SPRING 1999 VOLUME 15 NUMBER 2 Density Stratification in LNG Storage by David Sheats and Michael Capers, Scientific Instruments, Inc. The use of LNG (Liquid Natural Gas) as an important energy source around the world is increasing steadily. It currently represents about 6% of the world’s natural gas and is readily available at numerous sites worldwide. Factors contributing to this increased usage include the discovery of large resources, development of costeffective methods of production, transportation and storage and the fact that LNG is a very clean-burning fuel, making it an attractive option where environmental concerns are high. LNG is stored at cryogenic temperatures, which present some unique safety concerns and require specialized instrumentation to be able to detect potentially unsafe conditions. In the following discussion, these concerns are identified and the instrumentation techniques for addressing them are explained. The end result is a solution that gives confidence to the storage facility personnel that any potentially hazardous condition will be detected in a timely manner so that the proper corrective action may be taken. Production of LNG LNG is produced through a liquefaction process that lowers the temperature of the multi-component mixture of hydrocarbons (mainly methane with lower concentrations of higher hydrocarbons) to –160°C, a 600 to 1 reduction of volume from gas to liquid. In this state, the product is economically transported via specialized tanker ships from the production site typically quite remote) to the customer. There are three primary types of sites where LNG is stored, namely liquefaction/ export facilities, import / distribution facilities and peak shaving facilities. Liquefaction/Export The liquefaction/export facility is located at the gas source and performs the ʺcleaning,ʺ liquefaction and initial storage of the finished product. Such long-term supply countries as Indonesia, Algeria, Australia, Malaysia, Brunei and the United Arab Emirates represent this part of the LNG production train. New liquefaction facilities are or soon will be online in Nigeria, Trinidad, Oman and Qatar. New fields have been discovered and remain to be developed in Indonesia, Russia and off the coast of South America. A ʺtypicalʺ LNG exporting facility will operate up to 2-10 production trains and may have up to 10 LNG storage tanks. These tanks are located at a deep-water port and are used to load the tankers for the oceanic transportation of the product to customers. Typical LNG storage tank Import/Distribution An import/distribution facility capable of accommodating these LNG tankers is located at a deepwater port in countries that are using the LNG as an energy source. From these storage facilities, typically 3-10 storage tanks, natural gas is re-gasified and fed into a national pipeline system or trucked to remote storage locations. Such facilities are located in Spain, Japan, Taiwan, Korea and the United States. Peak Shaving Facilities A peak shaving facility is actually a production/ distribution plant combined into one. The purpose is to produce LNG during low usage periods, and store that gas for use during peak demands. The end result is the ability to ʺshave the peakʺ demand requirement off the gas supply lines, since that demand is normally only for a short period, such as a very cold day. It is typically owned and operated by a local gas company or pipeline distributor. While the process is very similar to the larger facilities, the production/ gasification rate is much lower. The very nature of this type of facility dictates that the gas will likely be stored for a much longer period, which has significant implications pertaining to possible density stratification as discussed below. The storage tanks used at all three of the above types of facilities may be above or below ground, but they are fundamentally the same. They have an inner tank, an insulation space and a concrete or high carbon steel outer tank. They are typically 150ʹ in diameter, 160ʹ in height, and have a storage volume of 15-18 million gallons of product. There are presently plans in development for tanks with significantly greater capacity than those previously built and in service. SPRING 1999 VOLUME 15 NUMBER 2 Density Stratification in LNG Storage Rollover A significant safety concern in the storage of LNG is a phenomenon known as ʺrollover.ʺ If this occurs, pressures inside the storage tank may rise to excessive levels. The tanks are equipped with safety vent valves that are designed to keep the pressures from rising to levels that could cause structural damage. However, when these valves operate, LNG is vented to the atmosphere at an uncontrolled rate, which is an additional safety concern. LNG is heavier than air and could settle in pockets of explosive mixtures. Perhaps the most well known case of rollover is that which occurred in La Spezia, Italy, in 1971. The actual pressures realized are unknown since they exceeded available instrumentation and gas vented uncontrolled in a highly populated area for several hours. Fortunately, there was no explosion and no major damage was done to the tanks. The possibility of both potential problems was very evident, and much attention to detecting and preventing a similar occurrence has taken place since that time. Rollover occurs under certain conditions as stratified LNG comes to equilibrium. Stratification occurs when the product in the tank forms in layers with different densities and different temperatures. Sudden mixing of LNG in any storage tank occurs as two or more layer densities approach equality. Any heat trapped in the system is released rapidly during mixing, generating a vapor which may exceed the venting capability of the tank. The exact conditions that lead to rollover are somewhat complex. If layering occurs (discussed below), each layer is initially uniform, with the upper layer lighter than the lower. Heat entering the top layer comes through the walls of the tank. The liquid next to the tank walls warms slightly, becomes less dense and rises to the top, where it evaporates. Since light gases evaporate first, the liquid in the top layer tends to become denser. Fluid circulation in a stratified LNG storage tank At the same time, the liquid in the lower layer gains heat through the floor and walls of the tank with a convection flow similar to the top layer. But because of the hydrostatic pressure of the upper layer, the rising liquid does not evaporate but superheats. Thus the lower layer becomes warmer and less dense. When the two layers approach the same density, the interface between the two becomes unstable and mixes rapidly. When this occurs, the liquid from the lower layer that is superheated gives off a large amount of vapor that rises to the surface. It is this phenomenon that is known as rollover. Causes of Layering What are the causes of layering? There are basically two ways that layering is produced. The first, and most obvious, occurs when liquid of a different composition than that which is already in the tank is introduced into the tank. This could be from a different gas field, or an altered process that results in a different composition. This is most likely to occur at a receiving terminal. The second cause of layering comes from a process referred to as ʺautostratification.ʺ In this mechanism, unstratified liquid gains heat at the walls of the tank and rises by convection. It flashes upon reaching the surface. If sufficient nitrogen is present, the remaining liquid will be less dense, creating a layer at the top. As this layer increases, it seals in the lower layer and can cause it to superheat, creating conditions leading to rollover. Layer Detection The most effective method of preventing rollover is to detect layering by means of instrumentation, and if layering is present, take action to mix the layers under controlled conditions before the final conditions leading to rollover develop. If the size and composition of the layers can be detected, the potential danger can be accurately determined and the most cost-effective approach can be chosen. This action may be the operation of recirculation pumps (if available), or by mixing with liquid in other tanks. Some installations that have the capability of recirculation within a tank choose to operate these pumps on a regular basis as a preventive measure. Operation of these pumps is expensive, however, and some facilities do not have a simple method of recirculation. Layer detection is best accomplished by means of a temperature sensor and density sensor that are run through the entire depth of the liquid. SPRING 1999 VOLUME 15 NUMBER 2 Density Stratification in LNG Storage In the absence of this, multiple temperature sensors located at fixed intervals will also give an indication of layering. The disadvantage to multiple sensors is the difficulty of accurate calibration. The cost of multiple density sensors is prohibitive. Instrumentation One instrument currently available for layer detection and installed at a number of facilities around the world is the M6280 LTD series from Scientific Instruments, Inc. It is specifically designed to detect temperature and density layering in LNG tanks. To accomplish this, a single probe with installed temperature, density and liquid level sensors is driven over the entire depth of the liquid in the tank. The data is collected at fixed intervals as specified by the customer. Simple data analysis is performed to alert the operator of apparent temperature or density layering. If certain areas of the tank are suspect, a feature known as ʺTop Scanʺ is available to examine a potential layer in more detail, providing an accurate picture of the suspected layer. As mentioned previously, because a single sensor is used for data collection, calibration errors are eliminated and an accurate relative profile is obtained. With an accurate temperature and density profile, detailed calculations can be performed Typical display from M6280LTD System showing stratification to properly determine the extent of the danger, and to enable cost-effective action in a timely manner to prevent rollover. Summary Although we are not aware of any rollover incidents that have resulted in fires, explosions or major structural tank damage, there have been many rollover incidents throughout the LNG industry. An increasing awareness of the potential problem has resulted in a greater emphasis on installing instrumentation. Proper instrumentation, such as Scientific Instruments, Inc. M6280 LTD, is the most secure way to obtain information so that preventive action can be quickly implemented to avert a potential problem. Scientific Instruments, Inc (SII) products are distributed by FlowQuip Group with offices in China, Vietnam, Cambodia, Hong Kong, Macau and Singapore. For more information, please contact us. FLOWQUIP PTE LTD ( 富 德 有 限 公 司) Head Office (新加坡总公司) : No. 8 Lorong Bakar Batu, #01-07, Kolam Ayer Industrial Park, Singapore 348743 Tel: (65) 6748 6353 (6 Lines) Fax: (65) 6748 1190 Email: flowquip@flowquip.com.sg Website: www.flowquip.com.sg FlowQuip Group Overseas Offices : China Guangzhou Office Tel : (86-20) 8732 6718 Fax : (86-20) 8732 6728 Email : china@flowquip.com.cn China Beijing Office Tel : (86-10) 8451 9991 Fax : (86-10) 6463 0616 Email : beijing@flowquip.com.cn Hong Kong SAR Office Tel : (852) 2440 3593 Fax : (852) 2440 4593 Email : hongkong@flowquip.com.hk Vietnam Office Tel : (84-8) 822 1308 Fax : (84-8) 829 7930 Email : vietnam@flowquip.com.vn Cambodia Office Tel : (855-23) 214 704 Fax : (855-23) 218 709 Email : flowquip@camnet.com.kh Macau SAR Office Tel : (852) 2440 3593 Fax : (852) 2440 4593 Email : hongkong@flowquip.com.hk