Flue gas treatment system and method

Patent metadata

Field	Value
Publication number	US-10005030-B2
Application number	US-201615014190-A
Country	US
Kind code	B2
Filing date	Feb 3, 2016
Priority date	Feb 17, 2015
Publication date	Jun 26, 2018
Grant date	Jun 26, 2018

Abstract

The flue gas treatment system ( 1 ) comprises a reactor ( 2 ), a pre-separator ( 3 ) downstream of the reactor ( 2 ), a separator ( 4 ) such as a fabric filter downstream of the pre-separator ( 3 ), a humidifier ( 5 ) downstream of the separator ( 4 ), a supply ( 7 ) of a pure fresh reagent into the flue gas (FG) downstream of the pre-separator ( 3 ) and upstream of or at the separator ( 4 ).

First claim

The invention claimed is:

1. A flue gas treatment system for a flue gas containing HCl and SO 2 , the system comprising:
a reactor;
a pre-separator downstream of the reactor;
a separator downstream of the pre-separator;
a humidifier downstream of the separator and connected to the reactor;
a supply of a pure fresh reagent into the flue gas downstream of the pre-separator and upstream of or at the separator; and
a collector connected to the pre-separator and to the separator and to the humidifier.

2. The system of claim 1 , wherein the collector is operable for mixing second dust products with a part of first dust products removed at the pre-separator for supply of this mixture to the humidifier.

3. The system of claim 1 , wherein the supply is only provided downstream of the pre-separator and upstream of or at the separator.

4. The system of claim 1 , wherein the separator comprises a fabric filter.

5. The system of claim 1 , wherein the pre-separator is operative to remove from the flue gas between 50-99% by weight and preferably 70-99% by weight of first dust products.

6. The system of claim 1 , wherein the pre-separator includes a cyclone.

7. The system of claim 1 , wherein the pre-separator includes an adjustable cyclone.

8. The system of claim 1 , wherein the reactor is arranged for reacting at least a part of HCl and/or SO 2 contained in the flue gas with a reactive dust forming first dust products, the pre-separator is arranged for removing a part of the first dust products from the flue gas and forwarding the flue gas containing a remainder of the first dust products to the separator, the separator is arranged for further reacting the HCl and/or SO 2 contained in the flue gas to contribute to generate second dust products and for removing the second dust products from the flue gas, the humidifier is arranged for humidifying the second dust products forming reactive dust and supplying the reactive dust to the reactor.

9. A method for treatment of a flue gas containing HCl and SO 2 , the method comprising:
reacting in a reactor at least a part of HCl and/or SO 2 contained in the flue gas with a reactive dust forming first dust products;
removing in a pre-separator a part of the first dust products from the flue gas and forwarding the flue gas containing a remainder of the first dust products to a separator;
removing in the separator second dust products from the flue gas;
humidifying in a humidifier the second dust products forming the reactive dust;
supplying the reactive dust to the reactor;
supplying a pure fresh reagent into the flue gas after removing in a pre-separator and before or during removing in the separator, and then further reacting the HCl and/or SO 2 contained in the flue gas to obtain the second dust products; and
mixing in a collector connected to the pre-separator and to the separator and to the humidifier, the second dust products with the part of the first dust products removed at the pre-separator for supply of this mixture to the humidifier.

10. The method of claim 9 , wherein the humidifier includes a water supply.

11. The method of claim 9 , further comprising supplying the pure fresh reagent only after removing in a pre-separator and before or during removing in the separator.

12. The method of claim 9 , wherein the separator comprises a fabric filter.

13. The method of claim 9 , further comprising removing from the flue gas, at the pre-separator, between 50-99% by weight and preferably 70-99% by weight of the first dust products.

14. The method of claim 9 , further comprising removing from the flue gas, at the pre-separator, between 50-99% by weight and preferably 70-99% by weight of the first dust products, and adjusting the amount of first dust products that is removed from the flue gas on the basis of:
a required SO 2 removal rate or a parameter indicative thereof, and/or
a required HCl removal rate or a parameter indicative thereof, and/or
a CaOHCl content in the first and/or second dust products or a parameter indicative thereof, and/or
a Cl total content in the first and/or second dust products or a parameter indicative thereof, and/or
an amount of fresh reagent supplied via the supply or a parameter indicative thereof.

15. The method of claim 9 , wherein the pre-separator includes a cyclone.

Assignees

• Alstom Technology Ltd
• General Electric Technology Gmbh

Inventors

• Råhlin Robert

Classifications

• B01D2258/0291

  from waste incineration plants · CPC title

• F23J2217/40

  by cyclones · CPC title

• B01D53/83 Primary

  with moving reactants · CPC title

• B01D2251/604

  Hydroxides · CPC title

• F23J2217/101

  Baghouse type · CPC title