CN107937130A - A kind of soybean oil treatment process for capacitor impregnant - Google Patents
A kind of soybean oil treatment process for capacitor impregnant Download PDFInfo
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- CN107937130A CN107937130A CN201711149413.6A CN201711149413A CN107937130A CN 107937130 A CN107937130 A CN 107937130A CN 201711149413 A CN201711149413 A CN 201711149413A CN 107937130 A CN107937130 A CN 107937130A
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- soybean oil
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- oil
- capacitor
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- 235000012424 soybean oil Nutrition 0.000 title claims abstract description 52
- 239000003549 soybean oil Substances 0.000 title claims abstract description 52
- 239000003990 capacitor Substances 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000012545 processing Methods 0.000 claims abstract description 26
- 230000008030 elimination Effects 0.000 claims abstract description 9
- 238000003379 elimination reaction Methods 0.000 claims abstract description 9
- 239000012535 impurity Substances 0.000 claims abstract description 9
- 230000020477 pH reduction Effects 0.000 claims abstract description 7
- 238000000746 purification Methods 0.000 claims abstract description 6
- 239000003921 oil Substances 0.000 claims description 22
- 235000019198 oils Nutrition 0.000 claims description 22
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 16
- 229960000892 attapulgite Drugs 0.000 claims description 8
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 238000001914 filtration Methods 0.000 claims description 8
- 239000003292 glue Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 8
- 229910052625 palygorskite Inorganic materials 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 8
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical class CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 6
- 230000008014 freezing Effects 0.000 claims description 5
- 238000007710 freezing Methods 0.000 claims description 5
- NGDQQLAVJWUYSF-UHFFFAOYSA-N 4-methyl-2-phenyl-1,3-thiazole-5-sulfonyl chloride Chemical compound S1C(S(Cl)(=O)=O)=C(C)N=C1C1=CC=CC=C1 NGDQQLAVJWUYSF-UHFFFAOYSA-N 0.000 claims description 4
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 4
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 4
- 239000004202 carbamide Substances 0.000 claims description 4
- DMEGYFMYUHOHGS-UHFFFAOYSA-N cycloheptane Chemical compound C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 claims description 4
- 150000002191 fatty alcohols Chemical class 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 235000007079 manganese sulphate Nutrition 0.000 claims description 4
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical class [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- RGSFGYAAUTVSQA-UHFFFAOYSA-N pentamethylene Natural products C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 claims description 4
- 125000004817 pentamethylene group Chemical group [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 4
- 235000011152 sodium sulphate Nutrition 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 238000003860 storage Methods 0.000 claims description 4
- 239000011592 zinc chloride Substances 0.000 claims description 4
- 235000005074 zinc chloride Nutrition 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 abstract description 6
- 238000007711 solidification Methods 0.000 abstract description 4
- 230000008023 solidification Effects 0.000 abstract description 4
- 238000013459 approach Methods 0.000 abstract description 2
- 230000001737 promoting effect Effects 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000004996 alkyl benzenes Chemical class 0.000 description 2
- 235000019197 fats Nutrition 0.000 description 2
- QBKSWRVVCFFDOT-UHFFFAOYSA-N gossypol Chemical compound CC(C)C1=C(O)C(O)=C(C=O)C2=C(O)C(C=3C(O)=C4C(C=O)=C(O)C(O)=C(C4=CC=3C)C(C)C)=C(C)C=C21 QBKSWRVVCFFDOT-UHFFFAOYSA-N 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 229940099596 manganese sulfate Drugs 0.000 description 2
- 239000011702 manganese sulphate Substances 0.000 description 2
- 239000002480 mineral oil Substances 0.000 description 2
- 235000010446 mineral oil Nutrition 0.000 description 2
- 150000003071 polychlorinated biphenyls Chemical class 0.000 description 2
- DGZUEIPKRRSMGK-UHFFFAOYSA-N quadricyclane Chemical compound C1C2C3C2C2C3C12 DGZUEIPKRRSMGK-UHFFFAOYSA-N 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- PKQYSCBUFZOAPE-UHFFFAOYSA-N 1,2-dibenzyl-3-methylbenzene Chemical compound C=1C=CC=CC=1CC=1C(C)=CC=CC=1CC1=CC=CC=C1 PKQYSCBUFZOAPE-UHFFFAOYSA-N 0.000 description 1
- GNPWYHFXSMINJQ-UHFFFAOYSA-N 1,2-dimethyl-3-(1-phenylethyl)benzene Chemical compound C=1C=CC(C)=C(C)C=1C(C)C1=CC=CC=C1 GNPWYHFXSMINJQ-UHFFFAOYSA-N 0.000 description 1
- PQTAUFTUHHRKSS-UHFFFAOYSA-N 1-benzyl-2-methylbenzene Chemical compound CC1=CC=CC=C1CC1=CC=CC=C1 PQTAUFTUHHRKSS-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- QHOPXUFELLHKAS-UHFFFAOYSA-N Thespesin Natural products CC(C)c1c(O)c(O)c2C(O)Oc3c(c(C)cc1c23)-c1c2OC(O)c3c(O)c(O)c(C(C)C)c(cc1C)c23 QHOPXUFELLHKAS-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- WUOIAOOSKMHJOV-UHFFFAOYSA-N ethyl(diphenyl)phosphane Chemical compound C=1C=CC=CC=1P(CC)C1=CC=CC=C1 WUOIAOOSKMHJOV-UHFFFAOYSA-N 0.000 description 1
- 229930000755 gossypol Natural products 0.000 description 1
- 229950005277 gossypol Drugs 0.000 description 1
- 230000003434 inspiratory effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000021281 monounsaturated fatty acids Nutrition 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 235000021003 saturated fats Nutrition 0.000 description 1
- 231100000004 severe toxicity Toxicity 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/001—Refining fats or fatty oils by a combination of two or more of the means hereafter
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G4/00—Fixed capacitors; Processes of their manufacture
- H01G4/002—Details
- H01G4/018—Dielectrics
- H01G4/20—Dielectrics using combinations of dielectrics from more than one of groups H01G4/02 - H01G4/06
- H01G4/22—Dielectrics using combinations of dielectrics from more than one of groups H01G4/02 - H01G4/06 impregnated
- H01G4/221—Dielectrics using combinations of dielectrics from more than one of groups H01G4/02 - H01G4/06 impregnated characterised by the composition of the impregnant
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Chemical & Material Sciences (AREA)
- Power Engineering (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Manufacturing & Machinery (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
- Lubricants (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
The invention discloses a kind of soybean oil treatment process for capacitor impregnant, belong to capacitor processing technique field, specifically comprise the following steps:(1)Impurity elimination processing,(2)Alkalization dewaxing,(3)Acidification,(4)Purification processes.The method of the present invention can effectively improve the performance parameters such as the solidification point, dielectric coefficient, dielectric loss of soybean oil, enhance its usability and function as impregnating agent, and holistic approach processing is simple, can complete to improve operation under condition of normal pressure, there is good promotional value.
Description
Technical field
The invention belongs to capacitor processing technique field, and in particular to a kind of soybean oil processing for capacitor impregnant
Technique.
Background technology
Insulation for oil immersed apparatus, widely used earliest is mineral oil, because it is with good thermal conductivity, insulation
Property, and it is cheap.Nineteen thirties once adopted used flame retardancy insulating oil polychlorinated biphenyls, because it has severe toxicity,
Environment is polluted, has been disabled in the whole world.Thereafter the capacitor impregnant used both at home and abroad has:Alkylbenzene(AB oil), phenyl diformazan
Diphenylphosphino ethane(PXE, also known as diarylethane, S oil)With mono-/bis-benzyl toluene(M/DBT is also known as C101).Wherein alkylbenzene be
Polychlorinated biphenyls once adopted a kind of used synthetic insulating oil after forbidding use, its electric physical property is better than mineral oil and price is low
It is honest and clean, but its pumping property is poor, so as to limit the raising of capacitor work field strength.Phenyl xylyl ethane and mono-/bis-benzyl
The electric durability of base toluene can be excellent, inspiratory good, but they have a kind of niff, often make one to be difficult to bear in production
By.PXE and C101 is currently mainly used as impregnating agent in China's Power capacitor industry.
Above-mentioned several impregnating agent are all hypotoxicity and are unable to complete biodegradable.With the raising of people's environmental consciousness
With the requirement of sustainable development, electric property is good, nontoxic and fully biodegradable vegetable oil becomes international academic community again
The impregnating agent of concern.Find in practical applications, although vegetable oil(Such as soybean oil oil)Thermal coefficient of expansion, flash-point, ignition point,
Breakdown voltage etc. is all relatively good, but the parameter such as its solidification point, dielectric coefficient, dielectric loss is then not satisfactory, limits it and is used as dipping
The type and function of the capacitor of agent.
The content of the invention
The present invention is intended to provide a kind of soybean oil treatment process for capacitor impregnant, the soybean oil synthesis after processing
Characteristic is preferable, optimizes it and uses characteristic.
The present invention is achieved through the following technical solutions:
A kind of soybean oil treatment process for capacitor impregnant, includes the following steps:
(1)Impurity elimination is handled:
Soybean oil to be processed is put into hermetically sealed can, attapulgite, 0.2% salt of its gross mass 0.5% is added, constantly stirs
After mixing uniformly, after standing storage 3 ~ 4 days, it is filtered, it is spare after elimination impurity;
(2)Alkalization dewaxing:
By step(1)Soybean oil after processing is put into reaction kettle, its gross mass 0.5 ~ 1.5% is added into soybean oil removes wax
Liquid, it is 8.0 ~ 8.5 to adjust soybean oil pH value, is then constantly stirred 1 ~ 2h with 400 ~ 500 revs/min of rotating speed, then
It is 1 ~ 2h of freezing processing under conditions of -4 ~ -8 DEG C to be placed on temperature, and filtration treatment standby is carried out to it with oil filter after taking-up
With;It is described to go each material composition and corresponding percentage by weight in wax liquor as follows:7 ~ 10% pentamethylene, 4 ~ 6% n-hexanes, 2 ~ 5% 4
Cycloheptane, 8 ~ 12% ether, 3 ~ 5% urea, 2 ~ 4% neopelexes, surplus are water;
(3)Acidification:
By step(2)Soybean oil after processing is put into reaction kettle, and the glue that goes of its gross mass 1 ~ 2% is added into soybean oil, is adjusted
It is 6.0 ~ 6.5 to save soybean oil pH value, is then constantly stirred 2 ~ 3h with 500 ~ 600 revs/min of rotating speed, is used after taking-up
Oil filter carries out it spare after filtration treatment;It is described to go each material composition and corresponding percentage by weight in glue as follows:6~
10% zinc chloride, 4 ~ 7% manganese sulfates, 5 ~ 8% calcium sulfate, 1 ~ 2% yttrium nitrate, 10 ~ 15% sodium sulfate of polyethenoxy ether of fatty alcohol, surplus
For water;
(4)Purification processes:
By step(3)Soybean oil after processing is put into distiller, and it is 200 ~ 210 DEG C that heating, which keeps temperature, and holding vacuum is
60 ~ 70Pa, the condensed device of obtained component are collected after being cooled to 17 ~ 25 DEG C.
Further, step(1)Described in attapulgite granular size be 500 ~ 600 mesh.
Further, step(2)Described in the pressure of oil filter be 0.3 ~ 0.4MPa.
Further, step(3)Described in the pressure of oil filter be 0.4 ~ 0.5MPa.
The present invention has the advantages that:
The defects of present invention is directed to existing soybean oil has carried out it improvement processing, and alkalization dewaxing operation reduces its wax, phosphorus
The content of fat etc., acidification operate the content for reducing colloid, gossypol etc., and purification processes operation reduces moisture, saturated fat
The content of fat acid etc., improves the content of monounsaturated fatty acid, and reduce influences soybean oil to the full extent uses quality
Component content, improve the performance parameters such as its solidification point, dielectric coefficient, dielectric loss, enhance its usability as impregnating agent
And function, and holistic approach processing is simple, can complete to improve operation under condition of normal pressure, there is good promotional value.
Embodiment
Embodiment 1
A kind of soybean oil treatment process for capacitor impregnant, includes the following steps:
(1)Impurity elimination is handled:
Soybean oil to be processed is put into hermetically sealed can, attapulgite, 0.2% salt of its gross mass 0.5% is added, constantly stirs
After mixing uniformly, after standing storage 3 days, it is filtered, it is spare after elimination impurity;
(2)Alkalization dewaxing:
By step(1)Soybean oil after processing is put into reaction kettle, and the wax liquor of going of its gross mass 0.5% is added into soybean oil, is adjusted
It is 8.0 ~ 8.5 to save soybean oil pH value, is then constantly stirred 1h with 400 revs/min of rotating speed, then be placed on temperature
With oil filter it is carried out for freezing processing 1h under conditions of -4 DEG C, after taking-up spare after filtration treatment;It is described to go in wax liquor respectively
Material composition and corresponding percentage by weight are as follows:7% pentamethylene, 4% n-hexane, 2% quadricyclane, 8% ether, 3% urea, 2%
Neopelex, surplus are water;
(3)Acidification:
By step(2)Soybean oil after processing is put into reaction kettle, and the glue that goes of its gross mass 1% is added into soybean oil, is adjusted
Soybean oil pH value is 6.0 ~ 6.5, then 2h is constantly stirred with 500 revs/min of rotating speed, with oil filter pair after taking-up
It is spare after its progress filtration treatment;It is described to go each material composition and corresponding percentage by weight in glue as follows:6% zinc chloride, 4%
Manganese sulfate, 5% calcium sulfate, 1% yttrium nitrate, 10% sodium sulfate of polyethenoxy ether of fatty alcohol, surplus are water;
(4)Purification processes:
By step(3)Soybean oil after processing is put into distiller, and it is 200 ~ 205 DEG C that heating, which keeps temperature, and holding vacuum is
60 ~ 70Pa, the condensed device of obtained component are collected after being cooled to 17 ~ 25 DEG C.
Further, step(1)Described in attapulgite granular size be 500 mesh.
Further, step(2)Described in the pressure of oil filter be 0.3MPa.
Further, step(3)Described in the pressure of oil filter be 0.4MPa.
Embodiment 2
A kind of soybean oil treatment process for capacitor impregnant, includes the following steps:
(1)Impurity elimination is handled:
Soybean oil to be processed is put into hermetically sealed can, attapulgite, 0.2% salt of its gross mass 0.5% is added, constantly stirs
After mixing uniformly, after standing storage 4 days, it is filtered, it is spare after elimination impurity;
(2)Alkalization dewaxing:
By step(1)Soybean oil after processing is put into reaction kettle, and the wax liquor of going of its gross mass 1.5% is added into soybean oil, is adjusted
It is 8.0 ~ 8.5 to save soybean oil pH value, is then constantly stirred 2h with 500 revs/min of rotating speed, then be placed on temperature
With oil filter it is carried out for freezing processing 2h under conditions of -8 DEG C, after taking-up spare after filtration treatment;It is described to go in wax liquor respectively
Material composition and corresponding percentage by weight are as follows:10% pentamethylene, 6% n-hexane, 5% quadricyclane, 12% ether, 5% urea,
4% neopelex, surplus are water;
(3)Acidification:
By step(2)Soybean oil after processing is put into reaction kettle, and the glue that goes of its gross mass 2% is added into soybean oil, is adjusted
Soybean oil pH value is 6.0 ~ 6.5, then 3h is constantly stirred with 600 revs/min of rotating speed, with oil filter pair after taking-up
It is spare after its progress filtration treatment;It is described to go each material composition and corresponding percentage by weight in glue as follows:10% zinc chloride,
7% manganese sulfate, 8% calcium sulfate, 2% yttrium nitrate, 15% sodium sulfate of polyethenoxy ether of fatty alcohol, surplus are water;
(4)Purification processes:
By step(3)Soybean oil after processing is put into distiller, and it is 205 ~ 210 DEG C that heating, which keeps temperature, and holding vacuum is
60 ~ 70Pa, the condensed device of obtained component are collected after being cooled to 17 ~ 25 DEG C.
Further, step(1)Described in attapulgite granular size be 600 mesh.
Further, step(2)Described in the pressure of oil filter be 0.4MPa.
Further, step(3)Described in the pressure of oil filter be 0.5MPa.
Comparative example 1
This comparative example 1 compared with Example 1, without step(2)The dewaxing treatment that alkalizes operation, method and step in addition
All same.
Comparative example 2
This comparative example 2 compared with Example 2, without step(3)Acidification operates, and method and step in addition is homogeneous
Together.
Control group
The existing soybean oil as capacitor impregnant.
In order to contrast effect of the present invention, performance detection is carried out to the soybean oil after above-mentioned five kinds of method alignment processings, specifically
Correction data is as shown in table 1 below:
Table 1
Relative dielectric constant, 80 DEG C | Solidification point(℃) | tanδ, 80℃(%) | |
Embodiment 1 | 3.52 | -28 | 0.23 |
Embodiment 2 | 3.56 | -29 | 0.20 |
Comparative example 1 | 3.41 | -25 | 0.36 |
Comparative example 2 | 3.37 | -24 | 0.38 |
Control group | 3.12 | -20 | 0.58 |
The performances such as soybean oil freezing point, dielectric coefficient, dielectric loss it can be seen from upper table 1 after present invention processing have well
Improve, use value is higher.
Claims (4)
1. a kind of soybean oil treatment process for capacitor impregnant, it is characterised in that include the following steps:
(1)Impurity elimination is handled:
Soybean oil to be processed is put into hermetically sealed can, attapulgite, 0.2% salt of its gross mass 0.5% is added, constantly stirs
After mixing uniformly, after standing storage 3 ~ 4 days, it is filtered, it is spare after elimination impurity;
(2)Alkalization dewaxing:
By step(1)Soybean oil after processing is put into reaction kettle, its gross mass 0.5 ~ 1.5% is added into soybean oil removes wax
Liquid, it is 8.0 ~ 8.5 to adjust soybean oil pH value, is then constantly stirred 1 ~ 2h with 400 ~ 500 revs/min of rotating speed, then
It is 1 ~ 2h of freezing processing under conditions of -4 ~ -8 DEG C to be placed on temperature, and filtration treatment standby is carried out to it with oil filter after taking-up
With;It is described to go each material composition and corresponding percentage by weight in wax liquor as follows:7 ~ 10% pentamethylene, 4 ~ 6% n-hexanes, 2 ~ 5% 4
Cycloheptane, 8 ~ 12% ether, 3 ~ 5% urea, 2 ~ 4% neopelexes, surplus are water;
(3)Acidification:
By step(2)Soybean oil after processing is put into reaction kettle, and the glue that goes of its gross mass 1 ~ 2% is added into soybean oil, is adjusted
It is 6.0 ~ 6.5 to save soybean oil pH value, is then constantly stirred 2 ~ 3h with 500 ~ 600 revs/min of rotating speed, is used after taking-up
Oil filter carries out it spare after filtration treatment;It is described to go each material composition and corresponding percentage by weight in glue as follows:6~
10% zinc chloride, 4 ~ 7% manganese sulfates, 5 ~ 8% calcium sulfate, 1 ~ 2% yttrium nitrate, 10 ~ 15% sodium sulfate of polyethenoxy ether of fatty alcohol, surplus
For water;
(4)Purification processes:
By step(3)Soybean oil after processing is put into distiller, and it is 200 ~ 210 DEG C that heating, which keeps temperature, and holding vacuum is
60 ~ 70Pa, the condensed device of obtained component are collected after being cooled to 17 ~ 25 DEG C.
A kind of 2. soybean oil treatment process for capacitor impregnant according to claim 1, it is characterised in that step
(1)Described in attapulgite granular size be 500 ~ 600 mesh.
A kind of 3. soybean oil treatment process for capacitor impregnant according to claim 1, it is characterised in that step
(2)Described in the pressure of oil filter be 0.3 ~ 0.4MPa.
A kind of 4. soybean oil treatment process for capacitor impregnant according to claim 1, it is characterised in that step
(3)Described in the pressure of oil filter be 0.4 ~ 0.5MPa.
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CN104140889A (en) * | 2014-04-29 | 2014-11-12 | 江苏悦禧玫瑰科技有限公司 | Preparation method for rose absolute oil |
CN106479672A (en) * | 2016-10-26 | 2017-03-08 | 安徽飞达电气科技有限公司 | A kind of modification processing method of the Oleum Ricini for capacitor impregnant |
CN106571250A (en) * | 2016-10-26 | 2017-04-19 | 安徽飞达电气科技有限公司 | Plant oil mixed impregnating agent used for capacitor |
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2017
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CN1978597A (en) * | 2005-11-30 | 2007-06-13 | 中国石油化工股份有限公司 | Method for improving solvent dewaxing efficiency |
CN104140889A (en) * | 2014-04-29 | 2014-11-12 | 江苏悦禧玫瑰科技有限公司 | Preparation method for rose absolute oil |
CN104017645A (en) * | 2014-06-30 | 2014-09-03 | 河南科技大学 | Method for dewaxing peony seed oil by combination of surfactant-crystallization copolymerization and alcohol extraction |
CN106479672A (en) * | 2016-10-26 | 2017-03-08 | 安徽飞达电气科技有限公司 | A kind of modification processing method of the Oleum Ricini for capacitor impregnant |
CN106571250A (en) * | 2016-10-26 | 2017-04-19 | 安徽飞达电气科技有限公司 | Plant oil mixed impregnating agent used for capacitor |
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