博碩士論文 89321013 完整後設資料紀錄

DC 欄位 語言
DC.contributor化學工程與材料工程學系zh_TW
DC.creator廖元璋zh_TW
DC.creatorYuan-Chang Liaoen_US
dc.date.accessioned2002-7-15T07:39:07Z
dc.date.available2002-7-15T07:39:07Z
dc.date.issued2002
dc.identifier.urihttp://ir.lib.ncu.edu.tw:444/thesis/view_etd.asp?URN=89321013
dc.contributor.department化學工程與材料工程學系zh_TW
DC.description國立中央大學zh_TW
DC.descriptionNational Central Universityen_US
dc.description.abstract摘 要 溫室效應已對全球氣候造成重大的變遷。因此,如何回收工廠所排放出來的二氧化碳將是解決二氧化碳問題的首要步驟。 本研究是由模擬方式進行三塔式變壓吸附程序的探討。進料為16%CO2和84%N2的混合氣體,吸附劑採用13X沸石,氣體吸附量採Langmuir平衡吸附式,分離機構為平衡模式,忽略吸附塔內的壓降,考慮非恆溫的變壓吸附程序。 以模擬程式探討不同操作參數對產物濃度與回收率的影響,濃縮後的CO2純度可達73%(此時回收率為77%),回收率可達87%(此時純度為70%),並考慮所做的功來計算「實際回收率」,此實際回收率的值會比原本的回收率減少2~5%左右,再利用實驗設計方法找出影響濃度與回收率的重要參數,並建立預測方程式,預測的結果平均誤差約5~8%。zh_TW
dc.description.abstractAbstract The global climate is greatly changed by greenhouse effect. The recovery of CO2 from flue gas is the first important step in solving CO2 problem. The three-bed pressure swing adsorption (PSA) processes were explored by simulation in this study. The feed gas contains 20% CO2 and 80% N2. The adsorbent is zeolite 13X. The amount of adsorption is calculated by Langmuir isotherm, and this study used the equilibrium model without the consideration of pressure drop. It is also considered non-isothermal operation. The simulation program has studied the influence of operation parameters. The higher purity of the concentrate CO2 is 73% (the recovery is 77%), and the higher recovery is 87% (the purity is 70%).It is also considered the work of the process to calculate the “actual recovery”. The values of the actual recovery reduce about 2~5% from recovery. The important parameters that affect the purities and recoveries were found by the method of experiment design, and we found the polynomials to predict the results. The average errors of the polynomials are about 5~8%.en_US
DC.subject二氧化碳zh_TW
DC.subject13X沸石zh_TW
DC.subject變壓吸附zh_TW
DC.subject模擬zh_TW
DC.subject實驗設計zh_TW
DC.subject溫室效應zh_TW
DC.subjectpressure swing adsorptionen_US
DC.subjectzeolite 13Xen_US
DC.subjectcarbon dioxideen_US
DC.subjectgreenhouse effecten_US
DC.subjectsimulationen_US
DC.subjectexperiment designen_US
DC.title多塔變壓吸附法回收二氧化碳之研究zh_TW
dc.language.isozh-TWzh-TW
DC.titleThe Study of Recovering CO2 by Multi-bed Pressure Swing Adsorptionen_US
DC.type博碩士論文zh_TW
DC.typethesisen_US
DC.publisherNational Central Universityen_US

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