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US4159310A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for recovering aluminum and other metal values from fly ash

Assignee: Public Service Company of New Mexico
•
Filing: 1978-01-30
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Granted: 1979-06-26
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Expires: 1998-01-30
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Abstract

Abstract A process for recovering aluminum from fly ash containing iron, silicon and titanium which comprises: (a) chlorinating the fly ash in an oxidizing atmosphere to selectively chlorinate and vaporize iron chloride from the remaining chlorides, (b) chlorinating the residue from step (a) in a reducing atmosphere of carbon monoxide, in the presence of added silicon chloride to suppress the chlorination of silicon, and vaporizing the chlorides of aluminum, silicon, titanium, and the residual iron, (c) separating and recovering the vaporized chlorides by selective condensation, and treating the residue of step (b) with sulfuric acid to convert calcium chloride to gypsum, and to regenerate a chloridizing and binder solution for pelletizing fly ash feed.

Inventors

  • 👤 James E. Reynolds
  • 👤 Alan R. Williams

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 08:05
CPC Classifications
C; C01; C01B; C01B33/00; C01B33/08; C01B33/107; C01B33/1071; C01B33/10715; C01B33/10721; B; B01; B01D; B01D49/00; B01D53/00; B01D53/34; B01D53/46; B01D53/68; C01F; C01F7/00; C01F7/48; C01F7/56; C01F7/58; C01F7/60; C01G; C01G23/00; C01G23/02; C01G23/022; C01G49/00; C01G49/10; C22; C22B; C22B21/00; C22B21/0038; C22B21/0046; C22B7/00; C22B7/02; Y; Y02; Y02P; Y02P10/00; Y02P10/20

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 122 words
A process for recovering aluminum from fly ash containing aluminum, iron and (silica) silicon which comprises: (a) chlorinating the material by subjecting it to the action of chlorine at a temperature of about 500° C.-1200° C. in an oxidizing atmosphere in the presence of added oxygen in an amount equal to about 5-100 volume percent of the chlorine to selectively vaporize iron as iron chloride; (b) chlorinating the residue from step (a) by subjecting it to the action of chlorine at a temperature of about 500° C.-1200° C. in a reducing atmosphere in the absence of solid carbon to vaporize the chlorides of aluminum (tatanium) and silicon; and (c) separating and recovering the formed (reacted) chlorides from the vapors by selective condensing.
Claim 2
Dependent Claim 122 words
A process for recovering aluminum from fly ash containing aluminum, iron and (silica) silicon which comprises: (a) chlorinating the material by subjecting it to the action of chlorine at a temperature of about 500° C.-1200° C. in an oxidizing atmosphere in the presence of added oxygen in an amount equal to about 5-100 volume percent of the chlorine to selectively vaporize iron as iron chloride; (b) chlorinating the residue from step (a) by subjecting it to the action of chlorine at a temperature of about 500° C.-1200° C. in a reducing atmosphere in the absence of solid carbon to vaporize the chlorides of aluminum (tatanium) and silicon; and (c) separating and recovering the formed (reacted) chlorides from the vapors by selective condensing.
Claim 3
Dependent Claim 25 words
The process of claim 1 in which the reductive chlorination of step (b) is performed in the presence of carbon monoxide as a reducing agent.
Claim 4
Dependent Claim 32 words
The process of claim 2 in which silicon tetrachloride is added to the residue from step (a) in an amount up to about 19.5 volume percent to suppress the chlorination of silicon.
Claim 5
Dependent Claim 19 words
The process of claim 3 in which the silicon tetrachloride is mixed with chlorine used as the chlorinating agent.
Claim 6
Dependent Claim 33 words
The process of claim 3 in which the reductive chlorination of step (b) is performed at about 1050° C. in the presence of silicon tetrachloride at a concentration of about 3 volume percent.
Claim 7
Dependent Claim 35 words
The process of claim 1 wherein the fly ash contains calcium and in which the material (residue of solid chlorides) from step (b) remaining after vaporization is reacted with sulfuric acid to produce disposable gypsum.
Claim 8
Dependent Claim 18 words
The process of claim 1 in which chlorine and oxygen are mixed for the chlorination of step (a).
Claim 9
Dependent Claim 25 words
The process of claim 1 in which the reductive chlorination of step (b) is performed in the presence of carbon monoxide as a reducing agent.
Claim 10
Dependent Claim 24 words
The process of claim 8 in which the carbon monoxide is introduced at a volume percent of about 20 percent to about 80 percent.
Claim 11
Dependent Claim 32 words
The process of claim 8 in which silicon tetrachloride is added to the residue from step (a) in an amount up to about 19.5 volume percent to suppress the chlorination of silicon.
Claim 12
Dependent Claim 18 words
The process of 10 in which the silicon tetrachloride is mixed with chlorine used as the chlorinating agent.
Claim 13
Dependent Claim 18 words
The process of 10 in which the silicon tetrachloride is mixed with chlorine used as the chlorinating agent.
Claim 14
Dependent Claim 23 words
The process of claim 11 in which the silicon tetrachloride is introduced in an amount of about 2.5 to about 19.5 volume percent.
Claim 15
Dependent Claim 40 words
The process of claim 1 wherein the fly ash contains calcium and in which the material (residue of solid chlorides) from step (b) remaining after vaporization is reacted with sulfuric acid to produce disposable gypsum and to form hydrochloric acid.
Claim 16
Dependent Claim 13 words
The process of claim 13 in which the fly ash feed is pelletized.
Claim 17
Dependent Claim 23 words
The process of claim 14 in which the fly ash feed is pelletized and bentonite is used as a binder for the pellets.
Claim 18
Dependent Claim 32 words
The process of claim 1 in which titanium is present in said fly ash and it is chlorinated in accordance with step (b) and separated and recovered in accordance with step (c).

References Cited (Backward Citations)

US1147832A Cited
US1600216A Cited
US1605098A Cited
US1875105A Cited
US1866731A Cited
US3244509A Cited
US3466169A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-06-25 1982-12-25 1983-06-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-06-25 1986-12-25 1987-06-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-06-25 1990-12-25 1991-06-26 $7700.00 Window Closed / Lapsed

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