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首页> 外文期刊>Chemical and Petroleum Engineering >COMPARATIVE ANALYSIS OF VERSIONS OF OPERATION OF UNITS FOR OBTAINING ULTRAHIGH-PURITY CRYOGENIC PRODUCTS
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COMPARATIVE ANALYSIS OF VERSIONS OF OPERATION OF UNITS FOR OBTAINING ULTRAHIGH-PURITY CRYOGENIC PRODUCTS

机译:获得超高纯低温产品的装置操作版本的比较分析

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摘要

In [1], we proposed a procedure that allows the production of ultrahigh-purity cryogenic products in air separation plants to be analyzed from the economic and technical point of view. This procedure was used to analyze how units for obtaining ultrahigh-purity nitrogen, argon, and oxygen function under various conditions. The conditions assumed for the calculations were: 1. the ultrahigh-purity nitrogen (UPN) unit consists of one rectification column for removing oxygen (residual impurity concentration 1 ppb, flowrate G_(UPN) = 1000 m~3/h); 2. the ultrahigh-purity argon (UPA) unit consists of two rectification columns for removing oxygen and nitrogen (residual impurity concentration 100 ppb, flowrate G_(UPA) = 100 m~3/h); 3. the ultrahigh-purity oxygen (UPO) unit consists of two rectification columns for removing argon and methane (residual impurity concentration 10 ppb, flowrate G_(UPO) = 100 m~3/h); 4. the thermodynamic parameters of rectification column operation are assumed to be the same as in [1]; and 5. the remaining initial data necessary for a technical and economic analysis are given in Tables 1-3. The results of the calculations are given in Figs. 1-3, which show the costs vs the relative reflux-to-product ratio βr at various values of thermal head ΔT in condensers (evaporators) of rectification columns, the overhead coefficient E_o, and the electricity rate C_(el). Taking the mixture separation into account, we used column packing as the contact device for UPAr and plates for UPN. Fin-plate condensers and evaporators were chosen, since in contrast to the coil type they ensure a minimal thermal head (at a level of 1 K). The calculations were done in U.S. dollars (means of calculation generally accepted in the world economy). A payback coefficient of 0.167 corresponds to the actual standard payback period (6 yr) and the value 0.25 was chosen with allowance for present-day tendency in the Russian economy to cut the payback period (4 yr). The electricity rate of 0.025 $/kWh is the weighted mean rate in the Russian economy and 0.065 $/kWh is the weighted mean rate in the West.
机译:在[1]中,我们提出了一种程序,该程序允许从经济和技术角度分析空分设备中超高纯度低温产品的生产。该程序用于分析在各种条件下获得超高纯度氮气,氩气和氧气的功能。计算所采用的条件为:1.超高纯氮(UPN)单元由一个精馏塔除去氧气(残留杂质浓度1 ppb,流量G_(UPN)= 1000 m〜3 / h)组成; 2.超高纯氩(UPA)装置由两个精馏塔组成,用于除去氧气和氮气(残留杂质浓度为100 ppb,流量G_(UPA)= 100 m〜3 / h); 3.超高纯氧(UPO)装置由两个精馏塔组成,用于除去氩气和甲烷(残留杂质浓度10 ppb,流量G_(UPO)= 100 m〜3 / h); 4.假定精馏塔运行的热力学参数与[1]中相同; 5.技术和经济分析所需的其余初始数据如表1-3所示。计算的结果在图1和2中给出。参照图1-3,其示出了在精馏塔的冷凝器(蒸发器)中的热头ΔT的各种值,开销系数E_o和电费C_(el)下,成本相对于相对回流产物比βr的关系。考虑到混合物的分离,我们将柱填料用作UPAr的接触装置,并将板用作UPN。之所以选择鳍板式冷凝器和蒸发器,是因为与盘管类型相比,它们确保了最小的热头(水平为1 K)。计算以美元进行(计算方法在世界经济中通常被接受)。投资回报系数为0.167对应于实际的标准投资回收期(6年),选择值0.25时考虑到了俄罗斯经济目前的趋势,即削减了投资回收期(4年)。 0.025美元/千瓦时的电价是俄罗斯经济的加权平均电价,0.065美元/千瓦时的电价是西方经济的加权平均电价。

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