洁净煤技术
潔淨煤技術
길정매기술
Clean Coal Technology
2015年
5期
80-84
,共5页
煤间接液化%技术经济%单元计算%项目评价
煤間接液化%技術經濟%單元計算%項目評價
매간접액화%기술경제%단원계산%항목평개
indirect coal liquefaction%technical economy%element calculation%project evaluation
为评价煤间接液化项目的技术经济性,提高项目前期研究和投资决策的效率,以煤间接液化各工艺环节为研究单元,对关键单元及设备的物流、能流进行研究,通过构建干煤粉气化模型计算了干煤气的组成,通过构建F-T合成模型计算烃类产率和烃类分布. 以Excel为计算的后台支撑,以VB可视化界面作为输出平台,构建了煤间接液化项目技术经济计算平台. 结果表明,干煤气组成、烃类产品分布的理论计算结果与工程设计数据基本吻合,烃类产品产率为150~155 g/m3. 煤炭间接液化基础模型能够计算出产品产量及组成、单位产品综合能耗、单位产品煤耗、单位产品水耗、全厂能效、单位产品CO2 排放、单位产品SO2 排放、单位产品NOx 排放及各装置的能耗和排放指标等,模型的计算值与设计值基本相符.
為評價煤間接液化項目的技術經濟性,提高項目前期研究和投資決策的效率,以煤間接液化各工藝環節為研究單元,對關鍵單元及設備的物流、能流進行研究,通過構建榦煤粉氣化模型計算瞭榦煤氣的組成,通過構建F-T閤成模型計算烴類產率和烴類分佈. 以Excel為計算的後檯支撐,以VB可視化界麵作為輸齣平檯,構建瞭煤間接液化項目技術經濟計算平檯. 結果錶明,榦煤氣組成、烴類產品分佈的理論計算結果與工程設計數據基本吻閤,烴類產品產率為150~155 g/m3. 煤炭間接液化基礎模型能夠計算齣產品產量及組成、單位產品綜閤能耗、單位產品煤耗、單位產品水耗、全廠能效、單位產品CO2 排放、單位產品SO2 排放、單位產品NOx 排放及各裝置的能耗和排放指標等,模型的計算值與設計值基本相符.
위평개매간접액화항목적기술경제성,제고항목전기연구화투자결책적효솔,이매간접액화각공예배절위연구단원,대관건단원급설비적물류、능류진행연구,통과구건간매분기화모형계산료간매기적조성,통과구건F-T합성모형계산경류산솔화경류분포. 이Excel위계산적후태지탱,이VB가시화계면작위수출평태,구건료매간접액화항목기술경제계산평태. 결과표명,간매기조성、경류산품분포적이론계산결과여공정설계수거기본문합,경류산품산솔위150~155 g/m3. 매탄간접액화기출모형능구계산출산품산량급조성、단위산품종합능모、단위산품매모、단위산품수모、전엄능효、단위산품CO2 배방、단위산품SO2 배방、단위산품NOx 배방급각장치적능모화배방지표등,모형적계산치여설계치기본상부.
To evaluate technical economy of indirect coal liquefaction project and improve the efficiency of project research and investment, the material flow and energy flow of coal indirect liquefaction was studied to form a model. The study was based on the research of every u-nit of project. The composition of dry gas was calculated by constructing the model of dry pulverized coal gasification,and the hydrocarbon production rate and hydrocarbon distribution were calculated by F-T model. Using Excel as the background support,the VB visual interface as the output platform,built the coal indirect liquefaction project technical and economic calculation platform,the product output and com-position,unit product investment,unit product comprehensive energy consumption,unit product water consumption,energy efficiency,CO2 emissions,SO2 emissions,NOx emissions and energy consumption and emissions targets could be calculated through the model. The value calculated by model was almost the same as the design value.