Wear-resistant antioxygen hydraulic oil compound formula and its preparation process
Technical field
The present invention relates to technical field of lubricating oil.It is more particularly related to which wear-resistant antioxygen hydraulic oil complexing agent is matched
Side and its preparation process.
Background technique
Hydraulic oil is an important component of hydraulic technique, in hydraulic system by it come realize energy conversion,
Transmitting and control.The effects of also playing the lubrication, antirust, anti-corrosion, cooling of system simultaneously.People see the oil pump in hydraulic system
Make heart, hydraulic oil is exactly the blood of system.Hydraulic system is widely used in various mechanical equipments, driven by a motor, passes through pump
Hydraulic oil is completed into the conversion from mechanical energy to pressure energy.
Existing antiwear hydraulic oil requires production according to national standards, not to the detergent-dispersant performance of oil product in its standard,
The wear scar diameter of abrasion resistance and the maximum nonseizure load P of extreme pressure propertyB, the specific data demand of propositions such as integrated abrasion value,
So differing greatly on the market according to the hydraulic oil quality that national standard is produced.The detergent-dispersant performance of oil product to hydraulic device also very
Important, gap very little when many equipment parts work in a high voltage state bears biggish fretting wear risk.Hydraulic oil uses
Water may be touched in the process, or is influenced by high temperature, and anticorrosive antioxygen is also a critically important index.So one
The antiwear hydraulic oil of money top grade will have preferable cleansing performance and antioxygen, anticorrosive, abrasion resistance.
Summary of the invention
It is an object of the present invention to provide wear-resistant antioxygen hydraulic oil compound formula and its preparation process, complexing agent cooperations
The hydraulic oil of base oil preparation has excellent antioxygen corrosion resistance and excellent abrasion resistance, while having preferable peace and quiet
Dispersion performance.
In order to realize these purposes and other advantages according to the present invention, provides wear-resistant antioxygen hydraulic oil complexing agent and match
Side, including following component by mass percentage:
Long-chain primary alcohols zinc dialkyl dithiophosphate 10-25%, di-tert-butyl p-cresol 10-30%, alkylated diphenylamine
0-15%, tricresyl phosphate 10-25%, high base number calcium alkylbenzenesulfonate 1-10%, double focusing isobutene imidodicarbonic diamide 1-10%, ten
Dialkylene succinic acid half ester 0-1%, alkaline dinonyl naphthalene sulfonate barium 1-8%, benzotriazole octadecylamine salt 1-3%, base oil 10~
30%.
The present invention also provides a kind of preparation processes of wear-resistant antioxygen hydraulic oil compound formula, by above-mentioned hydraulic oil complexing agent
It is added in reaction kettle by the mass percent of each component in its formula, is warming up to 70-80 DEG C, stirs 30-60 minutes, it is cooling.
Preferably, the reaction kettle includes:
Outer housing is sealing structure, is fixed at intervals with horizontal first partition and second inside the outer housing up and down
Partition will be divided into from top to bottom the first reaction chamber, the second reaction chamber and third reaction chamber, the second partition inside outer housing
It is upper that there are multiple through-holes;
Agitator is set in the first reaction chamber for multiple and uniform intervals, and the agitator is vertically arranged and upper end
Sealing, lower ending opening, the agitator lower end is fixed in first partition and lower ending opening perforation first partition connection described the
Two reaction chambers are provided with blender in the agitator;
Agitating shaft, is vertically positioned in outer housing and the central axis weight of the central axis of the agitating shaft and outer housing
It closes, the agitating shaft lower end is located at the lower end of third reaction chamber, and the agitating shaft upper end hermetically passing second partition is located at second
The upper end of reaction chamber, the part that the agitating shaft is located in the second reaction chamber are provided with external screw thread, and the agitating shaft is located at third
Part in reaction chamber is additionally provided with paddle;
Auxiliary body comprising sleeve, more connecting rods and multiple sealing blocks, the sleeve have internal screw thread and be matched with
On the external screw thread of the agitating shaft, more connecting rod levels are uniformly arranged along the circumferential direction of the sleeve, and multiple sealing blocks one are a pair of
More connection boom ends should be fixed on, and multiple sealing blocks correspond to the lower ending opening for sealing multiple agitators just.
Preferably, the second partition extends centrally out setting multi-turn through-hole ring along it, and every ring through hole ring includes
Circumferentially uniform intervals are arranged multiple through-holes, the reaction kettle further include:
Saddle, for inverted L shape and including perpendicular support and stull, the perpendicular support is located at multiple agitators outsides, under the perpendicular support
End be fixed on second partition, the stull towards outer housing central axis, between the stull upper surface and first partition
Spacing be slightly less than the height of the sealing block;
Cooperate disk, radius is slightly less than the horizontal distance between the perpendicular support and the agitating shaft central axis, described to stir
It mixes axis and is closely arranged with bearing in second partition top, outer ring upper end is outward extended with ring baffle, the cooperation disk turning set
Set on bearing outer ring and between ring baffle and second partition, the cooperation disk extends centrally out setting multi-turn along it and passes through
Through-hole ring, multiple through-holes that multiple through holes that every circle perforation orifice ring includes include with every ring through hole ring correspond just, institute
It states that through hole is consistent with the hole size and the spacing between adjacent through-holes is not less than the diameter of the through-hole, the cooperation disk
On be additionally provided with the first block, the spacing between the stull lower surface is slightly less than the height of the sealing block.
Preferably, the cooperation disk is circumferentially spaced-apart immediately below the ring baffle is provided with multiple limited blocks, described
Ring baffle lower surface is hinged with limit plate, and the lower end of the limit plate is lower than the upper end of the limited block, the ring baffle
Closely limit plate is further fixed on barrier plate for lower surface, and the barrier plate lower end is higher than the limited block upper end, the limited block, limit
Position plate and barrier plate are located at same circumferential direction, and when the auxiliary body moves downward, the barrier plate is located at relative to limit plate
The rear side of rotational axis direction is stirred at this time, the second block is additionally provided on the cooperation disk, and height is not less than the first gear
The height of block, second block also are located at the rear side for stirring rotational axis direction at this time relative to the first block.
Preferably, the saddle is located exactly at one of agitator lower ending opening side, when the auxiliary body to
When lower movement, the leading flank of rotational axis direction is stirred in the stull that one of sealing block is close to saddle just at this moment.
Preferably, from the outer ring of cooperation disk, outside inner walls extend to form rotary table upwards for the second partition upper surface
The guide surface of shape.
Preferably, the sealing block is that intermediate cylinder is integrally formed to a pair of of truncated cone-shaped that tapered formation is distinguished at both ends
Structure, the column diameter among the sealing block is equal to the internal diameter of the agitator, and connection is fixed in the sealing block lower end
Boom end.
The present invention is include at least the following beneficial effects:
Metal zinc ion content is very low in the hydraulic oil that the compound two classes base oil of complexing agent of the present invention modulates, reach compared with
While good high/low temperature antioxygen, anticorrosive, wear-resistant and preferable detergent-dispersant performance energy, the complexing agent of low zinc content can be obtained
Formula, cost substantially reduce.
Alkylated diphenylamine high temperature antioxygen property belongs to well ashless oxidation inhibitor and compatibility is good, and di-tert-butyl p-cresol is often low
Warm antioxygenic property is good, and the formula that the anti-oxidant anti-corrosion property of Long-chain primary alcohols zinc dialkyl dithiophosphate can be good therefore of the invention is not
Pipe is low temperature or high temperature, its inoxidizability is preferable after combination, and applicability is stronger.
Tricresyl phosphate has extreme pressure and antiwear behavior, PBValue is currently not the essential items for inspection of hydraulic oil, but PBValue is got over
Height, extreme pressure and antiwear behavior is better, and wear scar diameter is smaller, and extreme pressure and antiwear behavior is better;Benzotriazole octadecylamine salt, friction improver,
Wear scar diameter can be reduced.
High base number calcium alkylbenzenesulfonate, detergent-dispersant additive;Double focusing isobutene imidodicarbonic diamide, dispersing agent have certain low temperature
Antioxygen property;Alkaline dinonyl naphthalene sulfonate barium and dodecenylsuccinic acid half ester, the two are applied in combination, antirust agent, selection alkalinity
Dinonyl naphthalene sulfonate barium can prevent acidic materials from corroding equipment.
Further advantage, target and feature of the invention will be partially reflected by the following instructions, and part will also be by this
The research and practice of invention and be understood by the person skilled in the art.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of reaction kettle of the present invention;
Fig. 2 is the top view of present invention cooperation disk;
Fig. 3 is the main view of present invention cooperation disk and bearing.
Description of symbols:
1, outer housing, 2, first partition, 3, second partition, 4, agitator, 5, blender, 6, agitating shaft, 7, paddle, 8,
Connecting rod, 9, sealing block, 10, saddle, 11, cooperation disk, the 12, first block, the 13, second block, 14, guide surface, 15, perforation
Hole, 16, limited block, 17, bearing, 18, ring baffle, 19, limit plate, 20, barrier plate.
Specific embodiment
Present invention will be described in further detail below with reference to the accompanying drawings, to enable those skilled in the art referring to specification text
Word can be implemented accordingly.
It should be noted that experimental method described in following embodiments is unless otherwise specified conventional method, institute
Reagent and material are stated, unless otherwise specified, is commercially obtained;In the description of the present invention, term " transverse direction ", " vertical
To ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", the instructions such as "outside" side
Position or positional relationship are to be based on the orientation or positional relationship shown in the drawings, and are merely for convenience of description of the present invention and simplification of the description,
It is not that the device of indication or suggestion meaning or element must have a particular orientation, be constructed and operated in a specific orientation, because
This is not considered as limiting the invention.
Embodiment 1
Hydraulic oil compound formula each component is by mass percentage are as follows: Long-chain primary alcohols zinc dialkyl dithiophosphate
20%, di-tert-butyl p-cresol 10%, alkylated diphenylamine 10%, tricresyl phosphate 15%, high base number calcium alkylbenzenesulfonate
8%, double focusing isobutene imidodicarbonic diamide 5%, dodecenylsuccinic acid half ester 1%, alkaline dinonyl naphthalene sulfonate barium 4%, benzotriazole
Octadecylamine salt 1.5%, two class base oil of low viscosity are supplied.Preparation process are as follows: reaction is added by its mass percent in each component
In kettle, 75 DEG C are warming up to, stirs evenly and cools down.
Above-mentioned compound formula is that 2% plus dosage are added into 98% two class base oils by mass percentage, and anti-
It answers and is warming up to 55 DEG C in kettle, stir evenly and cool down, mix and carry out hydraulic oil with higher wear resistance but energy, maximum nonseizure load
PBIn 830N, wear scar diameter 0.45mm or less;Antioxygen excellent corrosion resistance, at 150 DEG C, rotary bomb oxidation test time of measuring is
390 minutes, copper corrosion reached 1a;With preferable detergent-dispersant performance energy, dispersion efficiency 96%.
Above-mentioned compound formula is that 1% plus dosage are added into 99% two class base oils by mass percentage, and anti-
It answers and is warming up to 55 DEG C in kettle, stir evenly and cool down, mix and carry out hydraulic oil with preferable abrasion resistance, maximum is without seizing negative
Lotus PBIn 720N, wear scar diameter 0.50mm or less;Antioxygen corrosion resistance is preferable, and at 150 DEG C, rotary bomb oxidation test time of measuring is
264 minutes, copper corrosion reached 1b;With preferable detergent-dispersant performance energy, dispersion efficiency 92%.
Embodiment 2
Hydraulic oil compound formula each component is by mass percentage are as follows: Long-chain primary alcohols zinc dialkyl dithiophosphate
10%, di-tert-butyl p-cresol 10%, alkylated diphenylamine 8%, tricresyl phosphate 20%, high base number calcium alkylbenzenesulfonate 5%,
Double focusing isobutene imidodicarbonic diamide 5%, dodecenylsuccinic acid half ester 1%, alkaline dinonyl naphthalene sulfonate barium 4%, benzotriazole 18
Amine salt 1.5%, two class base oil of low viscosity are supplied.Preparation process are as follows: each component is added in reaction kettle by its mass percent,
75 DEG C are warming up to, stir evenly and is cooled down.
Above-mentioned compound formula is that 2% plus dosage are added into 98% two class base oils by mass percentage, and anti-
It answers and is warming up to 55 DEG C in kettle, stir evenly and cool down, mix and carry out hydraulic oil with higher wear resistance but energy, maximum nonseizure load
PBIn 850N, wear scar diameter 0.40mm or less;At 150 DEG C, rotary bomb oxidation test time of measuring is 310 minutes, and copper corrosion reaches
1b;With preferable detergent-dispersant performance energy, dispersion efficiency 97%.
Comparative example 1
Hydraulic oil compound formula each component is by mass percentage are as follows: Long-chain primary alcohols zinc dialkyl dithiophosphate
20%, alkylated diphenylamine 10%, tricresyl phosphate 15%, high base number calcium alkylbenzenesulfonate 5%, double focusing isobutene imidodicarbonic diamide
5%, dodecenylsuccinic acid half ester 1%, alkaline dinonyl naphthalene sulfonate barium 4%, benzotriazole octadecylamine salt 1.5%, low viscosity two
Class base oil is supplied.Preparation process are as follows: each component is added in reaction kettle by its mass percent, is warming up to 75 DEG C, stirring is equal
It is even and cooling.
Above-mentioned compound formula is that 2% plus dosage are added into 98% two class base oils by mass percentage, and anti-
It answers and is warming up to 55 DEG C in kettle, stir evenly and cool down, mix and carry out hydraulic oil with higher wear resistance but energy, maximum nonseizure load
PBIn 830N, wear scar diameter 0.45mm or less;Antioxygen excellent corrosion resistance, at 150 DEG C, rotary bomb oxidation test time of measuring is
180 minutes, copper corrosion reached 1a;With preferable detergent-dispersant performance energy, dispersion efficiency 95%.
Comparative example 2
Hydraulic oil compound formula each component is by mass percentage are as follows: Long-chain primary alcohols zinc dialkyl dithiophosphate
20%, di-tert-butyl p-cresol 15%, alkylated diphenylamine 10%, tricresyl phosphate 15%, high base number calcium alkylbenzenesulfonate
5%, dodecenylsuccinic acid half ester 1%, alkaline dinonyl naphthalene sulfonate barium 4%, benzotriazole octadecylamine salt 1.5%, low viscosity two
Class base oil is supplied.Preparation process are as follows: each component is added in reaction kettle by its mass percent, is warming up to 75 DEG C, stirring is equal
It is even and cooling.
Above-mentioned compound formula is that 2% plus dosage are added into 98% two class base oils by mass percentage, and anti-
It answers and is warming up to 55 DEG C in kettle, stir evenly and cool down, mix and carry out hydraulic oil with higher wear resistance but energy, maximum nonseizure load
PBIn 830N, wear scar diameter 0.45mm or less;Antioxygen excellent corrosion resistance, at 150 DEG C, rotary bomb oxidation test time of measuring is
290 minutes, copper corrosion reached 1a;With preferable detergent-dispersant performance energy, dispersion efficiency 82%.
The present invention also provides one kind reaction kettles used in above-mentioned technique comprising:
Outer housing 1 is sealing structure, and 1 inside of the outer housing is fixed at intervals with horizontal first partition 2 and the up and down
Two partitions 3, will be divided into from top to bottom the first reaction chamber, the second reaction chamber and third reaction chamber inside outer housing 1, and described second
There are multiple through-holes on partition 3;
Agitator 4 is set in the first reaction chamber for multiple and uniform intervals, the agitator 4 be vertically arranged and on
End sealing, lower ending opening, 4 lower end of agitator is fixed in first partition 2 and lower ending opening perforation first partition 2 is connected to institute
The second reaction chamber is stated, is provided with blender 5 in the agitator 4;
Agitating shaft 6, is vertically positioned in outer housing 1 and the central axis of the central axis of the agitating shaft 6 and outer housing 1
It is overlapped, 6 lower end of agitating shaft is located at the lower end of third reaction chamber, and the 6 upper end hermetically passing second partition 3 of agitating shaft is located at
The upper end of second reaction chamber, the part that the agitating shaft 6 is located in the second reaction chamber are provided with external screw thread, the agitating shaft 6
Part in third reaction chamber is additionally provided with paddle 7;
Auxiliary body comprising sleeve, more connecting rods 8 and multiple sealing blocks 9, the sleeve have internal screw thread and cooperation
In on the external screw thread of the agitating shaft 6, the horizontal circumferential direction along the sleeve of more connecting rods 8 is uniformly arranged, multiple sealing blocks 9 one
One correspondence is fixed on more 8 ends of connecting rod, and multiple sealing blocks 9 correspond to the lower ending opening for sealing multiple agitators 4 just.
In the above-mentioned technical solutions, since the raw material components of reaction are more, raw material can be grouped, respectively in agitator
In 4 then stirring carries out being stirred in next step again, and the efficiency of stirring and the even results of each component mixing, agitator can be improved
4 settings 2~4, liquid and powdered or thick component when grouping usually in complexing agent are divided into one group wherein
It is mixed in one agitator 4, then unifies be stirred in next step again.Each agitator 4 is provided with feed inlet,
When original state, the sealing block 9 in auxiliary body respectively seals the lower ending opening of agitator 4, so that agitator 4 is closing
Structure, after the completion of each component feeds according to the proportion, feed inlet is sealed, and then carries out being sufficiently stirred one by blender 5
The section time;Then restart motor driven agitating shaft 6 rotation, sealing block 9 due to being sticked at 4 lower ending opening of agitator,
It can only be moved up and down, and when agitating shaft 6 rotates, auxiliary body is moved downward, and be opened until it is detached from 4 lower end of agitator
Mouthful, auxiliary body follows agitating shaft 6 to rotate together, and in the second reaction chamber, auxiliary body may act as rabbling mechanism at this time, to from
The each component that 4 lower ending opening of agitator falls carries out next step stirring, and each component raw material is relayed from multiple through-holes of second partition 3
It is continuous to fall, third reaction chamber is reached, realization futher stirs, and the setting of second partition 3 can increase the whereabouts resistance of raw material components,
Increase the mixed time.
In another technical solution, the second partition 3 extends centrally out setting multi-turn through-hole ring along it, and every circle is logical
Circumferentially uniform intervals are arranged multiple through-holes that orifice ring includes, the reaction kettle further include:
Saddle 10, for inverted L shape and including perpendicular support and stull, the perpendicular support is located on the outside of multiple agitators 4, the perpendicular support
Lower end is fixed on second partition 3, central axis of the stull towards outer housing 1, the stull upper surface and first partition 2
Between spacing be slightly less than the height of the sealing block 9;
Cooperate disk 11, radius is slightly less than the horizontal distance between the perpendicular support and 6 central axis of the agitating shaft, described
Agitating shaft 6 is closely arranged with bearing 17 above second partition 3, and outer ring upper end is outward extended with ring baffle 18, the cooperation
11 turning set of disk is set to 17 outer ring of bearing and between ring baffle 18 and second partition 3, and the cooperation disk 11 is along its center
Extend outwardly and multi-turn perforation orifice ring is set, every circle perforation orifice ring multiple through holes 15 for including and every ring through hole ring include multiple
Through-hole corresponds just, the through hole 15 is consistent with the hole size and adjacent through-holes between spacing not less than described
The diameter of through-hole is additionally provided with the first block 12 on the cooperation disk 11, and the spacing between the stull lower surface is smaller
In the height of the sealing block 9.
In the above-mentioned technical solutions, more abundant to contact in order to increase the time of each component mixing, it is logical on second partition 3
Hole first passes through cooperation disk 11 and is blocked, and when original state, the through-hole on through hole 15 and second partition 3 on disk 11 is cooperated to hand over
Mistake setting, constitutes a complete seal disc just, and when cooperating disk 11 to rotate, through hole 15 thereon can be with second partition 3
On through-hole correspond so that each component fall.Sealing block 9 is after being detached from 4 lower ending opening of agitator, due to not stopping,
It can follow agitating shaft 6 to rotate together, and stull is encountered after rotation, and under the barrier effect of stull, sealing block 9 can only be transported downwards again
Dynamic, until its blocking for being detached from stull, follows agitating shaft 6 to rotate again, and sealing block 9 can also be transported with the first block 12 at this time
Dynamic, so that cooperation disk 11 be driven to rotate, interval opens or closes the channel of component raw material whereabouts after cooperation disk 11 rotates, and increases each
It the time of component raw material contact, stirs more abundant.
In another technical solution, the cooperation disk 11 immediately below the ring baffle 18 it is circumferentially spaced-apart be provided with it is more
A limited block 16,18 lower surface of ring baffle are hinged with limit plate 19, and the lower end of the limit plate 19 is lower than the limit
The upper end of block 16, closely limit plate 19 is further fixed on barrier plate 20,20 lower end of barrier plate for 18 lower surface of ring baffle
Higher than 16 upper end of limited block, the limited block 16, limit plate 19 and barrier plate 20 are located at same circumferential direction, when the auxiliary machine
When structure moves downward, the barrier plate 20 is located at the rear side of 6 rotation direction of agitating shaft at this time, the cooperation relative to limit plate 19
The second block 13 is additionally provided on disk 11, height is not less than the height of first block 12, and second block 13 is opposite
The rear side of 6 rotation direction of agitating shaft at this time also is located in the first block 12.
In the above-mentioned technical solutions, when the direction that agitating shaft 6 rotates move downward sealing block 9 can, stirring at this time
Direction definition is mixed as clockwise, sealing block 9 drives the movement of the first block 12, the limit plate 19 on ring baffle 18 is cooperated
Limited block 16 on disk 11 stops, and clockwise rotation occurs, when between adjacent stopper, and can rotate automatically
For straight down, barrier plate 20 is located at clockwise rear relative to limit plate 19, when sealing block 9 need to move upwards it is close
When sealing 4 lower ending opening of agitator, agitating shaft 6 is rotated backward, that is, counterclockwise, sealing block 9 rotates backward at this time, until
It is turned at the second block 13, and cooperation disk 11 is driven also to rotate backward, and still, limited block 16 can be limited plate 19 and block, and
Limit plate 19 can be blocked plate 20 and block, and cooperation disk 11 cannot rotate, and therefore, upward movement can only occur for sealing block 9,
Until it is moved to above stull.
In another technical solution, the saddle 10 is located exactly at one of 4 lower ending opening side of agitator, works as institute
When stating auxiliary body and moving downward, one of sealing block 9 is close to the stull of saddle 10 6 rotation direction of agitating shaft at this moment just
Leading flank.
In the above-mentioned technical solutions, in order to enable when sealing block 9 moves up can automatic reduction to just by the lower end of agitator 4
Opening sealing, agitating shaft 6 rotationally clockwise when, the sealing block 9 of closely 10 stull of saddle is detached from 4 lower ending opening of agitator
When, far from 10 stull of saddle rotation closely, and when agitating shaft 6 rotates in an anti-clockwise direction, wherein a sealing block 9 quilt just
10 stull of saddle blocking is not able to rotate, and is located therein immediately below 4 lower ending opening of an agitator, therefore can guarantee sealing block 9 smoothly
It moves up, corresponds sealing 4 lower ending opening of agitator.
In another technical solution, 3 upper surface of second partition is from the outer ring of cooperation disk 11 upwards into outer housing 1
Wall extends to form the guide surface 14 of truncated cone-shaped.The setting of guide surface 14 may make on component raw material automatic fall-back to second partition 3.
In another technical solution, the sealing block 9 is a pair of circle that intermediate cylinder distinguishes tapered formation to both ends
The column diameter of the integrally formed structure of platform shape, 9 centre of sealing block is equal to the internal diameter of the agitator 4, the sealing block 9
8 end of connecting rod is fixed in lower end.The microcephaly of 9 top of sealing block is considered as guiding role, and the microcephaly of lower section is convenient to be connected with connecting rod 8
It connects, while may make the quality of sealing block 9 smaller, reduce resistance when rotation.
Although the embodiments of the present invention have been disclosed as above, but its is not only in the description and the implementation listed
With it can be fully applied to various fields suitable for the present invention, for those skilled in the art, can be easily
Realize other modification, therefore without departing from the general concept defined in the claims and the equivalent scope, the present invention is simultaneously unlimited
In specific details and legend shown and described herein.