IP Library Granted Patent US 10,919,790
Granted Patent B2
US 10,919,790 · App. 14/894,991 · Granted Feb 16, 2021

Method for removing selenium and apparatus for removing selenium

Inventors: Susumu Okino (Tokyo, JP); Kazuhide Kamimura (Hyogo, JP); Tetsuya Ito (Hyogo, JP); Morikata Nishida (Hyogo, JP); Hiroyuki Nakamura (Hyogo, JP)
Assignee: MITSUBISHI POWER ENVIRONMENTAL SOLUTIONS, LTD.
C02F1/722C02F1/5236C02F1/5245C02F1/56C02F9/00C02F1/76C02F1/78C02F2101/106C02F2103/18C02F2103/365C02F2209/04C02F2305/02C10J2300/093C10J2300/169C10J2300/1643Y02E20/16Y02E20/18
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Quick Facts
Patent No.
US 10,919,790
App. No.
14/894,991
Granted
Feb 16, 2021
Kind
B2
Abstract

A method for removing selenium according to the present invention comprises: a valence change step of adding an oxidant to a wastewater from a facility that gasifies a fuel containing selenium in a reducing atmosphere, and oxidizing the selenium to change the valence of the selenium, and a solid-liquid separation step of adding a flocculant to the wastewater, forming a floc containing the selenium for which the valence has been changed in the valence change step, and subjecting the floc to solid-liquid separation.

Claims (9)

1. A method for removing selenium from a wastewater from a facility that gasifies a coal fuel containing selenium in a reducing atmosphere, the method comprising:

a valence change step of adding an oxidant to the wastewater containing selenium, and oxidizing selenium having a valence lower than +4 to change the valence of the selenium to +4, and

a solid-liquid separation step of adding a flocculant to the wastewater, forming a floc containing the selenium for which the valence has been changed in the valence change step, and subjecting the floc to solid-liquid separation,

wherein the valence change step includes a step of adjusting a pH of the wastewater to 4 before adding the oxidant to the wastewater,

the solid-liquid separation step includes a step of adjusting a pH of the wastewater to 7 using an alkali agent before adding the flocculant to the wastewater,

wherein hydrogen peroxide is used as the oxidant in the valence change step and an oxidation-reduction potential of the wastewater is controlled to a value of at least 393 mV but not more than 433 mV so as to change the valence of the selenium to +4, or sodium hypochlorite is used as the oxidant in the valence change step and an oxidation-reduction potential of the wastewater is controlled to a value of at least 630 mV but not more than 900 mV so as to change the valence of the selenium to +4,

the flocculant comprises an inorganic flocculant and a polymer flocculant, and

the polymer flocculant is an anionic polymer flocculant or a nonionic polymer flocculant.

2. The method for removing selenium according to claim 1 , wherein an iron salt is added to the wastewater in the valence change step.

Assignments (3)
CHANGE OF NAME Recorded Dec 17, 2020
From: MITSUBISHI HITACHI POWER SYSTEMS ENVIRONMENTAL SOLUTIONS, LTD.
To: MITSUBISHI POWER ENVIRONMENTAL SOLUTIONS, LTD.
Reel/Frame 054798/0846 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 16, 2016
From: MITSUBISHI HEAVY INDUSTRIES MECHATRONICS SYSTEMS, LTD.
To: MITSUBISHI HITACHI POWER SYSTEMS ENVIRONMENTAL SOLUTIONS, LTD.
Reel/Frame 039460/0071 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 30, 2015
From: OKINO, SUSUMU; KAMIMURA, KAZUHIDE; ITO, TETSUYA; NISHIDA, MORIKATA; NAKAMURA, HIROYUKI
To: MITSUBISHI HEAVY INDUSTRIES MECHATRONICS SYSTEMS, LTD.
Reel/Frame 037172/0602 →
Continuity (1)
Related Publication 20160115053A1 · Apr 28, 2016