-
公开(公告)号：EP3323707B1
公开(公告)日：2024-07-03
申请号：EP16821573.9
申请日：2016-06-29
CPC分类号： B63B25/16 , F17C6/00 , F25J1/004 , F25J1/0045 , F25J1/0202 , F25J1/023 , F25J1/0277 , F25J2220/6220130101 , B63H21/38 , F02M21/0221 , F25J1/0025 , Y02T10/30
-
公开(公告)号：EP2623414A4
公开(公告)日：2018-07-18
申请号：EP11828834
申请日：2011-09-16
发明人： OKA MASARU
CPC分类号： F25J1/0025 , F17C2221/033 , F17C2223/0161 , F17C2223/033 , F17C2265/034 , F17C2270/0105 , F25J1/0045 , F25J1/005 , F25J1/0065 , F25J1/0067 , F25J1/0072 , F25J1/0204 , F25J1/0208 , F25J1/023 , F25J1/0247 , F25J1/0265 , F25J1/0267 , F25J1/0277 , F25J1/0282 , F25J1/0284 , F25J1/0288 , F25J1/0296 , F25J1/0298 , F25J2210/04 , F25J2220/62 , F25J2230/24 , F25J2230/30 , F25J2245/02 , F25J2290/34
摘要： Provided is a boil-off gas reliquefaction device that devises a disposition of equipment to be installable even in existing LNG carriers and that has a refrigeration cycle unit that reduces thermal load, is compact, and is highly efficient. The boil-off gas reliquefaction device (1) has: a liquefaction processing unit (5) having a BOG supply pipework (35), a fuel compressor (33), and a BOG transport pipework (39); and a refrigeration cycle unit (3) that further lowers the temperature of a coolant from a coolant compressor (6) by means of an expander (13) and that has a condenser (17) that cools BOG passing through the BOG transport pipework (39). The liquefaction processing unit (5) is provided with a BOG precooler (57) that performs heat exchange between BOG passing through the BOG transport pipework (39) on the upstream side of the condenser (17) and BOG passing through the BOG supply pipework (35). The refrigeration cycle unit (3) is provided with: a booster compressor (19) that is driven on the downstream side of the condenser (17) by the expander (13); and a second aftercooler (29) that cools the coolant from the booster compressor (19).
-
公开(公告)号：EP3325903A1
公开(公告)日：2018-05-30
申请号：EP16751198.9
申请日：2016-07-21
CPC分类号： F25J1/023 , F02C3/045 , F05B2210/11 , F25B1/00 , F25B1/053 , F25J1/0022 , F25J1/0042 , F25J1/0247 , F25J1/0263 , F25J1/0284 , F25J1/0298 , F25J2280/10
摘要： A method for starting and operating a plant for the liquefaction of a gaseous product comprising the steps of electrically connecting a variable frequency drive to a motor of a first machine string; increasing the speed of the motor of the first machine string up until a first predefined threshold; electrically disconnecting the variable frequency drive from the motor of the first machine string; electrically connecting the variable frequency drive to a motor of a second machine string; the first predefined threshold is function of said frequency of the power supply grid. The variable frequency drive can be switched during operation of the plant among the strings according to process requirements.
-
4.发明公开
公开(公告)号：EP3322946A1
公开(公告)日：2018-05-23
申请号：EP16732157.9
申请日：2016-06-14
CPC分类号： F25J3/08 , F25J1/0022 , F25J1/0035 , F25J1/0042 , F25J1/0072 , F25J1/0221 , F25J1/023 , F25J1/025 , F25J3/0233 , F25J3/0257 , F25J2200/02 , F25J2200/40 , F25J2200/74 , F25J2200/76 , F25J2205/02 , F25J2210/42 , F25J2210/60 , F25J2215/02 , F25J2215/04 , F25J2215/42 , F25J2220/44 , F25J2230/08 , F25J2230/30 , F25J2230/42 , F25J2230/60 , F25J2235/42 , F25J2240/02 , F25J2240/44 , F25J2245/02 , F25J2260/20 , F25J2270/14 , F25J2270/16 , F25J2270/58 , F25J2270/904
摘要： Described herein are systems and processes to produce liquefied natural gas (LNG) using liquefied nitrogen (LIN) as the refrigerant. Greenhouse gas contaminants are removed from the LIN using a greenhouse gas removal unit. The LNG is compressed prior to being cooled by the LIN.
-
公开(公告)号：EP3305648A1
公开(公告)日：2018-04-11
申请号：EP16803588.9
申请日：2016-04-05
发明人： AN, Su Kyung , CHOI, Dong Kyu , MOON, Young Sik , SHIN, Hyun Jun , JANG, Hyun Min , SON, Jae Wook , LEE, Joon Chae
CPC分类号： B63H21/38 , B63B25/16 , F02M21/0215 , F02M21/0287 , F17C6/00 , F17C9/02 , F17C2221/033 , F17C2227/0185 , F17C2227/0339 , F17C2227/0358 , F17C2265/03 , F17C2265/066 , F17C2270/0105 , F25J1/0025 , F25J1/0037 , F25J1/004 , F25J1/0045 , F25J1/0202 , F25J1/023 , F25J1/0249 , F25J1/0277 , F25J1/0288 , F25J1/0294 , F25J2290/72 , Y02T10/32
摘要： Disclosed is a ship including a storage tank for storing a liquefied gas. The ship includes: an boil-off gas heat exchanger installed on a downstream of the storage tank such that compressed boil-off gas (hereinafter, referred to as "first fluid") is made to exchange heat and cooled using boil-off gas, which is discharged from the storage tank, as a refrigerant; a compressor installed on a downstream of the boil-off gas heat exchanger so as to compress a part of the boil-off gas discharged from the storage tank; an extra compressor installed on a downstream of the boil-off gas heat exchanger in parallel with the compressor so as to compress the other part of the boil-off gas discharged from the storage tank; a refrigerant heat exchanger for additionally cooling the first fluid that is cooled by the boil-off gas heat exchanger; a refrigerant decompressing device which expands the second fluid, which is sent to the refrigerant heat exchanger (hereinafter, referred to as "second fluid") and cooled by the refrigerant heat exchanger, and then sends the second fluid back to the refrigerant heat exchanger; a first decompressing device which expands a part of the first fluid, which is cooled by the boil-off gas heat exchanger and by the refrigerant heat exchanger; and a third decompressing device which expands the remaining part of the first fluid, which is cooled by the boil-off gas heat exchanger and by the refrigerant heat exchanger, and sends the expanded remaining part of the first fluid back to the refrigerant heat exchanger, wherein the refrigerant heat exchanger heat-exchanges the first fluid to cool the first fluid, using the second fluid, a fluid expanded by the refrigerant decompressing device, and a fluid decompressed by the third decompressing device as a refrigerant; the first fluid is boil-off gas compressed by the compressor or is a confluent flow of the boil-off gas compressed by the compressor and the boil-off gas compressed by the extra compressor; and the second fluid is the boil-off gas compressed by the extra compressor or a confluent flow of the boil-off gas compressed by the compressor and the boil-off gas compressed by the extra compressor.
摘要翻译： 公开了一种包括用于存储液化气的储罐的船。 该船舶包括：蒸发气体热交换器，该蒸发气体热交换器安装在储罐的下游，使得压缩蒸发气体（在下文中称为“第一流体”）被交换热量并使用蒸发气体被冷却， 作为制冷剂从储罐中排出; 压缩机，其安装在所述蒸发气体热交换器的下游，以压缩从所述储罐排出的蒸发气体的一部分; 额外的压缩机，安装在蒸发气体热交换器的与压缩机平行的下游，以压缩从储罐排出的另一部分蒸发气体; 制冷剂热交换器，用于额外冷却由蒸发气体热交换器冷却的第一流体; 制冷剂减压装置，该制冷剂减压装置使送到制冷剂热交换器的第二流体（以下称为“第二流体”）膨胀并被制冷剂热交换器冷却，然后将第二流体送回制冷剂热交换器; 第一减压装置，所述第一减压装置使由所述蒸发气体热交换器和所述制冷剂热交换器冷却的所述第一流体的一部分膨胀; 以及第三减压装置，所述第三减压装置使由所述蒸发气体热交换器和所述制冷剂热交换器冷却的所述第一流体的剩余部分膨胀，并且将膨胀的所述第一流体的剩余部分返回到所述制冷剂热交换器， 其中，所述制冷剂热交换器使用所述第二流体，由所述制冷剂减压装置膨胀的流体以及由所述第三减压装置减压的流体作为制冷剂，对所述第一流体进行热交换以冷却所述第一流体; 第一流体是由压缩机压缩的蒸发气体或是由压缩机压缩的蒸发气体和由额外压缩机压缩的蒸发气体的汇合流; 第二流体是由额外压缩机压缩的蒸发气体或由压缩机压缩的蒸发气体和由额外压缩机压缩的蒸发气体的汇合流。
-
6.发明公开
公开(公告)号：EP2629035A4
公开(公告)日：2018-04-04
申请号：EP11832503
申请日：2011-10-07
发明人： OKA MASARU
CPC分类号： F25J1/0022 , B63B25/14 , F25J1/004 , F25J1/005 , F25J1/0072 , F25J1/0205 , F25J1/0207 , F25J1/023 , F25J1/0254 , F25J1/0263 , F25J1/0265 , F25J1/0267 , F25J1/0278 , F25J1/0282 , F25J1/0288 , F25J2230/20 , F25J2230/30 , F25J2240/40 , F25J2245/90 , F25J2270/16 , F25J2270/90
摘要： Provided is a liquefaction method, a liquefying apparatus, and a floating liquefied-gas production facility equipped with the same, with which it is possible to suppress a decrease in liquefaction efficiency when gas to be liquefied is liquefied, to ensure safety, and to make the facility compact. Gas to be liquefied that has been subjected to heat exchange with a high-pressure heating medium composed of a single component is reduced in pressure, after which the gas to be liquefied that has been reduced in pressure is made to exchange heat with a low-temperature-side heating medium that is lower in temperature than and of the same type as the high-pressure heating medium.
-
公开(公告)号：EP3112249A4
公开(公告)日：2018-02-21
申请号：EP15755871
申请日：2015-02-27
发明人： LEE JOON CHAE , KIM NAM SOO , JUNG JE HEON , PARK CHEONG GI
CPC分类号： F17C7/04 , B63H21/38 , B63J2099/003 , F02M21/0215 , F02M21/0224 , F02M21/0245 , F02M21/0287 , F17C9/02 , F17C2221/033 , F17C2223/0161 , F17C2223/033 , F17C2223/043 , F17C2223/047 , F17C2225/0123 , F17C2265/017 , F17C2265/033 , F17C2265/037 , F17C2265/038 , F17C2265/066 , F17C2270/0105 , F25J1/0025 , F25J1/004 , F25J1/0202 , F25J1/023 , F25J1/0277 , F25J2245/02 , Y02T10/32 , Y02T70/5209 , Y02T70/5263 , Y02T90/46
摘要： Disclosed herein is a boil-off gas treatment system. The boil-off gas treatment system includes a compressor compressing boil-off gas generated in an LNG storage tank of a ship or a floating structure, a heat exchanger cooling the compressed boil-off gas through heat exchange with boil-off gas to be supplied to the compressor, an expansion unit performing adiabatic expansion of the boil-off gas cooled by the heat exchanger, a gas-liquid separator performing gas/liquid separation of the boil-off gas subjected to adiabatic expansion by the expansion unit and supplying liquefied natural gas to the LNG storage tank, and a bypass line through which the boil-off gas subjected to adiabatic expansion is supplied from a downstream side of the expansion unit to a downstream side of the gas-liquid separator.
-
8.发明公开
公开(公告)号：EP3030757A2
公开(公告)日：2016-06-15
申请号：EP14744776.7
申请日：2014-07-29
CPC分类号： H02K7/1823 , F01K3/004 , F01K13/02 , F02C6/16 , F25J1/0012 , F25J1/0037 , F25J1/004 , F25J1/0042 , F25J1/0045 , F25J1/0202 , F25J1/0228 , F25J1/023 , F25J1/0251 , F25J1/0264 , F25J2205/24 , F25J2205/66 , F25J2210/06 , F25J2235/02 , F25J2240/10 , F25J2240/80 , F25J2240/82 , F25J2240/90 , F25J2270/06 , Y02E60/15
摘要： A method for producing electrical energy in a combined energy generation plant (100, 200) which comprises an air treatment unit (10) and a power station unit (20) is proposed. In a first operating mode, air (AIR) is liquefied to form an air liquefaction product (LAIR) and, in a second operating mode, an air liquefaction product (LAIR) is converted into a gaseous or supercritical state, in which said product is introduced into the power station unit (20) and is used for producing electrical energy. In a third operating mode, air (AIR) is condensed in the air treatment unit (10) and used in the power station unit (20) directly for producing electrical energy. It is envisaged that, in the first operating mode, the air (AIR) is cooled to several temperature levels (T1 - T5) by two liquid coolants and the air liquefaction product (LAIR) is correspondingly heated. In addition, in the first operating mode, the air (AIR) is condensed stepwise over several pressure levels (LP, MP, MP1, HP). In addition, in the second operating mode, the air liquefaction product (LAIR) is heated to a further pressure level (HP1) and introduced into the power station unit (20) at this pressure level in gaseous form. Finally, in the third operating mode, the air (AIR) is introduced into the power station unit (20) in separate batches and at different pressure levels (MP1, HP or HP1). A corresponding energy generation plant (100, 200) is likewise the subject matter of the invention.
-
9.发明公开Method and apparatus for producing a liquefied hydrocarbon stream 审中-公开Verfahren und Vorrichtung zur Erzeugung einesverflüssigtenKohlenwasserstoffstroms
公开(公告)号：EP2796818A1
公开(公告)日：2014-10-29
申请号：EP13164692.9
申请日：2013-04-22
CPC分类号： F25J1/0022 , F25J1/004 , F25J1/0042 , F25J1/0045 , F25J1/0052 , F25J1/0055 , F25J1/0214 , F25J1/0216 , F25J1/023 , F25J1/0237 , F25J1/0245 , F25J1/0255 , F25J1/0274 , F25J1/0283 , F25J3/0209 , F25J3/0233 , F25J3/0257 , F25J2200/02 , F25J2200/40 , F25J2200/50 , F25J2200/74 , F25J2205/02 , F25J2210/06 , F25J2230/60 , F25J2240/30 , F25J2245/02 , F25J2245/90 , F25J2260/60 , F25J2270/02 , F25J2270/12 , F25J2280/02
摘要： A first nitrogen stripper feed stream is fed into a nitrogen stripper column at a stripping pressure. A nitrogen-stripped liquid is drawn from a sump space of the nitrogen stripper column, depressurized to a flash pressure that is lower than the stripping pressure, and fed to an end flash separator. A liquefied hydrocarbon product stream is discharged from the end flash separator, as well as a process vapour. The process vapour is compressed to at least the stripping pressure, and, split in a stripping vapour stream and a fuel gas vapour stream. The stripping vapour stream is fed into the nitrogen stripper column, while the fuel gas vapour stream is passed to a gas turbine. Another fuel gas, having a lower heating value, is obtained from the overhead vapour from the nitrogen stripper column. This other fuel gas is combusted in a combustion device other than a gas turbine.
摘要翻译： 将第一氮气汽提器进料流在汽提压力下进料到氮气汽提塔中。 氮气汽提液体从氮气汽提塔的贮槽空间抽出，减压至低于汽提压力的闪蒸压力，并进料到末端闪蒸分离器。 液化烃产物流从终端闪蒸分离器以及工艺蒸汽排出。 工艺蒸汽被压缩至少至剥离压力，并且在汽提蒸汽流和燃料气体蒸汽流中分离。 将汽提蒸汽流送入氮气汽提塔，同时将燃料气体蒸气流送入燃气轮机。 具有较低热值的另一种燃料气体是从氮气汽提塔的塔顶蒸气获得的。 这种其它燃料气体在除燃气轮机之外的燃烧装置中燃烧。
-
公开(公告)号：EP2501984A1
公开(公告)日：2012-09-26
申请号：EP10776378.1
申请日：2010-11-16
IPC分类号： F17C1/00
CPC分类号： F17C1/002 , F17C2221/033 , F17C2223/0161 , F17C2223/033 , F17C2265/032 , F17C2265/036 , F17C2265/037 , F25J1/0022 , F25J1/004 , F25J1/0055 , F25J1/0214 , F25J1/023 , F25J1/0245 , F25J2210/06 , F25J2220/62 , F25J2220/64 , F25J2230/32 , F25J2230/60 , F25J2245/90
摘要： A boil-off gas (BOG) stream (15) from a liquefied hydrocarbon storage tank is split into a BOG heat exchanger feed stream (25) and a BOG bypass stream (35). The BOG heat exchanger feed stream (25) is heat exchanged in a BOG heat exchanger (40) against a process stream (135), thereby providing a warmed BOG stream (45) and a cooled process stream (195). The warmed BOG stream (45) is combined with the BOG bypass stream (35) to provide a temperature controlled BOG stream (55). Herein, the mass flow of the process stream (135) is controlled in response to a measured first temperature of at least one of (i) the warmed BOG stream (45) and (ii) the cooled process stream (195) to move the measured first temperature towards a first set point temperature; and the mass flow of one or both of the BOG heat exchanger feed stream (25) and the BOG bypass stream (35) are controlled in response to a measured second temperature of the temperature controlled BOG stream (55), to move the measured second temperature towards a second set point temperature.
-
-
-
-
-
-
-
-
-
搜索结果
138 条记录 (耗时 0.024 秒)
