CN107599212A - A kind of process equipment using wet processing cloth pier kir - Google Patents
A kind of process equipment using wet processing cloth pier kir Download PDFInfo
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- CN107599212A CN107599212A CN201710872493.1A CN201710872493A CN107599212A CN 107599212 A CN107599212 A CN 107599212A CN 201710872493 A CN201710872493 A CN 201710872493A CN 107599212 A CN107599212 A CN 107599212A
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- Prior art keywords
- agitator tank
- kir
- cloth pier
- process equipment
- filter
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000004744 fabric Substances 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims abstract description 22
- 238000012545 processing Methods 0.000 title claims abstract description 19
- 230000008569 process Effects 0.000 title claims abstract description 18
- 239000010426 asphalt Substances 0.000 claims abstract description 31
- 238000010008 shearing Methods 0.000 claims abstract description 16
- 238000000227 grinding Methods 0.000 claims abstract description 15
- 230000001105 regulatory effect Effects 0.000 claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 15
- 238000005520 cutting process Methods 0.000 claims abstract description 10
- 238000005303 weighing Methods 0.000 claims abstract description 10
- 238000009826 distribution Methods 0.000 claims abstract description 8
- 239000002283 diesel fuel Substances 0.000 claims abstract description 7
- 239000011159 matrix material Substances 0.000 claims description 8
- 230000009471 action Effects 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 3
- 238000012216 screening Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 claims 1
- 239000011435 rock Substances 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 abstract description 5
- 238000010276 construction Methods 0.000 abstract description 3
- 238000001035 drying Methods 0.000 abstract description 2
- 150000001875 compounds Chemical class 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 230000008859 change Effects 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- QFUKUPZJJSMEGE-UHFFFAOYSA-N 5-(hydroxymethyl)-1-(3-methylbutyl)pyrrole-2-carbaldehyde Chemical compound CC(C)CCN1C(CO)=CC=C1C=O QFUKUPZJJSMEGE-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 238000010382 chemical cross-linking Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- VIKNJXKGJWUCNN-XGXHKTLJSA-N norethisterone Chemical compound O=C1CC[C@@H]2[C@H]3CC[C@](C)([C@](CC4)(O)C#C)[C@@H]4[C@@H]3CCC2=C1 VIKNJXKGJWUCNN-XGXHKTLJSA-N 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Road Paving Machines (AREA)
Abstract
The present invention discloses a kind of process equipment using wet processing cloth pier kir, and this kind of process equipment includes：Temperature regulating device, weigh lifting device, premixing agitating device, shearing grinding and filter and power distribution equipment；The temperature regulating device includes：Heat conducting oil pipe, head tank, thermocouple, heat exchanger, heater, diesel fuel tanks and burner；The weighing lifting device includes：Meter electronics, pneumatic tripper and elevator；The premixing agitating device includes：Conveyance conduit, the first agitator tank, the second agitator tank and the stirring motor being arranged on agitator tank；The shearing grinding and filter include：Premix pump, cutting mill and asphalt filter.The problems such as cloth pier processes of rock asphalt modified asphalt that the equipment is produced is used to prepare asphalt, and the Asphalt Mixture Performance variability caused by can solving dry process is big, construction workability is poor.
Description
Technical field
The present invention relates to a kind of pitch process equipment, and more specifically, the present invention relates to one kind to utilize wet processing cloth Dun Yan
The process equipment of pitch.
Background technology
In recent years, with the continuous growth of the volume of traffic, and the influence of the factor such as vehicle maximization, traffic channelization, drip
Blue or green road surface is faced with acid test.The early damage phenomenon of many new highways is more serious, as rut, Water Damage, it is loose,
Pit, check crack, serious curtailment service life of road surface bring huge economic loss, and wherein rut has become bituminous paving most
One of serious early disease.Kir has higher anti-flow deformation ability as a kind of high-quality natural ganoine bitumen,
With good rutting resistance, the performance of pitch and asphalt can be effectively improved, at home and abroad many high speeds are public
Road etc. is applied, and achieves good using effect.
The Gilsonite rock asphalt of the domestic and international mainstream product of kir including Utah, USA, France plus moral, Switzerland watt
The Sha Taier in Le Detela Floexs area, La Gusa, the Iranian Kerman sand Ah of Italy be regional and Indonesian cloth
Honest kir, Kelamayi kir and the Sichuan Guangyuan kir of Xinjiang of China.Wherein Indonesian BUTON rock asphalt
Turn into representative products therein by its excellent quality and abundant reserves.Pitch of the cloth pier kir greatly containing about 20%,
80% mineral constituents, has that nitrogen content high, " half polymerize " effect, weatherability be good, gummy, not the advantages of the content of wax.Composition
Kir microstructure is centered on the big micella molecule of bitumen, and plain asphalt small molecule is filled, the new colloid of encirclement
Structure.Because BUTON rock asphalt has flourishing network structure, therefore after being mixed with plain asphalt, can by plain asphalt molecule its
It is brought into asphalt, effectively strengthens intermolecular force and polar bond effect, and wax, naphthalene equimolecular can be converted or divided
Son group, chemical crosslinking, polymerization generation macromolecular network structure are formed, the low-density surface charge of bulky grain pitch aggregation can
Effectively absorption affinity, improvement wetability of the enhancing to mineral building stones, is finally reached the purpose for improving Asphalt Mixture Performance.
The application method of kir, two kinds of wet method and dry method can be divided into, the former changing using bitumen as matrix pitch
Property agent use；The latter then uses bitumen as the outer-penetrating agent of compound, is added during the mixing of compound.Relatively
For, wet processing has the advantages of easy to control the quality, stable performance, is more suitable for engineer applied, while BUTON rock asphalt has
The technical characterstics such as high softening-point, meltbility difference, during dry use, can not fully it be merged with compound in the short time, property
Can also it have a greatly reduced quality.Therefore, " wet method " production technology is the developing direction of BUTON rock asphalt popularization and application.
The information for being disclosed in the background of invention technology segment is merely intended to deepen the reason of the general background technology to the present invention
Solution, and be not construed as recognizing or imply known to those skilled in the art existing of the information structure in any form
Technology.
The content of the invention
Equipment is processed to cloth pier kir using wet processing it is an object of the invention to provide one kind.
Using the process equipment of wet processing cloth pier kir, it includes this kind：Temperature regulating device, weigh lifting device, be pre-
Mixed stirring device, shearing grinding and filter and power distribution equipment；
The temperature regulating device includes：Heat conducting oil pipe, head tank, thermocouple, heat exchanger, heater, diesel fuel tanks and burning
Device；Conduction oil is transported in heater and the heater passes through heat conducting oil pipe, head tank and heat exchanger and agitator tank phase
Even；The temperature regulating device is configured to the heat exchange action of the continuous heating and heat exchanger by diesel fuel tanks and burner, is set to each
It is standby to be preheated and cloth pier kir is heated；
The weighing lifting device includes：Meter electronics, pneumatic tripper and elevator；The weighing lifting device configures
(to weigh quantitative cloth pier kir by meter electronics, and cloth pier that is broken and being dehydrated having been carried out by elevator
Kir is promoted to feeding mouth, and the cloth pier kir after screening is added in agitator tank by pneumatic tripper；
The premixing agitating device includes：Conveyance conduit, the first agitator tank, the second agitator tank and it is arranged on agitator tank
On stirring motor；First agitator tank and the second agitator tank are connected by conveyance conduit with the heat exchanger and heater, are passed through
Matrix pitch after preheating is pumped to the first agitator tank or the second agitator tank by head tank, and is made in agitator tank after temperature rise
Start stirring motor；
The shearing grinding and filter include：Premix pump, cutting mill and asphalt filter；The shearing grinding and mistake
Filter device is configured to that the premix in agitator tank is pumped into cutting mill by premix pump, to carry out mixing shear action,
And the cloth pier kir after processing is transported in asphalt filter, to be filtered to it；
The power distribution equipment is to the temperature regulating device, weighing lifting device, premixing agitating device and shearing grinding and mistake
Filter device is powered.
Preferably, the temperature regulating device also includes：The valve being arranged between the heat conducting oil pipe and head tank.
Preferably, the top of first agitator tank is provided with the first batching hole, and the top of second agitator tank is provided with the
Two batching holes.
Preferably, it is respectively equipped with steam vent at the top of first agitator tank and the second agitator tank.
Preferably, the stirring motor is started when temperature is increased to 160 DEG C~170 DEG C in agitator tank.
It is highly preferred that the time being stirred by stirring motor is 0.5 to 1 hour.
Preferably, the shearing grinding and filter also include backflow insulation threeway, the premix in agitator tank via
The backflow is incubated threeway and is pumped into the cutting mill.
The cloth pier processes of rock asphalt modified asphalt that the equipment is produced is used to prepare asphalt, can solve dry process and be made
Into Asphalt Mixture Performance variability it is big, construction workability is poor the problems such as, while prepare asphalt also have
High-temperature behavior and water stabilizing are more preferably, construction workability is high, the features such as easily storing, to be suitable for large-scale production.
Brief description of the drawings
The exemplary embodiment of the present invention is described in more detail below in conjunction with accompanying drawing.For clarity, no
Shown with identical part in accompanying drawing with identical label.It should be noted that accompanying drawing only plays signal effect, it is not necessarily pressed
Drawn according to ratio.In the accompanying drawings：
Fig. 1 is the structural representation of the process equipment using wet processing cloth pier kir of the present invention.
Embodiment
The exemplary embodiment of the present invention is described in detail below with reference to appended accompanying drawing.
With reference to shown in Fig. 1, using the process equipment of wet processing cloth pier kir, it includes this kind：Temperature regulating device, weighing
Lifting device, premixing agitating device, shearing grinding and filter and power distribution equipment.
The power distribution equipment include control electrical control cubicles, electric power system of the device as equipment for integrated processing, have overload,
The defencive functions such as short circuit, open-phase protection, it can be combined according to actual control, can both realize that single cabinet automatically controls, and also may be used
To realize more cabinets controls and form Distributed Control System by EPA or industrial field bus network.
The temperature regulating device includes：Heat conducting oil pipe 8, valve 9, head tank 10, thermocouple 11, heat exchanger 7, heater
15th, diesel fuel tanks 26 and burner 28.Specifically, conduction oil is transported in heater 15 and the heater passes through heat-conducting oil pipes
Road 8, valve 9, head tank 10 are connected with heat exchanger 7 and agitator tank, ultimately form the temperature regulating device of UNICOM and circulation.It is in addition, logical
The continuous heating of diesel fuel tanks 26 and burner 28 and the heat exchange action of heat exchanger 7 are crossed, reaches pre-heating device and heated asphalt
Purpose.
The weighing lifting device includes：Meter electronics 22, pneumatic tripper 37 and elevator 42.Pass through electronic measurement
Device 22 weighs the cloth pier kir for taking certain volume, and will carry out broken by elevator 42 and " activation " punishment such as be dehydrated
Cloth pier kir be promoted to feeding mouth, the cloth pier kir after screening is added into two finally by pneumatic tripper 37 stirs
Mix in tank.
The premixing agitating device includes：Conveyance conduit 33, the first agitator tank 34, the second agitator tank 38 and stirring motor
43.Specifically, the first agitator tank 34 and the second agitator tank 38 pass through conveyance conduit 33 and the heat exchanger and heater phase respectively
Even.In addition the top of the agitator tank 38 of the first agitator tank 34 and second is respectively equipped with steam vent 3.
First, the matrix pitch after preheating is fed intake via be arranged on top first respectively by head tank, valve etc.
The batching hole 39 of hole 36 and second is pumped to the first agitator tank 34 or the second agitator tank 38, then, passes through thermocouple, conduction oil etc.
Heat effect makes temperature in tank rise to 160 DEG C~170 DEG C, now opens agitating device.Then by 1/2 design quantity and in high temperature
The lower cloth pier kir for carrying out hot fine grinding is slowly added in matrix pitch, i.e., in the first agitator tank 34 and the second agitator tank 38,
Bian Jiabu pier kir side stirring 0.5h~1h (hour).Finally, add remaining cloth pier kir, continue stir 0.5h~
1h, cloth pier kir is tentatively mixed with matrix pitch, form premix.Characterized, found " living by high temperature by micro image
Kir molecular polarity after change " is extremely strong, and the resin in the asphaltene molecule and kir in matrix pitch, ash content are all connected to
Together, a kind of multidimensional network structure of stabilization is formed, effectively increases the performance of matrix pitch.
The shearing grinding and filter include：Premix pump 4, cutting mill 1 and asphalt filter 2.Specifically, pass through
Premix in agitator tank is pumped into cutting mill 1 by premix pump 4, to carry out sufficiently mixing shear action, then, through returning
Flow tube enters in filter, and gravel content should be the 20% of 300 mesh in the cloth pier kir compound after filtering, 200 purposes
30%, the 50% of 100 mesh, qualified finished fabric pier kir compound is under the control action of flowmeter and screw pump, pumping
To hold-up tank, according to code requirement, reasonably stored, for future use.In addition, shearing grinding and filter also include
Flow back insulation threeway 31, and the premix in agitator tank is incubated threeway 31 via the backflow and is pumped into the cutting mill 1.This
Outside, the power distribution equipment is carried out to temperature regulating device, weighing lifting device, premixing agitating device and shearing grinding and filter
Power supply.
The description above presented to the specific illustrative embodiment of the present invention is in order at the purpose of illustration and description.Above
Description be not intended to turn into milli exhaustively, be not intended to limit the invention to disclosed precise forms, it is clear that root
Much change according to above-mentioned teaching and change is all possible.It is to explain this hair to select illustrative embodiments and be described
Bright certain principles and its practical application, so that others skilled in the art can realize and utilize each of the present invention
Kind illustrative embodiments and its various selection forms and modification.The scope of the present invention be intended to by appended claims and
Its equivalents is limited.
Claims (7)
- A kind of 1. process equipment using wet processing cloth pier kir, it is characterised in that including：Temperature regulating device, weigh lifting dress Put, be pre-mixed agitating device, shearing grinding and filter and power distribution equipment；The temperature regulating device includes：Heat conducting oil pipe (8), head tank (10), thermocouple (11), heat exchanger (7), heater (15), diesel fuel tanks (26) and burner (28)；Conduction oil is transported in heater (15) and the heater passes through conduction oil Pipeline (8), head tank (10) are connected with heat exchanger (7) and agitator tank；The temperature regulating device is configured to by diesel fuel tanks (26) and combustion The continuous heating of burner (28) and the heat exchange action of heat exchanger (7), are preheated to each equipment and to cloth pier kir Heated；The weighing lifting device includes：Meter electronics (22), pneumatic tripper (37) and elevator (42)；The weighing is lifted Device is configured to weigh quantitative cloth pier kir by meter electronics (22), and will have been broken by elevator (42) Cloth pier kir that is broken and being dehydrated is promoted to feeding mouth, and is added the cloth pier kir after screening by pneumatic tripper (37) Enter into agitator tank；The premixing agitating device includes：Conveyance conduit (33), the first agitator tank (34), the second agitator tank (38) and setting Stirring motor (43) on agitator tank；First agitator tank (34) and the second agitator tank (38) by conveyance conduit (33) with it is described Heat exchanger is connected with heater, and the matrix pitch after preheating is pumped into the first agitator tank (34) or the second stirring by head tank Tank (38), and make to start stirring motor after temperature rise in agitator tank；The shearing grinding and filter include：Premix pump (4), cutting mill (1) and asphalt filter (2)；The shearing is ground Mill and filter are configured to that the premix in agitator tank is pumped into cutting mill (1) by premix pump (4), to be mixed Shear action is closed, and the cloth pier kir after processing is transported in asphalt filter (2), to be filtered to it；The power distribution equipment is ground by the temperature regulating device, weighing lifting device, premixing agitating device and shearing and filtering dress Put and be powered.
- 2. the process equipment according to claim 1 using wet processing cloth pier kir, it is characterised in that：The temperature control Device also includes：The valve (9) being arranged between the heat conducting oil pipe (8) and head tank (10).
- 3. the process equipment according to claim 1 using wet processing cloth pier kir, it is characterised in that：Described first The top of agitator tank (34) is provided with the first batching hole (36), and the top of second agitator tank (38) is provided with the second batching hole (39)。
- 4. the process equipment using wet processing cloth pier kir according to claims 1 to 3 any one, its feature exist In：Steam vent (3) is respectively equipped with the top of first agitator tank (34) and the second agitator tank (38).
- 5. the process equipment according to claim 1 using wet processing cloth pier kir, it is characterised in that：Work as agitator tank Interior temperature is increased to start the stirring motor at 160 DEG C~170 DEG C.
- 6. the process equipment according to claim 5 using wet processing cloth pier kir, it is characterised in that：Pass through stirring The time that motor is stirred is 0.5 to 1 hour.
- 7. the process equipment according to claim 1 using wet processing cloth pier kir, it is characterised in that：The shearing Grinding and filter also include backflow insulation threeway (31), the premix in agitator tank be incubated threeway (31) via the backflow and It is pumped into the cutting mill (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710872493.1A CN107599212A (en) | 2017-09-25 | 2017-09-25 | A kind of process equipment using wet processing cloth pier kir |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710872493.1A CN107599212A (en) | 2017-09-25 | 2017-09-25 | A kind of process equipment using wet processing cloth pier kir |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107599212A true CN107599212A (en) | 2018-01-19 |
Family
ID=61058181
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710872493.1A Pending CN107599212A (en) | 2017-09-25 | 2017-09-25 | A kind of process equipment using wet processing cloth pier kir |
Country Status (1)
| Country | Link |
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| CN (1) | CN107599212A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109212633A (en) * | 2018-08-13 | 2019-01-15 | 江苏硕延光学眼镜有限公司 | A kind of macromolecule resin eyeglass and its preparation process with shock resistance |
| CN110215874A (en) * | 2019-05-05 | 2019-09-10 | 深圳市格瑞实业发展有限公司 | A kind of flow-type multifunctional modified asphalt production equipment |
| CN113372637A (en) * | 2021-06-08 | 2021-09-10 | 江苏洁润管业有限公司 | High-gloss antibacterial PE water supply pipe and preparation method and device thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2488954Y (en) * | 2001-07-09 | 2002-05-01 | 毕庆柏 | Asphalt modification machine of zoom type in times of complete milling |
| CN2908601Y (en) * | 2006-06-27 | 2007-06-06 | 浙江大学 | Improved modified asphalt production equipment |
| CN104371340A (en) * | 2014-11-07 | 2015-02-25 | 交通运输部科学研究院 | Styrene-butadiene rubber modified asphalt mixture and preparation method thereof |
| CN105735089A (en) * | 2016-04-07 | 2016-07-06 | 无锡华通沥青新技术发展有限公司 | Energy-saving type modified asphalt production system |
| CN207415747U (en) * | 2017-09-25 | 2018-05-29 | 交通运输部科学研究院 | A kind of process equipment using wet processing cloth pier rock asphalt |
-
2017
- 2017-09-25 CN CN201710872493.1A patent/CN107599212A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2488954Y (en) * | 2001-07-09 | 2002-05-01 | 毕庆柏 | Asphalt modification machine of zoom type in times of complete milling |
| CN2908601Y (en) * | 2006-06-27 | 2007-06-06 | 浙江大学 | Improved modified asphalt production equipment |
| CN104371340A (en) * | 2014-11-07 | 2015-02-25 | 交通运输部科学研究院 | Styrene-butadiene rubber modified asphalt mixture and preparation method thereof |
| CN105735089A (en) * | 2016-04-07 | 2016-07-06 | 无锡华通沥青新技术发展有限公司 | Energy-saving type modified asphalt production system |
| CN207415747U (en) * | 2017-09-25 | 2018-05-29 | 交通运输部科学研究院 | A kind of process equipment using wet processing cloth pier rock asphalt |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109212633A (en) * | 2018-08-13 | 2019-01-15 | 江苏硕延光学眼镜有限公司 | A kind of macromolecule resin eyeglass and its preparation process with shock resistance |
| CN110215874A (en) * | 2019-05-05 | 2019-09-10 | 深圳市格瑞实业发展有限公司 | A kind of flow-type multifunctional modified asphalt production equipment |
| CN113372637A (en) * | 2021-06-08 | 2021-09-10 | 江苏洁润管业有限公司 | High-gloss antibacterial PE water supply pipe and preparation method and device thereof |
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Application publication date: 20180119 |