A low cost and high efficient facility for removal of SO/sub 2/ and NO/sub x/ in the flue gas from coal fire power plant

Author(s):  
Yuan Ji Pei ◽  
Ge Li ◽  
Xiang Qi Wang ◽  
Yun Wu Zhang ◽  
Guang Yao Feng ◽  
...  
Author(s):  
Willy Aulia

The concentration of CO2 gas in the air has continued to increase since before the industrial revolution until 2017. This condition is exacerbated by the reduction of Green Open Space (RTH) which serves as an absorber of gas CO2. Private green open space has the potential to be developed as a CO2 reduction (carbon sink) content in the air. The Coal Fire Power Plant (CFPP) XYZ has an area of 72 hectares with open space of 18 hectares. The purpose of this study is to analyze the amount of carbon sink from Green Open Space of CFPP XYZ and planning for reforestation through the approach of carbon sink potential. Methodology of this research using quantitative methods with calculate biomass of three. The results showed the potential for carbon sink from existing green open space of the CFPP XYZ was 1,082.79 Ton CO2 eqf/year or 77.34 eqf Ton/Ha/year and reforestation through the carbon sink potential approach produces a carbon sink capability of 20,825 Ton CO2 eqf/year.


2011 ◽  
Vol 10 (3) ◽  
pp. 341-347 ◽  
Author(s):  
Maria Harja ◽  
Marinela Barbuta ◽  
Lacramioara Rusu ◽  
Corneliu Munteanu ◽  
Gabriela Buema ◽  
...  

1991 ◽  
Vol 24 (7) ◽  
pp. 277-284 ◽  
Author(s):  
E. Gomólka ◽  
B. Gomólka

Whenever possible, neutralization of alkaline wastewater should involve low-cost acid. It is conventional to make use of carbonic acid produced via the reaction of carbon dioxide (contained in flue gases) with water according to the following equation: Carbon dioxide content in the flue gas stream varies from 10% to 15%. The flue gas stream may either be passed to the wastewater contained in the recarbonizers, or. enter the scrubbers (which are continually sprayed with wastewater) from the bottom in oountercurrent. The reactors, in which recarbonation occurs, have the ability to expand the contact surface between gaseous and liquid phase. This can be achieved by gas phase dispersion in the liquid phase (bubbling), by liquid phase dispersion in the gas phase (spraying), or by bubbling and spraying, and mixing. These concurrent operations are carried out during motion of the disk aerator (which is a patent claim). The authors describe the functioning of the disk aerator, the composition of the wastewater produced during wet gasification of carbide, the chemistry of recarbonation and decarbonation, and the concept of applying the disk aerator so as to make the wastewater fit for reuse (after suitable neutralization) as feeding water in acetylene generators.


Energies ◽  
2021 ◽  
Vol 14 (8) ◽  
pp. 2174
Author(s):  
Marta Marczak-Grzesik ◽  
Stanisław Budzyń ◽  
Barbara Tora ◽  
Szymon Szufa ◽  
Krzysztof Kogut ◽  
...  

The research presented by the authors in this paper focused on understanding the behavior of mercury during coal combustion and flue gas purification operations. The goal was to determine the flue gas temperature on the mercury emissions limits for the combustion of lignites in the energy sector. The authors examined the process of sorption of mercury from flue gases using fine-grained organic materials. The main objectives of this study were to recommend a low-cost organic adsorbent such as coke dust (CD), corn straw char (CS-400), brominated corn straw char (CS-400-Br), rubber char (RC-600) or granulated rubber char (GRC-600) to efficiently substitute expensive dust-sized activated carbon. The study covered combustion of lignite from a Polish field. The experiment was conducted at temperatures reflecting conditions inside a flue gas purification installation. One of the tested sorbents—tire-derived rubber char that was obtained by pyrolysis—exhibited good potential for Hg0 into Hg2+ oxidation, resulting in enhanced mercury removal from the flue. The char characterization increased elevated bromine content (mercury oxidizing agent) in comparison to the other selected adsorbents. This paper presents the results of laboratory tests of mercury sorption from the flue gases at temperatures of 95, 125, 155 and 185 °C. The average mercury content in Polish lignite was 465 μg·kg−1. The concentration of mercury in flue gases emitted into the atmosphere was 17.8 µg·m−3. The study analyzed five low-cost sorbents with the average achieved efficiency of mercury removal from 18.3% to 96.1% for lignite combustion depending on the flue gas temperature.


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