IP Library Granted Patent US 7,871,586
Granted Patent B2
US 7,871,586 · App. 11/921,683 · Granted Jan 18, 2011

Mercury removal system and method

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Quick Facts
Patent No.
US 7,871,586
App. No.
11/921,683
Granted
Jan 18, 2011
Kind
B2
Abstract

The present invention provides a mercury removal system and method for effectively removing a mercury component, which is present in a gas stream in an extremely small amount in wet gas cleaning. The mercury removal system in wet gas cleaning includes a water washing tower for introducing therein a target gas containing a mercury component and transferring the mercury component into an absorbing solution, a flash drum ( 10 ) for flashing the absorbing solution discharged from the water washing tower to separate the absorbing solution into a gas component and waste water, an oxidation treatment means ( 1 ) for adding an oxidizing agent to the absorbing solution at the preceding stage of the flash drum, and a waste water treatment means for subjecting to coagulation sedimentation treatment the separated waste water containing the mercury component at the following stage of the flash drum to dispose of the mercury component as sludge.

Claims (25)

1. A mercury removal system in wet gas cleaning, comprising a water washing tower for introducing thereinto a target gas containing a mercury component and transferring the mercury component into an absorbing solution, and a flash drum for flashing the absorbing solution discharged from the water washing tower to separate the absorbing solution into a gas component and waste water,

characterized in that the system further comprises an oxidation treatment means for adding an oxidizing agent to the absorbing solution at the preceding stage of the flash drum, and a waste water treatment means for subjecting to coagulation sedimentation treatment the separated waste water containing the mercury component at the following stage of the flash drum to dispose of the mercury component as sludge.

2. A mercury removal system in wet gas cleaning, comprising a water washing tower for introducing thereinto a target gas containing a mercury component and transferring the mercury component into an absorbing solution, and a flash drum for flashing the absorbing solution discharged from the water washing tower to separate the absorbing solution into a gas component and waste water,

characterized in that the system further comprises a coagulation sedimentation treatment means for adding a coagulant aid to the absorbing solution at the preceding stage of the flash drum to remove the mercury component from the absorbing solution as sludge.

3. The mercury removal system according to claim 1 , characterized in that the system further comprises

a hydrogen sulfide absorption tower for introducing thereinto a water-washed gas sent from the water washing tower and absorbingly removing hydrogen sulfide from the water-washed gas by using an absorbing solution containing an amine compound, and

a second flash drum for flashing the absorbing solution discharged from the hydrogen sulfide absorption tower to separate the absorbing solution into a gas component and an absorbing solution to be sent to a regeneration tower.

4. The mercury removal system according to claim 1 , characterized in that the target gas is a product gas obtained by gasifying a fossil fuel by a gasification furnace.

5. A mercury removal method in wet gas cleaning, comprising a water washing step of introducing a target gas containing a mercury component into an absorbing solution and transferring the mercury component from the target gas into the absorbing solution, and a flash step of flashing the absorbing solution discharged from the water washing step to separate the absorbing solution into a gas component and waste water,

characterized in that the method further comprises an oxidation treatment step of adding an oxidizing agent to the absorbing solution at the upstream of the flash step, and a waste water treatment step of subjecting to coagulation sedimentation treatment the separated waste water containing the mercury component at the downstream of the flash step to dispose of the mercury component as sludge.

6. A mercury removal method in wet gas cleaning, comprising a water washing step of introducing a target gas containing a mercury component into an absorbing solution and transferring the mercury component from the target gas into the absorbing solution, and a flash step of flashing the absorbing solution discharged from the water washing step to separate the absorbing solution into a gas component and waste water,

characterized in that the method further comprises

a coagulation sedimentation step of adding a coagulant aid to the absorbing solution at the upstream of the flash step to remove the mercury component from the absorbing solution as sludge.

7. The mercury removal method according to claim 5 , characterized in that the method further comprises

a hydrogen sulfide absorption step of absorbingly removing hydrogen sulfide from a water-washed gas sent and introduced from the water washing step by using an absorbing solution containing an amine compound, and

a second flash step of flashing the absorbing solution discharged from the hydrogen sulfide absorption step to separate the absorbing solution into a gas component and an absorbing solution to be sent to a regeneration tower.

8. The mercury removal method according to claim 5 , characterized in that the target gas is a product gas obtained by gasifying a fossil fuel by a gasification furnace.

9. The mercury removal system according to claim 2 , characterized in that the system further comprises

a hydrogen sulfide absorption tower for introducing thereinto a water-washed gas sent from the water washing tower and absorbingly removing hydrogen sulfide from the water-washed gas by using an absorbing solution containing an amine compound, and

a second flash drum for flashing the absorbing solution discharged from the hydrogen sulfide absorption tower to separate the absorbing solution into a gas component and an absorbing solution to be sent to a regeneration tower.

10. The mercury removal system according to claim 2 , characterized in that the target gas is a product gas obtained by gasifying a fossil fuel by a gasification furnace.

11. The mercury removal method according to claim 6 , characterized in that the method further comprises

a hydrogen sulfide absorption step of absorbingly removing hydrogen sulfide from a water-washed gas sent and introduced from the water washing step by using an absorbing solution containing an amine compound, and

a second flash step of flashing the absorbing solution discharged from the hydrogen sulfide absorption step to separate the absorbing solution into a gas component and an absorbing solution to be sent to a regeneration tower.

12. The mercury removal method according to claim 6 , characterized in that the target gas is a product gas obtained by gasifying a fossil fuel by a gasification furnace.

Assignments (8)
NUNC PRO TUNC ASSIGNMENT Recorded Dec 14, 2023
From: MHI ENGINEERING, LTD.
To: MITSUBISHI HEAVY INDUSTRIES, LTD.
Reel/Frame 066014/0870 →
CHANGE OF NAME Recorded Dec 14, 2023
From: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
To: MHI ENGINEERING, LTD.
Reel/Frame 066014/0774 →
CHANGE OF NAME Recorded Jan 13, 2021
From: MITSUBISHI HITACHI POWER SYSTEMS, LTD.
To: MITSUBISHI POWER, LTD.
Reel/Frame 054975/0438 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 12, 2018
From: MITSUBISHI HEAVY INDUSTRIES, LTD.
To: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
Reel/Frame 047054/0898 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ADDRESS OF ASSIGNEE AND EXECUTION DATE OF ASSIGNOR PREVIOUSLY RECORDED ON REEL 042109 FRAME 0001. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded May 11, 2017
From: TOKYO ELECTRIC POWER CO., INC.
To: TOKYO ELECTRIC POWER COMPANY HOLDINGS, INCORPORATED
Reel/Frame 042444/0419 →
CORRECTIVE ASSIGNMENT TO CORRECT THE THE ASSIGNEE ADDRESS PREVIOUSLY RECORDED AT REEL: 041717 FRAME: 0286. ASSIGNOR(S) HEREBY CONFIRMS THE CHANGE OF NAME. Recorded Mar 29, 2017
From: TOKYO ELECTRIC POWER CO., INC
To: TOKYO ELECTRIC POWER COMPANY HOLDINGS, INCORPORATED
Reel/Frame 042109/0001 →
CHANGE OF NAME Recorded Feb 2, 2017
From: TOKYO ELECTRIC POWER CO., INC.
To: TOKYO ELECTRIC POWER COMPANY HOLDINGS, INCORPORATED
Reel/Frame 041717/0286 →
MERGER Recorded May 30, 2013
From: CLEAN COAL POWER R & D CO., LTD.
To: JOBAN JOINT POWER CO., LTD.
Reel/Frame 030510/0491 →