Gaseous hydrocarbons, which are hydrocarbons that are gaseous at mild environmental temperatures such as 20° C. and atmospheric pressure, are often transported great distances by tanker in liquid form as LNG (liquified natural gas). To keep the gas liquid, it is stored on the tanker at a low temperature such as −160° C. in highly thermally insulated tanks. At the tanker offloading destination, the LNG is offloaded to a receiving station where it is regassed (heated to turn it into a gas) and stored for later use.
Proposed prior art offloading stations include a large fixed platform extending up from the sea floor to a height above the sea surface. Such platform would contain a heating system that regassed the LNG, a pump system that pressurizes the gas, and crew quarters or other crew facilities. The regas unit or system must heat the LNG sufficiently that the gas is warm enough to avoid ice formations around noncryogenic hoses or pipes that carry the gas, and the pump system must pump the gas to a high enough pressure to inject it into a storage cavern and/or pump the gas to a shore station. A platform that is large enough to carry such gas heating and pumping systems would be expensive.
One large expense in operating such as system is the tanker daily rate, which may be about US $100,000 per day. It is therefore desirable to offload the tanker as rapidly as possible. This leads to the need for the receiving facility to be able to receive and process all LNG received so the tanker can sail away in a short period of time, and so the tanker can return soon thereafter and unload a new load of LNG. This is in addition for the need to be able to construct the receiving facility at minimum cost.
In accordance with one embodiment of the invention, applicant constructs the receiving facility at low cost and with the ability to quickly receive all LNG from a tanker. The receiving facility includes a moored floating structure or vessel which can directly receive LNG from a tanker, and which holds a regas unit, a pump unit and crew quarters. The cost for a floating vessel that is moored to the sea floor to weathervane with the tanker and that holds the large amount of equipment, is much less that than of a platform.
In shallow waters, where it is difficult to moor a vessel by catenary chains, applicant uses a bare tower with a lower end mounted in the sea floor. The bare tower is used only to moor the vessel, with the regas unit, pump unit and crew quarters all on the vessel.
To minimize the tanker rental costs, applicant constructs the vessel with large capacity LNG storage tanks. The storage tanks are large enough to store all LNG offloaded by the tanker, that has not been regassed by the regas unit at the end of offloading. The cost of LNG storage tanks on the vessel is less than the extra charge for tanker rental so the tanker can wait for the LNG being offloaded to be gassed by the regas unit. The cost of LNG storage tanks is also less than the cost for a very large regas unit, which anyway might be prohibited from full operation by environmental laws. However, the regas unit is large enough to heat all offloaded LNG before the tanker next arrives with a load of LNG.
The gas produced by regasing offloaded LNG is preferably stored in an underground cavern before being passed though a seafloor pipeline to a consumer such as an onshore gas distribution facility. Metering of gas (measuring and recording the quantity of gas) delivered to the consumer is made by a metering system that lies on the vessel and though which all gas, from the vessel and from the cavern, passes.
The novel features of the invention are set forth with particularity in the appended claims. The invention will be best understood from the following description when read in conjunction with the accompanying drawings.
When the tanker 30 begins offloading LNG, the regas unit 36 is immediately energized to begin heating the LNG, with the gas being passed through a riser 42. Some or all of the gas is passed though a sea floor pipe 44 (that extends partially along the sea floor) to the consumer, which is shown as an onshore gas distribution facility 46 in
Apparatus for transferring LNG between the tanker and another structure, such as the transfer unit 34, can be constructed with a large capacity at a moderate cost. Thus, the transfer unit 34 may be able to transfer the entire load of LNG carried by the tanker to the floating structure 16 in one or two days instead of four days, at only a modest additional cost for the transfer unit. This would reduce the required tanker time to transfer a load of LNG. Tanker rental rates are high, such as about US $100,000 per day for a 135,000 ton LNG carrying tanker, so reducing the tanker time for unloading is important. One solution to reduce tanker time is to use a larger regas unit 36. However, regas units use sea water as a source of heat to heat LNG (LNG is at perhaps −160° C.), and there usually are local regulations that limit the rate at which cold water can be released into the environment. Also, if the regas unit produces gas at a higher rate, then the cavern 40 that must store the gas when the tanker is not unloading, must be of larger capacity. Also, a larger regas unit costs more.
In accordance with the present invention, applicant constructs the floating structure 16 so it contains insulated tanks 100 that store LNG. As the tanker unloads LNG, some of it is directly passed to the regas unit 36, and the rest is directed to the LNG storage tanks 100. This allows the tanker to offload during perhaps one or two days, with much of the LNG going to the tanks 100 during offloading. When the tanker sails away, the LNG stored in the tanks is fed to the regas unit. The regas unit gasified all of the LNG over a longer period of time such as during a period of eight days instead of four days. This facilitates compliance with local environmental laws that limit how much cold water can be released and its temperature, reduces the required size of the regas unit 36 and the pressurizing unit 38, reduces the required size of the storage cavern 40, and reduces the tanker rental time for a given transport rate of LNG.
In one example, the tanker carries 1000 tons of LNG, and offloads it during a period of two days. It then sails away and returns in five more days, so the “turn-around time” is seven days. The regas unit 36 has a capacity of 150 tons per day, and therefore requires almost seven days to regas an entire tanker load. The LNG storage capacity provided by the tanks on the floating structure 16 is 700 tons. The storage capacity of the cavern can be small since the regas unit feeds gas into the cavern only slightly faster than gas is withdrawn from the cavern during offloading and the cavern is the sole source of gas to the consumer for less than a day. Applicant has calculated the costs for extra cavern storage capacity (e.g. for 700 tons of natural gas in a gaseous state), and the cost for the same capacity of natural gas in the form of LNG buffer tanks on a floating structure, and finds that the costs are about the same. The benefit of reduced tanker rental time as well as reduced regas unit size and less environmental problems, makes the substitution worthwhile.
The relationship between gas mass A (in tons of LNG) carried by the tanker, the interval B between tanker visits to the floating structure in days, the unloading time period C in days, the regas unit capacity D in tons per day, and the LNG storage capacity E of tanks 100 on the floating structure in tons of LNG is given approximately (within 33% of the actual values) by:
E=A−(D×C), and
D=A/B
The LNG tanks on the tanker must be well insulated because any gas that evaporates (without refrigeration) would have to be released into the environment or burned (which is dangerous and costly). The tanks 100 on the receiving floating structure do not have to be well insulated because any gas that evaporates is pumped to the consumer or storage cavern without even passing though the regas unit. In fact, such evaporated gas can be considered part of the output of the regas unit. However, the tanks must be moderately insulated to limit the amount of ice that is formed on the storage tanks from water vapor in the atmosphere, to protect personnel, and to prevent sea water from turning into ice against the vessel.
An important aspect in offloading an LNG tanker, regasing the LNG and pressuring it, possibly storing gas in a cavern or in tanks, and carrying the gas to an on-shore facility, is metering of the gas which is measuring the quantity of gas that has been sent to the consumer. An accurate measure of the amount of gas delivered to the consumer such as an onshore facility must be maintained to assure complete payment for the gas.
LNG that exits the regas unit 130 (or that evaporates from an LNG tank) on the floating structure may be released to pass though pipe 132. Such gas then flows directly through the metering unit 112 to flow through pipe 116 to the onshore facility. Alternatively, the gas from the regas unit 130 may be released to flow though a pipe 134 to flow down though a riser 136 to cavern 140 where the gas is stored. When gas is to be withdrawn from the cavern, it flows upward through the same riser 136 (which is being used bidirectionally). The gas then flows through a portion of the pipe 134, though a dehydration unit 142 and an input 143 to the metering unit 112. From there, the gas flows though pipe 116 and to the onshore facility. Thus, the regas and metering units are both positioned on the floating structure, gas can flow from the regas unit directly to shore, or gas can flow to a cavern and then back to the floating structure and through the metering unit to shore.
Applicant notes that LNG coming from the tanker (e.g. 30 in
The system 10 of
Thus, the invention provides a low cost system for offloading and regasing LNG from a tanker, which minimizes the tanker unloading time, minimizes the required sizes of the regas unit and storage cavern and avoids the release of cold water at an excessive rate. This is accomplished by mounting the regas unit on a floating structure that is moored (directly or indirectly) to the sea. The floating structure includes an LNG storage capacity of 100's of tons, which enables rapid LNG offloading from the tanker and provides other advantages. In a shallow sea location, the system includes a bare tower, and the floating structure is moored to the tower to allow weathervaning and to enable gas to be transferred to a pipe on the tower, but with the LNG storage and the regas unit both mounted on the floating structure.
Although particular embodiments of the invention have been described and illustrated herein, it is recognized that modifications and variations may readily occur to those skilled in the art, and consequently, it is intended that the claims be interpreted to cover such modifications and equivalents.
Applicant claims priority from U.S. provisional application Ser. No. 60/566,680 filed Apr. 30, 2004.
Number | Name | Date | Kind |
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6973948 | Pollack et al. | Dec 2005 | B1 |
6979147 | Wille et al. | Dec 2005 | B1 |
6997643 | Wille et al. | Feb 2006 | B1 |
Number | Date | Country | |
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20060080973 A1 | Apr 2006 | US |
Number | Date | Country | |
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60566680 | Apr 2004 | US |