Wet type flue-gas desulfurization method

Patent metadata

Field	Value
Publication number	US-9327236-B2
Application number	US-201514638801-A
Country	US
Kind code	B2
Filing date	Mar 4, 2015
Priority date	Aug 12, 2011
Publication date	May 3, 2016
Grant date	May 3, 2016

Abstract

A wet type flue-gas desulfurization apparatus, into which exhaust gas containing mercury goes, includes an upstream absorption tower, an upstream absorbent spray nozzle and a make-up water supply unit on an upstream side of a desulfurization apparatus body in a flow direction of the gas. The upstream absorption tower has a circulation tank reserving absorbent slurry. The make-up water supply unit supplies make-up water into the circulation tank to keep the chloride ion concentration of the absorbent in the circulation tank not lower than 50,000 ppm. Thus, it is possible to provide a wet type flue-gas desulfurization apparatus by which Hg can be prevented from being released again from the desulfurization apparatus, the purity of recovered gypsum can be increased and the usage of industrial water can be reduced.

First claim

What is claimed is:

1. A wet type flue-gas desulfurization method for desulfurizing by using a wet type flue-gas desulfurization apparatus comprising:
an apparatus body side absorption tower which has an apparatus body side circulation tank in a lower portion thereof, the apparatus body side circulation tank reserving absorbent slurry;
an apparatus body side absorbent spray nozzle which is placed inside the apparatus body side absorption tower to spray the absorbent slurry;
an oxidation gas supply portion which supplies oxidation gas to the absorbent slurry reserved in the apparatus body side circulation tank; and
a desulfurization apparatus body which includes the apparatus body side absorption tower, the apparatus body side absorbent spray nozzle and the oxidation gas supply portion, and in which gas to be treated, containing sulfur compounds, is introduced into the apparatus body side absorption tower and brought into gas-liquid contact with the absorbent slurry sprayed from the apparatus body side absorbent spray nozzle, so that the sulfur compounds in the gas to be treated can be absorbed by the absorbent slurry; wherein:
the gas to be treated contains mercury;
the desulfurization apparatus is provided with, on an upstream side of the desulfurization apparatus body in a flow direction of the gas to be treated:
an upstream absorption tower which includes an upstream circulation tank reserving absorbent slurry;
an upstream absorbent spray nozzle which is placed inside the upstream absorption tower to spray the absorbent slurry; and
a make-up water supply unit which supplies make-up water into the upstream circulation tank,
the method comprising the acts of:
keeping a chloride ion concentration of the absorbent slurry in the upstream circulation tank not lower than 50,000 ppm by a process in which the make-up water supply unit supplies make-up water into the upstream circulation tank;
collecting liquid by an upstream mist eliminator provided between the upstream absorbent spray nozzle and the desulfurization apparatus body; and
returning the collected liquid obtained by the upstream mist eliminator to the upstream absorption tower.

2. A wet type flue-gas desulfurization method according to claim 1 , wherein:
the make-up water is seawater.

3. A wet type flue-gas desulfurization method according to claim 1 , wherein:
the make-up water is chloride-ion concentrated water obtained by a concentrated water manufacturing apparatus.

4. A wet type flue-gas desulfurization method according to claim 3 , wherein:
the concentrated water manufacturing apparatus is a desalination apparatus which obtains water from seawater so that the water obtained by the desalination apparatus is used as rinse water for gypsum obtained by reaction between the gas to be treated and the absorbent.

Assignees

• Mitsubishi Hitachi Power Sys

Inventors

• Mitsui Yoshiaki
• Ishizaka Hiroshi
• Omine Naruhito
• Katagawa Atsushi
• Ochiai Ryota

Classifications

• F23J2215/60

  Heavy metals; Compounds thereof · CPC title

• B01D53/75

  Multi-step processes · CPC title

• B01D53/78 Primary

  with gas-liquid contact · CPC title

• B01D53/64

  Heavy metals or compounds thereof, e.g. mercury · CPC title

• B01D2251/606

  Carbonates · CPC title