杨烨, 李魁亮, 卢绪涛, 孟韩, 郝勇. 大型LNG工厂夏季生产装置安全控制方案[J]. 油气储运, 2019, 38(11): 1282-1287. DOI: 10.6047/j.issn.1000-8241.2019.11.013
引用本文: 杨烨, 李魁亮, 卢绪涛, 孟韩, 郝勇. 大型LNG工厂夏季生产装置安全控制方案[J]. 油气储运, 2019, 38(11): 1282-1287. DOI: 10.6047/j.issn.1000-8241.2019.11.013
YANG Ye, LI Kuiliang, LU Xutao, MENG Han, HAO Yong. A safety control scheme on the production devices of large LNG plants in summers[J]. Oil & Gas Storage and Transportation, 2019, 38(11): 1282-1287. DOI: 10.6047/j.issn.1000-8241.2019.11.013
Citation: YANG Ye, LI Kuiliang, LU Xutao, MENG Han, HAO Yong. A safety control scheme on the production devices of large LNG plants in summers[J]. Oil & Gas Storage and Transportation, 2019, 38(11): 1282-1287. DOI: 10.6047/j.issn.1000-8241.2019.11.013

大型LNG工厂夏季生产装置安全控制方案

A safety control scheme on the production devices of large LNG plants in summers

  • 摘要: 在夏季高温环境下,大型LNG工厂容易发生设备异常停机问题。以昆仑能源黄冈LNG工厂为例,基于某年满负荷下其主要装置的循环水冷却、空温器冷却、自然散热等冷却温度点典型数据,运用层次分析法建立模型,对夏季高温诱发安全问题的各项因素进行权重量化,结合工厂工艺控制参数,制订夏季生产装置的安全生产方案:当气温超过40 ℃时,开夏季喷淋系统,严格控制循环水出口、丙烯冷凝器循环水进出口水、贫液空冷器胺液出口、酸气空冷器酸气出口的温度分别低于32 ℃、42 ℃、55 ℃、55 ℃;再生气经过再生气空冷器后的温度低于35 ℃;压缩机润滑油温度应低于45 ℃;循环水系统进油站换热温度则低于30 ℃。结果表明:大型LNG工厂的夏季安全生产不能单一停留在传统的“夏季四防”工作、条例化的安全守则上,应结合生产实际需要,以生产平稳率为前提,将定性的夏季高温诱发问题量化为科学权重,制订切实可行的解决方案,可以有效降低生产风险。

     

    Abstract: The equipment in large LNG plants tends to suffer abnormal shutdown in the environment of high temperature in summers. In this paper, Huanggang LNG Plant of Kunlun Energy was taken as an example to deal with this problem. Based on the typical data of its main devices under the full load of one certain year at the temperature points of circulating water cooling, air cooling and natural cooling, the weight of each factor inducing the safety problems due to high temperature in summers was quantified by means of analytic hierarchy process modeling. Then, combined with the process control parameters of the LNG plant, its summer safety production scheme was prepared as follows. When the air temperature is over 40 ℃, turn on the summer spray system to strictly control the outlet temperature of circulating water, the inlet/outlet temperature of circulating water of propylene cooler, the outlet temperature of amine solution of barren-solution air cooler and the outlet temperature of acid gas of acid-gas air cooler below 32 ℃, 42 ℃, 55 ℃ and 55 ℃, respectively. After the regenerated gas flows through the regenerated-gas air cooler, its temperature is below 35 ℃. The temperature of the compressor lubricant shall be lower than 45 ℃. And the heat transfer temperature of circulating water system while entering the station is lower than 30 ℃. It is indicated that the safety production of Large LNG plants in summers shall not simply comply with the traditional work of "four defenses in summer" and the regulatory code of safety. It is necessary to take the smooth production rate as the prerequisite, combined with the demands of actual production, to quantify the qualitative problems induced by high temperature in summers into the scientific weights and formulate practical and feasible solution, so as to reduce the production risks.

     

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