Gas absorbing and regenerating apparatus and method for operating same

Patent metadata

Field	Value
Publication number	US-10016718-B2
Application number	US-201514898855-A
Country	US
Kind code	B2
Filing date	Jan 21, 2015
Priority date	Jan 31, 2014
Publication date	Jul 10, 2018
Grant date	Jul 10, 2018

Abstract

When CO 2 gas is absorbed by using an absorbent circulating in an absorption tower and an absorbent regeneration tower, a first sampling part at which a lean solution sample is collected in the vicinity of an inlet for a lean solution supply line in the absorption tower, a second sampling part at which a rich solution sample is collected in the vicinity of an outlet for a rich solution supply line in the absorption tower, and an analyzing device which analyzes the collected lean solution sample and rich solution sample are provided; the lean solution sample at the first sampling part and the rich solution sample at the second sampling part are collected, respectively, in the same time period, and concentrations of CO 2 gas in the lean solution sample and the rich solution sample are measured, and then the gas absorbing/regenerating operation is controlled based on measured results.

First claim

The invention claimed is:

1. A gas absorbing and regenerating apparatus, comprising:
an absorption tower which absorbs CO 2 gas from introduced gas containing the CO 2 gas by using an amine absorbent circulating in a closed system;
an absorbent regeneration tower which releases the CO 2 gas from the amine absorbent which absorbs the CO 2 gas in the absorption tower;
a rich solution supply line which draws off the amine absorbent which absorbs the CO 2 gas in the absorption tower from the absorption tower as rich solution and introduces the amine absorbent into the absorbent regeneration tower;
a lean solution supply line which draws off the amine absorbent regenerated in the absorbent regeneration tower from the absorbent regeneration tower as lean solution and introduces the amine absorbent into the absorption tower;
a first sampling part at which a lean solution sample is collected in the vicinity of an inlet for the lean solution supply line in the absorption tower;
a second sampling part at which a rich solution sample is collected in the vicinity of an outlet for the rich solution supply line in the absorption tower; and
a total organic carbon (TOC) analyzer which analyzes CO 2 concentrations in the collected lean solution sample and rich solution sample,
wherein the gas absorbing and regenerating apparatus collects the lean solution sample at the first sampling part and the rich solution sample at the second sampling part, respectively, in the same time period, and measures the concentrations of the CO 2 gas in the lean solution sample and the rich solution sample, and then controls a flow rate of the amine absorbent introduced into the absorption tower or heat load in a reboiler based on the measured results.

2. The gas absorbing and regenerating apparatus according to claim 1 , comprising:
a packed bed unit which is provided in the absorption tower and in which the introduced gas is brought into countercurrent contact with the amine absorbent;
a gas discharge line which discharges discharge gas obtained by removal of the CO 2 gas from a top of the absorption tower;
a cleaning unit which is provided in downstream side of gas flow of the packed bed unit and cleans the discharge gas with a cleaning water; and
a third sampling part at which a gas sample is collected in the vicinity of an outlet for the gas discharge line in the absorption tower;
wherein the gas absorbing/regenerating apparatus collects the gas at the third sampling part in the same time period as the collection of the lean solution sample and the rich solution sample, and measures an amine concentration of the amine absorbent entrained in the discharge gas, and then controls at least one of a temperature of the cleaning water, the flow rate of the amine absorbent introduced into the absorption tower and the heat load in the reboiler based on the measured result.

3. A method for operating a gas absorbing and regenerating apparatus using a gas absorbing and regenerating apparatus comprising:
an absorption tower which absorbs CO 2 gas from introduced gas containing the CO 2 gas by using an amine absorbent circulating in a closed system;
an absorbent regeneration tower which releases the CO 2 gas from the amine absorbent which absorbs the CO 2 gas in the absorption tower;
a rich solution supply line which draws off the amine absorbent which absorbs the CO 2 gas in the absorption tower from the absorption tower as rich solution and introduces the amine absorbent into the absorbent regeneration tower;
a lean solution supply line which draws off the amine absorbent regenerated in the absorbent regeneration tower from the absorbent regeneration tower as lean solution and introduces the amine absorbent into the absorption tower;
a first sampling part at which a lean solution sample is collected in the vicinity of an inlet for the lean solution supply line in the absorption tower;
a second sampling part at which a rich solution sample is collected in the vicinity of an outlet for the rich solution supply line in the absorption tower; and
a total organic carbon (TOC) analyzer which analyzes CO 2 concentrations in the collected lean solution sample and rich solution sample,
wherein the gas absorbing and regenerating apparatus collects the lean solution sample at the first sampling part and the rich solution sample at the second sampling part, respectively, in the same time period, and measures the concentrations of the CO 2 gas in the lean solution sample and the rich solution sample, and then controls a flow rate of the amine absorbent introduced into the absorption tower or heat load in a reboiler based on the measured results,
the method comprising, when the introduced gas is boiler flue gas containing CO 2 , simultaneously figuring out the CO 2 concentrations of both the lean solution and the rich solution and an amine concentration of the amine solution of the lean solution, and decreasing the heat load in the reboiler when a CO 2 recovery rate by absorption satisfies a predetermined recovery rate.

4. A method for operating a gas absorbing and regenerating apparatus using a gas absorbing and regenerating apparatus comprising:
an absorption tower which absorbs CO 2 gas from introduced gas containing the CO 2 gas by using an amine absorbent circulating in a closed system;
an absorbent regeneration tower which releases the CO 2 gas from the amine absorbent which absorbs the CO 2 gas in the absorption tower;
a rich solution supply line which draws off the amine absorbent which absorbs the CO 2 gas in the absorption tower from the absorption tower as rich solution and introduces the amine absorbent into the absorbent regeneration tower;
a lean solution supply line which draws off the amine absorbent regenerated in the absorbent regeneration tower from the absorbent regeneration tower as lean solution and introduces the amine absorbent into the absorption tower;
a first sampling part at which a lean solution sample is collected in the vicinity of an inlet for the lean solution supply line in the absorption tower;
a second sampling part at which a rich solution sample is collected in the vicinity of an outlet for the rich solution supply line in the absorption tower; and
a total organic carbon (TOC) analyzer which analyzes CO 2 concentrations in the collected lean solution sample and rich solution sample,
wherein the gas absorbing and regenerating apparatus collects the lean solution sample at the first sampling part and the rich solution sample at the second sampling part, respectively, in the same time period, and measures the concentrations of the CO 2 gas in the lean solution sample and the rich solution sample, and then controls a flow rate of the amine absorbent introduced into the absorption tower or heat load in a reboiler based on the measured results;
the method comprising, when the introduced gas is gasification gas containing H 2 S and CO 2 , simultaneously figuring out the CO 2 concentrations of both the lean solution and the rich solution and an amine concentration of the lean solution, and minimizing an absorbed amount of CO 2 when a concentration of H 2 S satisfies a predetermined value.

5. The gas absorbing and regenerating apparatus according to claim 1 , comprising:
an ion chromatography (IC) analyzer which measures the amine concentration in the lean solution sample at the first sampling part;
wherein the gas absorbing and regenerating apparatus collects a sample in the same time period as the collection of a sample for measuring the CO 2 concentrations, and measures the amine concentration, and then adjusts water balance in the absorber or controls circulation amount of the amine absorbent based on the measured results of the amine concentration.

6. The method

Assignees

• Mitsubishi Heavy Ind Ltd

Inventors

• Okamoto Shinichi
• Chiyomaru Masaru
• Tanaka Hiroshi
• Nagayasu Hiromitsu
• Hirata Takuya
• Oishi Tsuyoshi
• Shimada Daisuke

Classifications

• B01D53/30

  Controlling by gas-analysis apparatus (regulating non electrical variables in general G05D) · CPC title

• B01D53/52

  Hydrogen sulfide · CPC title

• B01D53/14

  by absorption · CPC title

• B01D53/77

  Liquid phase processes · CPC title

• B01D53/1475

  Removing carbon dioxide · CPC title