IP Library Granted Patent US 7,622,092
Granted Patent B2
US 7,622,092 · App. 11/798,365 · Granted Nov 24, 2009

Method and device for removing mercury

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Quick Facts
Patent No.
US 7,622,092
App. No.
11/798,365
Granted
Nov 24, 2009
Kind
B2
Abstract

A mercury removing device includes a gasification unit that converts a non-gaseous-mercury-chlorinating agent, which is non-gaseous at room temperature and normal pressure, into gaseous-mercury-chlorinating agent by heating the non-gaseous-mercury-chlorinating agent with heat of hot air generated by using the exhaust gas or hot air generated by using an air heater installed in a flue that conveys the exhaust gas. The gaseous-mercury-chlorinating agent produced in this manner is supplied to the exhaust gas in the flue.

Claims (27)

1. A method of removing mercury from exhaust gas that contains nitrogen oxide, sulfur oxide, and mercury, the method comprising:

converting a non-gaseous-mercury-chlorinating agent, which is non-gaseous at room temperature and normal pressure, into gaseous-mercury-chlorinating agent by heating the non-gaseous-mercury-chlorinating agent with heat of hot air generated by using the exhaust gas or hot air generated by using an air heater installed in a flue that conveys the exhaust gas;

supplying the gaseous-mercury-chlorinating agent to the exhaust gas in the flue thereby obtaining agent-added exhaust gas;

performing selective catalytic reduction on the agent-added exhaust gas by using a solid catalyst thereby obtaining denitrated exhaust gas; and

performing wet desulfurization on the denitrated exhaust gas by using an alkali absorbing solution thereby obtaining desulfurized exhaust gas.

2. The method according to claim 1 , further comprising removing soot from the hot air before using the hot air at the converting.

3. The method according to claim 1 , wherein a temperature of the hot air is in a range between about 300° C. and about 400° C.

4. The method according to claim 1 , further comprising:

measuring a concentration of gaseous-mercury-chlorinating agent in the desulfurized exhaust gas;

calculating an initial concentration of gaseous-mercury-chlorinating agent to be supplied to the exhaust gas at the supplying based on the concentration measured at the measuring; and

controlling an amount of the non-gaseous-mercury-chlorinating agent to be used at the converting for producing the gaseous-mercury-chlorinating agent based on the initial concentration calculated at the calculating.

5. The method according to claim 1 , wherein the non-gaseous-mercury-chlorinating agent is any one of ammonium chloride, aqueous hydrogen chloride, and liquefied chlorine.

6. A mercury removing device that removes mercury from exhaust gas that contains nitrogen oxide, sulfur oxide, the mercury removing device comprising:

a gasification unit that converts a non-gaseous-mercury-chlorinating agent, which is non-gaseous at room temperature and normal pressure, into gaseous-mercury-chlorinating agent by heating the non-gaseous-mercury-chlorinating agent with heat of hot air generated by using the exhaust gas or hot air generated by using an air heater installed in a flue that conveys the exhaust gas;

a mercury-chlorinating-agent supply unit that supplies the gaseous-mercury-chlorinating agent to the exhaust gas in the flue thereby obtaining agent-added exhaust gas;

a selective catalytic reducer that performs selective catalytic reduction on the agent-added exhaust gas by using a solid catalyst thereby obtaining denitrated exhaust gas; and

a desulfurization unit that performs wet desulfurization on the denitrated exhaust gas by using an alkali absorbing solution thereby obtaining desulfurized exhaust gas.

7. The mercury removing device according to claim 6 , wherein a temperature of the hot air is in a range between about 300° C. and about 400° C.

8. The mercury removing device according to claim 6 , further comprising:

a concentration measuring unit that measures a concentration of gaseous-mercury-chlorinating agent in the desulfurized exhaust gas;

a calculating unit that calculates an initial concentration of the gaseous-mercury-chlorinating-agent to be supplied to the mercury-chlorinating-agent supply unit based on the concentration measured by the concentration measuring unit; and

a control unit that controls an amount of the non-gaseous-mercury-chlorinating agent to be supplied to the gasification unit for producing the gaseous-mercury-chlorinating agent based on the initial concentration calculated by the calculating unit.

9. The mercury removing device according to claim 6 , wherein the non-gaseous -mercury-chlorinating agent is any one of ammonium chloride, aqueous hydrogen chloride, and liquefied chlorine.

10. The mercury removing device according to claim 6 , further comprising:

a mercury-concentration measuring unit that measures a concentration of mercury in at least one of the denitrated exhaust gas and the desulfurized exhaust gas;

a second calculating unit that calculates an initial concentration of the gaseous-mercury-chlorinating-agent to be supplied to the mercury-chlorinating-agent supply unit based on the concentration measured by the mercury-concentration measuring unit; and

a second control unit that controls an amount of the non-gaseous-mercury-chlorinating agent to be supplied to the gasification unit for producing the gaseous-mercury-chlorinating agent based on the initial concentration calculated by the second calculating unit.

Assignments (3)
CORRECTIVE ASSIGNMENT TO CORRECT THE REMOVING PATENT APPLICATION NUMBER 11921683 PREVIOUSLY RECORDED AT REEL: 054975 FRAME: 0438. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded May 26, 2023
From: MITSUBISHI HITACHI POWER SYSTEMS, LTD.
To: MITSUBISHI POWER, LTD.
Reel/Frame 063787/0867 →
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 Feb 26, 2015
From: MITSUBISHI HEAVY INDUSTRIES, LTD.
To: MITSUBISHI HITACHI POWER SYSTEMS, LTD.
Reel/Frame 035101/0029 →