CN104629619A - Anti-scaling and drag-reducing coating for oil pipeline inner walls and preparation method thereof - Google Patents
Anti-scaling and drag-reducing coating for oil pipeline inner walls and preparation method thereof Download PDFInfo
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- CN104629619A CN104629619A CN201510056273.2A CN201510056273A CN104629619A CN 104629619 A CN104629619 A CN 104629619A CN 201510056273 A CN201510056273 A CN 201510056273A CN 104629619 A CN104629619 A CN 104629619A
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- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 239000011248 coating agent Substances 0.000 title abstract description 19
- 238000000576 coating method Methods 0.000 title abstract description 19
- 229920001296 polysiloxane Polymers 0.000 claims abstract description 34
- -1 polysiloxane Polymers 0.000 claims abstract description 26
- 238000003756 stirring Methods 0.000 claims abstract description 26
- 239000011347 resin Substances 0.000 claims abstract description 24
- 229920005989 resin Polymers 0.000 claims abstract description 24
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 23
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims abstract description 14
- 239000002904 solvent Substances 0.000 claims abstract description 8
- 238000000227 grinding Methods 0.000 claims abstract description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 30
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 23
- 239000011737 fluorine Substances 0.000 claims description 23
- 229910052731 fluorine Inorganic materials 0.000 claims description 23
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 23
- 239000002245 particle Substances 0.000 claims description 21
- 239000003973 paint Substances 0.000 claims description 18
- 230000005764 inhibitory process Effects 0.000 claims description 17
- 239000000470 constituent Substances 0.000 claims description 15
- 238000010792 warming Methods 0.000 claims description 15
- 239000007789 gas Substances 0.000 claims description 12
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 claims description 11
- MIOSQLBVJPELHK-UHFFFAOYSA-N trifluoro(trifluoromethoxy)silane Chemical compound F[Si](OC(F)(F)F)(F)F MIOSQLBVJPELHK-UHFFFAOYSA-N 0.000 claims description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- 239000004210 ether based solvent Substances 0.000 claims description 8
- 239000001257 hydrogen Substances 0.000 claims description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims description 8
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 8
- 230000002209 hydrophobic effect Effects 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- 239000013543 active substance Substances 0.000 claims description 6
- 239000013530 defoamer Substances 0.000 claims description 6
- 238000013019 agitation Methods 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 5
- 150000002148 esters Chemical class 0.000 claims description 5
- 238000007789 sealing Methods 0.000 claims description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 235000011089 carbon dioxide Nutrition 0.000 claims description 2
- 238000005516 engineering process Methods 0.000 abstract description 7
- 239000007788 liquid Substances 0.000 abstract description 6
- 230000001603 reducing effect Effects 0.000 abstract description 6
- 239000004094 surface-active agent Substances 0.000 abstract description 5
- 230000008021 deposition Effects 0.000 abstract description 4
- 230000007774 longterm Effects 0.000 abstract description 3
- AQYSYJUIMQTRMV-UHFFFAOYSA-N hypofluorous acid Chemical group FO AQYSYJUIMQTRMV-UHFFFAOYSA-N 0.000 abstract 3
- 239000002518 antifoaming agent Substances 0.000 abstract 2
- 239000004810 polytetrafluoroethylene Substances 0.000 abstract 2
- 239000000843 powder Substances 0.000 abstract 2
- 230000002401 inhibitory effect Effects 0.000 abstract 1
- 238000002156 mixing Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 24
- 239000000126 substance Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- 239000006185 dispersion Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000012948 isocyanate Substances 0.000 description 3
- 150000002513 isocyanates Chemical class 0.000 description 3
- 239000010410 layer Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000002688 persistence Effects 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 241000233805 Phoenix Species 0.000 description 1
- 241001274961 Rubus repens Species 0.000 description 1
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 210000003746 feather Anatomy 0.000 description 1
- 238000003958 fumigation Methods 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 239000002455 scale inhibitor Substances 0.000 description 1
- 229910000077 silane Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
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- Paints Or Removers (AREA)
Abstract
The invention discloses anti-scaling and drag-reducing coating for oil pipeline inner walls and a preparation method thereof. The anti-scaling and drag-reducing coating comprises the following components in parts by weight: 25-35 parts of terminal hydroxyl fluorine-containing linear polysiloxane resin, 10-15 parts of polytetrafluoroethylene micro powder, 0.5-2 parts of leveling agent, 1-3 parts of surfactant, 0.2-1 part of antifoaming agent, 1-3 parts of curing agent and 20-40 parts of solvent. The preparation method comprises the following steps: preparing terminal hydroxyl fluorine-containing linear polysiloxane resin; pre-mixing and dispersing the terminal hydroxyl fluorine-containing linear polysiloxane resin, the polytetrafluoroethylene micro powder, the leveling agent, the surfactant, the antifoaming agent and the solvent, and grinding the mixture in a nanometer grinding machine; and dropwise adding the curing agent, continuously stirring at room temperature after dropwise adding the curing agent, and hermetically storing for use. The anti-scaling and drag-reducing coating disclosed by the invention can be used for improving the durability of the particular drag reducing effect of the coating, inhibiting the deposition of incrustation, and improving the conveying efficiency and reducing the actual operation cost in combination with a liquid pipeline conveying technology, so as to achieve long-term stable and efficient oil transportation.
Description
Technical field
The present invention relates to paint field, particularly relate to a kind of oil pipeline inwall scale inhibition anti-drag paint and preparation method thereof.
Background technology
The Drag reduction devices of current domestic oil pipeline, mainly through heating oil product, the way reducing viscosity of crude reduces the resistance to flow of course of conveying.In addition, when in oil product during calcium ions and magnesium ions excessive concentration easily in inner-walls of duct fouling, affect operational throughput, increase resistance.
Such scheme pipeline outer wall needs to increase following measures: (1) installs heating unit, improves oil product temperature; (2) pressurizeed by pressurized pump station oil supply, overcome transporting resistance; (3) lagging material is wrapped up, holding temperature; (4) in crude oil, drop into Scale inhibitors, stop fouling.
Above measure makes fuel transfer system Infrastructure increase input, and safeguards and use cost increase, and, directly consume the energy by the method for heating, be unfavorable for energy-saving and emission-reduction.Strengthening fuel transfer pressure makes the compressive strength of e-quipment and pipe require to improve, and increase input, and safety in operation reduces.Adding of scale inhibition chemical agent, improve running cost, and increasing energy consumption and resource consumption when removing afterwards.
In the coating of domestic and international use, less with the surface energy of fluorocarbon resin paint, but the contact angle of itself and oil is still comparatively large, reduces DeGrain to the resistance in oil product course of conveying.This is also the domestic major cause not having this type of application example why at present.But fluororine-carbon coating is still very significant to preventing the effect of fouling, due to low surface energy, even if dirt can be formed can not be firmly attached to coatingsurface.
Summary of the invention
The technical problem that the present invention mainly solves is to provide a kind of oil pipeline inwall scale inhibition anti-drag paint, by reducing frictional coefficient, reduce transport resistance, improve the persistence of this special drag-reduction effect of coating, suppress the deposition of incrustation scale, improve transport efficiency at cooperation liquid pipe transportation technology simultaneously, reduce actual operation cost, thus realize effective oil transportation steady in a long-term.
For solving the problems of the technologies described above, the technical scheme that the present invention adopts is: provide a kind of oil pipeline inwall scale inhibition anti-drag paint, it comprises the formula constituent of following weight part:
The fluorine-containing linear silicones resin of terminal hydroxy group 25 ~ 35 parts,
Ptfe micropowder 10 ~ 15 parts,
Flow agent 0.5 ~ 2 part,
1 ~ 3 part, tensio-active agent,
Defoamer 0.2 ~ 1 part,
1 ~ 3 part, solidifying agent,
Solvent 20 ~ 40 parts.
In a preferred embodiment of the present invention, described flow agent is hydroxyl polysiloxane.
In a preferred embodiment of the present invention, described tensio-active agent is non-ionic type fluorochemicals.
In a preferred embodiment of the present invention, described defoamer is the polysiloxane containing hydrophobic particles.
In a preferred embodiment of the present invention, described solidifying agent is isocyanic ester.
In a preferred embodiment of the present invention, described solvent is hydrogen fluorine ether solvents.
In a preferred embodiment of the present invention, the particle diameter of described ptfe micropowder is 50 ~ 200nm.
For solving the problems of the technologies described above, another technical solution used in the present invention is: the preparation method providing a kind of oil pipeline inwall scale inhibition anti-drag paint, comprises the following steps:
(1) the fluorine-containing direct-connected polysiloxane preparation of terminal hydroxy group: take perfluoromethoxy silane according to weight proportion, acetic acid and fluorocarbon resin, first perfluoromethoxy silane is added in container, add acetic acid again, stirring at normal temperature 22 ~ 26h, be warming up to 60 ~ 80 DEG C, then fluorocarbon resin is slowly dripped, constant temperature stirs, 200 ~ 250 DEG C are warming up to after dropwising, constant temperature stirs 7 ~ 9 h, a vacuum is taken out every 1 h, naturally cool to room temperature to add the vitriol oil and continue stirring until normal temperature state, then continue to be warming up to 100 ~ 150 DEG C, collect fugitive constituent, continue stirring until non-volatile point of generation, being cooled to Room-temperature seal preserves stand-by,
(2) formula constituent is taken according to weight proportion;
(3) fluorine-containing for terminal hydroxy group linear silicones resin, ptfe micropowder, flow agent, tensio-active agent, defoamer and solvent premix are disperseed, add nano-level grinder grinding, crossing and sifting out particle diameter is that the material of 100 ~ 500nm is positioned in there-necked flask, and passes into shielding gas protection;
(4) normal temperature slowly drips solidifying agent, completes in 25 ~ 35min, is added dropwise to complete rear room temperature Keep agitation 1h, then closes gas discharging sealing and preserves stand-by.
In a preferred embodiment of the present invention, described shielding gas is carbonic acid gas or nitrogen.
The invention has the beneficial effects as follows: the present invention is by reducing frictional coefficient, reduce transport resistance, improve the persistence of this special drag-reduction effect of coating, suppress the deposition of incrustation scale, improve transport efficiency at cooperation liquid pipe transportation technology simultaneously, reduce actual operation cost, thus realize effective oil transportation steady in a long-term.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme in the embodiment of the present invention, below the accompanying drawing used required in describing embodiment is briefly described, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings, wherein:
Fig. 1 is that contact angle experiments figure is dried in the spraying of the embodiment of the present invention 1;
Fig. 2 is that the spraying of the embodiment of the present invention 1 is from stem grafting feeler lab diagram;
Fig. 3 is the stifling oven dry contact angle experiments figure of the embodiment of the present invention 2;
Fig. 4 is the stifling from stem grafting feeler lab diagram of the embodiment of the present invention 2;
Fig. 5 is the electron-microscope scanning figure of the coating of the spraying method of the embodiment of the present invention 3;
Fig. 6 is the electron-microscope scanning figure of the coating of the atomization fumigation of the embodiment of the present invention 3.
Embodiment
Be clearly and completely described to the technical scheme in the embodiment of the present invention below, obviously, described embodiment is only a part of embodiment of the present invention, instead of whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art, not making other embodiments all obtained under creative work prerequisite, belong to the scope of protection of the invention.
Embodiment 1
A kind of oil pipeline inwall scale inhibition anti-drag paint, it comprises the formula constituent of following weight part: the fluorine-containing linear silicones resin of terminal hydroxy group 30 parts, particle diameter is the ptfe micropowder 12 parts of 100nm, TG2050 hydroxyl polysiloxane leveling agents (Ying Chuan Specialty Chemical company) 1 part, F4432 non-ionic type fluorochemical surfactant (3M China Co., Ltd.) 2 parts, N900 is containing the polysiloxane defoamers (Ying Chuan Specialty Chemical company) 0.7 part of hydrophobic particles, N3390 isocyanate curing agent (in Bayer Co., Ltd) 2 parts, 860S hydrogen fluorine ether solvents (Zhong Hua blue sky, Zhejiang polymkeric substance company limited) 30 parts.
Its preparation method specifically comprises the following steps:
(1) the fluorine-containing direct-connected polysiloxane preparation of terminal hydroxy group: take 300 parts, perfluoromethoxy silane according to weight proportion, acetic acid 3 parts and fluorocarbon resin 300 parts, first perfluoromethoxy silane is added in 1000ml there-necked flask, add acetic acid again, stirring at normal temperature 24h, be warming up to 70 DEG C, then fluorocarbon resin is slowly dripped, constant temperature stirs, 220 DEG C are warming up to after dropwising in 120min, constant temperature stirs 8 h, a vacuum is taken out every 1 h, naturally cool to room temperature to add the vitriol oil 0.2 part and continue stirring until normal temperature state, then continue to be warming up to 120 DEG C, install prolong additional and collect fugitive constituent, continue stirring until non-volatile point of generation, being cooled to Room-temperature seal preserves stand-by,
(2) formula constituent is taken according to weight proportion;
(3) by fluorine-containing for terminal hydroxy group linear silicones resin, particle diameter be the ptfe micropowder of 100nm, hydroxyl polysiloxane, non-ionic type fluorochemicals, containing the polysiloxane of hydrophobic particles and the dispersion of hydrogen fluorine ether solvents premix, add nano-level grinder grinding, crossing and sifting out particle diameter is that the material of 100 ~ 500nm is positioned in there-necked flask, and passes into nitrogen protection gas shield;
(4) normal temperature slowly drips isocyanic ester, completes in 30min, is added dropwise to complete rear room temperature Keep agitation 1h, then closes gas discharging sealing and preserves stand-by.
Embodiment 2
A kind of oil pipeline inwall scale inhibition anti-drag paint, it comprises the formula constituent of following weight part: the fluorine-containing linear silicones resin of terminal hydroxy group 25 parts, particle diameter is the ptfe micropowder 10 parts of 200nm, TG2050 hydroxyl polysiloxane leveling agents (Ying Chuan Specialty Chemical company) 0.5 part, F4432 non-ionic type fluorochemical surfactant (3M China Co., Ltd.) 1 part, N900 is containing the polysiloxane defoamers (Ying Chuan Specialty Chemical company) 0.2 part of hydrophobic particles, N3390 isocyanate curing agent (in Bayer Co., Ltd) 1 part, 860S hydrogen fluorine ether solvents (Zhong Hua blue sky, Zhejiang polymkeric substance company limited) 20 parts.
Its preparation method specifically comprises the following steps:
(1) the fluorine-containing direct-connected polysiloxane preparation of terminal hydroxy group: take 300 parts, perfluoromethoxy silane according to weight proportion, acetic acid 3 parts and fluorocarbon resin 300 parts, first perfluoromethoxy silane is added in 1000ml there-necked flask, add acetic acid again, stirring at normal temperature 26h, be warming up to 60 DEG C, then fluorocarbon resin is slowly dripped, constant temperature stirs, 200 DEG C are warming up to after dropwising in 120min, constant temperature stirs 9 h, a vacuum is taken out every 1 h, naturally cool to room temperature to add the vitriol oil 0.2 part and continue stirring until normal temperature state, then continue to be warming up to 150 DEG C, install prolong additional and collect fugitive constituent, continue stirring until non-volatile point of generation, being cooled to Room-temperature seal preserves stand-by,
(2) formula constituent is taken according to weight proportion;
(3) by fluorine-containing for terminal hydroxy group linear silicones resin, particle diameter be the ptfe micropowder of 200nm, hydroxyl polysiloxane, non-ionic type fluorochemicals, containing the polysiloxane of hydrophobic particles and the dispersion of hydrogen fluorine ether solvents premix, add nano-level grinder grinding, crossing and sifting out particle diameter is that the material of 100 ~ 500nm is positioned in there-necked flask, and passes into carbon-dioxide protecting gas shield;
(4) normal temperature slowly drips isocyanic ester, completes in 35min, is added dropwise to complete rear room temperature Keep agitation 1h, then closes gas discharging sealing and preserves stand-by.
Embodiment 3
A kind of oil pipeline inwall scale inhibition anti-drag paint, it comprises the formula constituent of following weight part: the fluorine-containing linear silicones resin of terminal hydroxy group 35 parts, particle diameter is the ptfe micropowder 15 parts of 50nm, TG2050 hydroxyl polysiloxane leveling agents (Ying Chuan Specialty Chemical company) 2 parts, F4432 non-ionic type fluorochemical surfactant (3M China Co., Ltd.) 3 parts, N900 is containing the polysiloxane defoamers (Ying Chuan Specialty Chemical company) 1 part of hydrophobic particles, N3390 isocyanate curing agent (in Bayer Co., Ltd) 3 parts, 860S hydrogen fluorine ether solvents (Zhong Hua blue sky, Zhejiang polymkeric substance company limited) 40 parts.
Its preparation method specifically comprises the following steps:
(1) the fluorine-containing direct-connected polysiloxane preparation of terminal hydroxy group: take 300 parts, perfluoromethoxy silane according to weight proportion, acetic acid 3 parts and fluorocarbon resin 300 parts, first perfluoromethoxy silane is added in 1000ml there-necked flask, add acetic acid again, stirring at normal temperature 22h, be warming up to 80 DEG C, then fluorocarbon resin is slowly dripped, constant temperature stirs, 250 DEG C are warming up to after dropwising in 120min, constant temperature stirs 7 h, a vacuum is taken out every 1 h, naturally cool to room temperature to add the vitriol oil 0.2 part and continue stirring until normal temperature state, then continue to be warming up to 100 DEG C, install prolong additional and collect fugitive constituent, continue stirring until non-volatile point of generation, being cooled to Room-temperature seal preserves stand-by,
(2) formula constituent is taken according to weight proportion;
(3) by fluorine-containing for terminal hydroxy group linear silicones resin, particle diameter be the ptfe micropowder of 50nm, hydroxyl polysiloxane, non-ionic type fluorochemicals, containing the polysiloxane of hydrophobic particles and the dispersion of hydrogen fluorine ether solvents premix, add nano-level grinder grinding, crossing and sifting out particle diameter is that the material of 100 ~ 500nm is positioned in there-necked flask, and passes into nitrogen protection gas shield;
(4) normal temperature slowly drips isocyanic ester, completes in 25min, is added dropwise to complete rear room temperature Keep agitation 1h, then closes gas discharging sealing and preserves stand-by.
Test example
The preparation of coating:
(1) coating prepared by embodiment 1 and embodiment 3 is sprayed one deck under the pressure of 0.6 ~ 0.8MPa, dry film film thickness controls at 35 ~ 40 μm, unsuitable blocked up, and normal temperature self-drying 24 hours is to be measured, dry 1 hour to be measured;
(2) coating prepared by embodiment 2 and embodiment 3 is placed in beaker, be heated to 405 DEG C, the iron plate handled well need be coated with to face down is buckled on beaker, stifling 10 ~ 15min, be as the criterion with surface knot pearl, once find that visible dewdrop stops immediately and painting faced up, to be measured after normal temperature self-drying 24h, dry 1 hour to be measured.
The object of oil transportation drag reduction is to reduce skin friction coefficient, and coefficient is exactly relevant with medium contact area, relative movement between liquid and solid also depends on surface tension, be 18N/m by the surface tension measuring embodiment 1 ~ embodiment 3 coating, and then explain why all embody very high contact angle at water oil.First physical process forms a large amount of nanometer micropores by the spatial configuration of coating in essence and causes water can not enter guarantee liquid interface and be coated with interlayer leaving a part of rarefied air, due to ultralow surface tension can make oil body on surface with very low resistance quickly through, experimental result display tests through the decay of 3 years the contact angle still keeping 150 °, because current domestic in be all phoenix feathers and unicorn horns more than 6 months, the popularization of achievement will be the important topic in the coming years.
Fig. 5 display surface tentacle is all reunited, and be complete spread apart, unimolecular layer can not embody completely, and its effect is slightly poor.
Fig. 6 display surface uniformity, tentacle distribution is consistent, and monomolecular coating is formed, and effects on surface energy tension force reduces synergy.
The present invention is mainly the distribution of the host molecule structure of draft reduction material, common silane, perfluor analog assistant can reduce coating surface tension really to realize drag reduction, but majority has the degree of branching of a large amount of by product and principal product high, effective content is truly not high, and form almost not having of unimolecular layer perfluor base, correlative study is had although domestic, but all can not realize commercialization, and the present invention to be exactly the problem that should solve unimolecular layer realize commercialization is simultaneously worth, by reducing frictional coefficient, reduce transport resistance, improve the persistence of this special drag-reduction effect of coating, suppress the deposition of incrustation scale, improve transport efficiency at cooperation liquid pipe transportation technology simultaneously, reduce actual operation cost, and then realize the new ideas of pipeline corrosion protection.
The foregoing is only embodiments of the invention; not thereby the scope of the claims of the present invention is limited; every utilize description of the present invention to do equivalent structure or equivalent flow process conversion; or be directly or indirectly used in other relevant technical field, be all in like manner included in scope of patent protection of the present invention.
Claims (9)
1. an oil pipeline inwall scale inhibition anti-drag paint, is characterized in that, it comprises the formula constituent of following weight part:
The fluorine-containing linear silicones resin of terminal hydroxy group 25 ~ 35 parts,
Ptfe micropowder 10 ~ 15 parts,
Flow agent 0.5 ~ 2 part,
1 ~ 3 part, tensio-active agent,
Defoamer 0.2 ~ 1 part,
1 ~ 3 part, solidifying agent,
Solvent 20 ~ 40 parts.
2. oil pipeline inwall scale inhibition anti-drag paint according to claim 1, it is characterized in that, described flow agent is hydroxyl polysiloxane.
3. oil pipeline inwall scale inhibition anti-drag paint according to claim 1, it is characterized in that, described tensio-active agent is non-ionic type fluorochemicals.
4. oil pipeline inwall scale inhibition anti-drag paint according to claim 1, is characterized in that, described defoamer is the polysiloxane containing hydrophobic particles.
5. oil pipeline inwall scale inhibition anti-drag paint according to claim 1, it is characterized in that, described solidifying agent is isocyanic ester.
6. oil pipeline inwall scale inhibition anti-drag paint according to claim 1, is characterized in that, described solvent is hydrogen fluorine ether solvents.
7. oil pipeline inwall scale inhibition anti-drag paint according to claim 1, is characterized in that, the particle diameter of described ptfe micropowder is 50 ~ 200nm.
8. the preparation method of oil pipeline inwall scale inhibition anti-drag paint according to claim 1, is characterized in that, comprise the following steps:
(1) the fluorine-containing direct-connected polysiloxane preparation of terminal hydroxy group: take perfluoromethoxy silane according to weight proportion, acetic acid and fluorocarbon resin, first perfluoromethoxy silane is added in container, add acetic acid again, stirring at normal temperature 22 ~ 26h, be warming up to 60 ~ 80 DEG C, then fluorocarbon resin is slowly dripped, constant temperature stirs, 200 ~ 250 DEG C are warming up to after dropwising, constant temperature stirs 7 ~ 9 h, a vacuum is taken out every 1 h, naturally cool to room temperature to add the vitriol oil and continue stirring until normal temperature state, then continue to be warming up to 100 ~ 150 DEG C, collect fugitive constituent, continue stirring until non-volatile point of generation, being cooled to Room-temperature seal preserves stand-by,
(2) formula constituent is taken according to weight proportion;
(3) fluorine-containing for terminal hydroxy group linear silicones resin, ptfe micropowder, flow agent, tensio-active agent, defoamer and solvent premix are disperseed, add nano-level grinder grinding, crossing and sifting out particle diameter is that the material of 100 ~ 500nm is positioned in there-necked flask, and passes into shielding gas protection;
(4) normal temperature slowly drips solidifying agent, completes in 25 ~ 35min, is added dropwise to complete rear room temperature Keep agitation 1h, then closes gas discharging sealing and preserves stand-by.
9. preparation method according to claim 8, is characterized in that, described shielding gas is carbonic acid gas or nitrogen.
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CN107163845A (en) * | 2017-06-28 | 2017-09-15 | 武汉轻工大学 | A kind of ant-scaling antifouling composition |
CN109972459A (en) * | 2017-12-27 | 2019-07-05 | 金箭印刷事业有限公司 | The manufacturing method of paper-plastic products |
CN110804380A (en) * | 2019-11-20 | 2020-02-18 | 中国人民解放军军事科学院国防科技创新研究院 | Antifouling coating material and preparation method and application thereof |
CN111442140A (en) * | 2020-05-14 | 2020-07-24 | 深圳市博新美纳米科技有限公司 | Nano-antibacterial PE water supply pipeline and manufacturing process thereof |
CN111607097A (en) * | 2020-05-18 | 2020-09-01 | 广东健玺表面工程技术有限公司 | Titanium-based fluorine-silicon polymer alloy and synthesis and application methods thereof |
CN110484129B (en) * | 2019-07-02 | 2022-01-25 | 昆山联滔电子有限公司 | Product with protective coating and preparation method thereof |
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