共查询到19条相似文献,搜索用时 156 毫秒
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以一艘17万立方米新型独立B型液化天然气(LNG)船为研究对象,将该型围护系统与传统薄膜型和MOSS独立球型围护系统进行详细对比,突出该型围护系统的特点;分析船体和舱室结构后,通过合理和必要的简化,提供了一种计算独立B型液货舱传热的方法,通过数值模拟计算不同工况条件下液货舱的蒸发率,研究了聚氨酯泡沫绝热材料的热导率变化对液货舱蒸发率的影响。得到以下结论:(1)新型独立B型围护系统与传统围护系统相比有突出优势,在将来有很好的应用前景;(2)绝热层厚度为450 mm时,为了满足日蒸发率不能超过0.1%的限定要求,所选用的绝热材料的热导率应当小于或等于0.03 W·m-1·K-1。 相似文献
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以LNG(液化天然气)为介质、以密闭LNG生产储罐为对象进行了储罐的压力及日蒸发气体量及蒸发率测试实验,结果证明:密闭LNG储罐内的温度场是非均匀的,即气相部分温度高于气液分界面处温度、气液分界面处液体温度高于液相主体的温度;在实验条件下,当初始充满率为0.475时,3部分的温差最大约为2~3℃。存在临界初始充满率,即当初始充满率小于临界充满率时,某一充满率下的日蒸发气体量和蒸发率随时间而增大;当初始充满率大于临界充满率时,某一充满率下的日蒸发气体量和蒸发率先随着时间增加而增大,然后又随着时间的增加而减小。 相似文献
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LNG集液池用于收集事故工况下泄漏的LNG,是保证LNG接收站安全的重要组成部分,LNG和水接触会发生爆沸,因而需要设置排液系统将集液池内的雨水及时排除.本文以某LNG接收站项目为例,对LNG集液池排液系统进行研究,对排液泵参数、管道参数、排液泵类型、控制系统进行设计. 相似文献
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LNG物性参数是LNG接收站模型建立、工艺流程模拟计算及研究必不可少的基础数据。以国外实验数据为基础,采用Aspen HYSYS软件分析评价PR、SRK、LKP、BWRS状态方程对气液相组成、焓、密度等物性参数的预测结果,比选汽液相平衡和热力学参数的计算状态方程,建立了LNG接收站储罐蒸发模型,并比较了四种状态方程的准确度。结果表明:PR方程在汽液相平衡计算方面计算精度最高,相对误差为4.70%;LKP方程计算热力学参数最准确,预测误差为2.59%。综合考虑相平衡参数和热力学参数计算精度,PR方程精度最高,预测误差为3.77%。此外,PR方程对LNG储罐蒸发和储罐压力的模拟计算值与现场数据吻合度最好,因此LNG接收站蒸发计算推荐选用PR方程。研究结果对物性参数和LNG接收站蒸发计算状态方程的选择具有借鉴意义。 相似文献
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在LNG接收站的设计建造过程中,BOG(boil-off gas)生成量计算的准确性将直接影响到项目建设的设备投资和日常操作的稳定性。为了提高BOG生成量计算的准确性,以某实际项目为例,在传统BOG计算方法的基础上引入计算机模拟软件--Aspen Hysys,选择Peng-Robinson状态方程对整个接收站的工艺流程进行模拟计算,得到BOG生成量最大工况的BOG量,通过与传统静态设计计算结果进行比较分析,发现了传统静态设计计算方法存在的不足,结果说明了使用Hysys模拟计算接收站BOG生成量更能准确反映LNG接收站的实际情况,适合于LNG接收站项目在初步设计和详细设计阶段的工艺计算,而传统静态设计计算可用于项目建设初期可行性研究阶段的粗略工艺计算。 相似文献
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Myung Wook Shin Dongil Shin Soo Hyoung Choi En Sup Yoon 《Korean Journal of Chemical Engineering》2008,25(1):7-12
Proper handling of boil-off gas (BOG) significantly affects the operational efficiency as well as the safety of the whole
LNG gasification plant. Due to the not well-known inherent dynamics, it has been suspected that the BOG compressors are being
operated at too much capacity, unnecessarily consuming too much energy. An empirical model is proposed for the estimation
of the boil-off rate (BOR) in an LNG storage tank, based on the specification supplied by the LNG storage tank manufacturer.
By using the BOR model, an optimal operation algorithm is proposed for a safe and energy-saving BOG compressor operation,
which minimizes the power consumption while preparing against the potential failure of one of the operating compressors. Case
study results indicate that the energy consumption could be reduced by a half of the conventional method, by increasing the
tank pressure while the safety is maintained. The proposed method is expected to be able to contribute to improving the efficiency
of the whole gasification plant operation and control without tempering the safety requirements. 相似文献
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对比分析了LNG(液化天然气)加气站3种BOG(蒸发气)回收方式,指出采用大冷量斯特林制冷机的BOG再液化回收技术,不仅解决了传统回收方式对天然气管网和CNG(压缩天然气)站的依赖,而且实现了液化天然气储运过程中的"零排放",经济和社会效益显著。在此基础上,探讨了单级整体式斯特林制冷机的制冷能力以及BOG的液化量,试验和计算结果表明:单级斯特林制冷机的制冷量达到1 kW@77 K和2 kW@110 K,每月BOG液化能力≥8 t,满足了我国小型LNG站BOG回收过程对冷量的需求。 相似文献
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国内外学者提出过许多关于液化天然气(liquefied natural gas,LNG)接收站蒸发气(boil-off gas,BOG)再冷凝工艺的优化方案。其中,采用预冷法对再冷凝工艺进行优化的方案由于前期投入较少且优化效果明显,更具有现实意义。然而,现有的预冷法优化方案还存在着优化原则不清晰和考虑工况不全面等问题。本文介绍了LNG接收站现有BOG再冷凝工艺流程与经预冷法优化后的再冷凝工艺流程,分析得到了预冷法优化的理论原理。针对接收站两种典型工况提出了相应的优化原则。以江苏如东LNG接收站现有再冷凝工艺流程为计算实例,运用HYSYS软件对优化前后的再冷凝工艺进行模型建立与流程模拟,应用所建模型对优化前后的再冷凝工艺总功耗进行对比分析。结果表明:经改进后的再冷凝工艺预冷法优化方案可以有效地根据相应的优化原则对两种典型工况进行优化。通过将研究成果应用于江苏如东LNG接收站可知,在两种典型工况下,优化后的BOG再冷凝工艺较原工艺分别节约系统总功耗9.8%和21.5%。 相似文献
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The boil-off gas (BOG) recondensation system is one of the most important facilities at liquefied natural gas (LNG) storing and receiving terminals, whose failure may cause BOG loss and/or severe accidents. Operation of a BOG recondensation system requires sufficient care under various situations, especially when LNG load and BOG load fluctuate. This study improves the control algorithm for a BOG recondensation system at an LNG receiving terminal and employs dynamic simulations to examine its operation reliability and energy minimization. Key system parameters, such as recondenser pressure, liquid level, and high-pressure pump suction pressure are tracked during simulation. On the basis of process dynamic simulation by use of DYNSIM and analysis of tracked key system parameters, the developed control algorithm is verified as reliable and is expected to be applied to other LNG terminals. 相似文献
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LNG接收站蒸发气体(BOG)处理量和液化天然气(LNG)外输量的波动对BOG再冷凝工艺提出低能耗、大弹性、易操作的要求。以系统总能耗最小为目标函数,对建立的BOG多阶压缩再液化工艺模型中压缩阶数和阶压比等参数进行了优化,并分析了该工艺模型在工况波动影响系统能耗时的各阶压比的抗干扰性及系统的操作弹性。结果表明:多阶压缩工艺系统阶数越多,系统的总压比、总能耗越小,BOG处理能力也越大;但随着系统阶数的增加,节能效果降低。多阶再液化工艺中二阶系统比现有一阶系统的操作弹性增大12%,且在LNG与BOG质量比≤10时,二阶系统的BOG压缩功耗可节约33%以上。针对一般气源型接收站工况,二阶系统是节能且操作弹性大的BOG处理工艺。 相似文献
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Dynamic simulation and optimization of the operation of boil-off gas compressors in a liquefied natural gas gasification plant 总被引:1,自引:0,他引:1
Namjin Jang Myoung Wook Shin Soo Hyoung Choi En Sup Yoon 《Korean Journal of Chemical Engineering》2011,28(5):1166-1171
We propose an algorithm for the optimal operation schedule of the BOG compression process based on simulation of the dynamic
behavior of an LNG tank. The algorithm uses an empirical boil-off rate model to predict the amount of BOG generation, and
an MILP formulation to distribute the BOG compressors loads. Finally, a safety analysis is done using a dynamic simulator.
To improve the accuracy, Aspen Dynamics with the Peng-Robinson equation of state is used in place of a simplified dynamic
model used before. The dynamic simulation of the LNG tank pressure showed the results of oscillation within a safe pressure
range while the BOG compressors were operated normally. The performance of the proposed algorithm was found to be superior
to the algorithm used in routine processes as well as those from previous works in terms of safety and energy savings. 相似文献
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In view of high energy consumption and poor flexibility in boil-off gas (BOG) recondensation operation at liquefied natural gas (LNG) terminals, a flexible and cost-effective optimization including the control system and flow process has been proposed. The optimized control system maintains BOG recondenser pressure via the condensing LNG flow and recondenser liquid level via bypass LNG flow. A BOG recondensation process with pre-cooling operation utilizes high-pressure pump LNG to pre-cool compressed BOG before it is directed into recondenser. The engineering application in a case of 6.69 tons/hour (t/h) BOG and LNG output fluctuating between 49 t/h and 562 t/h shows, after the flexible and cost-effective optimization, that process energy decreases 91.2 kW, more 1.28 t/h BOG is recovered when LNG output load reaches the valley, and the operation stability is well improved. 相似文献