensed polychlorinated biphenyls from the remaining condensate.
Claim 11
Dependent Claim
26 words
The method of claim 8 wherein the gases removed from the vaporization chamber are chilled to a temperature below about 200° F. to form said condensate.
Claim 12
Dependent Claim
26 words
The method of claim 9 wherein the gases removed from the vaporization chamber are chilled to a temperature below about 100° F. to form said condensate.
Claim 13
Dependent Claim
29 words
The method of claim 8 wherein the soil includes at least 10% by weight water and including separating the water from the polychlorinated biphenyls by decanting the water therefrom.
Claim 14
Dependent Claim
47 words
The method of claim 7 wherein the removed gases and entrained particulates are conveyed through a means for separating solids from gas and the gaseous portion is conveyed to a condenser to condensate a major portion of the polychlorinated biphenyls from the vapor as a toxic condensate.
Claim 15
Dependent Claim
24 words
The method of claim 12 including conveying the toxic condensate through a filter capable of selectively filtering said polychlorinated biphenyls from the remaining condensate.
Claim 16
Dependent Claim
25 words
The method of claim 7 wherein the fluidizable solids comprises a sludge having 10-90% fluidizable solids solids and 10-90% liquid, said liquid being predominantly water.
Claim 17
Dependent Claim
37 words
The method of claim 14 wherein the fluidizable solids contains at least 20% by weight water so that water vapor formed in the first fluidized bed aids in entraining vaporizing polychlorinated biphenyls out of the vaporization chamber.
Claim 18
Dependent Claim
126 words
The method of claim 6 including directing the fluidizable solids into the separator and onto a first drying surface disposed within said separator, said first surface angled downwardly from a periphery of the separator towards a longitudinal center of the separator for directing the fluidizable solids into a position at the longitudinal center of the separator for contact with the hot turbulent gas and vaporization of the polychlorinated biphenyls; and dropping the fluidizable solids from said first surface onto a lower, second drying surface disposed within said separator, said second surface angled downwardly from the longitudinal center of the separator towards the periphery of the separator for directing the fluidizable solids toward the periphery of the separator, while vaporizing the polychlorinated biphenyls from the fluidizable solids.
Claim 19
Dependent Claim
15 words
The method of claim 16 wherein said first and second drying surfaces are frusto-conically shaped.
Claim 20
Independent Claim
243 words
A method of removing polychlorinated biphenyls from a fluidizable solid material comprising: conveying said fluidizable solids and a hot, turbulent gas at a temperature of about 850°-2500° F. into a vaporization chamber; contacting said fluidizable solids with said hot turbulent gas in a hot gas-fluidizable solids first fluidized bed contacting zone in a lower portion of said vaporization chamber to fluidize at least a portion of said fluidizable solids in said lower portion of said vaporization chamber, to vaporize a majority of said polychlorinated biphenyls from said fluidizable solids in said lower portion thereby forming a gaseous stream recoverable from said vaporization chamber; and to cool said hot gases; conveying said cooled hot gas upwardly through said vaporization chamber at a rate sufficient to propel a finer particulate portion of the fluidizable solids above the first fluidized bed contacting zone to a second fluidized bed contacting zone at a lower temperature than, and disposed above, said first fluidized bed contacting zone, whereby a finer particulate portion of the fluidizable solids is fluidized by said cooled hot gases and additional polychlorinated biphenyls are vaporized from said fluidized finer particulates in said second fluidized bed contact zone; recycling a portion of the fluidizable solids particulates from the second fluidized bed down to the first fluidized bed for further vaporization of polychlorinated biphenyls from said recycled particulates; and removing said gaseous stream containing said gases and vaporized polychlorinated biphenyls from the vaporization chamber for further treatment.
Claim 21
Independent Claim
243 words
A method of removing polychlorinated biphenyls from a fluidizable solid material comprising: conveying said fluidizable solids and a hot, turbulent gas at a temperature of about 850°-2500° F. into a vaporization chamber; contacting said fluidizable solids with said hot turbulent gas in a hot gas-fluidizable solids first fluidized bed contacting zone in a lower portion of said vaporization chamber to fluidize at least a portion of said fluidizable solids in said lower portion of said vaporization chamber, to vaporize a majority of said polychlorinated biphenyls from said fluidizable solids in said lower portion thereby forming a gaseous stream recoverable from said vaporization chamber; and to cool said hot gases; conveying said cooled hot gas upwardly through said vaporization chamber at a rate sufficient to propel a finer particulate portion of the fluidizable solids above the first fluidized bed contacting zone to a second fluidized bed contacting zone at a lower temperature than, and disposed above, said first fluidized bed contacting zone, whereby a finer particulate portion of the fluidizable solids is fluidized by said cooled hot gases and additional polychlorinated biphenyls are vaporized from said fluidized finer particulates in said second fluidized bed contact zone; recycling a portion of the fluidizable solids particulates from the second fluidized bed down to the first fluidized bed for further vaporization of polychlorinated biphenyls from said recycled particulates; and removing said gaseous stream containing said gases and vaporized polychlorinated biphenyls from the vaporization chamber for further treatment.
Claim 22
Dependent Claim
18 words
The method of claim 18 wherein the second fluidized bed has a temperature of 250° to 500° F.
Claim 23
Dependent Claim
18 words
The method of claim 19 wherein the second fluidized bed has a temperature of 300° to 350° F.
Claim 24
Dependent Claim
20 words
The method of claim 18 including separating the fluidizable solids particulates from the gaseous stream removed from the vaporization chamber.
Claim 25
Dependent Claim
20 words
The method of claim 18 including condensing the vaporized polychlorinated biphenyls from the gaseous stream removed from the vaporization chamber.
Claim 26
Dependent Claim
23 words
The method of claim 18 including grinding the fluidizable solids in the vaporization chamber while contacting said fluidizable solids with said hot gas.
Claim 27
Dependent Claim
62 words
The method of claim 23 wherein said first fluidized bed is disposed below an area in said vaporization chamber where said fluidizable solids are ground and including conveying a coarser portion of the ground fluidizable solids down to said first fluidized bed and agitating the coarser fluidizable solids in said first fluidized bed to achieve more efficient vaporization of said polychlorinated biphenyls.
Claim 28
Dependent Claim
51 words
The method of claim 18 wherein the vaporization chamber includes a rotating member having radially extending blades disposed in an upper portion of the vaporization chamber whereby a portion of the particulates entrained in the rising gas is mechanically pushed downwardly by said blades for recycling to said first fluidized bed.
References Cited (Backward Citations)
US4140066A
Cited
US4699721A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-12-27 | 1992-06-27 | 1992-12-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-12-27 | 1996-06-27 | 1996-12-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-12-27 | 2000-06-27 | 2000-12-27 | $7700.00 | Window Closed / Lapsed |