EP2135228B1 - Méthode de détection de gaz autour de systèmes de stockage de gaz - Google Patents
Méthode de détection de gaz autour de systèmes de stockage de gaz Download PDFInfo
- Publication number
- EP2135228B1 EP2135228B1 EP08723280.7A EP08723280A EP2135228B1 EP 2135228 B1 EP2135228 B1 EP 2135228B1 EP 08723280 A EP08723280 A EP 08723280A EP 2135228 B1 EP2135228 B1 EP 2135228B1
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- European Patent Office
- Prior art keywords
- gas
- detectors
- enclosed space
- flammable
- limit
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- 238000000034 method Methods 0.000 title claims description 26
- 239000007789 gas Substances 0.000 claims description 259
- 231100001261 hazardous Toxicity 0.000 claims description 39
- 238000004880 explosion Methods 0.000 claims description 28
- 238000009423 ventilation Methods 0.000 claims description 23
- 238000001514 detection method Methods 0.000 claims description 15
- 239000000446 fuel Substances 0.000 claims description 13
- 230000005540 biological transmission Effects 0.000 claims description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 6
- 239000002737 fuel gas Substances 0.000 claims description 4
- 239000006185 dispersion Substances 0.000 claims description 2
- 230000035945 sensitivity Effects 0.000 claims description 2
- 238000005070 sampling Methods 0.000 description 18
- 239000003949 liquefied natural gas Substances 0.000 description 10
- 239000000969 carrier Substances 0.000 description 6
- 230000004308 accommodation Effects 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 239000003915 liquefied petroleum gas Substances 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 2
- 238000012937 correction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 238000007792 addition Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 238000005399 mechanical ventilation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G08—SIGNALLING
- G08B—SIGNALLING OR CALLING SYSTEMS; ORDER TELEGRAPHS; ALARM SYSTEMS
- G08B21/00—Alarms responsive to a single specified undesired or abnormal condition and not otherwise provided for
- G08B21/02—Alarms for ensuring the safety of persons
- G08B21/12—Alarms for ensuring the safety of persons responsive to undesired emission of substances, e.g. pollution alarms
- G08B21/16—Combustible gas alarms
-
- G—PHYSICS
- G08—SIGNALLING
- G08B—SIGNALLING OR CALLING SYSTEMS; ORDER TELEGRAPHS; ALARM SYSTEMS
- G08B29/00—Checking or monitoring of signalling or alarm systems; Prevention or correction of operating errors, e.g. preventing unauthorised operation
- G08B29/16—Security signalling or alarm systems, e.g. redundant systems
Definitions
- the present invention relates to flammable gas detection for released gas in a hazardous area of gas carriers, and more particularly it concerns devices and methods of detecting and ventilating leaked flammable gases in hazardous area of a gas carrier. They can immediately detect the leakage of flammable gas in enclosed spaces in gas carriers or onshore or offshore facilities where boil-off gas (BOG) is compressed to be used as fuel or to be re-liquefied, or in any other places of hazardous area where have potential gas leakages to eliminate the possibility of gas explosion.
- BOG boil-off gas
- the traditional gas detection system samples the gases at a number of sampling heads around cargo tanks and enclosed spaces of the hazardous area by the procedure regulated in IGC Code (International code for the construction and equipment of ships carrying liquefied gases in bulk).
- IGC Code International code for the construction and equipment of ships carrying liquefied gases in bulk.
- the sampled gases are analyzed with a gas analyzer, which is located in a safe area (an accommodation side) according to a predefined sequence.
- LNG liquefied natural gas
- LPG liquefied petroleum gas
- onshore and offshore facilities using boil-off gas generated by atmospheric heat sources have an auxiliary equipment such as cargo compressors or re-liquefaction systems so that boil-off gas is compressed to be used as fuel for propulsion or power generation, or is re-liquefied to be stored as cargo.
- the cargo compressors or the re-liquefaction systems are installed in a separate enclosed space for the protection and the separation thereof. Gas in the enclosed space is periodically sampled, and analyzed to measure the concentration of the flammable gas contained therein in order to eliminate the possibility of an explosion. That is to say, in an enclosed space such as a cargo compressor room, a valve room and a pump room, gas is periodically sampled and the concentration of the flammable gas contained therein is measured.
- Conventional gas detection system constituted with a flammable gas analyzer and sampling scheme and it sequentially samples and analyses the sampled gases come from a number of sampling ports in the hazardous area and enclosed spaces of a gas carrier. For analyzing all the sampling head locations including response time, approximately 30 minutes to complete the whole sequences will be taken and this means that the gas release to start right after the previous sampling turn will be continued during maximum 30 minutes and will be detected on the next turn. (In the IGC Code, it is stipulated that the gas detection equipment should be capable of sampling and analyzing for each sampling head location sequentially at intervals not exceeding 30 minutes, except that in the case of gas detection for the ventilation hoods and gas ducts sampling should be continuous).
- maximum length of pipeline for gas sampling from an analyzer to sampling head locations in the hazardous area is more than 260m, and up to 140 seconds are required for the sampled gas to reach the analyzer. This means, if flammable gas leaks right after the first sampling sequence, there are lots of possibilities to occur explosion due to the gas cloud comes from the released gas during at least 140 seconds by the second sampling sequence.
- Fig 4 shows the typical arrangement for installation of gas sampling pipeline.
- gas sampling pipes are installed therein and are connected to a gas detection equipment via tubes.
- the gas detection equipment is installed in an accommodation zone which is separate from the cargo compressor room as a separately enclosed space, by the distance of about 50-100 m, about 30 to 60 seconds are required for sampled gas to reach the gas detection equipment through the gas sampling pipes.
- an object of the present invention is to provide a method of detecting leaking gas in a hazardous area of a gas carrier, in which direct sensing type detectors are installed in the enclosed spaces and the hazardous area of a gas carrier so that leaking gas can be detected in real time.
- Another object of the present invention is to provide a method of detecting leaking gas in a hazardous area of a gas carrier, in which an LOS (line of sight) type infrared gas detector is installed as a direct sensing type detector, so that the leakage of gas can be immediately detected over a wide area.
- LOS line of sight
- Another object of the present invention is to provide a method of detecting leaking gas in a hazardous area of a gas carrier, in which at least two direct sensing type detectors are installed in the same area, so that malfunction of the detectors can be monitored.
- Still another object of the present invention is to provide a method of detecting leaking gas in a hazardous area of a gas carrier, which can immediately detect and forcibly ventilate leaking gas in the enclosed space, such as a cargo compressor room, a valve room and a pump room, of an LNG carrier or onshore or offshore facilities having steam turbines, or medium speed dual-fuel diesel engines, or a re-liquefaction system, or dual-fuel gas turbines, or slow speed dual-fuel diesel engine, etc. installed therein and operating at a high operating pressure.
- a still further object of the present invention is to provide a method of detecting leaking gas in a hazardous area of a gas carrier, in which at least one exhaust fan is operated at the time of the detection of leaking gas in a enclosed space to forcibly ventilate the enclosed space, so that the dispersion of flammable gas and the possibility of an explosion can be prevented.
- the leakage of gas can be immediately detected and confirmed over a wide area.
- a hazardous area and an enclosed space can be immediately and forcibly ventilated.
- the likelihood of an explosion due to the leakage of flammable gas can be decreased.
- leaking gas in the case of a enclosed space such as a cargo compressor room, a valve room or a motor room, leaking gas can be immediately detected and confirmed by the direct sensing type gas detector, and by operating two exhaust fans in association with the gas detection system, the enclosed space can be immediately and forcibly ventilated, whereby the possibility of an explosion due to the leakage of flammable gas can be prevented.
- FIG. 1 is a flow chart illustrating a method of detecting leaking gas in a hazardous area of a gas carrier according to the present invention
- FIG. 2 is a view illustrating an application example of the present invention
- FIG. 3 is a view illustrating the installed state of an LOS (line of sight) type gas detector according to the present invention.
- At least two direct sensing type gas detectors 130, 140 and 150 are installed in a enclosed space, such as a cargo compressor room, a valve room and a pump room, defined to protect and separate apparatuses for handling compressed boil-off gas (BOG) of liquefied natural gas and liquefied petroleum gas generated due to heat transfer from the outside to thereby use the compressed boil-off gas as fuel for a propulsion engine or a power generation apparatus or for re-liquefying the boil-off gas, and in a hazardous area including these provisions, so that the leakage of gas into the hazardous area can be immediately detected.
- a cargo compressor room such as a cargo compressor room, a valve room and a pump room
- BOG compressed boil-off gas
- the method of detecting leaking gas in a hazardous area of a gas carrier includes the steps of sensing amounts of leaking gas using direct sensing type gas detectors (S100), comparing the amounts of leaking gas detected by the gas detectors with an alarm issuance limit, and issuing an alarm and operating a forced exhaust fan when the amount of leaking gas detected by at least one gas detector exceeds the alarm issuance limit (S200), and actuating an emergency stop system when the amounts of leaking gas detected by at least two detectors exceed an emergency stop limit (S300).
- S100 direct sensing type gas detectors
- S200 alarm issuance limit
- S300 emergency stop system
- the method further includes the step of re-sensing amounts of leaking gas in a hazardous area in which forced ventilation is implemented using the forced exhaust fan, using the gas detectors (S400), and sequentially stopping issuance of the alarm and operation of the forced exhaust fan when the re-detected amounts of leaking gas do not exceed a reference value (S500).
- the amounts of leaking gas are detected by the gas detectors 130, 140 and 150 which are installed in the hazardous area and an enclosed space 350, such as a cargo compressor room 330, a valve room, a pump room and a motor room 340.
- the gas detectors 130, 140 and 150 which are installed in the hazardous area and an enclosed space 350, such as a cargo compressor room 330, a valve room, a pump room and a motor room 340.
- at least two electric gas detectors 140 and 150 having an Ex-D class based on IEC, International Electro-technical Commission) or LOS (line of sight) type detectors 130, which are direct sensing type detectors approved by the IGC Code (International code for the construction and equipment of ships carrying liquefied gases in bulk) and are explosion-proof, are installed.
- IGC Code International code for the construction and equipment of ships carrying liquefied gases in bulk
- the LOS (line of sight) type detector 130 comprises a transmission section 110 capable of transmitting an infrared signal and a reception section 100 capable of receiving the infrared signal transmitted from the transmission section 110. If flammable gas reaches an infrared gas sensing line 120 between the transmission section 110 and the reception section 100, a change in the infrared sensitivity of the reception section 100 is detected, and thereby, the leakage of gas is detected.
- the amounts of leaking gas detected by the gas detectors 130, 140 and 150 are compared with a preset reference value, that is, the alarm issuance limit, set to correspond to about 30% of the lower explosion limit of flammable gas, so as to eliminate the likelihood of an explosion.
- a preset reference value that is, the alarm issuance limit
- the alarm issuance limit corresponds to about 30% of the lower explosion limit of the flammable gas
- the alarm issuance limit corresponds to 1.5 vol% of methane, which is a concentration at which an explosion does not actually occur.
- methane which is the main constituent of the cargo of an LNG carrier
- the present invention applies to an LNG carrier operating at a high pressure of 6 barg to 250 barg, if the leakage of gas occurs, the flammable gas can immediately exceed the lower explosion limit and reach a concentration at which an explosion can easily occur.
- the reference value for the issuance of a warning alarm be set to correspond to about 30% of the lower explosion limit of the leaking gas.
- the emergency stop limit corresponding to about 60% of the lower explosion limit of the leaking gas, is compared with the amounts of leaking gas.
- the travel of the ship is stopped. That is to say, when the leaking gas is detected by amounts exceeding about 60% of the lower explosion limit of the flammable gas, the emergency stop system is actuated to stop the travel of the ship so as to prevent the amounts of leaking gas from reaching an explosion threshold.
- a warning alarm is issued to warn of the corresponding situation, and at the same time, a ventilation system, such as the forced exhaust fan, etc. is operated. Also, when the detected amounts of the leaking gas exceed the emergency stop limit, the emergency stop system is actuated so that the travel of the ship is stopped.
- the ventilation system such as the forced exhaust fan, etc. is a conventional provision which is installed in the hazardous area and the enclosed space of a gas carrier, the detailed description thereof will be omitted herein.
- the forced exhaust fan when used as the ventilation system, the forced exhaust fan has capacity sufficient to ventilate a volume corresponding to 30 times the volume of the enclosed space per hour, and is configured such that exhausted gas is not re-introduced into the enclosed space.
- the capacity of the forced exhaust fan is determined in conformity with the fan capacity prescribed in the IGC Code.
- At least two electric gas detectors 140 and 150 (having an Ex-D design based on IEC) and at least two LOS (line of sight) type detectors 130, which are direct sensing type detectors and are explosion-proof, are installed together or independently in the same area.
- a warning alarm is issued depending upon the detected amount of the leaking gas, and only when at least two gas detectors simultaneously detect leaking gas exceeding the emergency stop limit, corresponding to 60% of the lower explosion threshold of the flammable gas, is the emergency stop system actuated.
- step S400 amounts of leaking gas are re-detected in the hazardous area and the enclosed space in which a warning alarm is issued and the emergency stop system is actuated.
- the amounts of leaking gas in the hazardous area 320 and the enclosed space 350 in which the ventilation is being conducted through the operation of the ventilation system are rapidly re-detected using at least two direct sensing type gas detectors 130, 140 and 150.
- the re-detected amounts of leaking gas are compared with the reference value. When the re-detected amounts are less than the reference value, the actuation of the emergency stop system or the issuance of the warning alarm is stopped.
- the amounts of the leaking gas detected by the gas detectors are transmitted to a control system 400 as electrical signals. Also, these transmitted amounts of the leaking gas are converted through the internal operation of the control system 400 into commands for enabling the issuance of the alarm or the actuation of the emergency stop system.
- the leaking gas can be detected through the sensing step, the warning alarm issuing step, the emergency stopping step, the gas re-sensing step and the fan stopping step, and by operating the ventilation system, the probability of an explosion can be eliminated.
- the forced exhaust fan be installed as the ventilation system so that, when gas leakage is detected by the gas detectors, quick ventilation of the leaking gas by the forced fan is implemented, unlike the hazardous area.
- At least two direct sensing type detectors are installed in the enclosed space of a gas carrier or similar onshore or offshore facilities equipped with a dual-fuel diesel engine, a gas turbine engine, re-liquefaction apparatus, etc., and at least two forced exhaust fans operating in cooperation with the detectors are also installed to implement ventilation.
- FIG. 5 is a flow chart illustrating a method for independently detecting leaking gas in an enclosed space according to the present invention
- FIG. 6 is a view illustrating the state in which a gas detector according to the present invention is installed in an enclosed space.
- At least two electric gas detectors 140 or 150 (having an Ex-D design based on IEC), which are explosion-proof, are installed in an enclosed space.
- two forced exhaust fans 20 operating in cooperation with the direct sensing type gas detectors 140 or 150 are installed at one side of the enclosed space 350 to communicate with air outlets 40.
- the method comprises the steps of sensing flammable gas leaking into an enclosed space using gas detectors (S100a), comparing the amounts of flammable gas detected by the gas detectors with a preset reference value (S200a), issuing a warning alarm and simultaneously operating the two forced exhaust fans installed in the enclosed space to forcibly implement ventilation when the detected amount of leaking gas exceeds the reference value (S300a), re-sensing gas in the enclosed space using the gas detectors while forced ventilation is implemented by the two forced exhaust fans (S400a), and stopping the issuance of the alarm and the operation of the forced exhaust fans when the re-detected amounts of leaking gas do not exceed a reference value (S500a), so that the leaking gas in the enclosed space can be immediately detected and the enclosed space can be forcibly ventilated.
- gas detectors S100a
- S200a preset reference value
- S300a the reference value
- S400a re-sensing gas in the enclosed space using the gas detectors while forced ventilation is implemented by the two forced
- the amounts of leaking gas are detected using the direct sensing type gas detectors installed in the enclosed space, such as a cargo compressor room, a valve room and a pump room.
- the direct sensing type gas detectors installed in the enclosed space, such as a cargo compressor room, a valve room and a pump room.
- at least two gas detectors having an Ex-D design based on IEC which are direct sensing type detectors approved by the IGC Code (International code for the construction and equipment of ships carrying liquefied gases in bulk), are installed.
- the amounts of leaking gas detected by the gas detectors are compared with the preset reference value.
- the reference value is preset as an alarm issuance limit in a hazardous area, that is, a limit corresponding to about 30% of the lower explosion limit of flammable gas.
- the forced insulation step S300a when the amount of leaking gas detected by the gas detectors is the same as or exceeds the preset reference value, apparatuses having increased probability of explosion are urgently stopped. Namely, when the detected amount of leaking gas exceeds the alarm issuance limit, an alarm is issued to warn of the emergency, and at the same time, the two forced exhaust fans installed in the enclosed space are operated. If the two forced exhaust fans are operated, since the enclosed space can be immediately ventilated, the amount of leaking gas in the enclosed space abruptly decreases below the alarm issuance limit. Between the two forced exhaust fans, one forced exhaust fan is always operated, and when the detected amount of the leaking gas exceeds the preset reference value, the remaining forced exhaust fan is forcibly operated to immediately ventilate the enclosed space.
- the forced exhaust fan has a capacity to ventilate a volume corresponding to 30 times the volume of the enclosed space per hour, and is configured such that exhausted gas is not re-introduced into the enclosed space.
- the capacity of the forced exhaust fan is determined in conformity with the fan capacity prescribed in the IGC Code.
- a separate exhaust fan may be installed as an auxiliary fan.
- the amounts of leaking gas in the enclosed space 350 are re-detected while forced ventilation is implemented. That is to say, the amounts of leaking gas are immediately re-detected by the direct sensing type gas detectors in the enclosed space for which the ventilation is being implemented by the simultaneous operation of the two forced exhaust fans.
- the re-detected amounts of leaking gas are compared with a reference value.
- the operation of the forced exhaust fans is stopped.
- the direct sensing type gas detectors and the two forced exhaust fans be operated in cooperation with each other to sense the leaking gas before the amounts of leaking gas in the enclosed space reach the emergency stop limit and to forcibly ventilate the leaking gas to thereby eliminate the possibility of an explosion.
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- Computer Security & Cryptography (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
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- Combustion & Propulsion (AREA)
- Health & Medical Sciences (AREA)
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Claims (15)
- Dispositif pour détecter en temps réel des gaz inflammables qui fuient dans une zone dangereuse (320) comprenant un espace fermé séparé dans (350) d'un système de stockage de gaz ayant une zone de sécurité (300) séparée par une cloison (310) de la zone dangereuse (320), ledit système de stockage de gaz utilisant un gaz d'évaporation généré par des sources de chaleur atmosphériques et ayant un équipement auxiliaire installé dans l'espace fermé séparé de sorte que le gaz d'évaporation soit comprimé pour être utilisé comme combustible ou pour être reliquéfié de nouveau pour être stocké comme cargaison,
ledit dispositif comprenant :- au moins deux détecteurs de gaz à détection directe (130, 140, 150) installés dans la zone dangereuse (320) du système de stockage de gaz, et configurés pour mesurer la concentration de gaz inflammable libéré, et- un système de détection et de commande de gaz (400) installé dans la zone de sécurité (300) du système de stockage de gaz, et configuré pour comparer la concentration de gaz inflammable détectée par les détecteurs de gaz (130, 140, 150) avec une limite d'émission d'alarme, pour émettre une alarme et pour faire fonctionner un ventilateur d'évacuation (20, 40) si la concentration de gaz inflammable détectée par au moins un détecteur de gaz dépasse la limite d'émission d'alarme; et pour actionner un système d'arrêt d'urgence lorsque les concentrations de gaz inflammable détectées par au moins deux détecteurs dépassent une limite d'arrêt d'urgence. - Dispositif selon la revendication 1, dans lequel les détecteurs de gaz (130, 140, 150) comprennent des détecteurs de gaz électriques ou des détecteurs de gaz infrarouges de type LOS (ligne de mire), à détection directe et antidéflagrants (classe Ex-D).
- Dispositif selon la revendication 2, dans lequel chacun des détecteurs de gaz de type LOS comprend une section de transmission (110) capable de transmettre des signaux infrarouges et une section de réception (100) capable de recevoir les signaux infrarouges transmis depuis la section de transmission (110) de sorte que, lorsque le gaz inflammable atteint une zone (120) entre la section de transmission (110) et la section de réception (100), un changement de sensibilité infrarouge de la section de réception est détecté, et ainsi une fuite de gaz est détectée.
- Dispositif selon l'une quelconque des revendications 1 à 3, dans lequel le système de stockage de gaz est un transporteur, une installation terrestre ou en mer.
- Dispositif selon l'une quelconque des revendications 1 à 4, dans lequel l'équipement auxiliaire est un compresseur de cargaison ou un système de re-liquéfaction.
- Dispositif selon l'une quelconque des revendications 1 à 5, dans lequel l'espace fermé est une salle de compresseur de chargement, une salle des vannes, une salle des machines ou une salle des pompes.
- Dispositif selon la revendication 4, dans lequel le transporteur est un méthanier équipé de moteurs diesel bicarburant à vitesse moyenne, ou d'un système de re-liquéfaction, ou de turbines à gaz bicarburant, ou de moteurs diesel bicarburant à vitesse lente, dans lequel le gaz d'évaporation est comprimé jusqu'à 6 Bar gauge, 8 Bar gauge, 40 Bar gauge et 250 Bar gauge respectivement.
- Dispositif selon la revendication 7, comprenant en outre au moins un ventilateur d'évacuation (20) installé dans l'espace fermé pour ventiler à force l'espace fermé, pour empêcher la dispersion de gaz inflammable et la possibilité d'une explosion.
- Dispositif selon la revendication 7, dans lequel au moins deux détecteurs de gaz du type à détection directe sont installés dans l'espace fermé et au moins deux ventilateurs d'extraction forcée (20) fonctionnant en coopération avec les détecteurs de gaz installés pour réaliser la ventilation.
- Procédé de détection de fuites de gaz dans une zone dangereuse d'un transporteur de gaz en utilisant le dispositif selon l'une quelconque des revendications 1 à 9,
dans lequel le procédé comprend les étapes consistant à :- mesurer (S100) la concentration de gaz inflammable libéré en utilisant des détecteurs de gaz à détection directe ;- comparer (S200) la concentration de gaz inflammable détectée par les détecteurs de gaz avec une limite d'émission d'alarme et émettre une alarme et actionner un ventilateur d'évacuation si la concentration de gaz inflammable détectée par au moins un détecteur de gaz dépasse la limite d'émission d'alarme; et- actionner (S300) un système d'arrêt d'urgence lorsque les concentrations de gaz inflammables détectées par au moins deux détecteurs dépassent une limite d'arrêt d'urgence. - Procédé selon la revendication 10, comprenant en outre les étapes consistant à: mesurer de nouveau (S400) la concentration du gaz inflammable dans une zone dangereuse où une ventilation forcée est mise en oeuvre par le ventilateur d'évacuation, en utilisant les détecteurs de gaz ; et arrêter séquentiellement (S500) l'émission de l'alarme et le fonctionnement des ventilateurs d'extraction dans le cas où les concentrations mesurées de nouveau du gaz inflammable ne dépassent pas une limite à émettre.
- Procédé selon la revendication 10, comprenant les étapes consistant à: détecter (S100a) un gaz inflammable libéré dans un espace fermé en utilisant des détecteurs de gaz; comparer (S200a) les concentrations de gaz inflammable détectées par les détecteurs de gaz avec une valeur de référence prédéfinie; émettre (S300A) une alarme d'avertissement et actionner simultanément deux ventilateurs d'évacuation installés dans un espace fermé pour mettre en oeuvre de façon forcée la ventilation lorsque la concentration mesurée de gaz inflammable libéré dépasse la valeur de référence prédéfinie ; mesurer de nouveau (S400a) le gaz dans l'espace fermé en utilisant les détecteurs de gaz tandis que la ventilation forcée est mise en oeuvre en utilisant les deux ventilateurs d'évacuation forcée ; et arrêter (S500a) l'émission de l'alarme et le fonctionnement des deux ventilateurs d'extraction lorsque les concentrations mesurées de nouveau de gaz inflammable ne dépassent pas une valeur de référence.
- Procédé selon l'une quelconque des revendications 10 à 12, dans lequel la limite d'émission d'alarme est fixée pour correspondre à environ 30% de la limite inférieure d'explosion de gaz qui fuit.
- Procédé selon l'une quelconque des revendications 10 à 13, dans lequel la limite d'arrêt d'urgence correspond à environ 60% de la limite d'explosion inférieure du gaz qui fuit.
- Procédé selon l'une quelconque des revendications 10 à 14, dans lequel la limite d'émission d'alarme correspond à 1,5% en volume de méthane.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020070023440A KR100787777B1 (ko) | 2007-03-09 | 2007-03-09 | 보일오프가스 활용설비의 밀폐공간내 누출가스 감지 및환기 방법 |
KR1020080019496A KR100935527B1 (ko) | 2008-03-03 | 2008-03-03 | 가스운반선의 가스위험지역내 누출가스 감지방법 |
PCT/KR2008/001243 WO2008111755A1 (fr) | 2007-03-09 | 2008-03-05 | Méthode de détection de gaz autour de systèmes de stockage de gaz |
Publications (3)
Publication Number | Publication Date |
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EP2135228A1 EP2135228A1 (fr) | 2009-12-23 |
EP2135228A4 EP2135228A4 (fr) | 2012-08-22 |
EP2135228B1 true EP2135228B1 (fr) | 2018-07-04 |
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Application Number | Title | Priority Date | Filing Date |
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EP08723280.7A Active EP2135228B1 (fr) | 2007-03-09 | 2008-03-05 | Méthode de détection de gaz autour de systèmes de stockage de gaz |
Country Status (3)
Country | Link |
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EP (1) | EP2135228B1 (fr) |
JP (1) | JP5114505B2 (fr) |
WO (1) | WO2008111755A1 (fr) |
Families Citing this family (15)
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US9000910B2 (en) * | 2010-06-25 | 2015-04-07 | Industrial Scientific Corporation | Multi-sense environmental monitoring device and method |
FI124835B (fi) | 2012-07-03 | 2015-02-13 | Lngtainer Ltd | Säiliö |
JP2015155787A (ja) * | 2014-02-20 | 2015-08-27 | 潮冷熱株式会社 | Lngの冷熱を用いた船舶の空気調和機の冷媒循環装置 |
DE102014109539A1 (de) * | 2014-07-08 | 2016-01-14 | Basf Se | System und Verfahren zum Betreiben eines Flüssiggasverdampfers |
US20160101842A1 (en) * | 2014-10-08 | 2016-04-14 | Avista Corporation | Fuel transfer and storage systems and methods |
WO2017184702A1 (fr) | 2016-04-19 | 2017-10-26 | Industrial Scientific Corporation | Système de sécurité de travailleur |
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JP2010534795A (ja) | 2010-11-11 |
WO2008111755A1 (fr) | 2008-09-18 |
JP5114505B2 (ja) | 2013-01-09 |
EP2135228A1 (fr) | 2009-12-23 |
EP2135228A4 (fr) | 2012-08-22 |
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