CN203771023U - Liquefied petroleum gas shipping system based on single point mooring - Google Patents
Liquefied petroleum gas shipping system based on single point mooring Download PDFInfo
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- CN203771023U CN203771023U CN201420132049.8U CN201420132049U CN203771023U CN 203771023 U CN203771023 U CN 203771023U CN 201420132049 U CN201420132049 U CN 201420132049U CN 203771023 U CN203771023 U CN 203771023U
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Abstract
The utility model discloses a liquefied petroleum gas shipping system based on single point mooring. The liquefied petroleum gas shipping system comprises a shore-based LPG (Liquefied Petroleum Gas) freezer, a single point mooring system, an LPG refreezing device and a whole cooling type LPG transport ship, wherein the shore-based LPG freezer is connected with the LPG refreezing device through the single point mooring system; the LPG refreezing device is connected with the whole cooling type LPG transport ship. Compared with a traditional block stowage technology, the liquefied petroleum gas shipping system is suitable for regions lacking of natural ports and a condition that a port plan is not easy to change; the investment is low and the construction period is short; equipment can be recycled after resources are exhausted.
Description
Technical Field
The utility model belongs to the technical field of the shipment technique of Liquefied Petroleum Gas (LPG for short) and specifically relates to a Liquefied Petroleum Gas shipment system based on single point mooring.
Background
The LPG is liquefied by pressurizing or cooling the petroleum gas to obtain Liquefied Petroleum Gas (LPG), the volume of the LPG is about 1/250 of the same volume of the petroleum gas, and the LPG has the advantages of flexible transportation, high storage efficiency and the like. LPG is derived from byproducts generated in crude oil extraction or associated products in the process of petroleum and natural gas extraction, and has the advantages of cleanness, environmental protection, high combustion heat value and the like.
The low-temperature normal-pressure storage of the LPG means that the LPG is stored at normal pressure and at saturation temperature. The saturation temperature of propane at atmospheric pressure was-42 deg.C, that of n-butane was-0.6 deg.C, that of isobutane was-12 deg.C, and the actual saturation temperature at atmospheric pressure was different due to the different components of the various LPG types.
The full-cooling LPG transport ship is also called as low-temperature normal-pressure LPG transport ship, and liquefied gas is stored in a liquid cabin which is not pressure-resistant and is in a boiling state under normal pressure. The design pressure of the liquid tank is generally 0.025MPa, the volume of a single liquid tank is rarely limited, and the liquid tank is suitable for building large ships, and the capacity is 50000-3。
Wherein, liquid tank structural style includes:
(1) a non-independent whole body fluid chamber type;
(2) an internally insulated storage tank;
(3) a freestanding liquid tank. The tank can be divided into three types A, B, C, which are not part of the hull and are self-sustaining.
Type A independent cabin: the liquid tank is mostly composed of a plane structure, the maximum allowable design pressure of the liquid tank is not more than 0.07MPa, the liquid tank is more adopted on a large-scale full-cold ship, and the working temperature is not lower than-55 ℃.
B type independent cabin: for accurate structural stress analysis and model testing, including finite element, shell theory, framework analysis may be used in some cases. Buckling, fatigue life, plastic deformation are all considered. The liquid tank type has prism shape and rotary spherical shape, and the pressure is less than 0.07 MPa. LNG ships use this type of formula more.
C type independent cabin: the C-shaped cabin is provided with a single tank, two lugs and a three-blade type, and the pressing force container is designed according to the standard. The design pressure is usually 1.8MPa and is not more than 2 MPa.
Generally, the shipping trade can not lack a dock, and the dock needs to be connected with the land, so that the goods can be conveniently transferred to land transportation. At the same time, huge investments are required to construct port facilities that provide services for the anchoring, port entry and exit, berthing and loading and unloading operations of transport vessels. For the full-cooling type LPG transport ship, due to the fact that the storage capacity is large, the length of the ship is 200-300 meters generally, and the full-loading draught is 12-16 meters, the dock is difficult to select the site, the manufacturing cost is high, and the construction period is long.
SUMMERY OF THE UTILITY MODEL
To solve the above problems, the utility model provides a Liquefied Petroleum Gas (LPG) shipment system and method based on single-point mooring, after the LPG reheat of low temperature storage on the bank, carry to the open sea through submarine pipeline and single-point mooring device and recool the device, realize the offshore loading to full cold type LPG transport ship to solve the pier construction difficult problem to full cold type LPG transport ship.
A Liquefied Petroleum Gas (LPG) shipment system based on single point mooring comprises a shore-based LPG refrigerator, a single point mooring system, an LPG re-freezing device and a full-cooling LPG transport ship, wherein the shore-based LPG refrigerator is connected with the LPG re-freezing device through the single point mooring system, the LPG re-freezing device is connected with the full-cooling LPG transport ship,
wherein,
the shore-based LPG refrigerator comprises a low-temperature storage tank, a recondenser and a heater which are sequentially connected;
the single point mooring system comprises a gas phase submarine pipeline, a liquid phase submarine pipeline and a single point mooring device;
the LPG refreezing device comprises a first-stage compressor, a second-stage compressor, a first-stage gas-liquid separator, a second-stage gas-liquid separator, a third-stage gas-liquid separator, a cryogenic pump and a cooler,
wherein,
the heater and the second-stage gas-liquid separator are connected through a liquid-phase submarine pipeline, the second-stage gas-liquid separator is respectively connected with the second-stage compressor and the first-stage gas-liquid separator, the second-stage compressor is connected with the third-stage gas-liquid separator through a cooler, the third-stage gas-liquid separator is respectively connected with the second-stage gas-liquid separator and the gas-phase submarine pipeline, a liquid-phase outlet of the first-stage gas-liquid separator is connected with the full-cooling type LPG transport ship, and a gas-phase outlet of the first.
As a preferred solution, the LPG refreezing device is provided on a ship.
Preferably, a cryopump is further provided in the cryogenic storage tank.
Preferably, the gas phase return port of the fully-cooled LPG carrier is further connected to the primary gas-liquid separator, so that gas phases of BOG generated by the fully-cooled LPG carrier during loading and the primary gas-liquid separator are mixed and compressed together, and a recovery device is not required to be separately provided.
As a preferable technical scheme, a gas phase outlet of the second-stage gas-liquid separator is connected with a second-stage compressor, a liquid phase outlet of the second-stage gas-liquid separator is connected with a first-stage gas-liquid separator, the second-stage compressor is connected with a third-stage gas-liquid separator through a cooler, a liquid phase outlet of the third-stage gas-liquid separator is connected with a second-stage gas-liquid separator, a gas phase outlet of the third-stage gas-liquid separator is connected with a gas phase submarine pipeline, a liquid phase outlet of the first-stage gas-liquid separator is connected with a full-cooling type LPG transport ship through a cryogenic pump.
As a preferred technical scheme, a gas phase outlet of the first-stage gas-liquid separator is provided with a BOG buffer tank connected with a first-stage compressor.
As a preferred technical scheme, a low-temperature storage tank is arranged at a liquid phase outlet of the primary gas-liquid separator, and the low-temperature storage tank is sequentially connected with a low-temperature pump and a full-cold LPG transport ship.
The heat balance of the above system operation is regulated by the cooler and the heater.
The above system can be used as an offshore LPG discharge vessel by adjusting the location of the cryogenic storage tank and the fully cooled LPG carrier.
The lowest operation temperature of the low-temperature storage tank can be-48 ℃.
Based on the shipment system, the utility model also provides a liquefied petroleum gas shipment method based on single-point mooring, including following step:
mixing low-temperature LPG in an LPG low-temperature storage tank with high-temperature BOG returned by a refreezing device (namely outlet gas of a three-stage gas-liquid separator returned by the refreezing device) in a recondensor for reheating, adjusting the temperature by a heater, and conveying the mixture to the refreezing device by a single-point mooring system;
step two, the LPG output by the shore-based LPG refrigerator is refrigerated to a low-temperature normal-pressure equilibrium state in a refreezing device, wherein:
LPG from a shore-based LPG refrigerating warehouse is firstly sent to a secondary gas-liquid separator, the LPG can be decompressed and flashed when entering the secondary gas-liquid separator, a generated gas phase enters a secondary compressor for compression, and an accumulated liquid phase enters a primary gas-liquid separator for flashing; after the outlet gas of the secondary compressor is cooled, the outlet gas enters a tertiary gas-liquid separator for separation, the outlet gas (namely high-temperature BOG) of the tertiary gas-liquid separator is conveyed back to a recondenser through a single-point mooring system to be mixed with LPG (liquefied petroleum gas) sent out of a low-temperature storage tank for reheating, and the accumulated liquid phase of the tertiary gas-liquid separator enters the secondary gas-liquid separator for flash evaporation; gas phase generated by flash evaporation of the first-stage gas-liquid separator is sent to a first-stage compressor for compression, and gas at the outlet of the first-stage compressor is sent to a second-stage gas-liquid separator for washing by low-temperature LPG liquid sent by a third-stage gas-liquid separator;
and step three, pressurizing the liquid phase of the primary gas-liquid separator, and conveying the liquid phase to a full-cold LPG transport ship for loading, preferably conveying the liquid phase after pressurization by a low-temperature pump.
The mixed reheating is controlled between 40 ℃ and 80 ℃ by a cooler according to the heat balance requirement of the system.
The low-temperature normal-pressure equilibrium state is generally a state in which the operating pressure is close to the atmospheric pressure and the temperature is at the saturation temperature.
Preferably, in the step one, the low-temperature LPG in the LPG low-temperature storage tank is pressurized by a low-temperature pump, and then mixed with the high-temperature BOG returned by the refreezing device in the recondensor for reheating, and the mixture is preferably pressurized to 0.35 to 0.46 MPa.
As a preferable scheme, in the second step, the LPG from the shore-based LPG freezer is decompressed and then sent to a secondary gas-liquid separator, the gas phase generated by the decompression and flash evaporation of the secondary gas-liquid separator enters a secondary compressor for compression, and the accumulated liquid phase in the secondary gas-liquid separator enters a primary gas-liquid separator for flash evaporation after being cooled and decompressed; cooling and cooling outlet gas of the secondary compressor, then separating the outlet gas in a tertiary gas-liquid separator, conveying the outlet gas (high-temperature BOG) of the tertiary gas-liquid separator back to a recondenser through a single-point mooring system, mixing the outlet gas with LPG (liquefied petroleum gas) conveyed by a low-temperature storage tank for reheating, cooling and decompressing liquid phase of the tertiary gas-liquid separator, and then, feeding the liquid phase into the secondary gas-liquid separator for flash evaporation; the gas phase of the first-stage gas-liquid separator is sent to a first-stage compressor for compression, and the gas at the outlet of the first-stage compressor is sent to the middle part of a second-stage gas-liquid separator and is washed by the low-temperature LPG liquid sent by the third-stage gas-liquid separator; the accumulated liquid phase of the primary gas-liquid separator is transported to a full-cooling LPG transport ship.
Preferably, the loaded BOG of the fully-cooled LPG carrier is returned to the refrigeration system and mixed with the gas phase of the primary gas-liquid separator and then compressed together, and thus a separate recovery facility is not required.
"Single Point Mooring" is derived from the English "Single Point Mooring", SPM for short. It should be noted that SPM is a general concept, generally referring to all single points, and allows a moored vessel to freely swing around a single mooring point as the prevailing wind and sea conditions change, so that mooring at the location of least wind, wave and current combined drag is constantly a single point mooring. Compared with a fixed wharf, the wharf has the characteristics of low investment cost, short construction period, large construction site selection range, low maintenance cost and the like. With the development of offshore oil exploration and development, the single point mooring technology is gradually applied to offshore oil production platforms, crude oil/product oil transfer stations and other wide applications from the initial offshore refueling.
The utility model discloses a theory of operation does:
the method comprises the following steps that low-temperature LPG stored in a shore-based LPG refrigerator is heated to a temperature above 0 ℃ through an LPG heater and then is sent to an offshore re-freezing device through a single-point mooring system; the re-freezing device realizes that the LPG is frozen to the saturation temperature under the normal pressure through the circulation combination of the compressor and the JT valve, and finally the LPG is pumped to a full-cooling LPG transport ship through the low-temperature pump of the LPG for loading. The BOG with higher temperature generated by the re-freezing device during cooling is returned to the shore-based LPG freezer through the single-point mooring system to heat incoming material LPG, so that the high-temperature BOG generated by the re-freezing device during working does not need to consume energy to carry out cooling treatment and can also replace an LPG heater to heat, and dual energy conservation is realized.
Compared with the prior art, the utility model has the positive effects that: after being reheated, LPG stored in a shore-based LPG refrigerating warehouse can be directly conveyed through a submarine pipeline and a single-point mooring device, and the purpose that goods are directly loaded on a full-cold LPG transport ship after being refrozen on the sea is achieved. Additionally, the utility model discloses the higher temperature BOG that produces when will refreeze LPG is defeated back ashore and low temperature storage tank export low temperature LPG are mixed, has solved LPG reheat's heat source problem to the technology energy consumption has been reduced. Compared with the traditional wharf loading technology, the utility model discloses the area that is suitable for very much and lacks natural harbour and the difficult condition of changing of harbour planning, the investment is low, and construction cycle is short, and the resource exhausts back equipment recoverable.
Drawings
The invention will now be described, by way of example, with reference to the accompanying drawings, in which:
FIG. 1 is a schematic illustration of a shipping system in an embodiment.
Detailed Description
All of the features disclosed in this specification, or all of the steps in any method or process so disclosed, may be combined in any combination, except combinations of features and/or steps that are mutually exclusive.
Any feature disclosed in this specification (including any accompanying claims, abstract and drawings), may be replaced by alternative features serving equivalent or similar purposes, unless expressly stated otherwise. That is, unless expressly stated otherwise, each feature is only an example of a generic series of equivalent or similar features.
As shown in fig. 1, the LPG shipment system based on single point mooring includes an LPG cryogenic tank 1, an LPG cryogenic pump 2, a BOG recondenser 3, an LPG heater 4, a gas phase subsea pipeline 5, a liquid phase subsea pipeline 6, a single point mooring 7, a primary compressor 8, a secondary compressor 9, a primary gas-liquid separator 10, a secondary gas-liquid separator 11, a tertiary gas-liquid separator 12, a cryogenic pump 13, a cooler 14, a fully-cooled LPG transport ship 15, and various valves 16-20 (including JT valves 16-17, FV valves 18, PV valves 19, LV valves 20, LV valves 21, TV valves 22), wherein the JT valves refer to joule-thomson throttle expansion valves, LV valve finger level interlock control valves, FV valve finger flow interlock control valves, TV valve finger temperature interlock control valves.
Wherein:
an LPG low-temperature storage tank 1, an LPG low-temperature pump 2, a BOG recondenser 3, an LPG heater 4, various valves (18-22) and the like form a shore-based LPG refrigeration storage, and the LPG low-temperature storage tank 1 can be a single-capacity tank, a double-capacity tank or a full-capacity tank and the like. The LPG cryopump 2 may be an immersed pump, a centrifugal pump, or the like. And the BOG recondenser 3 is responsible for mixing low-temperature LPG and high-temperature BOG returned by the refreezing device for reheating, and the LPG heater 4 is responsible for heating when the reheating temperature does not reach the standard in the heating and running processes when the system is started.
In particular, the amount of the solvent to be used,
1) an LPG low-temperature pump 2 is arranged in the low-temperature storage tank 1, an outlet of the low-temperature pump 2 is divided into two paths (flow distribution is carried out in real time according to the liquid level of the recondenser), one path is connected to an inlet at the upper part of the recondenser 3 through an LV valve 20 to recondense high-temperature BOG (namely outlet gas of the three-stage gas-liquid separator), and the other path is directly connected to an outlet of the recondenser 3 through an LV valve 21 to be used as.
2) A liquid phase outlet of the BOG recondenser 3 is connected with an inlet of an LPG heater 4, and an outlet of the LPG heater is connected with a liquid phase submarine pipeline 6; the gas phase outlet of the BOG recondenser 3 is returned to the cryogenic tank 1 via the PV valve 19 to equalize the tank pressure.
Wherein:
the gas phase subsea pipeline 5, the liquid phase subsea pipeline 6 and the single point mooring device 7 constitute a single point mooring system responsible for transporting material through the seabed to the re-freezing device. The single point mooring device 7 may be a catenary mooring system (CALM), a tower (soft rigid arm, etc.), or a turret (internal turret/external turret).
In particular, the amount of the solvent to be used,
1) the outlet of the LPG heater is sent to a secondary gas-liquid separator 11 through a liquid-phase submarine pipeline 6 and a single-point mooring device 7.
2) The gas phase outlet of the three-stage separator is sent back to the BOG recondenser 3 through the single-point mooring device 7, the gas phase submarine pipeline 5 and the FV valve 18 in sequence.
Wherein:
a refreezing device, which is responsible for refreezing the LPG and finally delivering it to the fully-cooled LPG carrier, is constituted by a primary compressor 8, a secondary compressor 9, a primary gas-liquid separator 10, a secondary gas-liquid separator 11, a tertiary gas-liquid separator 12, a cryogenic pump 13, a cooler 14, and various valves (16-17), and is preferably installed on the refreezing ship. The cooler 14 may be an air temperature cooler or a circulating water cooler, which mainly controls the heat outflow of the load heat balance; each gas-liquid separator is provided with JT valve and other throttling temperature reduction measures, and the lowest-temperature primary separator 10 is also provided with a low-temperature pump 13.
In particular, the amount of the solvent to be used,
1) a gas phase outlet of the second-stage gas-liquid separator 11 is connected with a second-stage compressor 9, and an outlet of the second-stage compressor 9 is connected into a third-stage gas-liquid separator 12 through a cooler 14; the liquid phase outlet of the secondary gas-liquid separator 11 is connected to the primary gas-liquid separator 10 via JT valve 18.
2) The gas phase outlet of the three-stage gas-liquid separator 12 is connected with the single point mooring device 7, and the liquid phase outlet of the three-stage gas-liquid separator 12 is connected to the second-stage gas-liquid separator 11 through a JT valve 19.
3) A gas phase outlet of the first-stage gas-liquid separator 10 is connected to the first-stage compressor 8, and an outlet of the first-stage compressor 8 is connected to the second-stage gas-liquid separator 11; the liquid phase outlet of the primary gas-liquid separator 10 is sent to a full-cooling LPG carrier 15 through a cryogenic pump 13.
4) The gas phase outlet of the full-cooling LPG transport ship 15 is connected with the primary gas-liquid separator 10; the connection of the gas-liquid ports of the full-cold LPG transport ship 15 can be realized through a ship loading arm or a ship loading hose.
The method for loading the ship by using the ship loading system comprises the following steps:
step one, after the low-temperature LPG in the LPG low-temperature storage tank 1 is pressurized to 0.35-0.46 MPa (G) through an LPG low-temperature pump 2, the low-temperature LPG is mixed with high-temperature BOG returned by a refreezing device in a BOG recondensor 3 for reheating, the temperature is adjusted to 0-10 ℃ through an LPG heater 4, and then the mixed high-temperature LPG is conveyed to the refreezing device through a gas-phase submarine pipeline 5 and a single-point mooring device 7.
Step two, the LPG conveyed from the shore-based LPG refrigerator is refrigerated to a low-temperature normal-pressure equilibrium state on a refreezing ship (the low-temperature state is different according to different components, such as pure propane is-42.07 ℃, and pure butane is-0.5 ℃), and specifically comprises the following steps:
LPG from a shore-based LPG refrigerating warehouse is decompressed by a pressure control valve 16 and then is firstly sent to a secondary gas-liquid separator 11, a gas phase generated by decompression and flash evaporation of the secondary gas-liquid separator 11 is sucked into a secondary compressor 9 through a pipeline for compression, liquid accumulated by the secondary gas-liquid separator 11 is cooled and decompressed by a JT valve 18 to become a saturated gas-liquid two-phase flow with the temperature of-6 to-40 ℃ and the pressure of 5 to 10KPa (G), and then enters a primary gas-liquid separator 10 for flash evaporation; the gas at the outlet of the secondary compressor 9 is cooled to 40-60 ℃ through a cooler 14, and then enters a three-stage gas-liquid separator 12 for separation, the high-temperature BOG at the gas phase outlet of the three-stage gas-liquid separator is returned to a shore-based freezer through a single-point mooring device 7 and a gas-phase submarine pipeline 5 so as to be mixed and condensed with the low-temperature LPG conveyed by the low-temperature storage tank in a BOG recondenser 3, and the amount of the high-temperature BOG returned to the freezer is automatically adjusted according to different compositions of the raw material LPG and the heat balance requirement of the whole conveying system, for example, the high-temperature BOG can usually account for 80-; the liquid phase of the three-stage gas-liquid separator 12 is cooled and decompressed by a JT valve 17 to become a saturated gas-liquid two-phase flow with the pressure of 0.35-0.46 MPa (G), and then the saturated gas-liquid two-phase flow enters the two-stage gas-liquid separator 11 to be mixed with LPG from a shore-based LPG refrigerator and is flashed; gas phase of the first-stage gas-liquid separator 10 is sent to the first-stage compressor 8 through a pipeline to be compressed, gas at the outlet of the first-stage compressor 8 is sent to the middle part of the second-stage gas-liquid separator 11 through a pipeline, and low-temperature LPG liquid sent by the third-stage gas-liquid separator 12 is washed;
and step three, pressurizing the liquid phase of the primary gas-liquid separator 10 through a low-temperature pump 13, then conveying the liquid phase to a full-cooling type LPG transport ship 15 for loading, reversely conveying ship-loading BOG generated in the loading process of the full-cooling type LPG transport ship 15, mixing the ship-loading BOG with flash gas of the primary gas-liquid separator 10, and conveying the mixture to a primary compressor for compression 10.
The present invention is not limited to the foregoing embodiments. The invention extends to any novel feature or any novel combination of features disclosed in this specification, and to any novel method or process steps or any novel combination of features disclosed.
Claims (5)
1. A liquefied petroleum gas ship loading system based on single point mooring is characterized by comprising a shore-based LPG refrigerator, a single point mooring system, an LPG re-freezing device and a full-cooling LPG carrier, wherein the shore-based LPG refrigerator is connected with the LPG re-freezing device through the single point mooring system, the LPG re-freezing device is connected with the full-cooling LPG carrier, and the shore-based LPG refrigerator comprises a low-temperature storage tank, a re-condenser and a heater which are connected in sequence; the single point mooring system comprises a gas phase submarine pipeline, a liquid phase submarine pipeline and a single point mooring device; the LPG refreezing device comprises a first-stage compressor, a second-stage compressor, a first-stage gas-liquid separator, a second-stage gas-liquid separator, a third-stage gas-liquid separator, a cryogenic pump and a cooler, wherein the heater and the second-stage gas-liquid separator are connected through a submarine pipeline, the second-stage gas-liquid separator is respectively connected with the second-stage compressor and the first-stage gas-liquid separator, the second-stage compressor is connected with the third-stage gas-liquid separator through the cooler, the third-stage gas-liquid separator is respectively connected with the second-stage gas-liquid separator and a gas-phase submarine pipeline, a liquid phase outlet of the first-stage gas-liquid separator is connected with.
2. A liquefied petroleum gas loading system based on single point mooring of claim 1, wherein the LPG refreezing device is provided on a ship.
3. A liquefied petroleum gas loading system based on single point mooring as claimed in claim 1, wherein a cryogenic pump is further provided in the cryogenic storage tank.
4. The liquefied petroleum gas loading system based on single point mooring of claim 1, wherein the gas phase return port of the fully-cooled LPG transport ship is connected with a primary gas-liquid separator.
5. A liquefied petroleum gas loading system based on single point mooring as claimed in any one of claims 1-4, wherein the gas phase outlet of the secondary gas-liquid separator is connected with the secondary compressor, the liquid phase outlet of the secondary gas-liquid separator is connected with the primary gas-liquid separator, the secondary compressor is connected with the tertiary gas-liquid separator through a cooler, the liquid phase outlet of the tertiary gas-liquid separator is connected with the secondary gas-liquid separator, the gas phase outlet of the tertiary gas-liquid separator is connected with a gas phase submarine pipeline, the liquid phase outlet of the primary gas-liquid separator is connected with the full-cooling LPG transport ship through a cryogenic pump, and the gas phase outlet of the primary gas-liquid separator is sequentially connected with the primary compressor and the secondary gas-.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103867884A (en) * | 2014-03-24 | 2014-06-18 | 中国石油集团工程设计有限责任公司 | Ship loading system and method of LPG (Liquefied Petroleum Gas)-based on single point mooring |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103867884A (en) * | 2014-03-24 | 2014-06-18 | 中国石油集团工程设计有限责任公司 | Ship loading system and method of LPG (Liquefied Petroleum Gas)-based on single point mooring |
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Effective date of registration: 20180110 Address after: 610041 Chengdu high tech Zone, Sichuan province sublimation Road No. 6 Patentee after: CHINA PETROLEUM ENGINEERING & CONSTRUCTION Corp. Address before: 610041 Chengdu high tech Zone, Sichuan province sublimation Road No. 6 Patentee before: CNPC ENGINEERING DESIGN Co.,Ltd. |
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Granted publication date: 20140813 |