CN109084172A - Liquefied gas tanker residual air remnant liquid recovering device - Google Patents
Liquefied gas tanker residual air remnant liquid recovering device Download PDFInfo
- Publication number
- CN109084172A CN109084172A CN201810993682.9A CN201810993682A CN109084172A CN 109084172 A CN109084172 A CN 109084172A CN 201810993682 A CN201810993682 A CN 201810993682A CN 109084172 A CN109084172 A CN 109084172A
- Authority
- CN
- China
- Prior art keywords
- gas
- residual
- valve
- liquid
- pipeline
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 70
- 230000006835 compression Effects 0.000 claims abstract description 45
- 238000007906 compression Methods 0.000 claims abstract description 45
- 238000003860 storage Methods 0.000 claims abstract description 41
- 239000000284 extract Substances 0.000 claims abstract description 7
- 238000011084 recovery Methods 0.000 claims abstract description 7
- 238000002347 injection Methods 0.000 claims abstract 6
- 239000007924 injection Substances 0.000 claims abstract 6
- 239000010410 layer Substances 0.000 claims description 48
- 239000003921 oil Substances 0.000 claims description 26
- 238000007667 floating Methods 0.000 claims description 16
- 239000011229 interlayer Substances 0.000 claims description 13
- 239000000945 filler Substances 0.000 claims description 12
- 239000010687 lubricating oil Substances 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims 2
- 238000000034 method Methods 0.000 abstract description 6
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 61
- 230000008676 import Effects 0.000 description 13
- 238000004064 recycling Methods 0.000 description 12
- 239000012530 fluid Substances 0.000 description 10
- 238000013461 design Methods 0.000 description 9
- 238000001802 infusion Methods 0.000 description 9
- 238000009833 condensation Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 7
- 238000010079 rubber tapping Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000007689 inspection Methods 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000033228 biological regulation Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- 241000521257 Hydrops Species 0.000 description 1
- 206010030113 Oedema Diseases 0.000 description 1
- 241000270295 Serpentes Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000003760 hair shine Effects 0.000 description 1
- 230000003434 inspiratory effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 230000005226 mechanical processes and functions Effects 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 235000015927 pasta Nutrition 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical group [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
- F17C5/02—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases
- F17C5/04—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases requiring the use of refrigeration, e.g. filling with helium or hydrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
- F17C13/025—Special adaptations of indicating, measuring, or monitoring equipment having the pressure as the parameter
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2260/00—Purposes of gas storage and gas handling
- F17C2260/04—Reducing risks and environmental impact
- F17C2260/046—Enhancing energy recovery
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
本发明涉及一种液化气罐车余气残液回收装置，包括移动式存储容器、余气压缩装置和液体注入装置，首先，余气压缩装置抽取移动式存储容器内的气体至罐车罐体，在罐车罐体与移动式存储容器之间形成压力差；然后，利用该压力差使罐车罐体内的残液压进移动式存储容器，直至把罐车罐体内的残液输送完毕为止；最后，通过液体注入装置向罐车罐体内注入相应液体，同时启动余气压缩装置抽取罐车罐体的余气，并将余气液化后压入移动式存储容器。有益效果是：本装置回收方法简单，回收彻底，大大降低了有害气体的排放；不需要设置专门的残液罐来进行回收，设施投资省，消防要求低，占地面积小。
The invention relates to a device for recovering residual gas and residual liquid of a liquefied gas tanker, which includes a mobile storage container, a residual gas compression device and a liquid injection device. First, the residual gas compression device extracts the gas in the mobile storage container to the tank body of the tanker. A pressure difference is formed between the tank body of the tanker and the mobile storage container; then, the pressure difference is used to make the residual hydraulic pressure in the tanker tank enter the mobile storage container until the residual liquid in the tanker tank is conveyed; finally, through the liquid injection device Inject the corresponding liquid into the tank body of the tanker, and at the same time start the residual gas compression device to extract the residual gas from the tanker tank, liquefy the residual gas and press it into the mobile storage container. The beneficial effects are: the recovery method of the device is simple, the recovery is thorough, and the emission of harmful gas is greatly reduced; no special residual liquid tank is required for recovery, the facility investment is low, the fire protection requirements are low, and the occupied area is small.
Description
Technical field
The present invention relates to a kind of Liquefied gas tanker residual air remnant liquid recovering devices.
Background technique
Tank car Inspection Unit is according to relevant regulations, it is necessary to have the ability of residual air raffinate recycling is carried out to medium in tank car,
Tank car Inspection Unit is recycled generally by way of residual liquid tank is arranged at present, and facility investment is big, and fire-fighting requirements are high, is used
Ground area is more, and often there is also recycling in actual use and be not thorough, even directly to environmental emission residual air raffinate
Not only there is serious security risk in situation, but also be not able to satisfy higher and higher environmental requirement, cause consequence is seriously to can't bear to set
Think.
Currently, there are two types of the conventional process of tank car residual air raffinate recycling.First is that by nitrogen pressurization tank body, it will be in tank car
Residual air raffinate is pressed into residual liquid tank.Its main feature is that simple process, safe operation is reliable, but there is also nitrogen is costly, when operation
It needs to open and close gas phase valve repeatedly and residual air is not easy the shortcomings that draining.Second is that extracting gas out of tank body using compressor, pressurize
After be discharged into residual liquid tank.Since common compressor negative suction value is higher, it is difficult to take out residual air in tank to the greatest extent, and tank body is repeatedly by negative
Pressure, is also easy to generate unnecessary fatigue damage.Both the above technique requires installation residual liquid tank, and facility investment is larger, and exists
Residual air the drawbacks of cannot recycling completely.
Summary of the invention
The technical problems to be solved by the present invention are: a kind of Liquefied gas tanker residual air remnant liquid recovering device is provided, safety, height
The residual air raffinate of the recycling Liquefied gas tanker of effect.
The technical solution adopted by the present invention to solve the technical problems is: a kind of Liquefied gas tanker residual air raffinate recycling dress
It sets, including mobile storage container, residual air compression set, fluid infusion apparatus, mobile storage container is compressed with residual air respectively
Device is connected with tank car tank body, and residual air compression set is used for the residual air boil down to liquefied gas in tank car tank body, residual air compression dress
It sets and is connect respectively with tank car tank body with fluid infusion apparatus, firstly, residual air compression set extracts the gas in mobile storage container
Body makes the pressure reduction in mobile storage container, is formed between tank car tank body and mobile storage container to tank car tank body
Pressure difference；Then, using existing pressure difference between tank car tank body and mobile storage container, make the raffinate pressure in tank car tank body
Into mobile storage container, until the raffinate conveying in tank car tank body is finished；Finally, passing through fluid infusion apparatus to tank
Respective liquid is injected in vehicle tank, while starting the residual air that residual air compression set extracts tank car tank body, and residual air boil down to is liquefied
Mobile storage container is pressed into after gas.
It further limits, mobile storage container is connected by the blowdown valve of the first pipeline and tank car tank body, in the first pipe
Road has the first valve for controlling the pipeline on-off, and residual air compression set is connected by the gas valve of the second pipeline and tank car tank body
It connects, residual air compression set is connect by third pipeline with mobile storage container, has the control pipeline logical on third pipeline
Disconnected third valve, residual air compression set realize the conversion of the airintake direction of residual air compression set by positive-negative connected valving,
Fluid infusion apparatus includes the 4th pipeline connecting with the blowdown valve of tank car tank body, has the control pipeline logical on the 4th pipeline
The 4th disconnected valve, the 4th pipeline with fluid supply for connecting.
It further limits, residual air compression set includes compressor and condenser, and the both ends of compressor pass through positive-negative connected valve
Door gear is connect with one end of the second pipeline and condenser respectively, the other end and third piping connection of condenser.
Specifically, positive-negative connected valving is two position four-way valves.
Specifically, mobile storage container is tank car, tank container or gas cylinder.
It further limits, the both ends of compressor are respectively inlet end and an outlet end, the input end setting gas-liquid point of compressor
From device, gs-oil separator is arranged in the outlet end of compressor.
Specifically, gas-liquid separator includes cylinder, float, stop valve and tapping valve, and the lower end side of cylinder has import,
The upper end of cylinder has outlet, has the stop valve of control outlet on-off in the upper end of the inner cavity of cylinder, float is column, is located at
In cylinder lumen, the liquid into cylinder makes float float, and float closes stop valve after touching stop valve, is arranged in import and filters
Core, cylinder lower end have tapping valve, and the liquid into cylinder is discharged by tapping valve.
Specifically, gs-oil separator includes floating ball, the filler oil strain layer in shell of tank and shell of tank, shell of tank
Inner cavity is divided into upper layer and lower layer, and floating ball is located at the lower layer of inner cavity, and filler oil strain layer is located at the upper layer of inner cavity, and the lower layer of inner cavity has one
A interlayer, the upper layer side of shell of tank have outlet, and the same side of the lower layer of shell of tank has import, import and interlayer phase
Logical, liquefied gas enters the interlayer of the lower layer of shell of tank by import, and the side of the separate import from interlayer enters inner cavity
Upper layer, the liquefied gas into the upper layer of inner cavity are discharged after the filtering of filler oil strain layer by outlet, and filler oil strain layer filters out
Lubricating oil be dropped into the lower layer of inner cavity locating for floating ball, the lower layer of inner cavity has ball-cock assembly, and floating ball floating opens ball-cock assembly
The lubricating oil filtered down is discharged, floating ball decline presses ball-cock assembly closing.
It further limits, balanced valve is set in residual air compression set, the both ends of balanced valve and the both ends of compressor connect.
It further limits, whole device is in skid-mounted type.
The beneficial effects of the present invention are:
(1) present apparatus recovery method is simple, and thoroughly, recovery efficiency is high for the recycling of residual air raffinate, greatly reduces pernicious gas
Discharge；
(2) device uses condensation principle, replaces residual liquid tank to realize the residual air raffinate recycling to tank car tank body with gas cylinder,
It does not need that special residual liquid tank is arranged to be recycled, facility investment saves, and fire-fighting requirements are low, and occupied area is small.
Detailed description of the invention
Present invention will be further explained below with reference to the attached drawings and examples；
Fig. 1 is overall structure schematic diagram of the invention；
Fig. 2 is the structural schematic diagram of gas-liquid separator of the invention；
Fig. 3 is the structural schematic diagram of gs-oil separator of the invention；；
In figure, 1. mobile storage containers, 2. residual air compression sets, 2-1. compressor, 2-2. condenser, 3. tank car tanks
Body, the first pipeline of 4-1., the second pipeline of 4-2., 4-3. third pipeline, the 4th pipeline of 4-4., the first valve of 5-1., 5-3. third
Valve, the 4th valve of 5-4., 6. gas valves, 7. positive-negative connected valvings, 8. weighing devices, 9. gas-liquid separators, 9-1. cylinder,
9-2. float, 9-3. stop valve, 9-4. tapping valve, 9-5. filter core, 10. gs-oil separators, 10-1. shell of tank, 10-2. are floating
Ball, 10-3. filler oil strain layer, 10-4. interlayer, 10-5. ball-cock assembly, 11. balanced valves, 12. blowdown valves, 13. pressure gauges, 14. peaces
Full valve, 15. check valves.
Specific embodiment
A kind of Liquefied gas tanker residual air remnant liquid recovering device is suitable for the Liquefied gas tanker of a variety of media, below with the stone that liquefies
This covering device is introduced for oil gas tank car, which includes mobile storage container 1, residual air
Compression set 2 and fluid infusion apparatus, mobile storage container 1 is connect with residual air compression set 2 and tank car tank body 3 respectively, remaining
Air pressure compression apparatus 2 is used for the residual air boil down to liquefied gas in tank car tank body 3, residual air compression set 2 and fluid infusion apparatus point
It does not connect with tank car tank body 3, firstly, residual air compression set 2 extracts the gas in mobile storage container 1 to tank car tank body 3, makes
Pressure reduction in mobile storage container 1 forms pressure difference between tank car tank body 3 and mobile storage container 1；Then,
Using existing pressure difference between tank car tank body 3 and mobile storage container 1, the raffinate in tank car tank body 3 is made to be pressed into movable type
Storage container 1, until the raffinate conveying in tank car tank body 3 is finished；Finally, passing through fluid infusion apparatus to tank car tank body
Respective liquid is injected in 3, while starting the residual air that residual air compression set 2 extracts tank car tank body 3, by the liquid of residual air boil down to liquid
Mobile storage container 1 is pressed into after changing gas.
It is water that fluid infusion apparatus, which injects respective liquid into tank car tank body 3,.
As shown in Figure 1, mobile storage container 1 is connect by the first pipeline 4-1 with the blowdown valve 12 of tank car tank body 3,
There is the first valve 5-1 for controlling the pipeline on-off, residual air compression set 2 passes through the second pipeline 4-2 and tank on first pipeline 4-1
The gas valve 6 of vehicle tank 3 connects, and residual air compression set 2 is connect by third pipeline 4-3 with mobile storage container 1, in third
There is the third valve 5-3 for controlling the pipeline on-off, residual air compression set 2 is real by positive-negative connected valving 7 on pipeline 4-3
The conversion of the airintake direction of existing residual air compression set 2, fluid infusion apparatus include the connect with the blowdown valve 12 of tank car tank body 3
There is four pipeline 4-4 the 4th valve 5-4 for controlling the pipeline on-off, the 4th pipeline 4-4 to be used for and work on the 4th pipeline 4-4
It is connected for the pond at water source.
Positive-negative connected valving 7 is two position four-way valves.
Mobile storage container 1 can be tank car, tank container or gas cylinder, and in Fig. 1, mobile storage container 1 is
Weighing device 8 is arranged in the bottom of gas cylinder in gas cylinder.
The both ends of compressor 2-1 are respectively inlet end and an outlet end, and gas-liquid separator 9 is arranged in the input end of compressor 2-1,
Gs-oil separator 10 is arranged in the outlet end of compressor 2-1.
Balanced valve 11 is set in residual air compression set 2, and the both ends of balanced valve 11 are connect with the both ends of compressor 2-1.
Whole device is in skid-mounted type.
Residual air compression condensation is liquefied gas by way of condensation by residual air compression set 2, and residual air compression set 2 includes pressure
The both ends of contracting machine 2-1 and condenser 2-2, compressor 2-1 by positive-negative connected valving 7 respectively with the second pipeline 4-2 and condensation
One end of device 2-2 connects, and the other end of condenser 2-2 is connect with third pipeline 4-3.
Residual air compression set 2 is the core of this recyclable device, and compressor 2-1 is by the low pressure residual air in tank car tank body 3
It is compressed into high pressure gas and is discharged into condenser 2-2, be filled with gas cylinder after liquid is converted into condenser 2-2.General tank car tank body 3
Interior low pressure residual air pressure is 0.2-0.3MPa (absolute pressure), and the pressure of compressor discharge gas has with liquefied gas type
It closes, by taking the liquefied gas of Yangtze petrochemical industry supply as an example, it is 1.5MPa (absolute pressure) that 40 DEG C of whens, which are saturation vapour pressure, is compressed at this time
Compression ratio needed for machine is 5~7.5.The liquefied gas recycle compressor that usual lpg filling station is selected, is mainly used for liquefied gas
Entrucking, unload, tank switching, occasions, the compression ratio such as canned are only 1.4~1.5, be unable to satisfy the requirement of gas recycling, therefore
The compressor of higher compression ratios has been selected in the present apparatus.The flow that the inspiratory flow of compressor is intake when can replace according to tank car
Selection, it is similar with flow of inlet water.
Since solubility of the liquefied gas to water is smaller, to prevent liquid from entering accidentally, " liquid hammer " occurs and damages compressor, this
Recyclable device has prepared efficient gas-liquid separator 9, prevents liquid and enters cylinder, it is ensured that the safe operation of compressor.
As shown in Fig. 2, gas-liquid separator 9 includes cylinder 9-1, float 9-2, stop valve 9-3 and tapping valve 9-4, cylinder 9-1
Lower end side there is import, the upper end of cylinder 9-1 has outlet, has control outlet logical in the upper end of the inner cavity of cylinder 9-1
Disconnected stop valve 9-3, float 9-2 are column, are located in the inner cavity cylinder 9-1, if liquid enters gas-liquid separator 9, into cylinder
The liquid of 9-1 can make float 9-2 float, and float 9-2 closes stop valve 9-3 after touching stop valve 9-3, can enter liquid not
Compressor 2-1 is arranged in import and filters to avoid the fouls such as iron rust, welding slag in tank car tank body 3 from scurrying into compressor 2-1 with air-flow
Core 9-5, the lower end cylinder 9-1 have tapping valve 9-4, and the liquid into cylinder 9-1 is discharged by tapping valve 9-4.
The import of gas-liquid separator 9 is communicated with two position four-way valves, when gas enters filter core 9-5 by two position four-way valves, gas
Foul in body is trapped in outside the strainer of filter core 9-5, and clean gas then flows into gas-liquid separator by the screen drum inner hole of filter core 9-5
Cylinder 9-1 inner cavity, to ensure that the cleaning of the gas into compressor 2-1, extend compressor 2-1 uses the longevity
Life.
Liquefied gas can dissolve lubricating oil to some extent, easily bring lubricating oil into condenser 2-2, cause the collection of condensation segment
Oil influences the heat transfer effect of condenser 2-2, and lubricating oil flows into gas cylinder, increases the consumption of lubricating oil, therefore this recycling fills
It sets and is provided with gs-oil separator in the outlet end of compressor 2-1, primary structure is as shown in Figure 3:
Gs-oil separator 10 includes floating ball 10-2, the filler oil strain layer 10- in shell of tank 10-1 and shell of tank 10-1
3, the inner cavity of shell of tank 10-1 is divided into upper layer and lower layer, and floating ball 10-2 is located at the lower layer of inner cavity, and filler oil strain layer 10-3 is located at interior
The upper layer of chamber, the lower layer of inner cavity have an interlayer 10-4, and the upper layer side of shell of tank 10-1 has outlet, shell of tank
The same side of the lower layer of 10-1 has import, and import is communicated with interlayer 10-4, and high-pressure liquefaction gas enters shell of tank by import
The interlayer 10-4 of the lower layer of 10-1, and the side of the separate import from interlayer 10-4 enters the upper layer of inner cavity, into the upper of inner cavity
The liquefied gas of layer is discharged after filler oil strain layer 10-3 filtering by outlet, the lubrication oil droplet that filler oil strain layer 10-3 is filtered out
The lower layer of inner cavity locating for floating ball 10-2 is fallen into, the lower layer of inner cavity has ball-cock assembly 10-5, when on the liquid level of the lubricating oil of drippage
When being raised to certain altitude, floating ball 10-2, which floats, makes ball-cock assembly 10-5 open the lubricating oil that discharge filters down, the lubricating oil of discharge
It is back to compressor 2-1, if pasta drops to certain position, floating ball 10-2 decline presses ball-cock assembly 10-5 closing.Divide to improve
Oily effect uses molecular sieve structure in the filler oil strain layer of gs-oil separator, can drop the concentration of lubricating oil in liquefied gas
Down to 10ppm or so.
The effect of condenser 2-2 is that high pressure gas is condensed into liquid.In the present apparatus, because required condensation capacity is not
Greatly, so condenser 2-2 has selected forced convection air cooled condenser, its main feature is that installation cooling water is not needed, thus use,
It is all more convenient to move dress.Condenser 2-2 is made of several coiled pipes in parallel, and liquefied gas enters every snake by top distributing manifold
Pipe flows down along pipe after condensing into liquid, is compiled in lower collector pipe.The exothermic coefficient of the air side of forced convection air cooled condenser
It is smaller, therefore casing fin has been used outside pipe.To avoid coiled pipe lower part from being liquid filled, condensation effect is influenced, control is every
The length of root coiled pipe, the length of single coiled pipe are unsuitable too long.
The design of present apparatus interior conduit:
The pipeline of recyclable device includes the first pipeline 4-1, the second pipeline 4-2, third pipeline 4-3 and the 4th pipeline 4-4 etc.,
Design pressure is 2.5MPa, and corrosion-resistant steel wire of the sebific duct using pressure rating not less than 6.4MPa winds high-pressure rubber pipe.Pipeline is straight
The calculating of diameter meets flow velocity in gas phase pipe and is not more than 12m/s, and flow velocity is not more than the requirement of 3m/s in liquid-phase tube.In device pipe it
Between connection using being welded to connect, connection with equipment uses flanged joint, and the horizontal segment of pipe arrangement is equipped with along liquid gas flow
The rate of descent in dynamic direction 5/1000.The inflow of liquid when to prevent compressor start, operation and parking, compressor 2-1 into
In mouthful pipeline U-bend is avoided the occurrence of, when condenser 2-2 is located at the compressor top 2-1, in the export pipeline of compressor 2-1
U-shaped hydrops elbow is provided on the downside of rising end.Check-valves and safety valve are provided on the outlet conduit of compressor 2-1.Selection with
The matched fast-assembling inlet suction port of tank car connector.Equipment, pipeline, valve etc. in recyclable device have been carried out reliably leading and destaticed
Ground connection, ground resistance are not more than 10 Ω, and the bridging resistance between pipeline upper flange is not more than 0.03 Ω.Consider that device is actually using
Middle possible needs are transported and are moved, and pipe support design guarantees that pipeline fixes reliable, no movement in transport or lifting, according to
It needs to be also provided with falsework.
The advantages of skid-mounted design:
To install and moving convenient for recyclable device, to various equipment, pipeline, instrument and it is electrical etc. carry out skid design,
It is integrated in a unsplit bedplate, is in skid-mounted type.Whole device has following apparent advantage in the design of skid-mounted type: 1. arrangement is tight
It gathers, occupied area is small.Skid mounted equipment occupied area is only 2m2, entire operation area area only 250m2Left and right.2. construction period
Short, construction organization is convenient.On the basis of need to only sled block being installed to, sled block and live pipeline and electric part are attached, i.e.,
It can be used, greatly reduce site workload and set-up time.3. prizing block assembly working mainly to complete in production unit, cost
It is low, high reliablity.It is easy 4. resettlement is mobile, convenient for adjustment in the venue.Inspection Unit examines the medium of tank car to be different,
Corresponding sled block can be selected to carry out the recycling of residual air raffinate according to different medium, significantly reduce inspection cost.5. due to reality
The high efficiente callback for having showed residual air raffinate, thoroughly solves environmental pollution problem.
Use the live setting requirements of this recyclable device.
1, position selects:
Centered on this recyclable device of skid-mounted type, the region that radius is 9m is as recycling operation area, the setting of operation area
Fire safety, environmental protection and requirement convenient to use should be met.The region should not exceed Inspection Unit's enclosure wall and the available boundary of a piece of land
Line must not be located at aerial power supply, communication line lower section, preferably be arranged in the weather side of annual minimum frequency wind direction.It is set in operation area
It is standby with unit outside build, the firebreak between structures or facility should meet the regulation of GB50016 " Code for fire protection design of buildings ", such as
Fruit Inspection Unit is in petroleum chemical enterprise, equipment and enterprise is built-in, the firebreak between structures and facility should also conform to GB50160
The regulation of " code for fire protection design of petrochemical enterprises " must not have place of open flame or place of spark-emission, power distribution station in operation area
It should be arranged in other than working region.Tank car parking stall is answered smooth, must not there is the gradient.
2, site requirements
Recycle operation area ground must not asphalt, should be using flashing ground, operation area surrounding should not set up obviously
Boundary line mark.Recyclable device uses outdoor arrangement, and height should be arranged not less than 0.5m bumping post.It is anti-that awning can be used in device
It shines, awning is built using incombustible material, masked area 2m outer not less than device plane projection.Underdrain should not be used in operation area
Draining, the surface water can diffusing discharge, flow out the water of operation area and collected by the bright ditch in periphery, and trapped well, water should be set on the bright ditch
Envelope height is not less than 0.25m.Operation area distribution line preferably uses cable directly buried installation, should be worn at the position for having vehicle to run
Water pipe precaution, electrical equipment and electrical connection should meet GB50058 " explosive hazard environment electric device design specification " in region
Regulation.Should have lightning protection anti electrostatic ground stud in operation area, facilitate the ground connection of tank car, all devices include cable protection steel pipe,
Armored hose both ends and awning etc. should all good earths.The fire distinguisher of operation area should be equipped with complete, should have around operation area and disappear
Waterproof system.
The actual mechanical process of the present apparatus is as follows:
When practical operation, two position four-way valves as positive-negative connected valving 7 are first placed into antiposition, open 6 He of gas valve
Third valve 5-3 closes blowdown valve 12 and the first valve 5-1, starts compressor 2-1.Compressor 2-1 suction at this time is as movement
Gas in the gas cylinder of formula storage container 1 simultaneously makes its pressure reduction, is then shut off gas valve 6 and third valve 5-3, opens blowdown
Valve 12 and the first valve 5-1, due to the effect of pressure difference, the raffinate in tank car tank body 3 is pressed into gas cylinder through the first pipeline 4-1, directly
Until the raffinate conveying in tank car tank body 3 is finished.Again by the first pipeline 4-1 blowdown valve 12 and the first valve 5-1 close
It closes, the handle of two position four-way valves is rotated 90 °, i.e., normotopia is become from antiposition, blowdown valve 12 and the 4th valve 5-4 are opened, by tank
The blowdown valve 12 of 3 bottom of vehicle tank is intake, and gas valve 6 and third valve 5-3 are opened simultaneously, and starting compressor 2-1 extracts tank car
Liquefied gas in tank body 3, the liquefied gas after pressurization enter condenser 2-2 through gs-oil separator 10, are pressed into gas after being condensed into liquid
Bottle.Gas cylinder is full of rear replaceable empty bottle, and the gas cylinder after being full of can be used as energy normal use.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810993682.9A CN109084172A (en) | 2018-08-29 | 2018-08-29 | Liquefied gas tanker residual air remnant liquid recovering device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810993682.9A CN109084172A (en) | 2018-08-29 | 2018-08-29 | Liquefied gas tanker residual air remnant liquid recovering device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109084172A true CN109084172A (en) | 2018-12-25 |
Family
ID=64795187
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810993682.9A Pending CN109084172A (en) | 2018-08-29 | 2018-08-29 | Liquefied gas tanker residual air remnant liquid recovering device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109084172A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110274151A (en) * | 2019-07-11 | 2019-09-24 | 福建久策气体集团有限公司 | A kind of ultra-pure ammonia tank car charging system and method |
| GB2580927A (en) * | 2019-01-30 | 2020-08-05 | Linde Ag | Method and filling device for filling a transport tank |
| CN111622925A (en) * | 2020-05-08 | 2020-09-04 | 中国科学院合肥物质科学研究院 | Self-pressurization device and pressurization method for liquid helium dewar |
| CN111734951A (en) * | 2020-07-27 | 2020-10-02 | 青岛乐戈新能源科技有限公司 | A kind of unloading device, unloading system and control method of low temperature liquid tank truck |
| CN112082086A (en) * | 2019-06-12 | 2020-12-15 | 中国石油化工股份有限公司 | Supercharged liquefied hydrocarbon loading and unloading residual liquid recovery system and method |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06235498A (en) * | 1993-02-04 | 1994-08-23 | Machida Giken Kogyo:Yugen | Recovery of residual gas in liquefied gas vessel and its device |
| CN2415239Y (en) * | 2000-01-20 | 2001-01-17 | 国内贸易部洛阳制冷机械厂 | Liquefied petroleum gas recovery device |
| CN202470557U (en) * | 2011-12-28 | 2012-10-03 | 滨州职业学院 | Filter type lubricating oil separator structure of marine cold store refrigeration device |
| CN202733449U (en) * | 2012-06-07 | 2013-02-13 | 武汉龙净环保工程有限公司 | Liquid ammonia storage replacement device |
| EP2565514A1 (en) * | 2011-08-30 | 2013-03-06 | Air Liquide Deutschland GmbH | Device and method for topping up a storage tank |
| CN203671240U (en) * | 2014-01-23 | 2014-06-25 | 山东省特种设备检验研究院聊城分院 | Liquefied petroleum gas tank emptying device |
| CN106090603A (en) * | 2016-07-28 | 2016-11-09 | 北京京诚泽宇能源环保工程技术有限公司 | Liquefied petroleum gas residual liquid recovery system and method |
| CN207647499U (en) * | 2017-12-14 | 2018-07-24 | 东营华辰石油装备有限公司 | A kind of oil well supercharging casing gas recovering device |
| CN208886375U (en) * | 2018-08-29 | 2019-05-21 | 江苏省特种设备安全监督检验研究院 | A liquefied gas tanker residual gas and residual liquid recovery device |
-
2018
- 2018-08-29 CN CN201810993682.9A patent/CN109084172A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06235498A (en) * | 1993-02-04 | 1994-08-23 | Machida Giken Kogyo:Yugen | Recovery of residual gas in liquefied gas vessel and its device |
| CN2415239Y (en) * | 2000-01-20 | 2001-01-17 | 国内贸易部洛阳制冷机械厂 | Liquefied petroleum gas recovery device |
| EP2565514A1 (en) * | 2011-08-30 | 2013-03-06 | Air Liquide Deutschland GmbH | Device and method for topping up a storage tank |
| CN202470557U (en) * | 2011-12-28 | 2012-10-03 | 滨州职业学院 | Filter type lubricating oil separator structure of marine cold store refrigeration device |
| CN202733449U (en) * | 2012-06-07 | 2013-02-13 | 武汉龙净环保工程有限公司 | Liquid ammonia storage replacement device |
| CN203671240U (en) * | 2014-01-23 | 2014-06-25 | 山东省特种设备检验研究院聊城分院 | Liquefied petroleum gas tank emptying device |
| CN106090603A (en) * | 2016-07-28 | 2016-11-09 | 北京京诚泽宇能源环保工程技术有限公司 | Liquefied petroleum gas residual liquid recovery system and method |
| CN207647499U (en) * | 2017-12-14 | 2018-07-24 | 东营华辰石油装备有限公司 | A kind of oil well supercharging casing gas recovering device |
| CN208886375U (en) * | 2018-08-29 | 2019-05-21 | 江苏省特种设备安全监督检验研究院 | A liquefied gas tanker residual gas and residual liquid recovery device |
Non-Patent Citations (1)
| Title |
|---|
| 赵阳春: "液化石油气铁路罐车余液余气回收利用", 铁道劳动安全卫生与环保, no. 03 * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2580927A (en) * | 2019-01-30 | 2020-08-05 | Linde Ag | Method and filling device for filling a transport tank |
| CN112082086A (en) * | 2019-06-12 | 2020-12-15 | 中国石油化工股份有限公司 | Supercharged liquefied hydrocarbon loading and unloading residual liquid recovery system and method |
| CN112082086B (en) * | 2019-06-12 | 2022-06-28 | 中国石油化工股份有限公司 | Supercharged liquefied hydrocarbon loading and unloading residual liquid recovery system and method |
| CN110274151A (en) * | 2019-07-11 | 2019-09-24 | 福建久策气体集团有限公司 | A kind of ultra-pure ammonia tank car charging system and method |
| CN110274151B (en) * | 2019-07-11 | 2023-11-17 | 福建久策气体集团有限公司 | Ultra-pure ammonia tank car filling system and method |
| CN111622925A (en) * | 2020-05-08 | 2020-09-04 | 中国科学院合肥物质科学研究院 | Self-pressurization device and pressurization method for liquid helium dewar |
| CN111734951A (en) * | 2020-07-27 | 2020-10-02 | 青岛乐戈新能源科技有限公司 | A kind of unloading device, unloading system and control method of low temperature liquid tank truck |
| CN111734951B (en) * | 2020-07-27 | 2025-01-10 | 青岛乐戈新能源科技有限公司 | A low-temperature liquid tank truck unloading device, unloading system and control method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109084172A (en) | Liquefied gas tanker residual air remnant liquid recovering device | |
| CN101284640B (en) | Safety, environmental protection, energy conservation and skidded refueling device | |
| US6214092B1 (en) | Fracturing material separator apparatus | |
| US20120012309A1 (en) | Flow Back Recovery System | |
| CN201335372Y (en) | Condensed water recovery device of steam system | |
| CN104791610B (en) | A kind of automatic draining device of skid-mounted type emptying liquid-separation | |
| CN201037112Y (en) | Safety environmental protection energy-saving pry-mounting type refueling unit | |
| CN204099894U (en) | A kind of sled of the liquefied natural gas filling for station of liquefying | |
| CN208886375U (en) | A liquefied gas tanker residual gas and residual liquid recovery device | |
| CN206188377U (en) | A small -size refueling equipment for general aviation | |
| CN206444996U (en) | Double pump multiphase extraction device applied to soil and groundwater remediation | |
| US20140020775A1 (en) | Manifold battery for hydrocarbon fields | |
| CN202055817U (en) | Deep well and high-temperature high-pressure well testing device | |
| CN105861025B (en) | Device and method for recovering liquid light hydrocarbon in gas pipeline | |
| CN202010684U (en) | Special buried dirty oil recovery skid-mounted device for launching/receiving ball barrel | |
| CN205676420U (en) | A recovery device for liquid light hydrocarbons in gas pipelines | |
| CN108505984B (en) | Oil well liquid drives pressure boost system | |
| CN108954007A (en) | A kind of integrated skid-mounted unit and seriation joining method | |
| CN208748026U (en) | A kind of oil and gas recovery condensate collection and delivery device | |
| CN204512953U (en) | A kind of flash distillation separatory integrated device | |
| CN207195147U (en) | Gas-pressed equipment | |
| CN108591814A (en) | A kind of liquid carbon dioxide storage tank and its application method | |
| CN204324860U (en) | One, two, three petroleum vapor recovery integrated treatment unit of petrol service station | |
| CN205314975U (en) | Individual well ground is evaporated auto parts and is annotated sledge | |
| CN208747625U (en) | A kind of clean and effective Sealed Unloading device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |