LNG Technology. - Linde Engineering
Transcription
LNG Technology. - Linde Engineering
→ Linde Engineering LNG Technology. 2 Contents. 3 Introduction 4 Pretreatment and separation of natural gas 5 LNG plant block scheme 6 Single mixed refrigerant liquefaction process: LIMUM®1 7 References LNG plant in Kollsnes, Norway LNG plant in Kwinana, Australia 8 Single mixed refrigerant liquefaction process: LIMUM®3 9 References MFC® and LIMUM® are registered trademarks of Linde AG LNG plants in China LNG plant in Stavanger, Norway LNG plant in Bintulu, Malaysia 10 MFC® process (mixed-fluid cascade) 11 LNG plant in Hammerfest, Norway 12 Coil-wound heat exchanger 14 Plate-fin heat exchanger 16 Contact 3 Introduction. Natural gas is a mixture of gases containing primarily hydrocarbon gases. It is colorless and odorless in its pure form. It is the cleanest fossil fuel with the lowest carbon dioxide emissions. Natural gas is an important fuel source as well as a major feedstock for fertilizers and petrochemicals. For economic transportation over great distances natural gas can be cooled and liquefied occupying only 1/600th of its normal volume in gaseous form at a temperature of around -162°C. Linde Engineering has a strong history in the LNG industry having developed, built and started-up over 20 LNG plants world-wide since 1967. Linde Engineering´s natural gas liquefaction processes can cover LNG plants ranging from 40 thousand to more than 10 million tons per year. 3 4 Pretreatment and separation of natural gas. Pretreatment of natural gas Prior to liquefaction natural gas often has to be pretreated. Such pretreatment typically consists of mercury removal, gas sweetening and drying. Depending on the downstream processing steps and the concentration of the sour gas components, it may be necessary to remove H2S and CO2 from the natural gas. Scrubbing processes such as MDEA, are offered for this application. Should only minor amounts of sour gas be present, they can be removed by adsorption along with the removal of water. Mercury guard beds are recommended to protect people and equipment. Separation of natural gas Cryogenic processes represent the most economical solutions to reject or to recover natural gas components. NGL, LPG, condensate or the pure components methane, ethane, propane and butane often have higher sales value compared to the pipeline gas itself. Therefore they are frequently extracted and fractionated in tailor made processing plants according to the specific requirements of the regional market. NGL and LPG are ideal feedstocks for steam crackers producing olefins. Removal of nitrogen leads to reduced transportation volumes and an increased heating value. Furthermore it is sometimes required for the usage as fuel gas feeding gas turbines. The gas turbines are installed to provide the required electrical or mechanical power of the LNG plants. C3+ recovery plant in Kollsnes, Norway (Photo courtesy of STATOIL) Helium recovery is often combined with nitrogen removal. High purity helium is produced by the combination of cryogenic and pressure swing adsorption process steps. All manner of processes for the pretreatment and separation of natural gas as well as the extraction of NGL, LPG, nitrogen and helium are offered by the Engineering Division. 5 LNG plant block scheme. A typical LNG plant is comprised of the following units: –LNG metering stations Sometimes in addition the following units are required: –Feed gas compression, in case the natural gas pressure is low –CO2 removal, mostly by a wash process and drying H2O removal by an adsorber (CO2 and H2O would otherwise freeze and cause clogging in the downstream liquefaction equipment) –Natural gas liquefaction –Refrigeration system and refrigerant make-up unit –LNG storage –LNG loading stations Sour gas Exhaust gas hot oil Feed gas compression Refrigerant make-up unit flue gas Gas turbine NG purification CO2 removal Fire fighting NG purification dryer Utilities liquid refr. dry NG vap. refr. fuel gas fuel gas hot oil purified NG Boil-off gas (fuel gas) compression Refrigeration system lean solvent rich NG solvent Solvent regeneration Natural gas Waste heat recovery hot oil hot oil Hot oil system hot oil Waste water –Condensate stabilisation –Fractionation –N2 removal NG liquefaction Flare LNG LNG storage LNG LNG loading station container LNG loading jetty LNG loading station truck LNG LNG meters LNG LNG LNG meters 6 Single mixed refrigerant liquefaction process: LIMUM®1 LIMUM®1 (Linde multi-stage mixed refrigerant process applying platefin heat exchanger) –The LP MR (mixed refrigerant) is compressed in a two stage centrifugal compressor and partially condensed against cooling water or air –Both phases of the compressed MR are jointly fed to a brazed aluminium plate-fin heat exchanger, are fully liquefied and subcooled –After expansion in a J-T valve the MR if fully vaporized under low pressure providing refrigeration for natural gas liquefaction and fractionation, if required. Basic single flow LNG process for less than 0.5 mtpa LNG NG Fractionator N2 NGL LNG LP MR HP MR 7 References. LNG plant in Kollsnes, Norway Capacity Customer Start-up 40,000 tpa Naturgass Vest, now Gasnor 2003 LNG is distributed by trucks and by small LNG transport ships to satellite stations. One innovative feature of this project is the use of LNG as fuel in ferry boats along the Norwegian coast. There are many advantages replacing diesel with LNG. The exhaust gas of the engines is clean and free of solid particles. NOx and CO2 emissions are reduced. The engines and therefore the ferries have a reduced noise level. LNG plant in Kwinana, Australia Capacity Customer Start-up 62,500 tpa Westfarmers Gas Limited 2008 LNG is produced from pipeline gas and is then distributed by truck to various customers, such as peak shaving power stations. Here the LNG replaces diesel and other fuels, which are less environmentally acceptable. 8 Single mixed refrigerant liquefaction process: LIMUM®3 LIMUM®3 (Linde multi-stage mixed refrigerant process applying coilwound heat exchanger) –The LP MR (mixed refrigerant) is compressed in a two stage centrifugal compressor and partially condensed against cooling water or air –The heavy, liquid MR fraction os used in a coil-wound heat exchanger to pre-cool natural gas and to condense the light, gaseous MR fraction partially –The resulting, intermediately boiling MR fraction serves as liquefaction refrigerant, while the remaining light ends MR fraction sub-cools the liquefied natural gas Advanced single flow LNG process for 0.2 to 1.0 mtpa LNG LNG Fractionator N2 NGL NG LP MR HP MR 9 References. LNG plants in China Capacity Customer Start-up 430,000 tpa Xin Jiang Guanghui 2004 Capacity Customer Start-up 430,000 tpa Xin Jiang Ji Munai Guanghui 2013 Capacity Customer Start-up 300,000 tpa Huineng Coal Chemical Co. Ltd. 2013 Capacity Customer Start-up 350,000 tpa Siehuang Tonghei Engery & Technology Dev. Co. Ltd. 2014 All of these LNG plants are highly flexible and excel due to their robustness. As special feature the plant in Jimunai has a nitrogen removal column integrated into the liquefaction process. This is an economically attractive concept for nitrogen rich feed gases. LNG is transported by trucks to a large number of satellite stations. This LNG scheme creates new gas markets and provides a great improvement in the tight energy supply situation in China. LNG plant in Stavanger, Norway Capacity Customer Start-up 300,000 tpa Lyse Gass AS 2010 Due to the high feed gas pressure and based on the Linde proprietary LIMUM® process this LNG plant achieves an outstanding energy efficiency. The plant supplies LNG to both the local industry and AGA, an affiliate of the Linde Gas division. The AGA quota of the produced LNG is first shipped to an import terminal in Nynäshamn, Sweden, which was built as well by Linde Engineering. LNG plant in Bintulu, Malaysia Capacity Customer Start-up 650,000 tpa MLNG 2014 The plant is the world´s largest re-liquefaction plant for N2 rich boil-off gases from MLNG´s LNG complex in Bintulu, Malaysia. 10 MFC® process (mixed-fluid cascade). The MFC® process is highly efficient due to the use of the three mixed refrigerant cycles. The process is comprised of: –Plate-fin heat exchangers for natural gas precooling –CWHEs (coil-wound heat exchangers) for natural gas liquefaction and LNG subcooling –Three separate mixed refrigerant cycles, each with different compositions, which result in minimum compressor shaft power requirement –Three cold suction centrifugal compressors > 10 mtpa LNG can be produced in a single train. MFC® (mixed-fluid cascade) process for 3 to 12 mtpa LNG NG LNG SMR E LMR LMR SMR E E 11 LNG plant in Hammerfest, Norway. Capacity Customer Start-up 4.3 mtpa (million tons per annum) Statoil 2007 This is Europe‘s first and the world´s northernmost LNG baseload plant. The MFC® (mixed fluid cascade) process together with the low cooling water temperature at the site are the basis for the extremely low specific power consumption of the plant (less than 250 kWh/t). This LNG project has another distinguishing feature: the entire LNG baseload plant was preassembled in various shipyards in Europe and transported to its operating location on HLVs (heavy lift vessels). The process plant itself was installed on a barge in a shipyard, transported by HLV and finally grounded in a prepared dock at the site. 12 Coil-wound heat exchanger. The ample choice of usable alloys including aluminium and stainless steel allow coil-wound heat exchangers to be used for a wide range of applications in cold as well as warm applications. The coil-wound heat exchanger is the core equipment in large base-load LNG plants. The Engineering Division has numerous references for coil-wound heat exchangers designed and manufactured in its own workshops. Benefits –Providing a large heating surface per shell –Tolerant against thermal shocks due to its robust design Manufacturing of coil-wound heat exchanger in Linde workshop 13 Refrigerant inlet Manhole Baffle plate Pre-distributor Tube bundle pigtail Mandrel Distributor Lifting trunnion Hand hole Bonnet Transition joint Bundle outlet nozzle Drain Vent Shroud Tube bundle with alternating winding direction Platform stubs Insulation support ring Vessel shell Vacuum ring 2” multi nozzle Temperature detector junction box Bundle inlet nozzle Tube sheet Refrigerant outlet Skirt The coil-wound heat exchanger is the core equipment in large baseload LNG plants. 14 Plate-fin heat exchanger. The vacuum brazed aluminium plate-fin heat exchangers are key components in many cryogenic process plants. They are the preferred heat exchangers in small LNG plants. Benefits –Compactness, saving installation space and investment costs –Many process streams can be handled in a single unit, thus avoiding expensive interconnecting piping of different units –Low equipment weight Aluminium plate-fin heat exchangers assembled in Linde workshop 15 ↓D ↓ A C ↓ Stub pipe Distributor fin Header tank Heat transfer fin ↓ B Partition plate Side bar Cover plate Scheme of an aluminium plate-fin heat exchanger ↓ B ↓ A ↓ ↓C D The vacuum brazed aluminium plate-fin heat exchangers are key components in many cryogenic process plants. They are the preferred heat exchangers in small LNG plants. Designing processes – constructing plants. Linde´s Engineering Division continuously develops extensive process engineering know-how for the planning, project management and construction of turnkey industrial plants. The range of products comprises: − Petrochemical plants − LNG and natural gas processing plants − Synthesis gas plants − Hydrogen plants − Gas processing plants − Adsorption plants − Air separation plants − Cryogenic plants − Biotechnology plants − Furnaces for petrochemical plants and refineries The Engineering Division and its subsidiaries manufacture: − Packaged units, coldboxes − Coil-wound heat exchangers − Plate-fin heat exchangers − Cryogenic standard tanks − Air-heated vaporizers − Spiral-welded aluminium pipes More than 4,000 plants worldwide document the leading position of the Engineering Division in international plant construction. Linde Impianti Italia S.L.R. 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