CN106499938A - Safety anti-explosive formula liquefied natural gas carrier vehicle - Google Patents
Safety anti-explosive formula liquefied natural gas carrier vehicle Download PDFInfo
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- CN106499938A CN106499938A CN201510557103.2A CN201510557103A CN106499938A CN 106499938 A CN106499938 A CN 106499938A CN 201510557103 A CN201510557103 A CN 201510557103A CN 106499938 A CN106499938 A CN 106499938A
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- tank body
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- pipeline
- outer tank
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Abstract
The invention discloses a kind of safety anti-explosive formula liquefied natural gas carrier vehicle, including locomotive and the LNG storage tank being arranged on locomotive, the LNG storage tank includes three layers of tank body, interior tank body, first outer tank body and second outer tank body are followed successively by from inside to outside, interior tank body is used for storing liquefied natural gas, it is closed vacuum heat-insulation interlayer between interior tank body and the first outer tank body, is vacuum-powders insulation interlayer between the first outer tank body and the second outer tank body；Which is provided with two pressure transducers, by pressure condition in two pressure transducer real-time monitoring inner canister bodies, plays a part of dual fail-safe；Vacuum detecting and control device is provided with, so as to ensure the vacuum heat-insulation of interlayer, prevents interior tank body thermal stress increase from producing dangerous；Liquid circulation line is provided with, vortex phenomenon is prevented；It is additionally provided with inert gas import.
Description
Technical field
The invention belongs to technical field transported safely by liquefied natural gas, a kind of safety anti-explosive formula liquefaction is related in particular to natural
Gas transport vehicle.
Background technology
Natural gas is inflammable and explosive fuel, and natural gas will be liquefied as through ultralow temperature (- 162 DEG C) normal pressure in storage transport
Liquefied natural gas LNG (Liquefied Natural Gas), the storage temperature very bottom of LNG and the danger for being susceptible to explode
And there is no the certain potential safety hazard of person in its filling and storage transportation, this is just to its storage facilities and means of transport
Safe and reliable strict demand is just proposed.
Content of the invention
It is an object of the invention to overcoming the deficiencies in the prior art, there is provided a kind of safety anti-explosive formula liquefied natural gas carrier vehicle.
The present invention employs the following technical solutions to realize：
A kind of safety anti-explosive formula liquefied natural gas carrier vehicle, including locomotive and the LNG storage tank being arranged on locomotive, described
LNG storage tank includes three layers of tank body, is followed successively by interior tank body, the first outer tank body and the second outer tank body from inside to outside, interior tank body and
It is closed vacuum heat-insulation interlayer between first outer tank body, is vacuum-powders insulation between the first outer tank body and the second outer tank body
Interlayer；
Interior tank body is provided with liquid entrance by pipeline, and arranges the first valve on pipeline；
The top of interior tank interior is provided with exhaust apparatus, and exhaust apparatus is connected by pipeline with air vent, and in aerofluxuss
The second valve and first pressure sensor and second pressure sensor is provided with air vent on the pipeline that device is connected；
The bottom of interior tank interior is provided with noble gases uniform distributor, and noble gases uniform distributor is entered with noble gases
Mouth is connected by pipeline, and on the pipeline that noble gases uniform distributor is connected with inert gas import is provided with the 3rd
Valve；
Vacuum heat-insulation interlayer between interior tank body and the first outer tank body is provided with vacuumizing and exhausting mouth by pipeline, and in pipeline
On be disposed with vacuum degree measurement sensor, the 4th valve and vacuum pump；
Liquid circulation lines, liquid circulation lines are provided with vacuum heat-insulation interlayer between interior tank body and the first outer tank body
Circulation import be arranged on the bottom of interior tank body, the loop exit of liquid circulation lines is arranged on the top of interior tank body, liquid
The 5th valve and circulating pump are set gradually along circulation import to loop exit on circulating line；
The first pressure sensor, second pressure sensor and vacuum degree measurement sensor respectively be arranged on locomotive driving
First pressure on the console of room shows that table, second pressure show that table and vacuum show table electrical connection.
The advantages of the present invention are：
By pressure condition in first pressure sensor and second pressure sensor real-time monitoring inner canister body, when pressure is excessive
Control the second valve and open internal tank interior and deflated to prevent pressure increase and occur quick-fried to reduce the pressure in inner canister body
Fried；Being monitored using first pressure sensor and second pressure sensor simultaneously can prevent because of one of pressure sensing
Device failure and cause potential safety hazard, so as to increased the effectiveness of pressure monitoring, play a part of dual fail-safe.
(the situation that is especially canned first or there is more air in interior tank body when the canned work of natural gas is carried out
Under), noble gases are filled with into inner storage tank by inert gas import and noble gases uniform distributor, and pass through aerofluxuss
Air in inner storage tank is discharged by device from air vent, so that the content in the gas in inner canister body reaches safe requirement,
Prevent air and natural gas mixing from causing danger.
By the vacuum in vacuum degree measurement sensor real-time monitoring vacuum heat-insulation the interlayer, (vacuum when vacuum declines
Insulating sandwich can not possibly be completely closed, and its vacuum slowly can decline under normal circumstances), vacuum pump simultaneously opened by the 4th valve
Work carries out evacuation, so as to ensure the vacuum heat-insulation of vacuum heat-insulation interlayer, prevents interior tank body thermal stress increase from producing
Dangerous.
The liquefied natural gas of the multiple filling in inner canister body can be made to be sufficiently mixed uniformly by open the circulation pump and the 5th valve,
Prevent vortex phenomenon (during LNG Storage, Transport, it may occur that a kind of non-stability phenomenon for being known as being vortexed.Whirlpool
Rotation be due to filling new LNG liquid in the low temperature storing tank for have been loaded with LNG, or due to LNG in nitrogen preferential evaporation
And it is layered the liquid in storage tank.Each layer liquid after layering is formed each solely under the heating that storage tank perisporium leaks heat
Vertical free convection circulation.The circulation makes the density of each layer liquid constantly change, when the density of adjacent two layers liquid near
During patibhaga-nimitta etc., two liquid layers will occur strong mixing, and so as to cause overheated liquefied natural gas in storage tank, evaporation is drawn in a large number
The accident of sending out).
The first pressure sensor of LNG storage tank, second pressure sensor and vacuum degree measurement sensor respectively be arranged on machine
First pressure on car driver's cabin console shows that table, second pressure show that table and vacuum show table electrical connection, so may be used
So that the safe condition of driver's convenient real-time monitoring LNG storage tank in driver's cabin in driving procedure.
Description of the drawings
Fig. 1 is the structural representation of the present invention.
Fig. 2 is the structural representation of the LNG storage tank in the present invention.
Fig. 3 is the structural representation of the locomotive driving cabin console in the present invention.
Wherein：1 is locomotive, and 2 is LNG storage tank, and G-1 is interior tank body, and G-2 is the first outer tank body, and G-3 is outside second
Tank body, a is exhaust apparatus, and b is noble gases uniform distributor, and K1 is liquid entrance, and K2 is air vent, K3
For inert gas import, K4 is vacuumizing and exhausting mouth, and L1 is liquid circulation lines, and P1 is first pressure sensor, P2
For second pressure sensor, R is vacuum degree measurement sensor, and D1 is vacuum pump, and D2 is circulating pump, and V1 is the first valve,
V2 is the second valve, and V3 is the 3rd valve, and V4 is the 4th valve, and V5 is the 5th valve, and P1-1 is that first pressure shows table, P2-1
Show table for second pressure, R-1 is that vacuum shows table.
Specific embodiment
Technical scheme is further illustrated with reference to specific embodiment.
As shown in Figure 1, a kind of safety anti-explosive formula liquefied natural gas carrier vehicle involved in the present invention includes locomotive 1 and sets
Put the LNG storage tank 2 on locomotive；As shown in Figure 2, the LNG storage tank 2 includes three layers of tank body, from inside to outside
Interior tank body G-1, the first outer tank body G-2 and the second outer tank body G-3 is followed successively by, interior tank body is used for storing liquefied natural gas, interior
It is closed vacuum heat-insulation interlayer, the first outer tank body G-2 and the second outer tank body between tank body G-1 and the first outer tank body G-2
For vacuum-powders insulation interlayer between G-3, realized by two-layer insulating sandwich the liquefied natural gas of interior tank interior with outer
Boundary heat-insulated, with avoid liquefied natural gas because temperature raise vaporization cause interior tank body pressure increase and occurs blast danger,
Traditional monolayer vacuum heat-insulation interlayer is compared, the present invention has more safety.
Interior tank body G-1 is provided with liquid entrance K1 by pipeline, and arranges the first valve V1 on pipeline, by liquid
Import and export K1 and complete the canned and discharging operation to liquefied natural gas, the first valve V1 controls the unlatching of liquid entrance K1
And closed mode.
Top inside interior tank body G-1 is provided with exhaust apparatus a, and exhaust apparatus a is connected by pipeline with air vent K2,
And be provided with the pipeline that exhaust apparatus a is connected with air vent K2 the second valve V2 and first pressure sensor P1 and
Second pressure sensor P2；In first pressure sensor P1 and second pressure sensor P2 real-time monitorings, tank body G-1 is intrinsic pressure
Power situation, controls to be deflated to reduce in inner canister body inside the internal tank body G-1 of the second valve V2 unlatchings when pressure is excessive
Pressure prevent pressure increase and explode；Entered using first pressure sensor P1 and second pressure sensor P2 simultaneously
Row monitoring can prevent from causing potential safety hazard because of one of pressure transducer failure, so as to increased having for pressure monitoring
Effect property, plays a part of dual fail-safe.
Bottom inside interior tank body G-1 is provided with noble gases uniform distributor b, noble gases uniform distributor b with lazy
Property gas feed K3 is connected by pipeline, and be connected with inert gas import K3 in noble gases uniform distributor b
The 3rd valve V3 is provided with pipeline；It is (especially canned first or in interior tank body when the canned work of natural gas is carried out
In the case of there is more air), in order to ensure safety, by inert gas import K3 and noble gases uniform distributor
B is filled with noble gases into inner storage tank, and discharges the air in inner storage tank from air vent K2 by exhaust apparatus a, with
Make the content in the gas in inner canister body reach safe requirement, prevent air and natural gas mixing from causing danger.
Vacuum heat-insulation interlayer between interior tank body G-1 and the first outer tank body G-2 is provided with vacuumizing and exhausting mouth by pipeline
K4, and vacuum degree measurement sensor R, the 4th valve V4 and vacuum pump D1 is disposed with pipeline；By vacuum
Vacuum in detection sensor R real-time monitoring interlayer, when vacuum declines (interior tank body G-1 and outer tank body G-2 it
Between interlayer can not possibly be completely closed, its vacuum slowly can decline under normal circumstances), the 4th valve V4 opens simultaneously vacuum pump
D1 work carries out evacuation, so as to ensure the vacuum heat-insulation of interlayer, prevents interior tank body thermal stress increase from producing dangerous.
Liquid circulation lines L1, liquid are provided with vacuum heat-insulation interlayer between interior tank body G-1 and the first outer tank body G-2
The circulation import of body circulation pipeline L1 is arranged on the bottom of interior tank body G-1, and the loop exit of liquid circulation lines L1 is arranged
On the top of interior tank body G-1, on liquid circulation lines L1 along circulation import to loop exit set gradually the 5th valve V5 and
Circulating pump D2；The liquefied natural gas that multiple filling in inner canister body can be made by open the circulation pump D2 and the 5th valve V5
It is sufficiently mixed uniform, prevents vortex phenomenon (during LNG Storage, Transport, it may occur that a kind of be known as being vortexed
Non- stability phenomenon.Vortex is due to filling new LNG liquid in the low temperature storing tank for have been loaded with LNG, or due to LNG
In nitrogen preferential evaporation and be layered the liquid in storage tank.Each layer liquid after layering leaks the heating of heat in storage tank perisporium
Under, form each independent free convection circulation.The circulation makes the density of each layer liquid constantly change, when adjacent two
During the density approximately equal of layer liquid, two liquid layers will occur strong mixing, so as to cause overheated liquefaction day in storage tank
So gas evaporates accidents caused in a large number).
As shown in figure 3, first pressure sensor P1, the second pressure sensor P2 of LNG storage tank and vacuum degree measurement are passed
Sensor R respectively with the first pressure display table P1-1, second pressure display table P2-1 being arranged on locomotive driving cabin console
Show that the pressure signal of detection is passed to first pressure display table by table R-1 electrical connections, first pressure sensor P1 with vacuum
P1-1 shows that the pressure signal of detection is passed to second pressure display table P2-1 and shows pressure by pressure, second pressure sensor P2
The vacuum signal of detection is passed to vacuum display table R-1 and shows vacuum by power, vacuum display table R-1, so may be used
So that the safe condition of driver's convenient real-time monitoring LNG storage tank in driver's cabin in driving procedure.
Exemplary description has been done to the present invention above, it should explanation, in the case of the core without departing from the present invention,
Any simple deformation, modification or other skilled in the art can not spend the equivalent of creative work to fall
Enter protection scope of the present invention.
Claims (1)
1. a kind of safety anti-explosive formula liquefied natural gas carrier vehicle, including locomotive and the LNG storage tank being arranged on locomotive, its
It is characterised by：The LNG storage tank includes three layers of tank body, is followed successively by outside interior tank body, the first outer tank body and second from inside to outside
Tank body, is closed vacuum heat-insulation interlayer between interior tank body and the first outer tank body, between the first outer tank body and the second outer tank body
For vacuum-powders insulation interlayer；
Interior tank body is provided with liquid entrance by pipeline, and arranges the first valve on pipeline；
The top of interior tank interior is provided with exhaust apparatus, and exhaust apparatus is connected by pipeline with air vent, and in aerofluxuss
The second valve and first pressure sensor and second pressure sensor is provided with air vent on the pipeline that device is connected；
The bottom of interior tank interior is provided with noble gases uniform distributor, and noble gases uniform distributor is entered with noble gases
Mouth is connected by pipeline, and on the pipeline that noble gases uniform distributor is connected with inert gas import is provided with the 3rd
Valve；
Vacuum heat-insulation interlayer between interior tank body and the first outer tank body is provided with vacuumizing and exhausting mouth by pipeline, and in pipeline
On be disposed with vacuum degree measurement sensor, the 4th valve and vacuum pump；
Liquid circulation lines, liquid circulation lines are provided with vacuum heat-insulation interlayer between interior tank body and the first outer tank body
Circulation import be arranged on the bottom of interior tank body, the loop exit of liquid circulation lines is arranged on the top of interior tank body, liquid
The 5th valve and circulating pump are set gradually along circulation import to loop exit on circulating line；
The first pressure sensor, second pressure sensor and vacuum degree measurement sensor respectively be arranged on locomotive driving
First pressure on the console of room shows that table, second pressure show that table and vacuum show table electrical connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510557103.2A CN106499938A (en) | 2015-09-06 | 2015-09-06 | Safety anti-explosive formula liquefied natural gas carrier vehicle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510557103.2A CN106499938A (en) | 2015-09-06 | 2015-09-06 | Safety anti-explosive formula liquefied natural gas carrier vehicle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106499938A true CN106499938A (en) | 2017-03-15 |
Family
ID=58287601
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510557103.2A Pending CN106499938A (en) | 2015-09-06 | 2015-09-06 | Safety anti-explosive formula liquefied natural gas carrier vehicle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106499938A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108050374A (en) * | 2017-12-25 | 2018-05-18 | 上海新奥新能源技术有限公司 | A kind of storage tank and LNG air supply systems |
| CN111692527A (en) * | 2020-06-25 | 2020-09-22 | 甘雨青 | Environment-friendly inflammable and explosive gas sealing and transporting device |
| CN114910213A (en) * | 2022-04-19 | 2022-08-16 | 广州美东能源有限公司 | Efficient LNG storage tank vacuum degree detection and maintenance method |
-
2015
- 2015-09-06 CN CN201510557103.2A patent/CN106499938A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108050374A (en) * | 2017-12-25 | 2018-05-18 | 上海新奥新能源技术有限公司 | A kind of storage tank and LNG air supply systems |
| CN111692527A (en) * | 2020-06-25 | 2020-09-22 | 甘雨青 | Environment-friendly inflammable and explosive gas sealing and transporting device |
| CN114910213A (en) * | 2022-04-19 | 2022-08-16 | 广州美东能源有限公司 | Efficient LNG storage tank vacuum degree detection and maintenance method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170315 |