CN205838902U - A kind of continuous modified asphalt production system - Google Patents
A kind of continuous modified asphalt production system Download PDFInfo
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- CN205838902U CN205838902U CN201620287136.XU CN201620287136U CN205838902U CN 205838902 U CN205838902 U CN 205838902U CN 201620287136 U CN201620287136 U CN 201620287136U CN 205838902 U CN205838902 U CN 205838902U
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- tank
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- asphalt
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- colophonium
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Abstract
The utility model discloses a kind of continuous modified asphalt production system, it includes that be rapidly heated system, mixing and stirring system, shearing grinding system and finished product of electric-control system and the Colophonium being sequentially connected with is grown and induction system；Described shearing grinding system includes the first rubber mill, the second rubber mill and transition tank；Described first rubber mill and the second rubber mill are arranged in parallel, and described first rubber mill and the second rubber mill are all connected with described transition tank；Transition tank agitator it is provided with in described transition tank；High level alarm and temperature sensor it is provided with on described transition tank.This utility model saves the energy, and production technology is alternative strong, and technical arrangement plan wide ranges uses this utility model, substantially increases production efficiency, saves the plenty of time, saves again manpower and materials simultaneously and puts into.
Description
Technical field
This utility model relates to the continuous modified asphalt equipment of a kind of improvement.
Background technology
Modified asphalt concrete road surface is widely used in urban road and highway with its excellent Pavement Performance.
Along with the quickening of urbanization process, the sharp increase of traffic volume of highway, concrete road surface in early days are destroyed, it is faced with overhaul task
Deng, cause the demand of modified pitch to increase, existing modified asphalt device production capacity is low, does not the most seriously catch up with the market demand.
Therefore, if existing modified asphalt device can be undergone technological transformation, it is possible not only to improve its production efficiency and can reduce again cost
Put into so that it is fully meet the market demand.
Utility model content
The technical problems to be solved in the utility model is the defect overcoming prior art, it is provided that the continuous way of a kind of improvement changes
Property asphalt equipment.
In order to solve above-mentioned technical problem, this utility model provides following technical scheme:
This utility model one continuous modified asphalt production system, it includes electric-control system and the Colophonium being sequentially connected with
Be rapidly heated system, mixing and stirring system, shearing grinding system and finished product growth and induction system；Described shearing grinding system bag
Include the first rubber mill, the second rubber mill and transition tank；Described first rubber mill and the second rubber mill are arranged in parallel, described first glue
Grinding machine and the second rubber mill are all connected with described transition tank；Transition tank agitator it is provided with in described transition tank；Described transition tank
On be provided with high level alarm and temperature sensor.
Further, the described Colophonium system of being rapidly heated includes adjustable flow bitumenpump, described adjustable flow bitumenpump
Import connects has filter, described adjustable flow Colophonium delivery side of pump to be connected with First Heat Exchanger, the second heat exchanger and stream in turn
Gauge；The inlet and outlet of described second heat exchanger is respectively equipped with the second asphalt valve and the 3rd asphalt valve, described second asphalt valve
Import and the outlet of described 3rd asphalt valve between connect have by-pass line, described by-pass line to be provided with the first asphalt valve；
The outlet of described First Heat Exchanger is connected, through the first asphalt valve and the 3rd Colophonium through the import of the second asphalt valve and the second heat exchanger
The outlet of valve is connected；Described 3rd asphalt valve is arranged between described second heat exchanger and described effusion meter；Described first heat exchange
It is mounted on pressure transducer on device and the second heat exchanger.
Further, described mixing and stirring system include the first material-compound tank, the second material-compound tank, modifying agent adding set and
Insulation three-way valve；The first material-compound tank agitator and the second material-compound tank it is respectively arranged with in described first material-compound tank and the second material-compound tank
Agitator；The import connection traffic meter of described insulation three-way valve, the outlet of described insulation three-way valve respectively with described first dispensing
The Colophonium import of tank is connected with the Colophonium import of described second material-compound tank；Described modifying agent adding set connects described first dispensing
Tank and the second material-compound tank.
Further, described first material-compound tank is provided with LOAD CELLS, and described second material-compound tank is provided with pressure type liquid
Level sensor.
Further, described finished product grow and induction system include the first growth tank, second grow tank, the 3rd grow tank and
4th grows tank；Described first growth tank, the second growth tank, the 3rd growth tank and the 4th are respectively arranged with first in growing tank
Educate jar agitator, the second growth jar agitator, the 3rd growth jar agitator and the 4th growth jar agitator；Described first grows
Tank, the second growth tank, the 3rd growth tank and the 4th are grown and are equipped with Colophonium import, asphalt outlet, auxiliary agent import, waste gas on tank
Mouth, high level alarm and temperature sensor.
Further, described transition tank is provided with the first Colophonium import, the second Colophonium import, asphalt outlet, high level report
Alert device and temperature sensor；The import of described first rubber mill passes sequentially through the first regulation pump, the 6th asphalt valve and the 4th Colophonium
Valve is connected with described first material-compound tank and the second material-compound tank；The outlet of described first rubber mill connects the first Colophonium of transition tank and enters
Mouthful；The import of described second rubber mill passes sequentially through the second regulation pump, the 7th asphalt valve and the 5th asphalt valve and joins with described first
Batch can and the second material-compound tank connect；The outlet of described second rubber mill connects the second Colophonium import of transition tank.
Further, also including booster pump, the import of described booster pump is through the Colophonium of the 8th asphalt valve Yu described transition tank
Outlet is connected, and described supercharging delivery side of pump divides through the 9th asphalt valve, the tenth asphalt valve, the 11st asphalt valve and the 12nd asphalt valve
Do not grow tank with described first, the second Colophonium import grown on tank, the 3rd growth tank and the 4th growth tank is connected.
Further, also including auxiliary agent pump, the import of described auxiliary agent pump connects auxiliary agent filter, described auxiliary agent delivery side of pump
It is sequentially connected with auxiliary agent effusion meter, the first valve, the second valve, the 3rd valve and the 4th valve；Described first valve, the second valve
Tank, the second growth tank, the 3rd growth tank and the 4th are grown in the outlet of door, the 3rd valve and the 4th valve respectively with described first
The auxiliary agent import educating tank is connected.
Further, also including Colophonium rear pump, the import of described Colophonium rear pump is through the 13rd asphalt valve, the 14th drip
Blue or green valve, the 15th asphalt valve and the 16th asphalt valve grow with described first respectively tank, second grow tank, the 3rd grow tank and
4th asphalt outlet growing tank is connected, and described Colophonium output delivery side of pump is connected with asphalt truck through the 17th asphalt valve.
This utility model is reached to provide the benefit that: this utility model saves the energy, and production technology is alternative strong, work
Skill parameter adjustment wide ranges, uses this utility model, substantially increases production efficiency, saves the plenty of time, saves again simultaneously
Manpower and materials inputs.
Accompanying drawing explanation
Accompanying drawing is used for providing being further appreciated by of the present utility model, and constitutes a part for description, with this practicality
Novel embodiment is used for explaining this utility model together, is not intended that restriction of the present utility model.In the accompanying drawings:
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of this utility model electric-control system.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is illustrated, it will be appreciated that described herein excellent
Select embodiment to be merely to illustrate and explain this utility model, being not used to limit this utility model.
As depicted in figs. 1 and 2, this utility model one continuous modified asphalt production system, it includes electric-control system 50
And the Colophonium being sequentially connected be rapidly heated system 51, mixing and stirring system 52, shear grinding system 53 and finished product and grow and defeated
Send system 54；Described shearing grinding system includes the first rubber mill the 16, second rubber mill 17 and transition tank 21；Described first colloid mill
Machine 16 and the second rubber mill 17 are arranged in parallel, and described first rubber mill 16 and the second rubber mill 17 are all with described transition tank 21 even
Connect；It is provided with transition tank agitator 20 in described transition tank 21；High level alarm 22 and temperature it is provided with on described transition tank 21
Degree sensor 23.
The described Colophonium system 51 that is rapidly heated includes adjustable flow bitumenpump 55, the import of described adjustable flow bitumenpump 55
Connecting has filter 56, the outlet of described adjustable flow bitumenpump 55 to be connected with First Heat Exchanger the 57, second heat exchanger 58 in turn
With effusion meter 5；The inlet and outlet of described second heat exchanger 58 is respectively equipped with the second asphalt valve 3 and the 3rd asphalt valve 4, and described
Connect between import and the outlet of described 3rd asphalt valve 4 of two asphalt valves 3 and have by-pass line, described by-pass line to be provided with the
One asphalt valve 2；The outlet of described First Heat Exchanger 57 is connected, through first through the import of the second asphalt valve 3 with the second heat exchanger 58
Asphalt valve 2 is connected with the outlet of the 3rd asphalt valve 4；Described 3rd asphalt valve 4 is arranged on described second heat exchanger 58 and described stream
Between gauge 5；It is mounted on pressure transducer 1 on described First Heat Exchanger 57 and the second heat exchanger 58.
Described mixing and stirring system 52 includes first material-compound tank the 6, second material-compound tank 7, modifying agent adding set 59 and protects
Temperature three-way valve 49；It is respectively arranged with the first material-compound tank agitator 60 and second in described first material-compound tank 6 and the second material-compound tank 7 to join
Batch can agitator 61；The import connection traffic meter 5 of described insulation three-way valve 49, the outlet of described insulation three-way valve 49 respectively with institute
The Colophonium import of the Colophonium import and described second material-compound tank 7 of stating the first material-compound tank 6 is connected；Described modifying agent adding set 59 is even
Connect described first material-compound tank 6 and the second material-compound tank 7.
Described first material-compound tank 6 is provided with LOAD CELLS 8, and described second material-compound tank 7 is provided with pressure type liquid level sensing
Device 13.
Described finished product is grown and induction system 54 includes that the first growth tank 40, second is grown tank the 42, the 3rd and grown tank 44 and
4th grows tank 46；Described first growth tank 40, second is grown in tank the 42, the 3rd grows tank 44 and the 4th growth tank 46 and is set respectively
It is equipped with the first growth jar agitator 25, second and grows jar agitator the 28, the 3rd growth jar agitator 31 and the 4th growth tank stirring
Device 34；It is equipped with Colophonium on described first growth tank the 40, second growth tank the 42, the 3rd growth tank 44 and the 4th growth tank 46 to enter
Mouth, asphalt outlet, auxiliary agent import, exhaust outlet, high level alarm 22 and temperature sensor 23.
Described transition tank 21 is provided with the first Colophonium import, the second Colophonium import, asphalt outlet, high level alarm 22 and
Temperature sensor 23；The import of described first rubber mill 16 passes sequentially through the first regulation pump the 14, the 6th asphalt valve 11 and the 4th drip
Blue or green valve 9 is connected with described first material-compound tank 6 and the second material-compound tank 7；The outlet of described first rubber mill 16 connects transition tank 21
First Colophonium import；The import of described second rubber mill 17 passes sequentially through the second regulation pump the 15, the 7th asphalt valve 12 and the 5th drip
Blue or green valve 10 is connected with described first dispensing 6 tank and the second material-compound tank 7；The outlet of described second rubber mill 17 connects transition tank 21
Second Colophonium import.
Also include that booster pump 19, the import of described booster pump 19 go out through the Colophonium of the 8th asphalt valve 18 with described transition tank 21
Mouth is connected, and the outlet of described booster pump 19 drips through the 9th asphalt valve the 24, the tenth asphalt valve the 27, the 11st asphalt valve the 30 and the 12nd
Blue or green valve 33 is grown tank 40, second respectively and is grown the Colophonium on tank the 42, the 3rd growth tank 44 and the 4th growth tank 46 with described first
Import is connected.
Also including auxiliary agent pump 37, the import of described auxiliary agent pump 37 connects auxiliary agent filter 38, the outlet of described auxiliary agent pump 37
It is sequentially connected with auxiliary agent effusion meter the 36, first valve the 26, second valve the 29, the 3rd valve 32 and the 4th valve 35；Described first valve
The outlet of door the 26, second valve the 29, the 3rd valve 32 and the 4th valve 35 is grown tank 40, second respectively and is grown with described first
Tank the 42, the 3rd is grown tank 44 and is connected with the 4th auxiliary agent import growing tank 46.
Also including Colophonium rear pump 47, the import of described Colophonium rear pump 47 is through the 13rd asphalt valve the 39, the 14th Colophonium
Valve the 41, the 15th asphalt valve the 43 and the 16th asphalt valve 45 grow with described first respectively tank 40, second grow tank 42, the 3rd
Educating tank 44 to be connected with the 4th asphalt outlet growing tank 46, the outlet of described Colophonium rear pump 47 is through the 17th asphalt valve 48 and drip
Blue or green tank car is connected.
Workflow of the present utility model is:
When production capacity of the present utility model is less than 40T/h, matrix pitch is through filter 56, adjustable flow bitumenpump 55
It is delivered to First Heat Exchanger 57 carry out heating up for the first time, judges whether to meet technique according to the temperature of display in temperature sensor 23
Requirement, otherwise closes the first asphalt valve 2, opens the second asphalt valve 3 and the 3rd asphalt valve 4, matrix pitch is delivered to second and changes
Hot device 58 carries out second time and heats up, and after in temperature sensor 23, the temperature of display meets working condition, matrix pitch is pumped
Stirring to the first material-compound tank 6, modifying agent is modified agent adding set 59 and is joined the first material-compound tank 6 by continuous and quantitative simultaneously
In, matrix pitch and modifying agent carry out sufficient mix, melt mixed, through after a period of time, when in the first material-compound tank 6 substrate drip
When green grass or young crops and modifying agent reach regulation liquid level, the warm three-way valve of matrix pitch 49 automatically switches to stir in the second material-compound tank 7, this
Time the first material-compound tank 6 in mixture regulate pump 14 through the 4th asphalt valve 9, first and be delivered to the first rubber mill 16 and be ground, cut
Cutting, the modified pitch after grinding is pumped to first through transition tank the 21, the 8th asphalt valve 18, booster pump the 19, the 9th asphalt valve 24
Growth tank 40 stirs, grows；When in the second material-compound tank 7 matrix pitch and modifying agent reach regulation liquid level time, matrix pitch
Warm three-way valve 49 automatically switch in the first material-compound tank 6 stir, now in the second material-compound tank 7 mixture through the 6th asphalt valve
11, the first regulation pump 14 is delivered to the first rubber mill 16 and is ground, shears, the modified pitch after grinding through transition tank 21, the
Eight asphalt valves 18, booster pump the 19, the 9th asphalt valve 24 are pumped in the first growth tank 40 stir, grow；When first grows tank
When modified pitch in 40 reaches regulation liquid level, PLC system is automatically switched off the 9th asphalt valve 24, opens the tenth asphalt valve 27, changes
Property Colophonium is pumped in the second growth tank 42 stir through transition tank the 21, the 8th asphalt valve 18, booster pump the 19, the tenth asphalt valve 27
Mix, grow；When the modified pitch in the second growth tank 42 reaches regulation liquid level, PLC system is automatically switched off the tenth asphalt valve 27,
Opening the 11st asphalt valve 30, modified pitch is through transition tank the 21, the 8th asphalt valve 18, booster pump the 19, the 11st asphalt valve 30 quilt
It is pumped in the 3rd growth tank 44 stir, grow；Grow modified pitch in tank 40 simultaneously to first and be sampled detection, modified drip
It is delivered to mixing building or asphalt tank through the 13rd asphalt valve 39, Colophonium rear pump the 47, the 17th asphalt valve 48 after blue or green detection is qualified
Car.When the modified pitch in the 3rd growth tank 44 reaches regulation liquid level, PLC system is automatically switched off the 11st asphalt valve 30, beats
Opening the 9th asphalt valve 24, modified pitch is pumped to through transition tank the 21, the 8th asphalt valve 18, booster pump the 19, the 9th asphalt valve 24
First growth tank 40 stirs, grows, so reach to circulate production continuously.
When modified asphalt device production capacity is more than 40T/h, matrix pitch is depended on through filter, adjustable flow bitumenpump
Secondary being delivered in First Heat Exchanger, the second heat exchanger carries out continuous warming, when in temperature sensor, the temperature of display meets production
After condition, matrix pitch is pumped in the first material-compound tank 6 stirring, and modifying agent is modified agent adding set by continuous and quantitative simultaneously
Join in the first material-compound tank 6, matrix pitch and modifying agent carry out sufficient mix, melt mixed, through after a period of time, when
When matrix pitch in one material-compound tank 6 and modifying agent reach regulation liquid level, the warm three-way valve of matrix pitch 49 automatically switches to
Stirring in second material-compound tank 7, now in the first material-compound tank 6, mixture is delivered to the first grinding machine through the 4th asphalt valve 9, regulation pump 14
16 being ground, shear, in the first material-compound tank 6, mixture is delivered to the second grinding machine through the 5th asphalt valve 10, regulation pump 15 simultaneously
17 being ground, shear, the modified pitch after the first grinding machine 16 and the second grinding machine 17 will grind is delivered in transition tank 21 stirring,
Modified pitch in transition tank 21 is pumped to the first growth tank 40 through the 8th asphalt valve 18, booster pump the 19, the 9th asphalt valve 24
Middle stirring, growth；When the matrix pitch in the second material-compound tank 7 and modifying agent reach regulation liquid level, matrix pitch warm three
Logical valve 49 automatically switches to stir in the first material-compound tank 6, now in the second material-compound tank 7 mixture through the 6th asphalt valve 11, regulation
Pump 14 is delivered to the first grinding machine 16 and is ground, shears, simultaneously in the second material-compound tank 7 mixture through the 7th asphalt valve 12, regulation
Pump 15 is delivered to the second grinding machine 17 and is ground, shears, and the modified pitch after the first grinding machine 16 and the second grinding machine 17 will grind is defeated
Delivering to stir in transition tank 21, the modified pitch in transition tank 21 is through the 8th asphalt valve 18, booster pump the 19, the 9th asphalt valve 24 quilt
It is pumped in the first growth tank 40 stir, grow；When the modified pitch in the first growth tank 40 reaches regulation liquid level, PLC system
System is automatically switched off the 9th asphalt valve 24, opens the tenth asphalt valve 27, and modified pitch is through the 8th asphalt valve 18, booster pump the 19, the tenth
Asphalt valve 27 is pumped in the second growth tank 42 stir, grow；When the second modified pitch grown in tank 42 reaches regulation liquid
During position, PLC system is automatically switched off the tenth asphalt valve 27, opens the 11st asphalt valve 30, and modified pitch is through the 8th asphalt valve 18, increasing
Press pump the 19, the 11st asphalt valve 30 is pumped in the 3rd growth tank 44 stir, grow；When the 3rd grows the modified drip in tank 44
When green grass or young crops reaches regulation liquid level, PLC system is automatically switched off the 11st asphalt valve 30, opens the 12nd asphalt valve 33, modified pitch warp
8th asphalt valve 18, booster pump the 19, the 12nd asphalt valve 33 are pumped in the 4th growth tank 46 stir, grow；Simultaneously to
One grows modified pitch in tank 40 is sampled detection, through the 13rd asphalt valve 39, Colophonium output after modified pitch detection is qualified
Pump the 47, the 17th asphalt valve 48 is delivered to mixing building or asphalt truck.When the modified pitch in the 4th growth tank 46 reaches regulation
During liquid level, PLC system is automatically switched off the 12nd asphalt valve 33, opens the 9th asphalt valve 24, modified pitch through the 8th asphalt valve 18,
Booster pump the 19, the 9th asphalt valve 24 is pumped in the first growth tank 40 stir, grow, and grows in tank 42 modified to second simultaneously
Colophonium is sampled detection, through the 14th asphalt valve 41, Colophonium rear pump the 47, the 17th asphalt valve after modified pitch detection is qualified
48 are delivered to mixing building or asphalt truck.So reach to circulate production continuously.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, it is not limited to this
Utility model, although being described in detail this utility model with reference to previous embodiment, for those skilled in the art
For, the technical scheme described in foregoing embodiments still can be modified by it, or to wherein portion of techniques feature
Carry out equivalent.All within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, all
Within protection domain of the present utility model should be included in.
Claims (9)
1. a continuous modified asphalt production system, it is characterised in that include that electric-control system and the Colophonium being sequentially connected with are fast
Speed temperature elevation system, mixing and stirring system, shearing grinding system and finished product are grown and induction system；Described shearing grinding system includes
First rubber mill, the second rubber mill and transition tank；Described first rubber mill and the second rubber mill are arranged in parallel, described first colloid mill
Machine and the second rubber mill are all connected with described transition tank；Transition tank agitator it is provided with in described transition tank；On described transition tank
It is provided with high level alarm and temperature sensor.
Continuous modified asphalt production system the most according to claim 1, it is characterised in that described Colophonium is rapidly heated and is
System includes adjustable flow bitumenpump, and the import of described adjustable flow bitumenpump connects filter, described adjustable flow bitumenpump
Outlet be connected with First Heat Exchanger, the second heat exchanger and effusion meter in turn；The inlet and outlet of described second heat exchanger is respectively
It is provided with the second asphalt valve and the 3rd asphalt valve, connects between import and the outlet of described 3rd asphalt valve of described second asphalt valve
By-pass line, described by-pass line is had to be provided with the first asphalt valve；The outlet of described First Heat Exchanger is through the second asphalt valve and
The import of two heat exchangers is connected, connected through the outlet of the first asphalt valve and the 3rd asphalt valve；Described 3rd asphalt valve is arranged on institute
State between the second heat exchanger and described effusion meter；It is mounted on pressure transducer on described First Heat Exchanger and the second heat exchanger.
Continuous modified asphalt production system the most according to claim 1, it is characterised in that described mixing and stirring system
Including the first material-compound tank, the second material-compound tank, modifying agent adding set and insulation three-way valve；Described first material-compound tank and the second dispensing
The first material-compound tank agitator and the second material-compound tank agitator it is respectively arranged with in tank；The import connection traffic of described insulation three-way valve
Meter, the outlet of described insulation three-way valve Colophonium with the Colophonium import of described first material-compound tank and described second material-compound tank respectively enters
Mouth is connected；Described modifying agent adding set connects described first material-compound tank and the second material-compound tank.
Continuous modified asphalt production system the most according to claim 3, it is characterised in that set on described first material-compound tank
LOAD CELLS, described second material-compound tank is had to be provided with pressure liquid level sensor.
Continuous modified asphalt production system the most according to claim 3, it is characterised in that described finished product is grown and conveying
System includes that tank grown by the first growth tank, the second growth tank, the 3rd growth tank and the 4th；Described first grows tank, the second growth
Tank, the 3rd grow tank and the 4th grow in tank be respectively arranged with the first growth jar agitator, second grow jar agitator, the 3rd
Educate jar agitator and the 4th and grow jar agitator；Described first grows tank, the second growth tank, the 3rd growth tank and the 4th growth tank
On be equipped with Colophonium import, asphalt outlet, auxiliary agent import, exhaust outlet, high level alarm and temperature sensor.
Continuous modified asphalt production system the most according to claim 3, it is characterised in that described transition tank is provided with
One Colophonium import, the second Colophonium import, asphalt outlet, high level alarm and temperature sensor；Entering of described first rubber mill
Mouth passes sequentially through the first regulation pump, the 6th asphalt valve and the 4th asphalt valve and is connected with described first material-compound tank and the second material-compound tank；
The outlet of described first rubber mill connects the first Colophonium import of transition tank；The import of described second rubber mill passes sequentially through second
Regulation pump, the 7th asphalt valve and the 5th asphalt valve are connected with described first material-compound tank and the second material-compound tank；Described second rubber mill
Outlet connect transition tank the second Colophonium import.
Continuous modified asphalt production system the most according to claim 5, it is characterised in that also include booster pump, described
The import of booster pump is connected with the asphalt outlet of described transition tank through the 8th asphalt valve, and described supercharging delivery side of pump is through the 9th Colophonium
Valve, the tenth asphalt valve, the 11st asphalt valve and the 12nd asphalt valve respectively with described first grow tank, second grow tank, the 3rd
The Colophonium import grown on tank and the 4th growth tank is connected.
Continuous modified asphalt production system the most according to claim 5, it is characterised in that also include auxiliary agent pump, described
The import of auxiliary agent pump connects auxiliary agent filter, and described auxiliary agent delivery side of pump is sequentially connected with auxiliary agent effusion meter, the first valve, the second valve
Door, the 3rd valve and the 4th valve；The outlet of described first valve, the second valve, the 3rd valve and the 4th valve respectively with institute
State the first growth tank, the second auxiliary agent import growing tank, the 3rd growth tank and the 4th growth tank is connected.
Continuous modified asphalt production system the most according to claim 5, it is characterised in that also include Colophonium rear pump,
The import of described Colophonium rear pump divides through the 13rd asphalt valve, the 14th asphalt valve, the 15th asphalt valve and the 16th asphalt valve
Do not grow tank with described first, the second asphalt outlet growing tank, the 3rd growth tank and the 4th growth tank is connected, and described Colophonium is defeated
Go out delivery side of pump to be connected with asphalt truck through the 17th asphalt valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620287136.XU CN205838902U (en) | 2016-04-07 | 2016-04-07 | A kind of continuous modified asphalt production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620287136.XU CN205838902U (en) | 2016-04-07 | 2016-04-07 | A kind of continuous modified asphalt production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205838902U true CN205838902U (en) | 2016-12-28 |
Family
ID=57628503
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620287136.XU Expired - Fee Related CN205838902U (en) | 2016-04-07 | 2016-04-07 | A kind of continuous modified asphalt production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205838902U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106433157A (en) * | 2016-04-07 | 2017-02-22 | 无锡华通沥青新技术发展有限公司 | Continuous modified asphalt production system |
| CN109825323A (en) * | 2019-04-03 | 2019-05-31 | 杭州欣亿广告有限公司 | A kind of equipment of producing modified asphalt |
| CN109954458A (en) * | 2017-12-26 | 2019-07-02 | 宜兴市兴南复合材料厂有限公司 | Resin continuous production device |
-
2016
- 2016-04-07 CN CN201620287136.XU patent/CN205838902U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106433157A (en) * | 2016-04-07 | 2017-02-22 | 无锡华通沥青新技术发展有限公司 | Continuous modified asphalt production system |
| CN106433157B (en) * | 2016-04-07 | 2020-05-15 | 无锡华通沥青新技术发展有限公司 | Continuous modified asphalt production system |
| CN109954458A (en) * | 2017-12-26 | 2019-07-02 | 宜兴市兴南复合材料厂有限公司 | Resin continuous production device |
| CN109825323A (en) * | 2019-04-03 | 2019-05-31 | 杭州欣亿广告有限公司 | A kind of equipment of producing modified asphalt |
| CN109825323B (en) * | 2019-04-03 | 2020-11-24 | 广州新粤交通技术有限公司 | Modified asphalt production equipment |
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