CN101704404A - 船舶 - Google Patents
船舶 Download PDFInfo
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- CN101704404A CN101704404A CN200910169658A CN200910169658A CN101704404A CN 101704404 A CN101704404 A CN 101704404A CN 200910169658 A CN200910169658 A CN 200910169658A CN 200910169658 A CN200910169658 A CN 200910169658A CN 101704404 A CN101704404 A CN 101704404A
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 70
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 35
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 35
- 238000005086 pumping Methods 0.000 claims abstract description 6
- 238000002347 injection Methods 0.000 claims description 44
- 239000007924 injection Substances 0.000 claims description 44
- 239000007788 liquid Substances 0.000 claims description 26
- 238000010992 reflux Methods 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 238000007710 freezing Methods 0.000 claims description 10
- 230000008014 freezing Effects 0.000 claims description 10
- 238000011144 upstream manufacturing Methods 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000000605 extraction Methods 0.000 claims description 6
- 230000009182 swimming Effects 0.000 claims description 6
- 238000009428 plumbing Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 8
- 239000012071 phase Substances 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 229930195733 hydrocarbon Natural products 0.000 description 4
- 150000002430 hydrocarbons Chemical class 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- NMJORVOYSJLJGU-UHFFFAOYSA-N methane clathrate Chemical compound C.C.C.C.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O NMJORVOYSJLJGU-UHFFFAOYSA-N 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 206010073753 Fear of injection Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 230000000881 depressing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
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- 238000012423 maintenance Methods 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C1/00—Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G5/00—Storing fluids in natural or artificial cavities or chambers in the earth
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- F17C1/00—Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge
- F17C1/002—Storage in barges or on ships
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
- F17C5/06—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with compressed gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C6/00—Methods and apparatus for filling vessels not under pressure with liquefied or solidified gases
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- F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
- F17C7/02—Discharging liquefied gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
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- F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
- F17C7/02—Discharging liquefied gases
- F17C7/04—Discharging liquefied gases with change of state, e.g. vaporisation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
- F17C9/02—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0352—Pipes
- F17C2205/0364—Pipes flexible or articulated, e.g. a hose
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/013—Carbone dioxide
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
- F17C2223/033—Small pressure, e.g. for liquefied gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/04—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
- F17C2223/042—Localisation of the removal point
- F17C2223/046—Localisation of the removal point in the liquid
- F17C2223/047—Localisation of the removal point in the liquid with a dip tube
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
- F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
- F17C2225/0107—Single phase
- F17C2225/0123—Single phase gaseous, e.g. CNG, GNC
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
- F17C2225/03—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
- F17C2225/035—High pressure, i.e. between 10 and 80 bars
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/01—Propulsion of the fluid
- F17C2227/0128—Propulsion of the fluid with pumps or compressors
- F17C2227/0135—Pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
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- F17C2227/0171—Arrangement
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
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- F17C2227/0171—Arrangement
- F17C2227/0185—Arrangement comprising several pumps or compressors
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0302—Heat exchange with the fluid by heating
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/01—Intermediate tanks
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2265/00—Effects achieved by gas storage or gas handling
- F17C2265/01—Purifying the fluid
- F17C2265/015—Purifying the fluid by separating
- F17C2265/017—Purifying the fluid by separating different phases of a same fluid
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
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- F17C2270/00—Applications
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- F17C2270/0102—Applications for fluid transport or storage on or in the water
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C2270/00—Applications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C2270/00—Applications
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- F17C2270/0144—Type of cavity
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Glass Compositions (AREA)
- Details Of Reciprocating Pumps (AREA)
- Devices For Medical Bathing And Washing (AREA)
- Cold Air Circulating Systems And Constructional Details In Refrigerators (AREA)
- Jet Pumps And Other Pumps (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Container, Conveyance, Adherence, Positioning, Of Wafer (AREA)
- Control Of Vehicles With Linear Motors And Vehicles That Are Magnetically Levitated (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Carbon And Carbon Compounds (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
Abstract
本发明提供一种水上的液化二氧化碳,即LCD运输船舶,其包括加压和冷冻的LCD容器,用于沿管道将LCD泵送出所述容器的所述容器内的货物排出泵,用于沿所述管道将LCD泵送到平台的增压泵,从所述货物泵的下游到所述容器的第一回流管线,从所述增压泵的下游到所述容器的第二回流管线,以及可选的加热器,所述加热器设置成加热从所述船舶沿所述管道流动的LCD。
Description
本申请是中国发明申请(发明名称:船舶;申请日:2005年07月14日;申请号:200580029387.2)的分案申请。
技术领域
本发明涉及对将液态二氧化碳(LCD)从水上(water-going)的LCD运输船舶传送到注入井口的工艺和设备的改进,以及水上的LCD运输船舶。
背景技术
二氧化碳(CO2)是在某些工业作业,例如氨的制造中作为副产品大量产生的气体。环境上不希望将这种副产品释放到大气中,这是由于其是温室效应的气体。因而,某种程度上已经对CO2处理技术的研制做出了许多的努力,而不是简单地释放到大气。特别重要的一种技术是将CO2泵送到多孔地下(sub-surface)地层中(即,封锁),例如泵送到油田的注入井。
如果该处理进入的地层是含有烃的,可以简单地使地下处理进入到多孔地层中,或者可以实现该地下处理的有益优点,这是由于注入的CO2用于朝向出油井(即萃取烃的井)驱动该地层中的烃(例如油或天然气)。因而CO2的注入是后期储油管理中的一项标准技术,以实现烃的加强开采。
地下注入处理所包含的二氧化碳的量通常大约几百万吨之大。这造成了将CO2从其产生的地点运输到其注入的地点方面的问题,特别是该注入的地点是海上的情况下。大气温度和气压下的二氧化碳是气态的,如果分批运输,则需要容积大的容器,以致于该过程难以实行。虽然在一些情况下可以实行通过管道的运输,但是所需的基础设施较昂贵。由此希望以液态的形式运输二氧化碳,特别是运输到海上注入地点。
然而,液态二氧化碳的运输不是一个没有问题或花费的实践。如果这种液态CO2不是冷冻的,则将其保持在液态所需的压力较高(60-70巴),这使得加压容器所需的墙壁厚度较高,并且使得运输这种大规模未冷冻的液态CO2的容器非常昂贵。在低于环境温度的情况下运输液态CO2减少了所需的压力和所需的容器墙壁厚度,但是其由于需要冷冻而较昂贵,并且由于二氧化碳具有固相,还具有会形成固态二氧化碳的风险。固态二氧化碳形式会对通过泵送运输的CO2造成问题,并且由于管道或阀阻塞的风险,还会造成潜在的危险。
因此,在平衡冷冻和容器的经济成本以及避免固态CO2形成的风险中,在任何给定的情况下,通常具有对该容器中的液态CO2最佳的温度和压力,例如,在低于环境温度的温度,以及在高于大气压但是仍然是亚临界的压力(CO2的临界点是73.8巴)。一般对液态CO2的运输来说,该最佳温度可能在-55至-48℃的范围内,而该压力可能是5.5至7.5巴,即对应于CO2相图中温度和压力仅在三相点之上的位置。CO2的三相点是5.2巴和-56.6℃。高压需要更昂贵的容器;而低压和低温会产生固态形式的风险。
将液化石油气(LPG)从出油井口运输到海岸的水上的船舶上所使用的加压容器的类型通常不适于运输LCD,这是由于LCD运输所需的压力更高.而且,将LPG从海上出油井运输到水上流经的船舶(即船)的液态运输设备不适于将LCD从该船舶运输到注入井口,这是由于LPG不会造成与LCD相冲突的固态形式的风险.
尽管如此,仍然需要用于LPG、LNG、PLNG运输以及LCD运输的液化气运输船舶,以及可以安全有效地用于将LCD从运输船舶运输到海上注入井口的运输系统。
现在,我们已经研制了一种可以安全有效地用于将LCD从运输船舶运输到海上注入井口的LCD运输方法和设备。而且,根据本发明的运输船舶上的LCD容器可以安全有效地用于将LPG、LNG或PLNG从海上出油井运输到海岸。
发明内容
因此,从本发明的一个方面来看,提供一种将液态二氧化碳从水上的运输船舶(在下文中称作“船”)上的加压和冷冻液化气容器运输到连接到水面平台的海上注入井的方法,所述方法包括:将所述容器和所述平台与管道连接、所述管道包括:其至少一部分浸入在所述船舶和所述平台之间的水中的挠性段,第一泵、第二泵、加热器、膨胀箱以及第三泵;使用所述第一泵,将液态二氧化碳沿所述管道从所述容器泵送到所述第二泵;使用所述第二泵,将所述液态二氧化碳沿所述管道并且经过所述加热器泵送到所述第三泵;使用所述加热器,在其到达所述第三泵之前加热所述液态二氧化碳,优选在其进入所述挠性段浸入水中的所述部分之前,使用所述第三泵将所述液态二氧化碳向下泵送到所述注入井;在所述第三泵将所述液态二氧化碳向下泵送到所述注入井的操作之前的期间内,使用所述膨胀箱调整所述第三泵的所述管道上游以及所述挠性段的上游端的下游中的压力;以及在所述第三泵将所述液态二氧化碳向下泵送到所述注入井的操作期间内,使用泵送或加压的气体将在所述膨胀箱中收集的液态二氧化碳运输到所述管道。
在本发明的方法中,在LCD运输中使用的船舶优选具有至少两个泵:在该LCD容器内的排出泵和在该容器外部的增压泵。优选在上述温度和压力条件下即在该三相点之上的压力下将该LCD容纳在该容器内。
可以理解,使用传统的泵可将该CO2从该容器泵送。因此,该第一“泵”可以是任何适于从该容器排出CO2的装置。
例如,在一个可选的设置中,可以通过增压该LCD容器将该CO2从该容器排出到第二(或增压)泵,以便转移该LCD。在该设置中,在所需的第二泵的入口用所需的压力限定该LCD容器的最小压力,以便避免在该泵的入口形成蒸汽泡。通过所述第二泵所需的净压吸高(Net Positive SuctionHeight)HPSH来指定该泡点所需的界限。
在可选的设置中,可以通过借助放置在该LCD容器内部的热交换器来汽化LCD,或者通过在该LCD船舶外部汽化LCD以注入该LCD船舶而加压该LCD容器。该运输压力接近饱和,并且在卸载LCD之前或期间增加该压力。
该船舶优选具有加热器,以便如果必要的话,至少LCD的加热部分会在该LCD进入该管道的浸入部分之前出现.这用于避免对该平台上的加热器的需要,或者减少对该平台上的加热器的需要,或者保证可以得到充足的热容量,以及减少该管道浸入水中的部分冻结的风险,以及该管道中的固态二氧化碳从该容器引导到该平台的风险.这种船上的加热器优选位于该排出和增压泵的下游.优选提取、汽化来自该货物和/或增压泵下游的一些二氧化碳,并且将其反馈到该LCD容器中,以便保持其中的压力,从而保持该LCD在该三相点之上,由此保证LCD的最佳运输.
还希望该船舶具有管道接头,借助该管道接头可以将来自该容器的管道连接到引导到浸在水中的转动架装载(STL)系统的挠性管道。另一挠性管道(挠性立管)优选从该STL引导到海床,以便连接到引导到另一刚性或挠性立管的海下(sub-sea)管线,从而将该LCD带到该平台。至少该管道的引导到该平台并且未浸在水中的部分优选是隔热的,以便防止大气的过度结冰和凝结。
该管道上的膨胀箱用于保证在从船到平台的每个LCD的运输之间的期间,该管道内的压力不会超过设计压力。在每个运输之间,该管道中的LCD会从环境吸热,并且膨胀。该膨胀箱用作调节该膨胀的储油器,并且在随后的LCD运输操作期间,可以将其中收集的LCD反馈到该管道中。
如果还未达到井下注入所需的温度,则希望使用位于该平台上的加热器来将该平台加热至这个温度。通常,为了避免井下形成天然气水合物,将该LCD加热至大约10℃或更多,优选12℃或更多,特别是14至20℃。可以类似地将该LCD加热至0℃或0℃之上,以便避免井下形成天然气水合物。这种相对于运输温度(即LCD容器中的温度)的温度升高包含伴随的压力升高,以便避免在加热期间形成CO2的气相,从而,该第二(增压)泵应当具有出口压力,其保证该LCD在加热至注入温度期间远离该泡点。
将该管道中的LCD提供到该注入泵(例如,串联的一个、两个、三个或四个泵),以便使其达到注入所需的压力,希望大约是150至350巴,例如200至300巴。当不进行LCD注入时,可以将这些泵中的一个或多个设置为井下水注入;然而,通过在该泵之后且更优选地在为了多孔平台中的不同孔设计的用于分离注入液体的歧管件之后连接的管道系统,也可以将更多通常不同的泵送系统用于水和LCD注入。
由于通常分批执行LCD注入,而水注入在来自连续的LCD运输船舶的LCD注入之间出现,由于在水和LCD注入转换期间将该注入井保持加压,且由于在达到完全LCD注入速率之前会有延时,因而希望在该注入泵启动阶段,来自该注入泵下游的二氧化碳再循环到流向该注入泵的二氧化碳中,可选地在该再循环期间具有冷却。
在具体的优选实施方式中,该LCD运输船舶上的泵和加热器设置成使得在-50℃至+0℃范围内的温度以及该CO2是液相并且避免空化的压力情况下,将LCD引入该挠性管道的浸入段。然而,更优选地,在保证避免CO2气相直到其到达该平台的压力情况下操作该增压泵;在这种场合下,一部分二氧化碳可以从该主LCD流分离,蒸发以及再循环到该LCD容器中,以便当排出其含量时保持该LCD容器内的压力。这种回流管线可以来自该货物泵的加压侧,或者来自该增压泵的加压侧。然而,优选地,具有来自该货物泵的下游以及该增压泵的下游的回流管线。第一保证了启动是适当的之前该增压泵入口的流速和压力,并且避免了启动时该管道内液相到气相的转变。第二保证了在启动是适当的之前到该平台的流速和压力,并且帮助防止了启动时该管道内不希望有的液相到气相的转变。
该平台优选具有膨胀箱,该膨胀箱可以在LCD注入之间的期间积累LCD。该箱优选离开该管道,并且通过阀连接到该管道,该阀是压力激活的,以便在该管道中的CO2通过环境加热时调节增加该CO2的容量。这样,可以避免或者最小化不需要释放到大气的CO2。否则,该CO2将直接排出到大气。
该平台还优选具有从该注入泵的加压侧到该注入泵的输入侧的回流管线.这样做保证了启动期间所希望的流速和压力,直到实现设计的注入压力和流速.为了避免高回流速率的温度升高,该回流管线优选具有冷却器,例如热交换器.
希望LCD在水上船只上的运输压力和温度是5.2至10巴(bar),对应于-57至-40℃的温度;该LCD离开该船时的压力优选是30至70巴,对应于-50至0℃的温度。该LCD离开该注入泵时的压力取决于具体的井,但是一般可以是100至300巴,对应于10至20℃的温度。
因此,使用的容器、管道、接头、泵等应当能够经受住这些温度和压力。
从本发明的另一个方面看,提供一种LCD运输系统,所述系统包括:连接到注入井的水面平台LCD运输船舶,以及连接所述平台上的所述船舶和LCD注入泵的管道,所述船舶具有加压和冷冻的LCD容器,用于沿所述管道将LCD泵送出所述容器的所述容器内的货物排出泵,用于沿所述管道将LCD泵送到所述平台的增压泵,从所述货物泵的下游到所述容器的第一回流管线,从所述增压泵的下游到所述容器的第二回流管线,以及可选的第一加热器,所述第一加热器设置成加热从所述船舶沿所述管道流动的LCD,所述第一加热器优选地位于所述增压泵的下游,并且所述平台具有用于将LCD向下注入所述井的注入泵,膨胀箱设置成用以调节所述注入泵的所述管道上游中的LCD的压力,来自所述注入泵的下游的第三回流管线,可选的第二加热器,所述第二加热器设置成加热所述注入泵的所述管道上游中的LCD,以及可选的冷却器,所述冷却器设置成冷却所述第三回流管线中的二氧化碳;所述第一和第二加热器中的至少一个位于所述系统中。
从本发明的另一个方面来看,提供了一种水流LCD运输船舶,所述船舶包括加压和冷冻的LCD容器,用于沿所述管道将LCD泵送出所述容器的所述容器内的货物排出泵,用于沿所述管道将LCD泵送到所述平台的增压泵,从所述货物泵的下游到所述容器的第一回流管线,从所述增压泵的下游到所述容器的第二回流管线,以及可选的第一加热器,所述第一加热器设置成加热沿所述管道从所述船舶流动的LCD,所述第一加热器优选位于所述增压泵的下游。本发明的船舶中的LCD容器优选具有至少500m3、特别是1000至10000m3的内部容积。
在此的水面平台表示位于水面或之上的平台,例如固定或浮动的平台。
附图说明
现在参照附图描述本发明的实施方式,其中
附图1是根据本发明的LCD运输系统的示意图。
具体实施方式
参照附图1,所示的船舶1具有经由管道3连接到水面平台4的冷冻和加压LCD箱2。
该LCD容器内的是货物泵5,其将LCD驱动到增压泵6,该增压泵自身驱动LCD经由STL7到该平台。该货物泵5和增压泵6的下游分别是回流管线8和9,它们将CO2反馈到该LCD容器中.该船还具有加热离开该船的LCD的加热器10.到达平台4的管道具有膨胀箱11,以便调节该LCD由于环境加热造成的膨胀.在该膨胀箱11之后,该管道经由加热器12引导到用于将LCD注入井下的注入泵13.在该注入泵13的下游,该管道具有将过量的CO2反馈到该加热器12的上游位置的回流管线14。为了避免注入泵13在启动阶段过热,回流管线14自身具有热交换器15。
Claims (14)
1.一种水上液态二氧化碳(LCD)运输船舶,所述船舶包括:加压和冷冻的LCD容器,用于沿管道将LCD泵送出所述容器的所述容器内的货物排出泵,用于沿所述管道将LCD泵送到水面平台的增压泵,从所述货物泵的下游到所述容器的第一回流管线,以及从所述增压泵的下游到所述容器的第二回流管线。
2.如权利要求1所述的船舶,包括第一加热器,所述第一加热器设置成加热从所述船舶沿所述管道流动的LCD。
3.如权利要求2所述的船舶,其中所述第一加热器位于所述增压泵的下游。
4.如权利要求1-3中任一项所述的船舶,包括管道接头,该管道接头将来自该容器的所述管道连接到通向浸在水中的转动架装载(STL)系统的挠性管道。
5.一种液态二氧化碳(LCD)运输系统,所述系统包括:如权利要求1-4中任一项所述的LCD运输船舶,连接到注入井的水面平台,以及连接所述平台上的LCD注入泵和所述船舶的管道,
所述平台具有:用于将LCD向下注入所述井的注入泵,膨胀箱,以及来自所述注入泵的下游的第三回流管线,所述膨胀箱被布置以便调节所述注入泵的所述管道上游中的LCD的压力,
且所述系统包括下列部件中的至少一个:
位于所述船舶上的第一加热器,所述第一加热器设置成加热从所述船舶沿所述管道流动的LCD;以及
位于所述平台上的第二加热器,所述第二加热器设置成加热所述注入泵的所述管道上游中的LCD。
6.如权利要求5所述的系统,其中所述平台包括冷却器,所述冷却器设置成冷却所述第三回流管线中的二氧化碳。
7.如权利要求5或6所述的系统,其中连接所述容器和平台的所述管道包括挠性段,该挠性段的至少一部分在工作中浸入在所述船舶和所述平台之间的水中。
8.如权利要求5-7中任一项所述的系统,其中装置被如此布置以致在所述注入泵将所述液态二氧化碳向下泵送到所述注入井的操作期间内,泵或加压气体被用于将在所述膨胀箱中收集的液态二氧化碳运输到所述管道。
9.一种将液态二氧化碳(LCD)从LCD运输船舶上的加压和冷冻的LCD容器经由水面平台运输到注入井的方法,该方法包括:
利用在所述容器中的货物排出泵以及在管道上的增压泵将LCD泵送出所述容器并沿所述管道泵送LCD;以及
使用第一和第二回流管线将过量的二氧化碳从所述货物泵的下游和所述增压泵的下游反馈到所述容器。
10.如权利要求9所述的方法,包括加热从所述船舶沿着所述管道流动的LCD。
11.如权利要求9所述的方法,其中所述平台包括注入泵和膨胀箱;且该方法包括:
使用注入泵将LCD注入所述井中;
使用所述膨胀箱调节所述注入泵的所述管道上游中的LCD的压力;
使用第三回流管线将过量二氧化碳从所述注入泵下游反馈到所述容器;以及
在从所述船舶沿所述管道流动期间和/或在所述注入泵的管道上游中加热LCD。
12.如权利要求11所述的方法,包括使用所述平台上的冷却器冷却在所述第三回流管线中的二氧化碳。
13.如权利要求11或12所述的方法,其中连接所述容器和平台的所述管道包括挠性段,且所述方法包括将所述挠性段的至少一部分浸入到所述船舶和所述平台之间的水中。
14.如权利要求11-13中任一项所述的方法,其中在所述注入泵将所述液态二氧化碳向下泵送到所述注入井的操作期间内,泵或加压气体被用于将在所述膨胀箱中收集的液态二氧化碳运输到所述管道。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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GB0416003.2 | 2004-07-16 | ||
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CN114761317A (zh) * | 2019-12-19 | 2022-07-15 | 三菱造船株式会社 | 船舶、船舶中的液化二氧化碳的装载方法 |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102582796A (zh) * | 2012-03-19 | 2012-07-18 | 大连海事大学 | 一种天然气存储和运输船 |
CN112512911A (zh) * | 2018-06-01 | 2021-03-16 | 斯蒂尔赫德液化天然气有限公司 | 液化设备、方法和系统 |
US11959700B2 (en) | 2018-06-01 | 2024-04-16 | Steelhead Lng (Aslng) Ltd. | Liquefaction apparatus, methods, and systems |
CN114761317A (zh) * | 2019-12-19 | 2022-07-15 | 三菱造船株式会社 | 船舶、船舶中的液化二氧化碳的装载方法 |
CN114761317B (zh) * | 2019-12-19 | 2024-04-09 | 三菱造船株式会社 | 船舶、船舶中的液化二氧化碳的装载方法 |
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