首頁(yè) > 資料下載 > PC和IGCC裝置的成本與性能 對于二氧化碳捕集范圍Cost and Performance of PC and IGCC Plants for a Range of Carbon Dioxide C
PC和IGCC裝置的成本與性能 對于二氧化碳捕集范圍Cost and Performance of PC and IGCC Plants for a Range of Carbon Dioxide C PC和IGCC裝置的成本與性能 對于二氧化碳捕集范圍Cost and Performance of PC and IGCC Plants for a Range of Carbon Dioxide C

PC和IGCC裝置的成本與性能 對于二氧化碳捕集范圍Cost and Performance of PC and IGCC Plants for a Range of Carbon Dioxide C

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  • 更新時(shí)間:2021-09-09
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這項研究的目的是確定碳的成本和性能。 新型超臨界(SC)煤粉的二氧化碳(CO2)捕集水平及其集成 氣化聯(lián)合循環(huán)(IGCC)發(fā)電廠(chǎng)。SC PC案例(案例1系列)的利用 氟_生態(tài)胺FG PlusSM工藝用于變溫燃燒后CO2捕集 用30wt%單乙醇胺(MEA)溶液作為化學(xué)溶劑進(jìn)行吸收。這個(gè) IGCC案例(案例2系列)采用漿料輸送、夾帶流通用電能(GEE) 氣化器和杠桿UOP_s(前通用石油產(chǎn)品)兩階段Selexol 變壓吸附法捕集CO2并選擇性脫除硫化氫(H2S)。 Selexol?工藝使用聚乙二醇二甲醚(DEPG)作為物理溶劑 用于預燃燒捕獲。

The objective of this study was to establish the cost and performance for a range of carbon dioxide (CO2) capture levels for new supercritical (SC) pulverized coal (PC) and integrated gasification combined cycle (IGCC) power plants. The SC PC cases (Case 1 series) utilize Fluor?s Econamine FG PlusSM process for post-combustion CO2 capture via temperature swing absorption with a 30 wt% monoethanolamine (MEA) solution as the chemical solvent. The IGCC cases (Case 2 series) employ a slurry-fed, entrained-flow General Electric Energy (GEE) gasifier and leverage UOP?s (formerly Universal Oil Products) two-stage Selexol? process for bulk CO2 capture and selective hydrogen sulfide (H2S) removal via pressure swing absorption. The Selexol? process uses dimethyl ether of polyethylene glycol (DEPG) as a physical solvent for pre-combustion capture.

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