Process and plant for separating heavy metals from phosphoric starting material

Patent metadata

Field	Value
Publication number	US-9840415-B2
Application number	US-201314409487-A
Country	US
Kind code	B2
Filing date	Jun 21, 2013
Priority date	Jun 21, 2012
Publication date	Dec 12, 2017
Grant date	Dec 12, 2017

Abstract

A process for separating heavy metals from a phosphoric starting material includes, in a step (i), heating the starting material to a temperature between 700 and 1,100° C. in a first reactor and withdrawing combustion gas. In a step (ii), the heated starting material at the temperature between 700 and 1,100° C. is transferred to a second reactor, chlorides of alkaline and alkaline earth metals are added and process gas is withdrawn.

First claim

The invention claimed is:

1. A process for separating heavy metals from a phosphoric starting material, the process comprising:
(i) heating the starting material by combustion of fuel with air to a temperature between 700 and 1,100° C. in a first reactor and withdrawing combustion gas;
(ii) transferring the heated starting material at the temperature between 700 and 1,100° C. to a second reactor, adding chlorides of alkaline and alkaline earth metals to the heated starting material and withdrawing process gas so as to obtain a semi-product; and
(iii) admixing and homogenizing a measured quantity of triple-superphosphate, phosphate rock or phosphoric acid to the semi-product so as to obtain a final product having a phosphate concentration.

2. The process according to claim 1 , further comprising quenching the process gas after withdrawal from the second reactor.

3. The process according to claim 1 , further comprising filtering the process gas or reacting the process gas with magnesite so as to form a solid salt.

4. The process according to claim 3 , wherein the solid salt is recycled to step (ii).

5. The process according to claim 1 , wherein the air and the fuel are supplied to the first reactor in step (i).

6. The process according to claim 5 , further comprising preheating at least one of the starting material, the fuel and the air using the combustion gas withdrawn from the first reactor and recycled for the preheating.

7. The process according to claim 6 , wherein at least one of outlet gas from the preheating, the combustion gas and the process gas are separately or in combination passed through at least one cleaning stage.

8. The process according to claim 1 , further comprising mixing the final product with a nutrient carrier and granulating the final product.

9. The process according to claim 1 , wherein the starting material in step (i) is sewage sludge ash.

Assignees

• Outotec Finland Oy

Inventors

• Lohrberg Dirk
• Stegemann Bertold
• Schneider Guenter
• Hermann Ludwig

Classifications

• C02F11/10

  by pyrolysis · CPC title

• B01J2208/00017

  Controlling the temperature · CPC title

• B01J8/24

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• B01J8/1836

  Heating and cooling the reactor (B01J8/42 takes precedence) · CPC title

• C02F11/004

  Sludge detoxification · CPC title