CN101139030A - Method for controlling evaporating loss of light fuel oil in oil tank - Google Patents

Method for controlling evaporating loss of light fuel oil in oil tank Download PDF

Info

Publication number
CN101139030A
CN101139030A CNA200710132598XA CN200710132598A CN101139030A CN 101139030 A CN101139030 A CN 101139030A CN A200710132598X A CNA200710132598X A CN A200710132598XA CN 200710132598 A CN200710132598 A CN 200710132598A CN 101139030 A CN101139030 A CN 101139030A
Authority
CN
China
Prior art keywords
oil
fuel oil
light fuel
oil tank
evaporation loss
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
Application number
CNA200710132598XA
Other languages
Chinese (zh)
Inventor
费逸伟
朱焕勤
佟丽萍
杨宏伟
张永国
孙元宝
刘芳
刘广龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
XUHOU AIR FORCE COLLEGE OF PLA
Original Assignee
XUHOU AIR FORCE COLLEGE OF PLA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by XUHOU AIR FORCE COLLEGE OF PLA filed Critical XUHOU AIR FORCE COLLEGE OF PLA
Priority to CNA200710132598XA priority Critical patent/CN101139030A/en
Publication of CN101139030A publication Critical patent/CN101139030A/en
Pending legal-status Critical Current

Links

Abstract

The present invention discloses a method to control evaporation loss of light fuel oil in oil tank. The main technical proposal is that a fluoride-treated oil resistance plastic product is filled with phase change material; at last, treated plastic product can be put into an oil storage tank, evaporation loss of light fuel oil can be further inhibited as phase change endothermic of phase change material can reduce temperature on the evaporation surface of oil product. The positive effect of the present invention means that evaporation loss of light fuel oil can be greatly reduced. The present invention is suitable for the oil tank of various shapes; the oil tank needs no modification and processing, with convenient and reliable applying processing; the coating surface of light fuel oil has corrosion resistance, oxidation resistance and long service life; recycling is convenient and do not affect normal repairing and maintenance of the oil tank.

Description

The method of control evaporation loss of light fuel oil in oil tank
Technical field
The present invention relates to a kind of technology of controlling evaporating loss of light fuel oil, specifically a kind of method by the phase transformation cooling is controlled the method for evaporation loss of light fuel oil in oil tank.The evaporation loss that is applicable to light-weight fuel oil in the storage oil tank of different shape suppresses.
Background technology
Oil and products thereof occupies important status as the irreproducibility energy in economic construction and national defense construction.The evaporation loss of oil product accounts for 76% of storing and transporting system overall loss, not only causes economic waste, and influences the quality of oil product and cause environmental pollution.For reducing the loss of oil product in storage process, the patent documentation of the application number of having announced 200610040981.8 discloses a kind of soft floater technology of controlling evaporating loss of light fuel oil, this technology is the oil resistant hollow plastic articles of different size and shape to be carried out surface fluorination handle, and then the plastic product after will handling renders to and stores in the oil tank, reduces the evaporation loss that the free evaporation surface of oil product suppresses light-weight fuel oil above the oil product by floating the covering of hollow plastic articles.Though this technology can significantly reduce the evaporation loss of oil product, and is perfect not enough.Given this, the present invention has carried out improving to the soft floater technology of control evaporating loss of light fuel oil.
Summary of the invention
The purpose of this invention is to provide a kind of method of controlling evaporation loss of light fuel oil in oil tank, by the method control evaporation loss of light fuel oil in oil tank of phase transformation cooling, to obtain the effect that reduces oil product evaporating loss to greatest extent.
Technical scheme of the present invention is as follows: a kind of method of controlling evaporation loss of light fuel oil in oil tank, be to carry out fluorination treatment with the oil resistant hollow plastic articles that oil resistant plastics is made, combine firmly with plastic substrate in the formation of hollow plastic articles surface, the fluorinated layer of surface compact, in the cavity of hollow oil resistant plastics goods, also be perfused with phase-change material, the plastic product that will be perfused with phase-change material is then rendered in the storage oil tank, covers the free evaporation surface of minimizing oil product above the oil product and reduces the evaporation loss that the oil evaporation surface temperature suppresses light-weight fuel oil by the heat absorption of phase transformation material phase transformation by hollow plastic articles is floating.
The described floating quantity of the lip-deep plastic product of oil product that covers is can be paved with pasta one deck at least.
Described phase-change material is meant any one in four water potassium fluorides, Copper nitrate hexahydrate, six water ferric bromides, washing soda, two water lithium bromides, dimethyl sulfoxide (DMSO), butyl stearate, paraffin, dimethyl sebacate, carbowax E600, ethene stearic acid and the capric acid.Its concrete hot rerum natura can be as shown in table 1:
The hot rerum natura of table 1 phase-change material
Phase-change material Fusing point (℃) Heat of fusion (kJ/kg) Density (kg/m 3)
Four water potassium fluorides 18.5 231 1447
Copper nitrate hexahydrate 26.4 154 2074
Six water ferric bromides 27 105
Washing soda 32 267 1442
Two water lithium bromides 34 124
Dimethyl sulfoxide (DMSO) 16.5 85.7 1009 (solid-state or liquid)
Butyl stearate .19 140,123-200
Paraffin 28,27.5 244,243.5 774(70℃),814(20℃)
Dimethyl sebacate 21 120-135
Carbowax E600 22 127.2 1126(25℃),1232(4℃)
The ethene stearic acid 27-29 122
Capric acid 36 148
The amount of described phase-change material perfusion is advisable with the 1/4-3/4 of filled plastics product volume.
Described oil resistant plastics is meant polyethylene (PE), polyvinylchloride (PVC), polyvinyl alcohol (PVA), polypropylene (PP), polystyrene (PS), polyphenylene oxide (PPO), polyphenylene sulfide (PPS) and polyamide (PA), and its specific performance requires as follows:
The plastics title Weight average molecular weight (ten thousand) Density (Gcm -3) Water absorption rate (%) Resistance to heat (℃) Specific inductance capacity (60Hz)
Polyethylene and polyvinyl chloride polyvinyl alcohol polypropylene polystyrene polyphenylene oxide polyphenylene sulfide polyamide 4.8~35 3~25 7~22 6~25 5~20 2~5 7~16 1.5~8 0.94~0.965 1.35~1.45 1.26~1.35 0.90~0.915 1.05~1.09 1.06 1.15~1.26 1.00~1.15 <0.01 0.15~0.75 1 0.03~0.04 0.03~0.05 0.07 0.009 1~2.5 108 70 100 120 75 190 101 140 2.35 5.0~9.0 1.5~1.8 2.1 2.45~2.65 2.85 3.26 3.5~4.4.
Described fluorination treatment material comprises fluorine gas, and the cation of solid or liquid is fluoridized thing, anion fluoride or both sexes fluoride, and fluorine coating, fluorocarbon resin.The thickness of fluorinated layer is 5~20 μ m.
Described hollow plastic articles is that length is that 5mm~20mm, wall thickness are hollow square or the cuboid of 0.5mm~2mm; Or diameter is that Φ 5mm~Φ 20mm, wall thickness are the hollow ball of 0.5mm~2mm.
Beneficial effect of the present invention is: the present invention controls the soft floater technology of evaporating loss of light fuel oil when suppressing the evaporation loss of light-weight fuel oil by the free evaporation surface of minimizing oil product, reduce the temperature on oil evaporation surface by adding phase-change material, thereby significantly reduce the evaporation loss of light-weight fuel oil.The present invention is applicable to the oil tank of different shape; Need not oil tank is transformed and handled, implementing process is convenient and reliable; Light Fuel oil overlay withstanding corrosion, antioxidant, tenure of use is long; It is convenient to reclaim, and does not influence the normal maintenance and the maintenance of oil tank.
The specific embodiment
The present invention is described in more detail below in conjunction with embodiment.
Embodiment 1:
Under 125 ℃~135 ℃, be 10~120,000 with weight average molecular weight, density is 0.94~0.965Kg/m 3High density polyethylene (HDPE) is made the hollow plastic beads of Φ 15mm * 1.5mm.Be that 15~180,000 perfluoro alkoxy benzoic acid utilizes vacuum evaporation gas phase lamination method to handle hollow plastic beads surface then with weight average molecular weight, form the perfluoro alkoxy benzoic acid molecule film of fine and close flawless 5~10 μ m of one deck on the bead surface.The inner perfusion of hollow plastic beads phase-change material ethene stearic acid (fusing point is that 27 ℃, heat of fusion are 122kJ/kg), the amount of perfusion is 1/2 of a plastic beads volume at last.Bead after handling is thrown in into oil tank by certain thickness, covered the evaporation loss that the light-weight fuel oil surface can suppress oil product, compare with the holding vessel of not implementing soft floater technology, this technology can make the evaporation loss of light-weight fuel oil reduce by 80%.
Implement the phase transformation cool-down method and compare, can make the evaporation loss of light-weight fuel oil reduce by 20% again with the soft floater technology of not implementing cool-down method.
Embodiment 2:
Under 150 ℃~160 ℃, be 5~200,000 with weight average molecular weight, density is 1.35~1.45Kg/m 3Polyvinylchloride (PVC) to make the length of side be 20mm, thickness is the square hollow plastic product of 0.5mm.Be 38 with relative molecular weight then, density is 1.696Kg/m 3, purity is higher than 99% high-purity fluorine gas and slowly feeds and fluoridize stove hollow plastic articles is carried out fluorination treatment, and the reaction time was controlled at 48~72 hours, and feeding the fluorine gas amount is 15~25Kg/m by handling frosting long-pending 2The amount of being equipped with is finally at the surperficial fluorine-containing molecular film that forms fine and close flawless 5~20 μ m of one deck of hollow plastic articles.(fusing point is that 28 ℃, heat of fusion are that 244kJ/kg, density are 814kg/m at the inner perfusion of hollow plastic beads phase-change material paraffin then 3), the amount of perfusion is 1/2 of a plastic beads volume.Hollow plastic articles after the fluorination treatment is thrown in into oil tank by certain thickness, covered the evaporation loss that the light-weight fuel oil surface can suppress oil product, compare with the holding vessel of not implementing soft floater technology, the light-weight fuel oil evaporation loss can reduce by 82%.
Implement the phase transformation cool-down method and compare, can make the evaporation loss of light-weight fuel oil reduce by 20% again with the soft floater technology of not implementing cool-down method.

Claims (3)

1. method of controlling evaporation loss of light fuel oil in oil tank, it is characterized in that and to carry out fluorination treatment with the oil resistant hollow plastic articles that oil resistant plastics is made, combine firmly with plastic substrate in the formation of hollow plastic articles surface, the fluorinated layer of surface compact, in the cavity of hollow oil resistant plastics goods, also be perfused with phase-change material, the plastic product that will be perfused with phase-change material is then rendered in the storage oil tank, covers the free evaporation surface of minimizing oil product above the oil product and reduces the evaporation loss that the oil evaporation surface temperature suppresses light-weight fuel oil by the heat absorption of phase transformation material phase transformation by hollow plastic articles is floating.
2. the method for control evaporation loss of light fuel oil in oil tank according to claim 1, it is characterized in that described phase-change material is that fusing point is any one in 10 ℃-40 ℃ material four water potassium fluorides, Copper nitrate hexahydrate, six water ferric bromides, washing soda, two water lithium bromides, dimethyl sulfoxide (DMSO), butyl stearate, paraffin, dimethyl sebacate, carbowax E600, ethene stearic acid and the capric acid.
3. the method for control evaporation loss of light fuel oil in oil tank according to claim 1 is characterized in that, the amount of described phase-change material perfusion is the 1/4-3/4 of hollow plastic articles cavity volume.
CNA200710132598XA 2007-09-20 2007-09-20 Method for controlling evaporating loss of light fuel oil in oil tank Pending CN101139030A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA200710132598XA CN101139030A (en) 2007-09-20 2007-09-20 Method for controlling evaporating loss of light fuel oil in oil tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA200710132598XA CN101139030A (en) 2007-09-20 2007-09-20 Method for controlling evaporating loss of light fuel oil in oil tank

Publications (1)

Publication Number Publication Date
CN101139030A true CN101139030A (en) 2008-03-12

Family

ID=39191174

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA200710132598XA Pending CN101139030A (en) 2007-09-20 2007-09-20 Method for controlling evaporating loss of light fuel oil in oil tank

Country Status (1)

Country Link
CN (1) CN101139030A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102287214A (en) * 2011-06-29 2011-12-21 李光武 Phase-change cooling device for rescue capsule and refuge chamber
CN102305467A (en) * 2011-09-16 2012-01-04 广东纽恩泰新能源科技发展有限公司 Heat-storage heat pump water heater device
CN103612833A (en) * 2013-12-06 2014-03-05 上海应用技术学院 Device containing phase change materials and used for heat insulation of solution in open system
CN106586300A (en) * 2016-07-19 2017-04-26 北京众信远新能源技术有限公司 Soft floating roof method for reducing evaporation of liquid fuel storage tank through hollow plastic product

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102287214A (en) * 2011-06-29 2011-12-21 李光武 Phase-change cooling device for rescue capsule and refuge chamber
CN102305467A (en) * 2011-09-16 2012-01-04 广东纽恩泰新能源科技发展有限公司 Heat-storage heat pump water heater device
CN103612833A (en) * 2013-12-06 2014-03-05 上海应用技术学院 Device containing phase change materials and used for heat insulation of solution in open system
CN106586300A (en) * 2016-07-19 2017-04-26 北京众信远新能源技术有限公司 Soft floating roof method for reducing evaporation of liquid fuel storage tank through hollow plastic product

Similar Documents

Publication Publication Date Title
CN101139030A (en) Method for controlling evaporating loss of light fuel oil in oil tank
US20110030915A1 (en) Improved latent heat storage device
CN106871211B (en) Phase-change energy-storage heating device
CN102514347B (en) Heat compounding technique and apparatus of BOPET film and tin-free steel plate
CN104608451B (en) A kind of multilamellar improvement thermal contraction preservative film/bag
US20170254601A1 (en) Thermal energy storage systems comprising encapsulated phase change materials and a neutralizing agent
CN103185367A (en) Heat pipe-type movable heating phase-change heat storage device
WO2016116406A1 (en) Gas pressure vessel containing a gas, a latent heat storage material and a porous solid material
CN103216955A (en) Energy-storage solar heat collector
CN107218832A (en) There are the sandstone heat-storing method and its device on carbon heat conduction top layer
Extrand The use of fluoropolymers to protect semiconductor materials
CN214369284U (en) Metal hydride hydrogen storage tank
CN108728047A (en) Purposes of the cetylamine as phase-changing energy storage material
CN108865081A (en) Purposes of the lauryl amine as phase-changing energy storage material
JP5680382B2 (en) Heat storage device and air conditioner equipped with the same
US6517918B1 (en) Multilayer composite plastics material containing a barrier layer of polybutylene terephthalate
US9897255B2 (en) Pressure vessel with PCM and method of use
CN102642684A (en) Liquid storage tank for storing low-temperature storage liquid
CN109181652A (en) Purposes of the tetradecy lamine as phase-changing energy storage material
CN202594191U (en) Low-temperature liquid storage tank
CN106282736B (en) Phase-change accumulation energy alloy and phase-change accumulation energy cup
CN213861152U (en) High-strength biaxially oriented polyolefin heat shrinkable film
CN202594189U (en) Adjustable low-temperature liquid storage tank
Krasnova et al. Gas-filled thermal insulation use in heat supply
CN204676032U (en) Coke-oven gas residual neat recovering system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication