CN203927381U - Modular cryogenic liquid basin BOG gas is liquefaction system again - Google Patents
Modular cryogenic liquid basin BOG gas is liquefaction system again Download PDFInfo
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- CN203927381U CN203927381U CN201420159764.0U CN201420159764U CN203927381U CN 203927381 U CN203927381 U CN 203927381U CN 201420159764 U CN201420159764 U CN 201420159764U CN 203927381 U CN203927381 U CN 203927381U
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- Prior art keywords
- drainer
- refrigerant
- cryogenic liquid
- solenoid valve
- bog gas
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Abstract
The utility model discloses a kind of modular cryogenic liquid basin BOG gas liquefaction system again, comprise: control system, drainer and refrigerant holding vessel, on described drainer, be connected with medium transport pipeline and medium back flow pipeline, between described drainer and refrigerant holding vessel, by refrigerant delivery line and refrigerant return pipe road, be connected, in described drainer, be provided with condenser, described condenser is connected with refrigerant delivery line, on described drainer, be connected with pressurized machine, described pressurized machine is connected with medium back flow pipeline.By the way, the utility model can modular cryogenic liquid basin BOG gas liquefaction system again, can be applicable to the cryogenic liquid storage systems of all BOG of facing gas treatment problems on market, system architecture is simple, modular design, applying flexible.
Description
Technical field
The utility model relates to cryogenic liquide and stores field, particularly relates to a kind of modular cryogenic liquid basin BOG gas liquefaction system again.
Background technique
Cryogenic liquide storing technology is mainly that the effective bunkerage as liquid nitrogen, liquid oxygen, liquified natural gas (LNG) etc. are researched and developed, is commonly referred to low-temperature liquid storage container for deep cooling (100 ℃ following) liquid medium.Low-temperature liquid storage container agent structure is comprised of three parts: inner container, shell and interlayer adiabatic space.With this structure, form to reach the object that stores deep cooling medium cold energy, thereby can long-term safety effectively store deep cooling medium.
Because temperature and the temperature difference between external environment of storage deep cooling medium are very large, under current cold insulation technical specifications, cryogenic storage container, in storing deep cooling medium process, can inevitably produce heat transmission between inner container and external environment, is referred to as Lou heat.Leaking heat will constantly vaporize the storage deep cooling medium in tank, produces boil-off gas (BOG gas).BOG gas is because of the Cryo Heat Insulation performance of low-temperature liquid storage container and the difference of storage tank system pipeline designs, and the impact of generation is also totally different.From feedack in the market, the continuous accumulation of BOG gas, easily cause the gas phase emission of storing cryogenic liquid medium, cause waste, and environmental pollution etc.
If storing deep cooling medium is inflammable and explosive medium (as LNG), once gas effectively not processed, the pressure of gas-phase space constantly rises, and the gas discharging of storage medium can cause serious potential safety hazard.
At present, the scheme of taking for BOG gas problem on market, is mainly outside cryogenic tank system, to increase in addition the BOG gas that a knock out drum is used for storing discharge, and then the gas in knock out drum is carried out to processing and utilizing.But the cost of this scheme is high, and process operation is loaded down with trivial details, it not a desirable solution.
Model utility content
The technical problem that the utility model mainly solves is to provide a kind of modular cryogenic liquid basin BOG gas liquefaction system again, can be applicable to the cryogenic liquid storage systems of all BOG of facing gas treatment problems on market, system architecture is simple, modular design, applying flexible.
For solving the problems of the technologies described above, the technological scheme that the utility model adopts is: a kind of modular cryogenic liquid basin BOG gas liquefaction system is again provided, comprise: control system, drainer and refrigerant holding vessel, on described drainer, be connected with medium transport pipeline and medium back flow pipeline, between described drainer and refrigerant holding vessel, by refrigerant delivery line and refrigerant return pipe road, be connected, in described drainer, be provided with condenser, described condenser is connected with refrigerant delivery line, on described drainer, be connected with pressurized machine, described pressurized machine is connected with medium back flow pipeline.
In preferred embodiment of the utility model, described medium transport pipeline is connected with cryogenic liquid tank respectively with medium back flow pipeline, on described medium transport pipeline, be provided with pipage control solenoid valve, on described medium back flow pipeline, being provided with refluxes controls solenoid valve, and described pipage control solenoid valve is all connected with control system with the control solenoid valve that refluxes.
In preferred embodiment of the utility model, described pressurized machine is connected on pressure piping, the described pressurization control solenoid valve that is connected with on pressure piping, described pressurization control solenoid valve is connected with control system, and described pressurized machine comprises from boost mode and pressure boost mode.
In preferred embodiment of the utility model, on described refrigerant delivery line, be provided with refrigerant pipage control solenoid valve, on described refrigerant return pipe road, be connected with other cooling requirement modules and coolant discharging control valve, described refrigerant pipage control solenoid valve is connected with PLC system with coolant discharging control valve.
In preferred embodiment of the utility model, described refrigerant return pipe road collects bag with low pressure refrigerant or atmosphere is connected.
In preferred embodiment of the utility model, on described drainer, be provided with drainer liquid level sensor and drainer pressure transducer, on described refrigerant holding vessel, be connected with coolant storage tank pressure transducer and coolant storage tank liquid level sensor, on described cryogenic liquid tank, be provided with sump pressure sensor, described drainer liquid level sensor, drainer pressure transducer, sump pressure sensor, coolant storage tank pressure transducer and coolant storage tank liquid level sensor are all connected with control system.
In preferred embodiment of the utility model, described control system is PLC control system.
In preferred embodiment of the utility model, on described refrigerant delivery line, be also provided with cryopump, described refrigerant holding vessel connects condenser by cryopump.
In preferred embodiment of the utility model, described condenser is bellow type, coil pipe type or plate type condenser.
In preferred embodiment of the utility model, described drainer comprises inner container, shell and the interlayer adiabatic space being formed by inner container and shell, described refrigerant holding vessel comprises inner container, shell and the interlayer adiabatic space being formed by inner container and shell, and the medium storing in described refrigerant holding vessel is liquid nitrogen.
The beneficial effects of the utility model are: the utility model modular cryogenic liquid basin BOG gas is liquefaction system again, can be applicable to the cryogenic liquid storage systems of all BOG of facing gas treatment problems on market, system architecture is simple, modular design, applying flexible.
Accompanying drawing explanation
In order to be illustrated more clearly in the technological scheme in the utility model embodiment, below the accompanying drawing of required use during embodiment is described is briefly described, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skills, do not paying under the prerequisite of creative work, can also according to these accompanying drawings, obtain other accompanying drawing, wherein:
Fig. 1 is the utility model modular cryogenic liquid basin BOG gas structural representation of liquefaction system one preferred embodiment again;
In accompanying drawing, the mark of each parts is as follows: 1, drainer, 2, refrigerant holding vessel, 3, control system, 3, 4, other cooling requirement modules, 5, medium transport pipeline, 6, medium back flow pipeline, 7, refrigerant delivery line, 8, refrigerant return pipe road, 9, condenser, 10, pressurized machine, 11, pipage control solenoid valve, 12, reflux and control solenoid valve, 13, pressurization control solenoid valve, 14, refrigerant pipage control solenoid valve, 15, sump pressure sensor, 16, coolant discharging control valve, 17, drainer liquid level sensor, 18, drainer pressure transducer, 19, coolant storage tank pressure transducer, 20, coolant storage tank liquid level sensor.
Embodiment
Below the technological scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only a part of embodiment of the present utility model, rather than whole embodiments.Embodiment based in the utility model, those of ordinary skills are not making all other embodiments that obtain under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, a kind of modular cryogenic liquid basin BOG gas is liquefaction system again, comprise drainer 1, refrigerant holding vessel 2 and control system 3, described drainer 1 comprises inner container, shell and the interlayer adiabatic space being formed by inner container and shell, described refrigerant holding vessel 2 comprises inner container, shell and the interlayer adiabatic space being formed by inner container and shell, described refrigerant holding vessel 2 is liquid nitrogen container, nitrogen is pollution-free, can directly be discharged in atmosphere and go, described control system 3 be PLC control system.
On drainer 1, be connected with medium transport pipeline 5 and medium back flow pipeline 6, medium transport pipeline 5 is connected with cryogenic liquid tank respectively with medium back flow pipeline 6, on medium transport pipeline 5, be provided with pipage control solenoid valve 11, on described medium back flow pipeline 6, being provided with refluxes controls solenoid valve 12, described pipage control solenoid valve 11 is all connected with control system 3 with the control solenoid valve 12 that refluxes, described condenser 9 is connected with refrigerant delivery line 7, on described drainer 1, be connected with pressurized machine 10, described pressurized machine 10 is connected with medium back flow pipeline 6, described pressurized machine 10 is connected on pressure piping, the described pressurization control solenoid valve 11 that is connected with on pressure piping, described pressurization control solenoid valve 11 is connected with control system 3, described pressurized machine comprises from boost mode and pressure boost mode.
Between described drainer 1 and refrigerant holding vessel 2, by refrigerant delivery line 7 and refrigerant return pipe road 8, be connected, in described drainer 1, be provided with condenser 9, described condenser 9 is bellow type, coil pipe type or plate type condenser, on described refrigerant delivery line 7, be provided with refrigerant pipage control solenoid valve 14, on described refrigerant return pipe road 8, be connected with other cooling requirement modules 4 and coolant discharging control valve 16, described refrigerant pipage control solenoid valve 14 is connected with control system 3 with coolant discharging control valve 16, described refrigerant return pipe road 8 collects bag with low pressure refrigerant or atmosphere is connected, on described refrigerant delivery line 7, be also provided with cryopump, described refrigerant holding vessel 2 connects condenser 9 by cryopump.
The motion-promotion force of the refrigerant in refrigerant delivery line 7 and refrigerant return pipe road 8 provides by circulation and acyclic two kinds of modes.Adopt circulating condensing circuit design to comprise following two kinds of modes: (1) refrigerant is pressed into condenser 9 by the fluid column static pressure in refrigerant holding vessel 2, then by refrigerant return pipe road 8, is back to refrigerant holding vessel 2 from condenser 9; (2) on condenser pipe, set up cryopump and carry out external force driving, realize refrigerant circulation operation.The outlet end of acyclic mode on refrigerant return pipe road 8 arranges low pressure refrigerant and collects bag or directly refrigerant entered in atmosphere.
In addition, on described drainer 1, be also provided with drainer liquid level sensor 17 and drainer pressure transducer 18, on described refrigerant holding vessel 2, be connected with coolant storage tank pressure transducer 19 and coolant storage tank liquid level sensor 20, on described cryogenic liquid tank, be provided with sump pressure sensor 15, described sump pressure sensor 15, drainer liquid level sensor 17, drainer pressure transducer 18, coolant storage tank pressure transducer 19 is all connected with control system 3 with coolant storage tank liquid level sensor 20, PLC control system is by collecting sump pressure sensor 15, drainer liquid level sensor 17, drainer pressure transducer 18, the output signal of coolant storage tank pressure transducer 19 and coolant storage tank liquid level sensor 20, and on the basis of above-mentioned signal workout system control command program, realize again the automatic operation of liquefaction system.
Liquefaction system specific works principle is as follows again for the utility model modular cryogenic liquid basin BOG gas: the pressure signal value of the sump pressure sensor 15 arranging to cryogenic liquid tank when PLC systematic collection is during higher than setting value, pipage control solenoid valve 11 is opened, the gas medium of cryogenic liquid tank is sent in drainer 1 by medium transport pipeline 5, the gaseous pressure of balance cryogenic liquid tank and drainer 1, simultaneously refrigerant pipage control solenoid valve 14 reaches to set under the condition requiring at coolant storage tank liquid level sensor 20 liquid level signals of refrigerant holding vessel 2 and automatically opens, refrigerant flow in drainer 1 by refrigerant delivery pipe 7 tunnels, enter again condenser 9, thereby the BOG gas medium importing in cryogenic liquid tank is carried out to condensation liquefaction, be converted into liquid.By the continuous condensation of BOG gas medium that cryogenic liquid tank is imported, the gaseous pressure of cryogenic liquid tank and drainer 1 constantly declines, the pressure signal that receives sump pressure sensor 15 output when PLC control system is during lower than setting value, or the liquid level signal that PLC control system receives the liquid level sensor 17 of drainer 1 is while expiring liquid level, pipage control solenoid valve 11 cuts out automatically, refrigerant pipage control solenoid valve 14 also cuts out simultaneously, stops refrigerant and carries, and completes control condensation process.After BOG gas medium in drainer 1 liquefies again, liquid phase medium is constantly accumulated, when the liquid level signal spreading out of when the drainer liquid level sensor 17 of drainer 1 arrives setting value, the pressurization control solenoid valve 13 of drainer 1 is opened, pressurized machine 10 is started working, and constantly increases the gaseous pressure in drainer 1; When the pressure signal that the drainer pressure transducer 18 in drainer 1 spreads out of reaches setting value, pressurization control solenoid valve 13 cuts out; Meanwhile, reflux controlling solenoid valve 12 opens the liquid phase medium of the liquefaction that is condensed in drainer 1 and is pushed back in cryogenic liquid tank by medium back flow pipeline 6.
Be different from prior art, the utility model modular cryogenic liquid basin BOG gas is liquefaction system again, can be applicable to the cryogenic liquid storage systems of all BOG of facing gas treatment problems on market, and system architecture is simple, modular design, applying flexible.
The foregoing is only embodiment of the present utility model; not thereby limit the scope of the claims of the present utility model; every equivalent structure or conversion of equivalent flow process that utilizes the utility model specification and accompanying drawing content to do; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present utility model.
Claims (10)
1. modular cryogenic liquid basin BOG gas liquefaction system again, it is characterized in that, comprise: control system, drainer and refrigerant holding vessel, on described drainer, be connected with medium transport pipeline and medium back flow pipeline, between described drainer and refrigerant holding vessel, by refrigerant delivery line and refrigerant return pipe road, be connected, in described drainer, be provided with condenser, described condenser is connected with refrigerant delivery line, on described drainer, be connected with pressurized machine, described pressurized machine is connected with medium back flow pipeline.
2. modular cryogenic liquid basin BOG gas according to claim 1 liquefaction system again, it is characterized in that, described medium transport pipeline is connected with cryogenic liquid tank respectively with medium back flow pipeline, on described medium transport pipeline, be provided with pipage control solenoid valve, on described medium back flow pipeline, being provided with refluxes controls solenoid valve, and described pipage control solenoid valve is all connected with control system with the control solenoid valve that refluxes.
3. modular cryogenic liquid basin BOG gas according to claim 1 liquefaction system again, it is characterized in that, described pressurized machine is connected on pressure piping, the described pressurization control solenoid valve that is connected with on pressure piping, described pressurization control solenoid valve is connected with control system, and described pressurized machine comprises from boost mode and pressure boost mode.
4. modular cryogenic liquid basin BOG gas according to claim 1 liquefaction system again, it is characterized in that, on described refrigerant delivery line, be provided with refrigerant pipage control solenoid valve, on described refrigerant return pipe road, be connected with other cooling requirement modules and coolant discharging control valve, described refrigerant pipage control solenoid valve is connected with PLC system with coolant discharging control valve.
5. modular cryogenic liquid basin BOG gas according to claim 4 liquefaction system again, is characterized in that, described refrigerant return pipe road collects bag with low pressure refrigerant or atmosphere is connected.
6. modular cryogenic liquid basin BOG gas according to claim 2 liquefaction system again, it is characterized in that, on described drainer, be provided with drainer liquid level sensor and drainer pressure transducer, on described refrigerant holding vessel, be connected with coolant storage tank pressure transducer and coolant storage tank liquid level sensor, on described cryogenic liquid tank, be provided with sump pressure sensor, described drainer liquid level sensor, drainer pressure transducer, sump pressure sensor, coolant storage tank pressure transducer and coolant storage tank liquid level sensor are all connected with control system.
7. modular cryogenic liquid basin BOG gas according to claim 6 liquefaction system again, is characterized in that, described control system is PLC control system.
8. modular cryogenic liquid basin BOG gas according to claim 1 liquefaction system again, is characterized in that, on described refrigerant delivery line, be also provided with cryopump, described refrigerant holding vessel connects condenser by cryopump.
9. modular cryogenic liquid basin BOG gas according to claim 1 liquefaction system again, is characterized in that, described condenser is bellow type, coil pipe type or plate type condenser.
10. modular cryogenic liquid basin BOG gas according to claim 1 liquefaction system again, it is characterized in that, described drainer comprises inner container, shell and the interlayer adiabatic space being formed by inner container and shell, described refrigerant holding vessel comprises inner container, shell and the interlayer adiabatic space being formed by inner container and shell, and the medium storing in described refrigerant holding vessel is liquid nitrogen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420159764.0U CN203927381U (en) | 2014-04-03 | 2014-04-03 | Modular cryogenic liquid basin BOG gas is liquefaction system again |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420159764.0U CN203927381U (en) | 2014-04-03 | 2014-04-03 | Modular cryogenic liquid basin BOG gas is liquefaction system again |
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| CN203927381U true CN203927381U (en) | 2014-11-05 |
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| CN201420159764.0U Withdrawn - After Issue CN203927381U (en) | 2014-04-03 | 2014-04-03 | Modular cryogenic liquid basin BOG gas is liquefaction system again |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104061431A (en) * | 2014-04-03 | 2014-09-24 | 查特深冷工程系统(常州)有限公司 | Modularized BOG (Boil Off Gas) re-liquefaction system of low-temperature liquid storage tank |
| CN110185919A (en) * | 2018-02-22 | 2019-08-30 | 张家港中集圣达因低温装备有限公司 | Low-temperature storage tank |
| CN114688447A (en) * | 2020-12-29 | 2022-07-01 | 连云港石化有限公司 | Receiving system of long-distance large-diameter pipeline and start-up method thereof |
| CN114688447B (en) * | 2020-12-29 | 2024-06-04 | 连云港石化有限公司 | Receiving system of long-distance large-diameter pipeline and starting method thereof |
-
2014
- 2014-04-03 CN CN201420159764.0U patent/CN203927381U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104061431A (en) * | 2014-04-03 | 2014-09-24 | 查特深冷工程系统(常州)有限公司 | Modularized BOG (Boil Off Gas) re-liquefaction system of low-temperature liquid storage tank |
| CN104061431B (en) * | 2014-04-03 | 2016-09-14 | 查特深冷工程系统(常州)有限公司 | The modular cryogenic liquid basin re-liquefied system of BOG gas |
| CN110185919A (en) * | 2018-02-22 | 2019-08-30 | 张家港中集圣达因低温装备有限公司 | Low-temperature storage tank |
| CN114688447A (en) * | 2020-12-29 | 2022-07-01 | 连云港石化有限公司 | Receiving system of long-distance large-diameter pipeline and start-up method thereof |
| CN114688447B (en) * | 2020-12-29 | 2024-06-04 | 连云港石化有限公司 | Receiving system of long-distance large-diameter pipeline and starting method thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141105 Effective date of abandoning: 20160914 |
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| C25 | Abandonment of patent right or utility model to avoid double patenting |