Apparatus and method for controlled alumina supply

1. An effluent gas treatment system ( 26 ) comprising:

a dedicated effluent gas treatment system ( 26 ) arranged a level vertically above that of an aluminum electrolytic cell ( 14 );

a housing ( 60 ) having an at least partially porous bottom ( 60 A) and defining an interior area ( 62 ) of the dedicated effluent gas treatment system ( 26 );

a flow control device ( 64 ) arranged vertically within the interior area ( 62 ) comprising an elongated hollow first portion ( 68 ) and a tapered second portion ( 78 ), the flow control device ( 64 ) arranged a predetermined distance (D) from the at least partially porous bottom ( 60 A) of the housing ( 60 );

an adsorbent hopper ( 24 ) extending across the at least partially porous bottom ( 60 A) of the housing ( 60 ) between the flow control device ( 64 ) and a dry scrubber contact reactor ( 46 );

a feeding pipe ( 30 ) fluidly connected between the adsorbent hopper ( 24 ) and the aluminum electrolytic cell ( 14 ) for supplying adsorbent (A) to the aluminum electrolytic cell ( 14 ); and

an effluent gas outlet ( 104 ) in a cell housing ( 36 ) for the aluminum electrolytic cell ( 14 ), fluidly connected to the dry scrubber contact reactor ( 46 ) for interaction of the effluent gas (EG) with adsorbent (A) supplied from the adsorbent hopper ( 24 ) to produce contacted gas (CG).

2. The effluent gas treatment system ( 26 ) of claim 1 , further comprising booster devices ( 124 ) to alter or boost adsorbent (A) fluidization within the effluent gas treatment system ( 26 ).

3. The effluent gas treatment system ( 26 ) of claim 1 , further comprising a fabric filter ( 48 ) comprising a plurality of removable fabric filter bags ( 100 ) arranged within the housing ( 60 ) at a level vertically above that of the flow control device ( 64 ), the adsorbent hopper ( 24 ), and the dry scrubber contact reactor ( 46 ).

4. The effluent gas treatment system ( 26 ) of claim 1 , wherein the flow control device ( 64 ) and/or a portion of the dry scrubber contact reactor ( 46 ) is movable to affect a rate of supply of adsorbent (A).

5. A flow control device ( 64 ) comprising:

a vertically arranged elongated hollow first portion ( 68 ) having an open bottom end ( 76 ) and an open top end ( 70 );

a vertically arranged second portion ( 78 ) defining an open interior area ( 80 ), the second portion ( 78 ) comprising a tapering wall ( 84 ) extending between a base edge ( 82 ) and a connection top ( 86 ), wherein the connection top ( 86 ) is fluidly connected to the open bottom end ( 76 ) of the first portion ( 68 );

an adsorbent supply ( 72 ) fluidly connected to the open top end ( 70 ) of the first portion ( 68 ); and

a portion of an adsorbent hopper ( 24 ) arranged a predetermined distance (D) vertically below the flow control device ( 64 );

wherein the flow control device ( 64 ) is mechanically operable to control a rate of supply of adsorbent (A) to a dry scrubber contact reactor ( 46 ) based on a rate of adsorbent (A) demand by an aluminum electrolytic cell ( 14 ).

6. The flow control device ( 64 ) of claim 5 , wherein the base edge ( 82 ) of the second portion ( 78 ) is arranged vertically below a top surface (S) of adsorbent (A) in the adsorbent hopper ( 24 ).

7. The flow control device ( 64 ) of claim 5 , wherein the first portion ( 68 ) is tubular.

8. The flow control device ( 64 ) of claim 5 , wherein the base edge ( 82 ) of the second portion ( 78 ) is of a larger dimension than that of the connection top ( 86 ) of the second portion ( 78 ).

9. A method of using a flow control device ( 64 ) comprising:

providing the flow control device ( 64 ) assembled by:

vertically arranging an elongated hollow first portion ( 68 ) having an open bottom end ( 76 ) and an open top end ( 70 );

vertically arranging a second portion ( 78 ) defining an open interior area ( 80 ), the second portion ( 78 ) comprising a tapered wall ( 84 ) extending between base edge ( 82 ) and a connection top ( 86 ), wherein the connection top ( 86 ) is fluidly connected to the open bottom end ( 76 ) of the first portion ( 68 );

fluidly connecting an adsorbent supply ( 72 ) to the open top end ( 70 ) of the first portion ( 68 ); and

arranging a portion of an adsorbent hopper ( 24 ) at a predetermined distance (D) vertically below the flow control device ( 64 ); and

operating the flow control device ( 64 ) to control a rate of supply of adsorbent (A) to a dry scrubber contact reactor ( 46 ) based on a rate of adsorbent (A) demand by an aluminum electrolytic cell ( 14 ).

10. The method of claim 9 , wherein adsorbent (A) flows via gravity through the flow control device ( 64 ) from the open top end ( 70 ) of the first portion ( 68 ) to the base edge ( 82 ) of the second portion ( 78 ).

11. The method of claim 9 , further comprising increasing the rate of supply of adsorbent (A) to the dry scrubber contact reactor ( 46 ) via a booster device ( 124 ).

12. The method of claim 9 , further comprising reducing the rate of supply of adsorbent (A) to the dry scrubber contact reactor ( 46 ) through static adsorbent (A) build-up in the open interior area ( 80 ) defined by the second portion ( 78 ).

13. The method of claim 9 , further comprising reducing the rate of supply of adsorbent (A) flow through the flow control device ( 64 ) to the dry scrubber contact reactor ( 46 ) through static adsorbent (A) build-up in the open interior area ( 80 ) defined by the second portion ( 78 ) and static adsorbent (A) build-up below the second portion ( 78 ).

14. The method of claim 9 , wherein the base edge ( 82 ) of the second portion ( 78 ) is of a larger dimension than that of the connection top ( 86 ) of the second portion ( 78 ).

15. The method of claim 9 , wherein the connection top ( 86 ) of the second portion ( 78 ) is of like dimension and configuration as that of the open bottom end ( 76 ) of the first portion ( 68 ).