Method of reducing carbon dioxide and air pollutants

Abstract

The present invention relates to a method of reducing carbon dioxide and air pollutants, and more particularly to a method of simultaneously reducing emissions of carbon dioxide and air pollutants, in which an off-gas containing carbon dioxide, SOx, and NOx is passed through a sulfur-oxidizing microorganism reactor, thereby converting carbon dioxide present in the off-gas into biomass, SOx into sulfate ions, and NOx into amino-N.

Claims

1. A method of reducing carbon dioxide, SO.sub.x and NO.sub.x simultaneously comprising passing an off-gas containing at least one selected from the group consisting of carbon dioxide, SOx, and NOx through a sulfur-oxidizing microorganism reactor, wherein a sulfur-oxidizing microorganism is a microorganism that grows using reduced sulfur as an energy source and carbon dioxide as a carbon source, and is at least one selected from the group consisting of Acidithiobacillus, Thiosphaera, Thermothrix, Beggiatoa, Thioploca, Thiodendron, Thiobacterium, Macromonas, Achromatium, Thiospira, Thioalkalimicrobium, Thioalkalispira, Sulfolobus and Acidianus.

2. The method of reducing carbon dioxide, SO.sub.x and NO.sub.x simultaneously of claim 1, wherein the off-gas is generated during a process in a power plant or a steel mill.

Description

DESCRIPTION OF THE INVENTION

(1) Unless otherwise defined, all technical and scientific terms used in the present specification have the same meanings as commonly understood by those skilled in the art to which the present disclosure pertains. In general, the nomenclature used in the present specification is well known and commonly used in the art.

(2) In the present invention, it is confirmed that, when an off-gas containing carbon dioxide and air pollutants is directly passed through a sulfur-oxidizing microorganism incubator, the microorganism uses carbon dioxide in the off-gas as a carbon source, SOx is dissolved in water, oxidized, and converted into sulfate ions, and NOx is oxidized by oxygen supplied to the reactor, is dissolved, grows into a source of N for the microorganism, and is converted into amino-N, thereby simultaneously reducing emissions of carbon dioxide and air pollutants and solving environmental problems due to greenhouse gases and particulate matter.

(3) Accordingly, an aspect of the present invention pertains to a method of reducing carbon dioxide and air pollutants including passing an off-gas containing at least one selected from the group consisting of carbon dioxide, SOx, and NOx through a sulfur-oxidizing microorganism reactor.

(4) In the present invention, the off-gas containing at least one selected from the group consisting of carbon dioxide, SOx, and NOx is passed through the sulfur-oxidizing microorganism reactor, so the microorganism uses the carbon dioxide contained in the off-gas as a carbon source, sulfur oxide (SOx) is dissolved in water, oxidized, and converted into sulfate ions, and nitrogen oxide (NOx) is oxidized by oxygen supplied to the reactor, dissolved, used as a nitrogen source for the microorganism, and converted into amino-N.

(5) In the present invention, the sulfur-oxidizing microorganism reactor or a microorganism reactor for producing sulfuric acid is a reactor in which carbon dioxide is selectively used as a carbon source and the sulfur-oxidizing microorganism is cultured in a sulfur-containing medium.

(6) Here, the sulfur-oxidizing microorganism may be a microorganism that grows using reduced sulfur as an energy source and carbon dioxide as a carbon source.

(7) In the present invention, the sulfur-oxidizing microorganism may be at least one selected from the group consisting of bacteria such as Acidithiobacillus, Thiobacillus, Thiosphaera, Thermothrix, Beggiatoa, Thioploca, Thiodendron, Thiobacterium, Macromonas, Achromatium, Thiospira, Thioalkalimicrobium, and Thioalkalispira, and archaea such as Sulfolobus and Acidianus.

(8) In the present invention, more specific examples of the microorganism are as follows.

(9) A. Acidithiobacillus: Acidithiobacillus thiooxidans, Acidithiobacillus albertensis, Acidithiobacillus caldus, Acidithiobacillus cuprithermicus, Acidithiobacillus ferridurans, Acidithiobacillus ferrivorans, or Acidithiobacillus ferrooxidans

(10) B. Thiobacillus: Thiobacillus denitrificans

(11) C. Thiosphaera: Thiosphaera pantotropha

(12) D. Thermothrix: Thermothrix thiopara

(13) E. Beggiatoa: Beggiatoa alba, Beggiatoa leptomitoformis

(14) F. Thioploca: Thioploca araucae, Thioploca chileae, Thioploca ingrica, Thioploca schmidlei

(15) G. Thiodendron: Thiodendron latens

(16) H. Thiobacterium: Thiobacterium bovistum

(17) I. Macromonas: Macromonas bipunctata

(18) J. Achromatium: Achromatium oxaliferum

(19) K. Thiospira: Thiospira winogradskyi

(20) L. Thioalkalimicrobium: Thioalkalimicrobium aerophilum, Thioalkalimicrobium cyclicum

(21) M. Thioalkalispira: Thioalkalispira microaerophila

(22) N. Sulfolobus: Sulfolobus solfataricus

(23) O. Acidianus: Acidianus infernus

(24) In the present invention, the off-gas may be generated during processing by power plants, petroleum plants, waste combustion plants, or steel mills, and may further include particulate matter in the air.

(25) Hereinafter, preferred examples will be presented to aid in understanding the present invention, but it will be apparent to those skilled in the art that the following examples are merely illustrative of the present invention, and various variations and modifications are possible without departing from the scope and spirit of the present invention. It should be understood that such variations and modifications fall within the scope of the appended claims.

EXAMPLES

(26) Example 1: Pre-Culture of Sulfur-Oxidizing Microorganism

(27) 50 ml of a medium containing 1 g/L of (NH.sub.4).sub.2SO.sub.4, 0.5 g/L of MgSO.sub.4.Math.7H.sub.2O, 250 mg/L of CaCl.sub.2.Math.2H.sub.2O, 3 g/L of KH.sub.2PO.sub.4, 10 mg/L of FeSO.sub.4.Math.7H.sub.2O, and 10 g/L of sulfur powder was placed in a 100 ml flask, and 1 ml of a sulfur-oxidizing microorganism (Acidithiobacillus thiooxidans E29) was inoculated thereto, cultured for 7 days in a shaking incubator at a culture temperature of 30° C. and 150 rpm, and then used for main culture inoculation.

(28) Example 2: Confirmation of SOx and NOx Reduction

(29) Comparative group: 1600 ml of water was placed in a 3 L incubator, after which whether the amounts of SOx and NOx were reduced by water at a temperature of 30° C. and a stirring rate of 800 rpm was evaluated. By recovering the product while supplying fresh water at a dilution rate of 0.5/day, corresponding to the same conditions as a control group, a working volume of 1600 ml was maintained. Here, the supply gas was composed of 95 ccm of mixed gas (30% of CO.sub.2, 200 ppm of SOx, 200 ppm of NOx, and the balance of N.sub.2) and 890 ccm of air. The amounts of SOx and NOx were analyzed through off-gas analysis once per hour.

(30) Control group: 1600 ml of a medium containing 1 g/L of (NH.sub.4).sub.2SO.sub.4, 0.5 g/L of MgSO.sub.4.Math.7H.sub.2O, 250 mg/L of CaCl.sub.2.Math.2H.sub.2O, 3 g/L of KH.sub.2PO.sub.4, 10 mg/L of FeSO.sub.4.Math.7H.sub.2O, and 10 g/L of sulfur powder was placed in a 3 L incubator, after which 50 ml of the pre-culture solution was inoculated thereto, followed by batch culture for 4 days at a pH of 3.5, a temperature of 30° C., and a stirring rate of 800 rpm and then continuous culture recovering the product while a fresh medium having the same composition was added at a dilution rate of 0.5/day. Here, the supply gas was composed of 95 ccm of mixed gas (30% of CO.sub.2, 200 ppm of SOx, 200 ppm of NOx, and the balance of N.sub.2) and 890 ccm of air. The amounts of SOx and NOx were analyzed through off-gas analysis once or twice per day.

(31) As is apparent from Table 1 below, it was confirmed that 95% or more of SOx was removed in both the comparative group and the control group, and also that NOx was hardly removed in the comparative group but decreased by 45% in the control group. The microorganism concentration in the control group was 4.2*10{circumflex over ( )}7 cells/ml at the time of initial inoculation, and the microorganism concentration during continuous culture was 8.5*10{circumflex over ( )}9 cells/ml. It can be found that the microorganism biomass is increased by fixing CO.sub.2, which is the sole carbon source.

(32) TABLE-US-00001 TABLE 1 SOx NOx SOx removal NOx removal Gas measurement result (ppm) (ppm) efficiency [%] efficiency [%] Supply gas 21 20 Exhaust gas in 1.0 19 95.2 5 comparative group Exhaust gas in control 1.0 11 95.2 45 group

INDUSTRIAL APPLICABILITY

(33) According to the present invention, the method of reducing carbon dioxide and air pollutants is effective at simultaneously reducing emissions of carbon dioxide and air pollutants based on the principle by which CO2 contained in an off-gas is used as a carbon source and NOx subjected to oxidative dissolution is used as an N nutrient source.

(34) Although the present invention has been described in detail with reference to specific features, it will be apparent to those skilled in the art that this description is only of a preferred embodiment thereof, and does not limit the scope of the present invention. Thus, the substantial scope of the present invention will be defined by the appended claims and equivalents thereto.