CN107338098A - A kind of air compressor oil and preparation method thereof - Google Patents
A kind of air compressor oil and preparation method thereof Download PDFInfo
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- CN107338098A CN107338098A CN201710513615.8A CN201710513615A CN107338098A CN 107338098 A CN107338098 A CN 107338098A CN 201710513615 A CN201710513615 A CN 201710513615A CN 107338098 A CN107338098 A CN 107338098A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M169/00—Lubricating compositions characterised by containing as components a mixture of at least two types of ingredient selected from base-materials, thickeners or additives, covered by the preceding groups, each of these compounds being essential
- C10M169/04—Mixtures of base-materials and additives
- C10M169/048—Mixtures of base-materials and additives the additives being a mixture of compounds of unknown or incompletely defined constitution, non-macromolecular and macromolecular compounds
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- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2203/00—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
- C10M2203/04—Well-defined cycloaliphatic compounds
- C10M2203/045—Well-defined cycloaliphatic compounds used as base material
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- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/02—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
- C10M2205/026—Butene
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- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/02—Hydroxy compounds
- C10M2207/023—Hydroxy compounds having hydroxy groups bound to carbon atoms of six-membered aromatic rings
- C10M2207/026—Hydroxy compounds having hydroxy groups bound to carbon atoms of six-membered aromatic rings with tertiary alkyl groups
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- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/10—Carboxylix acids; Neutral salts thereof
- C10M2207/14—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings
- C10M2207/144—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings containing hydroxy groups
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- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/10—Carboxylix acids; Neutral salts thereof
- C10M2207/16—Naphthenic acids
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/40—Fatty vegetable or animal oils
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2211/00—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
- C10M2211/08—Halogenated waxes
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- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
- C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
- C10M2219/044—Sulfonic acids, Derivatives thereof, e.g. neutral salts
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- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
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- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
- C10M2223/047—Thioderivatives not containing metallic elements
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- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/02—Groups 1 or 11
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- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/04—Groups 2 or 12
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/02—Pour-point; Viscosity index
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- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/04—Detergent property or dispersant property
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- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/06—Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
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- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/10—Inhibition of oxidation, e.g. anti-oxidants
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- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/12—Inhibition of corrosion, e.g. anti-rust agents or anti-corrosives
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Abstract
A kind of air compressor oil, including modified vegetable oil, base oil, antioxidant, antirust agent, antiwear additive, detersive and dispersant, mass percent of the base oil in air compressor oil is 30%~40%, mass percent of the antioxidant in air compressor oil is 1%~5%, mass percent of the antirust agent in air compressor oil is 1%~5%, antiwear additive is 1%~5% in the mass percent of air compressor oil, detersive is 1%~2% in the mass percent of air compressor oil, dispersant is 1%~2% in the mass percent of air compressor oil, surplus is modified vegetable oil;Defoamer is also added with, the concentration of defoamer is 50 100ppm of modified vegetable oil, base oil, antioxidant, antirust agent, antiwear additive, detersive and dispersant quality sum.Present invention also offers the preparation method of above-mentioned air compressor oil.The open flash point of the present invention can be to 270 300 DEG C, below 40 DEG C of pour point.
Description
Technical field
The present invention relates to chemical field, more particularly to air compressor oil, particularly a kind of air compressor oil and its system
Preparation Method.
Background technology
Air compressor oil, refer to for the air compressor lubrication of movement cylinder part and air bleeding valve in operation, with
Effectively protection screw rod, bearing, the part such as gear, and played by oil circulation and parts are cooled down, antirust and peace and quiet effect, simultaneously
For a kind of oil product to seal to screw rod and housing.Because air compressor is constantly in high pressure, high temperature and has cold
In environment existing for condensate, therefore air compressor oil should have excellent high temperature oxidation resistance, low tendency to soot, excellent
Viscosity temperature characteristic, good oil-water separativeness and rustless property.Air compressor oil is broadly divided into mineral type and synthesis type at present
Two major classes, the former, can be bad there is high-temperature oxidation stability as conventional air compressor oil, and product service life is not grown
(general 2000h or so), there is high tendency to soot, changed oil when so causing using machine frequently, energy consumption is big, is unfavorable for saving
Energy, environmental protection, the novel economizer development idea of sustainable development.It is (general that the latter can effectively improve oil product service life problem
6000h or so), can also solve the carbon-collecting problem of compressor in operation, still, due to making using synthetic ester and polyalphaolefin
The cost for causing product in use for raw material is too high, considerably increases the cost using air compressor oil so that product exists
Cost performance in use is not high, and the ratio that market uses is not high all the time.
Poly-alpha olefins (PAO) be by ethene it is aggregated reaction alhpa olefin is made, it is further aggregated and hydrogenation and be made.
It is the most frequently used synthetic lubricant base oil, and use range is most extensive.Poly alpha olefine synthetic oil (abbreviation PAO) has good
Viscosity temperature characteristic and low temperature flow, it is to prepare base oil high-grade, that special lube is ideal.
The content of the invention
The technical problems to be solved by the invention are to provide a kind of air compressor oil, described this air compressor oil
Solving air compressor oil high-temperature oxidation stability of the prior art can be bad, and product service life is not long, high carbon deposit
Question of The Tendency and the high technical problem of operating cost.
The invention provides a kind of air compressor oil, including it is modified vegetable oil, base oil, antioxidant, antirust agent, wear-resistant
Agent, detersive and dispersant, described base oil are PAO, mass percent of the described base oil in air compressor oil
For 30%~40%, mass percent of the described antioxidant in air compressor oil is 1%~5%, described antirust agent
Mass percent in air compressor oil is 1%~5%, mass percent of the described antiwear additive in air compressor oil
For 1%~5%, described detersive is 1%~2% in the mass percent of air compressor oil, and described dispersant is in sky
The mass percent of air compressor oil is 1%~2%, and surplus is described modified vegetable oil;Defoamer is also added with, it is described
The concentration of defoamer is modified vegetable oil, base oil, antioxidant, antirust agent, antiwear additive, detersive and dispersant quality sum
50-100ppm;
Further, the formula of described modified vegetable oil is as follows:
Wherein R1、R2、R3Respectively carbon number is any one in 12-23 alkyl or alkylene.
Further, described antioxidant is 2,6-di-tert-butylphenol or 2,6-BHT or phenolic ester type
Any one in antioxidant.
Further, described antirust agent is any one in barium mahogany sulfonate, petroleum sodium sulfonate or zinc naphthenate.
Further, described antiwear additive is (appointing in chlorinated paraffin, trimethyl phosphate phenol or trithiophenyl phosphate
Meaning is a kind of.
Further, described detersive is polyisobutene sulphur barium phosphate salt, alkyl sodium salicylate or sulfenyl phenolate
Any one in calcium.
Further, described dispersant is any in mono butonediimide ashless dispersant agent or trimethyl phosphate phenol
It is a kind of.
Further, described defoamer is non-silicon composite anti-foam agent.
Present invention also offers the method for preparing above-mentioned air compressor oil, comprise the following steps:
The step of step 1) prepares modified vegetable oil including one, two or more any vegetable seed is selected first
Oil, peanut oil, cotton seed oil, olive oil are raw material, first carry out hydrofinishing, in unifining process, the reaction pressure of reactor
For 6~12MPa, reaction temperature is 200~400 DEG C, and the total air speed of oil-feed be 0.5~1.0/h, reaction hydrogen to oil volume ratio for 600~
800, the catalyst in described unifining process is Ni-W/AL2O3Or Ni-Mo-Co/AL2O3, then carry out Atmospheric vacuum steaming
Evaporate, reduced pressure distillation process is 1~65mmHg of residual voltage, cuts 300~460 DEG C of atmospheric distillate, obtains hydrogenated vegetable oil;Then
An alkali cleaning, the NaOH solution for being 6%-10% with concentration are carried out, dosage is to be modified the 2%-6% of basic weight of oil, temperature control
System after washing 60-90min, after oil water separator, is once washed at 70-80 DEG C into next reactor, is used
Measure and 60-90min is washed, after oil water separator at 70-80 DEG C for the 5%-10% of the basic weight of oil of modification, temperature control;
Secondary alkali cleaning is carried out, uses the aqueous solution to be washed for the salt of alkalescence, the Na for being 5%-8% with concentration2CO3Solution, dosage are to change
Property basis weight of oil 1%-5%, temperature control is at 70-80 DEG C, after washing 60-90min, after oil water separator, enters
Once washed in next reactor, dosage for modified basic weight of oil 5%-10%, temperature control at 70-80 DEG C,
After washing 60-90min, after oil water separator, modified vegetable oil is obtained;
Step 2) according to mass percent weigh PAO, modified vegetable oil, antioxidant, antirust agent, antiwear additive, detersive, point
Powder and defoamer, PAO and modified vegetable oil are then first added in a reactor, 80 DEG C -100 DEG C are stirred 20~50 points
Zhong Hou, antioxidant, antirust agent, antiwear additive, detersive, dispersant and defoamer are added, mix and obtain air compressor oil.
The preparation method of the air compressor oil of the present invention is to add vegetable oil in a kettle, after hydrofinishing,
Pass through alkali cleaning twice again and wash twice, obtain modified vegetable oil;Hydrocarbon (PAO) will be synthesized and modified vegetable oil squeezes into reactor
In, after stirring, add antioxidant, antirust agent, antiwear additive, detersive, dispersant and defoamer.Air compressor of the present invention
Oil has good high temperature oxidation resistance, low tendency to soot, excellent viscosity temperature characteristic, good oil-water separativeness and antirust
Performance, modified vegetable oil is added in addition, greatly reduce the cost using air compressor oil, meet energy-saving and environmental protection, can hold
The novel economizer development idea of supervention exhibition.This product drain period performance is considerably longer than conventional air compressor oil.
The present invention compares with prior art, and its effect is positive and obvious.A kind of air compressor oil tool of the present invention
Have the advantage that:
1. this product open flash point can arrive 270-300 DEG C, below -40 DEG C of pour point, the opening of conventional air compressor oil is dodged
For point at 220-240 DEG C, the security performance of this product is high.
2. the oxidation stability (rotary bomb oxidation test) of this product can reach more than 2500h, traditional product oxidation stability exists
Between 1000h-1200h.
3. the oil product of this product can reach more than 8000h in 85 DEG C -95 DEG C of usage time, traditional oil product is in 2000h-
Between 4000h, oily periodic performance is considerably longer than conventional air compressor oil, has saved production cost.
4. this product adds reproducible modified vegetable oil, cost is saved, safety and environmental protection, has met sustainable development
Strategy.
Embodiment:
Embodiment 1
The invention provides a kind of air compressor oil, by modified vegetable oil, base oil PAO, adds antioxidant, antirust
Agent, antiwear additive, detersive, dispersant and defoamer composition.Quality hundred of the described modified vegetable oil in air compressor oil
Divide than being 55%, modified vegetable oil is made up of rapeseed oil and peanut oil.Described rapeseed oil is in described modified vegetable oil
Mass percent is 60%, and mass percent of the described peanut oil in described modified vegetable oil is 40%, is first added
Hydrogen refines, and the reaction pressure of reactor is 8MPa in unifining process, and reaction temperature is 300 DEG C, and the total air speed of oil-feed is 0.8/
H, reaction hydrogen to oil volume ratio are 700, and the catalyst in described unifining process is Ni-W/AL2O3, then carry out Atmospheric vacuum
Distillation, reduced pressure distillation process is 1~65mmHg of residual voltage, cuts 300~460 DEG C of atmospheric distillate, obtains hydrogenated vegetable oil.So
The NaOH solution that concentration is 8% is first used afterwards, and dosage is the 5% of improved plant weight of oil, and temperature control washs 80min at 80 DEG C
Afterwards, after by oil water separator, washed into next reactor, dosage is the 8% of improved plant weight of oil, temperature
Control is at 70 DEG C, after washing 60min, after oil water separator;Carry out secondary alkali cleaning, use concentration for 8% Na2CO3It is molten
Liquid, dosage are the 5% of improved plant weight of oil, and temperature control is at 75 DEG C, after washing 60min, after oil water separator, are entered
Once washed in next reactor, dosage is the 8% of improved plant weight of oil, and temperature control washs 70min at 70 DEG C
Afterwards, after by oil water separator, modified vegetable oil is obtained.Mass percents of the described PAO in air compressor oil be
35%, after taking 55% modified vegetable oil and 35% PAO to be stirred 30 minutes at 90 DEG C, add antioxidant, antirust agent, wear-resistant
Agent, detersive, dispersant and defoamer.Mass percents of the described antioxidant A in air compressor oil is 1%, described
Mass percents of the antioxidant B in air compressor oil be 1%, matter of the described antirust agent A in air compressor oil
It is 1% to measure percentage, and mass percents of the described antirust agent B in air compressor oil is 2%, and described antiwear additive A exists
The mass percent of air compressor oil is 1%, and described antiwear additive B is 2% in the mass percent of air compressor oil, institute
The detersive A stated is 1% in the mass percent of air compressor oil, quality of the described dispersant A in air compressor oil
Percentage is 1%, and also added with defoamer, the concentration of described defoamer is modified vegetable oil, base oil, antioxidant, antirust
Agent, antiwear additive, the 60ppm of detersive and dispersant quality sum.
Further, described antioxidant A is 2, and 6-di-tert-butylphenol, antioxidant B are 2,6-BHT.
Further, described antirust agent A is that T-701 (barium mahogany sulfonate), antirust agent B are T-702 (petroleum sodium sulfonate).
Further, described antiwear additive A is that T-301 (chlorinated paraffin), antiwear additive B are T-306 (trimethyl phosphate phenol).
Further, described detersive A is T-108 (polyisobutene sulphur barium phosphate salt).
Further, described dispersant A is T-151 (mono butonediimide ashless dispersant agent).
Further, described defoamer is 2# defoamers (non-silicon composite anti-foam agent).
Every physical and chemical index is shown in Table 1.
Embodiment 2
The invention provides a kind of air compressor oil, by oily based on modified vegetable oil, PAO, addition antioxidant, antirust
Agent, antiwear additive, detersive, dispersant and defoamer composition.Quality hundred of the described modified vegetable oil in air compressor oil
Divide than being 51%, modified vegetable oil is mixed by rapeseed oil, peanut oil and cotton seed oil.Described rapeseed oil is in described improved plant
Mass percent in oil is 50%, and mass percent of the described peanut oil in described modified vegetable oil is 30%, institute
Mass percent of the cotton seed oil stated in described modified vegetable oil is 20%, first carries out hydrofinishing, unifining process
The reaction pressure of middle reactor is 10MPa, and reaction temperature is 250 DEG C, and the total air speed of oil-feed is 0.6/h, and reaction hydrogen to oil volume ratio is
650, the catalyst in described unifining process is Ni-Mo-Co/AL2O3, atmospheric and vacuum distillation is then carried out, is evaporated under reduced pressure work
Skill is 1~65mmHg of residual voltage, cuts 300~460 DEG C of atmospheric distillate, obtains hydrogenated vegetable oil.Then it is 9% with concentration
NaOH solution, dosage are the 4% of improved plant weight of oil, and temperature control after washing 70min, passes through oil water separator at 80 DEG C
Afterwards, into being washed in next reactor, dosage is the 7% of improved plant weight of oil, and temperature control is at 70 DEG C, washing
After 60min, after oil water separator;Carry out secondary alkali cleaning, use concentration for 8% Na2CO3Solution, dosage are improved plant
The 4% of weight of oil, temperature control after washing 60min, after oil water separator, are entered at 75 DEG C into next reactor
Row is once washed, and dosage is the 10% of improved plant weight of oil, and temperature control after washing 70min, passes through water-oil separating at 70 DEG C
After device, modified vegetable oil is obtained.Mass percents of the described PAO in air compressor oil is 30%, takes 51% modification
Vegetable oil and 30% PAO add antioxidant, antirust agent, antiwear additive, detersive, dispersant after being stirred 30 minutes at 100 DEG C
And defoamer.Mass percents of the described antioxidant A in air compressor oil is 1%, and described antioxidant B is in air pressure
Mass percent in contracting machine oil is 2%, and mass percents of the described antioxidant C in air compressor oil is 2%, described
Mass percents of the antirust agent A in air compressor oil be 1%, matter of the described antirust agent B in air compressor oil
It is 2% to measure percentage, and mass percents of the described antirust agent C in air compressor oil is 2%, and described antiwear additive A exists
The mass percent of air compressor oil is 1%, and described antiwear additive B is 2% in the mass percent of air compressor oil, institute
The antiwear additive C stated is 2% in the mass percent of air compressor oil, quality of the described detersive A in air compressor oil
Percentage is 1%, and described detersive B is 1% in the mass percent of air compressor oil, and described dispersant A is in air
The mass percent of compressor oil is 1%, and described dispersant B is 1% in the mass percent of air compressor oil, described
Defoamer is the 80ppm of modified vegetable oil, base oil, antioxidant, antirust agent, antiwear additive, detersive and dispersant quality sum.
Further, described antioxidant A is 2, and 6-di-tert-butylphenol, antioxidant B are 2,6-BHT,
Antioxidant C is phenolic ester type antioxidant.
Further, described antirust agent A be T-701 (barium mahogany sulfonate), antirust agent B be T-702 (petroleum sodium sulfonate),
Antirust agent C is T-704 (zinc naphthenate).
Further, described antiwear additive A be T-301 (chlorinated paraffin), antiwear additive B be T-306 (trimethyl phosphate phenol),
Antiwear additive C is T-309 (trithiophenyl phosphate).
Further, described detersive A is that T-108 (polyisobutene sulphur barium phosphate salt), detersive B are T-109 (alkyl
Calcium salicylate).
Further, described dispersant A is T-151 (mono butonediimide ashless dispersant agent), dispersant B T-155
(trimethyl phosphate phenol).
Further, described defoamer is 2# defoamers (non-silicon composite anti-foam agent).
Every physical and chemical index is shown in Table 1.
Embodiment 3
The invention provides a kind of air compressor oil, by oily based on modified vegetable oil, PAO, addition antioxidant, antirust
Agent, antiwear additive, detersive, dispersant and defoamer composition.Quality hundred of the described modified vegetable oil in air compressor oil
Divide than being 50%, modified vegetable oil is mixed by rapeseed oil, peanut oil, cotton seed oil and olive oil.Described rapeseed oil is described
Mass percent in modified vegetable oil is 40%, and mass percent of the described peanut oil in described modified vegetable oil is
20%, mass percent of the described cotton seed oil in described modified vegetable oil is 20%, and described olive oil is described
Mass percent in modified vegetable oil is 20%.First carry out hydrofinishing, the reaction pressure of reactor in unifining process
For 7MPa, reaction temperature is 350 DEG C, and the total air speed of oil-feed is 0.7/h, and reaction hydrogen to oil volume ratio is 650, described hydrofinishing
During catalyst be Ni-Mo-Co/AL2O3, atmospheric and vacuum distillation is then carried out, reduced pressure distillation process is 1~65mmHg of residual voltage,
300~460 DEG C of atmospheric distillate is cut, obtains hydrogenated vegetable oil.With the NaOH solution that concentration is 10%, temperature control is 80
DEG C, after washing 60min, after oil water separator, washed into next reactor, dosage is modified vegetable oil weight
The 6% of amount, temperature control is at 70 DEG C, after washing 70min, after oil water separator;Carry out secondary alkali cleaning, use concentration for
8% Na2CO3Solution, dosage are the 4% of improved plant weight of oil, and temperature control after washing 60min, passes through profit at 75 DEG C
After separator, once washed into next reactor, dosage is the 10% of improved plant weight of oil, and temperature control exists
70 DEG C, after washing 70min, after oil water separator, obtain modified vegetable oil.Described PAO is in air compressor oil
Mass percent is 40%, takes 50% modified vegetable oil and 40% PAO to add antioxygen after being stirred 30 minutes at 80 DEG C
Agent, antirust agent, antiwear additive, detersive, dispersant and defoamer.Quality hundred of the described antioxidant A in air compressor oil
Divide than being 1%, mass percents of the described antioxidant C in air compressor oil is 1%, and described antirust agent A is in air
Mass percent in compressor oil is 1%, and mass percents of the described antirust agent C in air compressor oil is 1%, institute
The antiwear additive A stated is 1% in the mass percent of air compressor oil, quality of the described antiwear additive C in air compressor oil
Percentage is 1%, and described detersive B is 2% in the mass percent of air compressor oil, and described dispersant B is in air
The mass percent of compressor oil is 2%, and also added with defoamer, described defoamer is modified vegetable oil, base oil, antioxygen
Agent, antirust agent, antiwear additive, the 70ppm of detersive and dispersant quality sum.
Further, described antioxidant A is 2, and 6-di-tert-butylphenol, antioxidant C are phenolic ester type antioxidant.
Further, described antirust agent A is that T-701 (barium mahogany sulfonate), antirust agent C are T-704 (zinc naphthenate).
Further, described antiwear additive A be T-301 (chlorinated paraffin), antiwear additive C be T-306 (trimethyl phosphate phenol),
Antiwear additive C is T-309 (trithiophenyl phosphate).
Further, detersive B is T-109 (alkyl sodium salicylate).
Further, dispersant B is T-155 (trimethyl phosphate phenol).
Further, described defoamer is 2# defoamers (non-silicon composite anti-foam agent).
Every physical and chemical index is shown in Table 1.
Embodiment 4
The invention provides a kind of air compressor oil, by oily based on modified vegetable oil, PAO, addition antioxidant, antirust
Agent, antiwear additive, detersive, dispersant and defoamer composition.Quality hundred of the described modified vegetable oil in air compressor oil
Divide than being 44%, be made up of the mixing of peanut oil, cotton seed oil and olive oil.Peanut oil described in modified vegetable oil is in described modification
Mass percent in vegetable oil is 40%, and mass percent of the described cotton seed oil in described modified vegetable oil is
30%, mass percent of the described olive oil in described modified vegetable oil is 30%.First carry out hydrofinishing, hydrogenation essence
The reaction pressure of reactor is 11MPa during system, and reaction temperature is 300 DEG C, and the total air speed of oil-feed is 0.6/h, reactive hydrogen oil body
For product than being 600, the catalyst in described unifining process is Ni-W/AL2O3, atmospheric and vacuum distillation is then carried out, is evaporated under reduced pressure
Technique is 1~65mmHg of residual voltage, cuts 300~460 DEG C of atmospheric distillate, obtains hydrogenated vegetable oil.Then it is 8% with concentration
NaOH solution, dosage be improved plant weight of oil 5%, temperature control at 80 DEG C, wash 80min after, pass through water-oil separating
After device, washed into next reactor, dosage is the 8% of improved plant weight of oil, and temperature control is at 70 DEG C, washing
After 60min, after oil water separator;Carry out secondary alkali cleaning, use concentration for 8% Na2CO3Solution, dosage are improved plant
The 5% of weight of oil, temperature control after washing 60min, after oil water separator, are entered at 75 DEG C into next reactor
Row is once washed, and dosage is the 8% of improved plant weight of oil, and temperature control after washing 70min, passes through water-oil separating at 70 DEG C
After device, modified vegetable oil is obtained.Mass percents of the described PAO in air compressor oil is 40%, takes 44% modification
Vegetable oil and 40% PAO add antioxidant, antirust agent, antiwear additive, detersive, dispersant after being stirred 30 minutes at 100 DEG C
And defoamer.Mass percents of the described antioxidant B in air compressor oil is 2%, and described antioxidant C is in air pressure
Mass percent in contracting machine oil is 2%, and mass percents of the described antirust agent B in air compressor oil is 2%, described
Mass percents of the antirust agent C in air compressor oil be 2%, quality of the described antiwear additive B in air compressor oil
Percentage is 2%, and described antiwear additive C is 2% in the mass percent of air compressor oil, and described detersive B is in air
The mass percent of compressor oil is 2%, and described dispersant B is 2% in the mass percent of air compressor oil, is also added
Added with defoamer, described defoamer is modified vegetable oil, base oil, antioxidant, antirust agent, antiwear additive, detersive and disperseed
The 90ppm of agent quality sum.
Further, antioxidant B is 2, and 6-BHT, antioxidant C are phenolic ester type antioxidant.
Further, antirust agent B is that T-702 (petroleum sodium sulfonate), antirust agent C are T-704 (zinc naphthenate).
Further, antiwear additive B is that T-306 (trimethyl phosphate phenol), antiwear additive C are T-309 (trithiophenyl phosphate).
Further, detersive B is T-109 (alkyl sodium salicylate).
Further, dispersant B is T-155 (trimethyl phosphate phenol).
Further, described defoamer is 2# defoamers (non-silicon composite anti-foam agent).
Every physical and chemical index is shown in Table 1.
Table 1
The present invention is relatively shown in Table 2 with shell air compressor oil oil, each physical and chemical performance of conventional air compressor oil
As can be seen from Table 2 with, the present invention compared with shell air compressor oil, there is high flash-point and low pour point, peace
Full performance is higher, and the time of oxidation stability is longer in addition, has more preferable antioxygenic property;The present invention and conventional mineral air
Compressor oil is compared, and has higher flash-point and pour point, therefore substantially increase security performance;The oxidation stability of this product shows
Better than traditional product, therefore there is more preferable Oxidation Stability and longer service life, demulsification performance is better than biography in addition
System product, has good oil-water separativeness.
The beneficial effects of the present invention are:First, compared with conventional air compressor oil, this product adds reproducible
Vegetable oil, security performance environmental protection, has saved the production cost of air compressor oil;Secondly, this product part index number is due to the world
Import brand, technological precedence;3rd, this product is superior to national standard and the sky using produced in conventional processes on indices
Air compressor oil, drain period significantly extend the stability and security for substantially increasing compressor operation, improve pneumatics
The service life of machine, has saved operating cost.
Claims (9)
- A kind of 1. air compressor oil, it is characterised in that:Including modified vegetable oil, base oil, antioxidant, antirust agent, antiwear additive, Detersive and dispersant, described base oil are PAO, and mass percent of the described base oil in air compressor oil is 30%~40%, mass percent of the described antioxidant in air compressor oil is 1%~5%, and described antirust agent exists Mass percent in air compressor oil is 1%~5%, and described antiwear additive is in the mass percent of air compressor oil 1%~5%, described detersive is 1%~2% in the mass percent of air compressor oil, and described dispersant is in air The mass percent of compressor oil is 1%~2%, and surplus is described modified vegetable oil;Defoamer is also added with, described disappears The concentration of infusion is modified vegetable oil, base oil, antioxidant, antirust agent, antiwear additive, detersive and dispersant quality sum 50-100ppm。
- 2. air compressor oil according to claim 1, it is characterised in that:The formula of described modified vegetable oil is as follows:Wherein R1、R2、R3Respectively carbon number is any one in 12-23 alkyl or alkylene.
- 3. air compressor oil according to claim 1, it is characterised in that:Described antioxidant is 2,6-di-t-butyl Any one in phenol or 2,6-BHT or phenolic ester type antioxidant.
- 4. air compressor oil according to claim 1, it is characterised in that:Described antirust agent is barium mahogany sulfonate, stone Any one in oily sodium sulfonate or zinc naphthenate.
- 5. air compressor oil according to claim 1, it is characterised in that:Described antiwear additive is (chlorinated paraffin, phosphoric acid Any one in trimethyl phenol or trithiophenyl phosphate.
- 6. air compressor oil according to claim 1, it is characterised in that:Described detersive is polyisobutene sulphur phosphoric acid Any one in barium salt, alkyl sodium salicylate or sulfurized alkylphenol calcium.
- 7. air compressor oil according to claim 1, it is characterised in that:Described dispersant be mono butonediimide without Any one in grey dispersant or trimethyl phosphate phenol.
- 8. air compressor oil according to claim 1, it is characterised in that:Described defoamer is the compound anti-bubble of non-silicon Agent.
- A kind of 9. method for preparing the air compressor oil described in claim 1, it is characterised in that:Comprise the following steps:The step of step 1) prepares modified vegetable oil including one, two or more any rapeseed oil, flower is selected first Oil generation, cotton seed oil, olive oil are raw material, first carry out hydrofinishing, in unifining process, the reaction pressure of reactor for 6~ 12MPa, reaction temperature are 200~400 DEG C, and the total air speed of oil-feed is 0.5~1.0/h, and reaction hydrogen to oil volume ratio is 600~800, institute Catalyst in the unifining process stated is Ni-W/AL2O3Or Ni-Mo-Co/AL2O3, atmospheric and vacuum distillation is then carried out, is subtracted Pressure distillation technique is 1~65mmHg of residual voltage, cuts 300~460 DEG C of atmospheric distillate, obtains hydrogenated vegetable oil;Then carry out Alkali cleaning, the NaOH solution for being 6%-10% with concentration, to be modified the 2%-6% of basic weight of oil, temperature control exists dosage 70-80 DEG C, after washing 60-90min, after oil water separator, once washed into next reactor, dosage is The 5%-10% of modified basic weight of oil, temperature control wash 60-90min, after oil water separator at 70-80 DEG C;Carry out Secondary alkali cleaning, the aqueous solution is used to be washed for the salt of alkalescence, the Na for being 5%-8% with concentration2CO3Solution, dosage are modified base The 1%-5% of plinth weight of oil, temperature control is at 70-80 DEG C, and after washing 60-90min, after oil water separator, entrance is next Once washed in individual reactor, dosage is the 5%-10% of modified basic weight of oil, and temperature control is at 70-80 DEG C, washing After 60-90min, after oil water separator, modified vegetable oil is obtained;Step 2) weighs PAO, modified vegetable oil, antioxidant, antirust agent, antiwear additive, detersive, dispersant according to mass percent And defoamer, PAO and modified vegetable oil are then first added in a reactor, after 80 DEG C -100 DEG C are stirred 20~50 minutes, Antioxidant, antirust agent, antiwear additive, detersive, dispersant and defoamer are added, mixes and obtains air compressor oil.
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Cited By (2)
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---|---|---|---|---|
CN108977263A (en) * | 2018-09-17 | 2018-12-11 | 上海中孚特种油品有限公司 | A kind of environment-friendly type synthetic ester air compressor oil and preparation method thereof |
CN109722889A (en) * | 2019-01-02 | 2019-05-07 | 上海中孚特种油品有限公司 | A kind of environment-friendly type spinning oil and preparation method thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101724489A (en) * | 2008-10-15 | 2010-06-09 | 中国石油天然气股份有限公司 | Air compressor oil composition |
CN104250574A (en) * | 2013-06-26 | 2014-12-31 | 中国石油化工股份有限公司 | Compressor oil composition and use thereof |
CN105754693A (en) * | 2016-04-26 | 2016-07-13 | 苏州思创源博电子科技有限公司 | Method for preparing environment-friendly transformer oil |
CN106190501A (en) * | 2016-08-05 | 2016-12-07 | 上海中孚特种油品有限公司 | A kind of high flashover point transformer oil and preparation method thereof |
-
2017
- 2017-06-29 CN CN201710513615.8A patent/CN107338098B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101724489A (en) * | 2008-10-15 | 2010-06-09 | 中国石油天然气股份有限公司 | Air compressor oil composition |
CN104250574A (en) * | 2013-06-26 | 2014-12-31 | 中国石油化工股份有限公司 | Compressor oil composition and use thereof |
CN105754693A (en) * | 2016-04-26 | 2016-07-13 | 苏州思创源博电子科技有限公司 | Method for preparing environment-friendly transformer oil |
CN106190501A (en) * | 2016-08-05 | 2016-12-07 | 上海中孚特种油品有限公司 | A kind of high flashover point transformer oil and preparation method thereof |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108977263A (en) * | 2018-09-17 | 2018-12-11 | 上海中孚特种油品有限公司 | A kind of environment-friendly type synthetic ester air compressor oil and preparation method thereof |
CN108977263B (en) * | 2018-09-17 | 2021-03-26 | 上海中孚特种油品有限公司 | Environment-friendly synthetic ester air compressor oil and preparation method thereof |
CN109722889A (en) * | 2019-01-02 | 2019-05-07 | 上海中孚特种油品有限公司 | A kind of environment-friendly type spinning oil and preparation method thereof |
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Address after: 201823 No. 2122, Waiqian Road, Jiading District, Shanghai Patentee after: Shanghai Zhongfu Oil Group Co.,Ltd. Address before: 201823 No. 2122, Waiqian Road, Jiading District, Shanghai Patentee before: SHANGHAI ZHONGFU SPECIAL OIL Co.,Ltd. |