共查询到17条相似文献,搜索用时 93 毫秒
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在液化页岩气的同时分离制取液化乙烷是一种经济合理的选择。采用HYSYS软件进行流程模拟研究,在传统氮膨胀液化流程的基础上设计了一种高含乙烷天然气的液化分离流程,并根据天然气中的乙烷含量,取10%、20%、30%、40%共4种含量,分析比较了不同液化压力下流程的比功耗。为降低流程的能耗,在满足LNG产品中C2H6含量小于1%、液化乙烷纯度达到99.5%的情况下进一步研究了制冷剂流量、氮气膨胀机出口压力、节流温度的影响,在此基础上结合HYSYS软件中的优化器进一步对流程进行了优化。结果表明,对应10%、20%、30%、40%的乙烷含量,比功耗分别降低7.24%、6.13%、5.8%、7.07%。 相似文献
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以重油为原料的合成氨装置都配备空分装置以制备氧气,用部份氧化法制造油煤气,经过净化、配氮再合成为氨。空气中不仅含有氧和氮,还含有氩、氦、氖、氪、氙等惰性气体。其中氩在空气中占有0.93%(体积),它将影响到空分产品氧和氮的纯度。如果不采用分离氩的措施,则欲制得纯 相似文献
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介绍了国内某石化公司乙烯装置低压甲烷氢流程改造项目的背景、改造过程、运行状况、能耗分析,并对改造后的效果进行分析与评价。此次流程优化改造需增加1台甲烷氢压缩机,回收利用冷分离系统的低压甲烷氢,利用新增压缩机将低压甲烷氢进行增压并送至燃料气管网。流程改造提高了装置的操作灵活性,为后续原料轻质化提供了支撑,降低了装置能耗。 相似文献
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为了验证LNG-FPSO液化工艺及其核心设备--液化冷箱在海上晃荡条件下运行的可靠性,建造了小型撬装天然气液化装置,并通过冷箱的纵荡和横摇实验,对不同工况下板翅式换热器、膨胀机和分离器的工作性能及整体工艺系统的运行效果进行了分析。结果表明,晃荡条件下冷箱运行可靠,设备具有较强的抗晃动能力,带预冷的氮膨胀液化工艺可以适用于目标气田的海况;膨胀机水平安装可以减小晃荡的影响;横摇会提高气液两相分离过程的平衡程度及液相的蒸发率;横摇是对FPSO装置影响最大的运动形式,将工艺设备布置在船体的中轴线上可以减小设备晃荡的幅度。 相似文献
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In this study, the effect of hydrogen on methane combustion characteristic was tested. The ignition temperature (T10) and burn off temperature (T90) was carried out in a quartz reactor at atmospheric pressure with the mixture flow rate of 800 mL/min. The compositions of outlet gas were measured online by Gasmet DX4000 FTIR gas analyzer. The results showed that hydrogen enhanced the activity of methane. For all methane concentration range, the T10 of methane could decrease 50 °C–70 °C with the H2/CH4 mole ratio at 0.1. For 1 vol.% methane combustion, when the H2/CH4 was equal to 0.05, the T10 and T90 could decrease 45 °C and 42 °C, respectively. When the H2/CH4 was 2.5, the T10 and T90 could decrease about 170 °C and 180 °C, respectively. Further more, CO generated in a wider temperature range when the hydrogen was added. 相似文献
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大部分含氧煤层气由于技术限制没有被合理利用,而是直接放空,不仅浪费资源,而且污染大气环境。针对某一典型煤层气气源条件和组分特点,设计了一种新型的液化精馏工艺流程,结合HYSYS软件模拟计算结果以及爆炸极限理论,对该液化精馏工艺流程的爆炸极限进行了分析计算,结果表明煤层气中甲烷浓度在压缩、液化以及节流过程中都高于爆炸上限,操作过程安全性比较高。但在精馏塔顶部甲烷浓度开始低于爆炸上限而导致精馏过程存在安全隐患。首先对原料气进行初步脱氧,然后再通过调整精馏塔塔底采出量来控制塔顶杂质气体中甲烷含量,使得其在整个液化及精馏流程中始终高于爆炸上限。分析结果表明,采取安全措施后整个流程都不存在爆炸危险性,甲烷回收率和产品纯度都较高,而且整个流程能耗也比较低。模拟结果显示,所设计的液化及精馏流程对不同气源具有较好的适用性,分析计算结果为含氧煤层气的杂质分离、操作过程的爆炸极限分析以及安全措施的采取提供了一定的参考。 相似文献
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A. M. Dubinin V. G. Tuponogov I. S. Ikonnikov 《Theoretical Foundations of Chemical Engineering》2013,47(6):697-701
Using the chemical reactions that accompany the production of syngas via the steam reforming of methane as a basis, the differential material balance equations were derived and solved for all conversion products on an aluminum/nickel catalyst. For the following stage of hydrogen synthesis on an iron/chromium catalyst, the system of two differential equations of the material balance of the direct and reverse reactions of steam carbon monoxide conversion was obtained and solved. The analytical solutions were compared with the experiment. 相似文献
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Nitrogen-containing compounds such as hydrogen cyanide, acetonitrile, acrylonitrile, pyridine, benzonitrile, ammonia and methylamine, which are typical of the products likely to be encountered during the decomposition of nitrogen-containing polymers in fires, have been introduced into hydrogen and methane flames burning in oxygen-argon atmospheres. There is a complete conversion of fuel nitrogen in all cases to oxides of nitrogen and molecular nitrogen. The relative conversion to oxides of nitrogen (as NOx/N2) increases as the injection rate of nitrogen-containing fuels is decreased. The relative yields of oxides of nitrogen tend to be similar with methane and hydrogen premixed flames and markedly greater than observed with hydrogen diffusion flame. In all cases the yield of oxides of nitrogen-containing products such as hydrogen cyanide can also present a toxic risk during the burning of nitrogen-containing polymers, particularly when high temperature are involved. The combustion of these products in flame zones cannot be assumed to alleviate the additional toxic risk because of their conversion to oxides of nitrogen. 相似文献
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煤层气(CBM)作为一种非常规的天然气,常常含有较多氮气,因此其液化方法也有所不同。文章提出了一种针对带压气源的新型吸附-液化一体化的煤层气混合制冷剂循环(MRC)液化流程。首先通过变压吸附实现氮/甲烷的分离,之后浓缩甲烷进入后续液化流程,而分离出的带余压氮气则直接膨胀对浓缩甲烷进行预冷。并根据浓缩甲烷预冷后不同的温度范围分别设计了3种MRC液化过程。通过HYSYS模拟优化得出了不同含氮摩尔分数及不同吸附余压下使MRC流程单位液化功最小的混合制冷剂配比,并比较了相应的一体化流程和不带预冷的普通MRC液化流程的系统单位产品液化功。结果表明,高含氮摩尔分数下,一体化流程能够大大地降低系统单位功耗。 相似文献
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针对10 t/d级氢液化装置研制要求,构建了液氮预冷的连续转化型双压Claude氢液化流程,并开展了氢物性计算方法筛选、连续转化热模型构建以及流程热力设计与参数优化,分析了膨胀机等熵效率、换热器窄点温差以及原料氢沿程阻力等因素对流程参数的影响,给出了不同工况下的流程性能及各关键部件的热力设计参数范围,可为膨胀机、换热器的研制提供设计热力输入参数。该氢液化流程在基础工况下(考虑较恶劣膨胀机运行条件)的最大理论液氢产量12.96 t/d,液氢产品仲氢含量97%;理论总氢液化比功耗为10.50 kWh/kg LH2 (不含原料氢增压),对应的流程㶲效率为35.06%;可为连续转化式大型氢膨胀液化装置的研制提供参考。 相似文献