# US 9,751,762 B2 · Method for recycling organic waste material

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- Number: US 9,751,762 B2
- Document ID: US9751762B2
- Status: Granted
- Kind: B2
- Application number: 13/885,585
- Filed: 2011-10-18
- Published: 2013-10-17
- Granted: 2017-09-05
- Earliest claimed: 2010-11-15
- Assignees: ICL Europe Cooeperatief U.A.
- Applicants: Alfred Edlinger
- Inventors: Alfred Edlinger
- Web page: https://patentgrep.com/patent/US9751762B2

## CPC

- C01B 25/08: Other phosphides
- C01B 25/01: Treating phosphate ores or other raw phosphate materials to obtain phosphorus or phosphorus compounds
- C01B 25/02: Preparation of phosphorus
- C02F 11/18: by thermal conditioning (by pyrolysis C02F11/10)
- C02F 11/004: {Sludge detoxification}
- C02F 11/06: by oxidation (incinerators for burning waste liquors, e.g. sulfite liquor from paper-making plant F23G7/04)
- Y02W 10/40: Valorisation of by-products of wastewater, sewage or sludge processing
- C01B: NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; {METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C}
- C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes)
- Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT

## Abstract

A method for recycling organic waste material containing phosphorus oxides and metal oxides is particularly suited for recycling sewage sludge. The waste materials are mixed with chlorine carriers and then heat-treated at an air ratio of 0.85≦λ≦1.6 and at least partially oxidized. The metal chlorides thus formed are drawn off and recovered and the fraction remaining after the metal chlorides have been drawn off is subjected to reduction in order to obtain elemental phosphorus.

## Claims

### Claim 1

A method of extracting phosphorous or a derivative thereof from organic waste material containing oxides of phosphorus and metal oxides, the method which comprises:
mixing chlorine carriers into the organic waste material and adding lime to the waste material, to form a waste material admixture supplemented with chlorine carriers and lime;
heating the resulting admixture at an air ratio of 0.85≦λ≦ to 1.6 and at least partially oxidizing;
drawing off volatile metal chlorides thus formed with the gas phase, leaving a remaining melt fraction;
recovering the metal chlorides;
subjecting the remaining melt fraction which contains phosphorous to a reduction process to form gaseous elemental phosphorus or a derivative thereof; and
drawing off the gaseous elemental phosphorous or a derivative thereof.

### Claim 2 (depends on 1)

The method according to claim 1 wherein the organic waste material is sewage sludge.

### Claim 3 (depends on 1)

The method according to claim 1, wherein the heat-treating step comprises heat treatment at temperatures of 1300° C.-1600° C.

### Claim 4 (depends on 1)

The method according to claim 1, wherein the heating step comprises forcing the organic waste material mixed with the chlorine carriers into a combustion chamber with a carrier gas via a cyclone.

### Claim 5 (depends on 4)

The method according to claim 4, wherein an oxygen-containing gas is used as the carrier gas.

### Claim 6 (depends on 5)

The method according to claim 5, wherein the oxygen-containing carrier gas is hot air.

### Claim 7 (depends on 1)

The method according to claim 1, wherein the chlorine carriers are selected from the group consisting of chlorine-containing polymers, alkali chlorides, alkaline-earth chlorides, cement kiln dust, and steel mill dust.

### Claim 8 (depends on 1)

The method according to claim 1, wherein reducing the fraction remaining after drawing off metal chlorides is effected with an at least partially inductively heated column with lump coke and/or graphite, and the elemental phosphorus thereby liberated is drawn off.

### Claim 9 (depends on 8)

The method according to claim 8, wherein the phosphorus which is drawn off is quenched to obtain white phosphorus.

### Claim 10 (depends on 1)

The method according to claim 1, wherein the reduction process is performed in an inductively heated reactor controlled by electrical power and a redox potential of a column is adjusted by blowing in gases and adjusting a temperature of the column by adjusting the electrical power and by blowing in gases.

### Claim 11 (depends on 1)

A method according to claim 1, wherein the organic waste material contains iron oxide.

### Claim 12 (depends on 1)

A method according to claim 1, wherein the waste material supplemented with chloride carriers and lime is conveyed into the interior of a combustion chamber where a ratio of air, O2, and chloride gaseous carriers is set, the temperature is 1300° C.-1600° C., the product gas which contains the metal chlorides is drawn off via a discharge line and is separated from the melt, said melt being sent to a coke and/or graphite bed which is inductively heated, wherein reduction to elemental phosphorous occurs in the bed and the phosphorous is drawn off and condensed.