CN204400908U - A kind of modifying asphalt production system - Google Patents
A kind of modifying asphalt production system Download PDFInfo
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- CN204400908U CN204400908U CN201520038946.7U CN201520038946U CN204400908U CN 204400908 U CN204400908 U CN 204400908U CN 201520038946 U CN201520038946 U CN 201520038946U CN 204400908 U CN204400908 U CN 204400908U
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- oil
- modifying asphalt
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- asphalt production
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Abstract
The utility model relates to a kind of system of producing modification bi tumenf orr oad.This modifying asphalt production system, comprises matrix pitch e Foerderanlage, matrix pitch heat riser, mixed whipping appts, properties-correcting agent e Foerderanlage, shears colloidal mill, modifying asphalt grows device, modifying asphalt take-off equipment, automatic control device and hot oil heater; Also comprise stablizer e Foerderanlage; Described mixed whipping appts comprises mixing tank and angle-inserting type agitator; Described modifying asphalt is grown device and is included the heat-conducting oil pipes of growing tank, paddle stirrer and being arranged in this growth tank; Described hot oil heater comprises oil cistern, expansion slot, filling pump, oil-gas separator, heat conduction oil circulating pump, heat transfer oil heater, oil outlet pipe, used oil pipe, cold oil displacement pipe.The utility model modifying asphalt production system production efficiency is high, and cost is low, and asphalt quality is stablized and save energy.
Description
Technical field
The utility model relates to a kind of equipment producing modifying asphalt, particularly a kind of system of producing modification bi tumenf orr oad.
Background technology
At present along with the development of China's motorway, more and more higher to the quality requirements of bi tumenf orr oad.For this reason, national spread modifying asphalt.But modified asphalt device throughput, inefficiency now in highway industry, asphalt quality can not ensure, energy dissipation.Meanwhile, shear the easy to wear or mill of colloidal mill mill to grind one's teeth in sleep easy fracture.In addition, in prior art, hot oil heater is when having a power failure suddenly, and furnace tubing and thermal oil temperature can raise fast, easily cause heating unit to damage; Thermal oil in hot oil heater isolated non-condensable gases and water vapour in temperature-rise period reduce the thermo-efficiency of hot oil heater; In hot oil heater prior art, when thermal oil is not enough, can not supplement in time.
Summary of the invention
In order to overcome the shortcoming of above-mentioned prior art, the utility model provides a kind of production efficiency high, and cost is low, and asphalt quality is stablized and the continuous modified asphalt production system of save energy.
The technical scheme in the invention for solving the technical problem is:
A kind of modifying asphalt production system of the present utility model, comprise matrix pitch e Foerderanlage, the matrix pitch heat riser be connected with this matrix pitch e Foerderanlage outlet conduit, with the mixed whipping appts of this matrix pitch heat riser pipeline communication, the properties-correcting agent e Foerderanlage be connected with this mixed whipping appts, the shearing colloidal mill be connected with this mixed whipping appts pipeline, device is grown with the modifying asphalt of this shearing colloidal mill pipeline communication, the modifying asphalt take-off equipment installing pipes and be communicated with is grown with this modifying asphalt, and control the automatic control device that described modifying asphalt production system is run and the hot oil heater that described modifying asphalt production system is heated,
Also comprise the stablizer e Foerderanlage be connected with described mixed whipping appts;
Described mixed whipping appts comprises mixing tank and angle-inserting type agitator, and described angle-inserting type agitator is fixedly installed on described mixing tank top near tank side place, and this agitator stir shaft to stretch into and crossing with mixing tank medullary ray to tank is tilted;
Described modifying asphalt grow device include grow tank, paddle stirrer and be arranged in this growth tank with the heat-conducting oil pipes of described hot oil heater pipeline communication;
Described hot oil heater comprises oil cistern, be positioned at described hot oil heater highest point and the expansion slot be connected with oil cistern pipeline, filling pump between oil cistern and expansion slot pipeline, be positioned at the oil-gas separator be connected below expansion slot and with expansion slot pipeline, the heat conduction oil circulating pump be connected with oil-gas separator pipeline, the heat transfer oil heater be connected with heat conduction oil circulating pump pipeline, connect the oil outlet pipe of described heat transfer oil heater and described modifying asphalt production system, connect the used oil pipe of described modifying asphalt production system and oil-gas separator, cold oil displacement pipe between described oil outlet pipe and oil cistern.
Further, described hot oil heater also comprises one end and is fixedly connected with described used oil pipe and the auxiliary exhaust pipe communicated, and straight up, the other end communicates with described expansion slot described auxiliary exhaust pipe.
Further, the mixing tank of described mixed whipping appts is the jacketed mix tanks of heat-conducting oil heating.
Further, described matrix pitch heat riser is two heat exchangers in series of heat-conducting oil heating.
Further, described angle-inserting type agitator is double-deck hinging type agitator.
Further, the stir shaft of described paddle stirrer is fixedly connected with three layers or four layers of paddle, and every one deck has two or three paddles.
Further, the mill material in described shearing colloidal mill is 17-4 steel alloy.
The beneficial effects of the utility model are: modifying asphalt production system production efficiency of the present utility model is high, the reliable and stable and save energy of asphalt quality.Meanwhile, shear colloidal mill mill material owing to have employed 17-4 steel alloy, mill is not easy to wear, and mill is ground one's teeth in sleep and do not ruptured.In addition, hot oil heater, when having a power failure suddenly, can not damage by available protecting heating unit; Thermal oil in hot oil heater isolated non-condensable gases and water vapour in temperature-rise period can all be discharged, and substantially increase the thermo-efficiency of hot oil heater; Hot oil heater, when thermal oil is not enough, can supplement automatically in time.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model
Fig. 2 is hot oil heater structural representation
Fig. 3 is hot oil heater schematic diagram
In figure: 1. bitumen feed pump, 2. under meter, 3. heat exchanger, 4. pressure unit, 5. temperature sensor, 6. jacketed mix tanks, 7. angle-inserting type agitator, 8. variable valve, 9. high level alarm, 10. fluid level transmitter, 11. properties-correcting agent e Foerderanlages, 12. stablizer e Foerderanlages, 13. pitch force (forcing) pumps, 14. pneumatic pitch butterfly valves, 15. shear colloidal mill, 16. grow tank, 17. paddle stirrers, 18. thermal oil coil pipes, 19. radar level gauges, 20. automatic control devices, 21. pitch Send out pumps, 22. hot oil heaters, 2201. oil cistern, 2202. expansion slot, 2203. filling pump, 2204. oil-gas separator, 2205. heat conduction oil circulating pump, 2206. oil inlet pipe, 2207. heat transfer oil heater, 2208. oil outlet pipe, 2209. used oil pipe, 2210. cold oil displacement pipes, 2211. auxiliary exhaust pipe, 2212. upflow tube.
Embodiment
In Fig. 1: matrix pitch e Foerderanlage comprises bitumen feed pump 1 and under meter 2.
In Fig. 1: matrix pitch heat riser, comprise the heat exchanger 3 of two series connection, this heat exchanger is provided with pressure unit 4 and temperature sensor 5.
In Fig. 1: mixed stirring device comprises jacketed mix tanks 6, the double-deck hinging type agitator 7 of angle-inserting type and controls the variable valve 8 of jacketed mix tanks 6 bitumen level, and high level alarm 9, fluid level transmitter 10, temperature sensor 5.
In Fig. 1: properties-correcting agent e Foerderanlage 11 delivery port and stablizer e Foerderanlage 12 delivery port communicate with jacketed mix tanks 6 respectively by jacketed mix tanks 6 top.
In Fig. 1: modifying asphalt grow device include grow tank 16, paddle stirrer 17 and be arranged in this growth tank with the heat-conducting oil pipes 18 of described hot oil heater pipeline communication, the stir shaft of described paddle stirrer 17 is fixedly connected with four layers of paddle, and every one deck has three paddles; Described growth tank 16 is provided with high level alarm 9, temperature sensor 5 and radar level gauge 19.
In Fig. 1: automatic control device 20, be made up of PLC, system program software, touch-screen, under meter 2, pressure unit 4, temperature sensor 5, variable valve 8, high level alarm 9, fluid level transmitter 10, pneumatic pitch butterfly valve 14 etc.
In Fig. 2: hot oil heater 22 comprises oil cistern 2201, be positioned at hot oil heater highest point and the expansion slot 2202 be connected with oil cistern pipeline, filling pump 2203 between oil cistern 1 and expansion slot 2 pipeline, be positioned at the oil-gas separator 2204 be connected below expansion slot 2202 and with expansion slot 2202 pipeline, the heat conduction oil circulating pump 2205 be connected with oil-gas separator 2204 pipeline, by the heat transfer oil heater 2207 that oil inlet pipe 2206 is connected with heat conduction oil circulating pump 2205, connect the oil outlet pipe 2208 of heat transfer oil heater 2207 and modifying asphalt production system, connect the used oil pipe 2209 of described modifying asphalt production system and oil-gas separator 2204, cold oil displacement pipe 2210 between oil outlet pipe 2208 and oil cistern 2201, and one end is fixedly connected with used oil pipe 2209 and the auxiliary exhaust pipe 2211 communicated, straight up, the other end communicates with expansion slot 2202 this auxiliary exhaust pipe 2211.Expansion slot 2202 is provided with the upflow tube 2212 leading to oil cistern 2201.
The utility model design uses matrix pitch e Foerderanlage, matrix pitch heat riser, mixed whipping appts, properties-correcting agent e Foerderanlage, stablizer e Foerderanlage, shears colloidal mill, modifying asphalt growth device, modifying asphalt take-off equipment, automatic control device, hot oil heater etc., achieves the integration of modifying asphalt production system.
Modifying asphalt production system production process described in the utility model mainly comprises: (1) matrix pitch enters heat exchanger 3 rapid heating of two series connection by bitumen feed pump 1 pump, then pump, enter mixing tank 6, automatically controlled the bitumen level in mixing tank 6 by variable valve 8 and fluid level transmitter 10; (2) properties-correcting agent adds mixing tank 6 according to the certain proportion of matrix pitch amount by properties-correcting agent e Foerderanlage 11, and stablizer adds mixing tank 6 according to the certain proportion of matrix pitch amount by stablizer e Foerderanlage 12; (3) properties-correcting agent, stablizer are mixed by angle-inserting type agitator 7 in mixing tank 6 with matrix pitch, high level alarm 9 controls bitumen level and full level alarm in tank, temperature sensor 4 measures temperature in tank, by the flow being controlled thermal oil in mixing tank 6 chuck by automatic control device 20, mixture temperature is controlled, bitumen level in fluid level transmitter 10 the real time measure tank, and bitumen level full level alarm in tank can be realized, and control bitumen level in tank by automatic control device 20; (4) material mixed through force (forcing) pump 13 enter shear colloidal mill 15 carry out shearings grinding after, enter modifying asphalt growth tank 16; (5) asphalt mixture material carries out modification growth at modifying asphalt growth tank 16; Four layers of paddle stirrer strengthen pitch flowing and mixing effect, high level alarm 9 controls bitumen level and full level alarm in tank, temperature sensor 5 measures temperature in tank, the flow being controlled thermal oil in thermal oil coil pipe 18 by automatic control device 20 is controlled mixture heating and temperaturel, bitumen level in radar level gauge 19 the real time measure tank, and control bitumen level in tank by automatic control device 20; (6), after having grown through 1-8 hour, finished product tank car or finished pot storage is sent to through pitch Send out pump 21; (7) thermal oil delivers to modifying asphalt production system from hot oil heater 22 through thermal oil oil outlet pipe 2208, heat and pitch Pipeline clip sleeve pipe companion heat for heat exchanger 3, mixing tank 6, shearing colloidal mill 15, growth tank 16, return hot oil heater 22 through thermal oil used oil pipe; (8), at the end of production process, use air compressor to purge asphalt delivery pipeline, avoid pitch accumulate in pipeline and block; (9) automatic control device 20, to be automatically adjusted to whole production process by PLC, system program software, touch-screen, under meter 2, pressure unit 4, temperature sensor 5, variable valve 8, high level alarm 9, fluid level transmitter 10, pneumatic pitch butterfly valve 14 etc. and controls.
Hot oil heater principle of work is: with liquefied petroleum gas (LPG), Sweet natural gas, town gas for the energy, by the heat energy that gas combustion produces by burner hearth, using thermal oil as heat-transfer medium, by high temperature oil pump, thermal oil is carried out mandatory circulation in systems in which, make it by the heating gone round and begun again, thus reach and meet the object that heat user (heating equipment or with thermal cycling) obtains required heat energy continuously; And the requirement of technological temperature and the high accuracy temperature control set in Production Flow Chart can be met.
The utility model hot oil heater 22 thermal oil injects flow process:
Thermal oil-filling pump 2203 dozens is to-expansion slot 2202-oil-gas separator 2204-heat conduction oil circulating pump 2205-heat transfer oil heater stove 2207-modifying asphalt production system
The utility model hot oil heater 22 thermal oil circulation process:
Heat conduction oil circulating pump 2205 exports-heat transfer oil heater 2207-asphalt production system-used oil pipe 2209-oil-gas separator 2204-strainer---heat conduction oil circulating pump 2205 entrance-so circulate
the main support equipment effect of the utility model hot oil heater 22
1, the effect of expansion slot 2202
1) to compensate and stabilization: redeeming thermal oil produces volume change during because of temperature variation, because expansion slot is placed in a high position, therefore also plays a part steady head.
2) metathesis: when having a power failure suddenly, with the cold thermal oil in groove, the thermal conductance deep fat in furnace tubing is replaced, to protect boiler tube and thermal oil.
3) scavenging action: after fresh oil injects asphalt production system, thermal oil isolated gas and vapour in temperature-rise period of whole system discharge by it.
4) repairing effect: when occurring that thermal oil is not enough in systems in which, can automatically supplement in time.
5) effect in the middle of: thermal oil first can be injected in groove when noting thermal oil to production system, then flow automatically in groove injection heating stove and whole system.
2, the effect of oil cistern 2201
1) provide and store total system need thermal oil;
2) when receiving expansion slot oil level superelevation the thermal oil of overflow or compensate for dilatation groove oil level low time need the thermal oil that compensates;
3) thermal oil owing to releasing after safety valve unlatching is accepted.
3, heat conduction oil circulating pump 2205 acts on
Circular-pump is the power of the closed circuit pump circulation of thermal oil, and it will have enough flows and lift, and is good seal performance, resistant to elevated temperatures oil pump.
4, heat transfer oil filter effect
Pipeline before thermal oil enters heat conduction oil circulating pump must arrange strainer, and conventional form has y-type structure or basket type structure.
Strainer is made up of strainer main cylinder and filter screen, for impurity in filtering piping system and the carbon granules be suspended in thermal oil and high polymers, plays the effect of protection recycle pump
5, oil-gas separator 2204 acts on
Oil-gas separator for separating of and non-condensable gases, water vapour and the low Volatile Colstituent got rid of in pipeline thermal oil.When temperature variation, thermal oil passes through the shock absorption of oil-gas separator back and forth between system and expansion slot.Thus ensure that thermal oil can stably run under liquid phase state.
6, filling pump 2203 act on gear filling pump be used for system supplement or from system extract thermal oil.
The foregoing is only specific case of the present utility model, understanding the utility model for helping, being not limited to the utility model.For one of ordinary skill in the art, according to invention thinking of the present utility model, any change that embodiment is done, equivalent replacement etc., all should be included within protection domain of the present utility model.
Claims (7)
1. a modifying asphalt production system, comprise matrix pitch e Foerderanlage, the matrix pitch heat riser be connected with this matrix pitch e Foerderanlage outlet conduit, with the mixed whipping appts of this matrix pitch heat riser pipeline communication, the properties-correcting agent e Foerderanlage be connected with this mixed whipping appts, the shearing colloidal mill be connected with this mixed whipping appts pipeline, device is grown with the modifying asphalt of this shearing colloidal mill pipeline communication, the modifying asphalt take-off equipment installing pipes and be communicated with is grown with this modifying asphalt, and control the automatic control device that described modifying asphalt production system is run and the hot oil heater that described modifying asphalt production system is heated,
It is characterized in that:
Also comprise the stablizer e Foerderanlage be connected with described mixed whipping appts;
Described mixed whipping appts comprises mixing tank and angle-inserting type agitator, and described angle-inserting type agitator is fixedly installed on described mixing tank top near tank side place, and this agitator stir shaft to stretch into and crossing with mixing tank medullary ray to tank is tilted;
Described modifying asphalt grow device include grow tank, paddle stirrer and be arranged in this growth tank with the heat-conducting oil pipes of described hot oil heater pipeline communication;
Described hot oil heater comprises oil cistern, be positioned at described hot oil heater highest point and the expansion slot be connected with oil cistern pipeline, filling pump between oil cistern and expansion slot pipeline, be positioned at the oil-gas separator be connected below expansion slot and with expansion slot pipeline, the heat conduction oil circulating pump be connected with oil-gas separator pipeline, the heat transfer oil heater be connected with heat conduction oil circulating pump pipeline, connect the oil outlet pipe of described heat transfer oil heater and described modifying asphalt production system, connect the used oil pipe of described modifying asphalt production system and oil-gas separator, cold oil displacement pipe between described oil outlet pipe and oil cistern.
2. modifying asphalt production system according to claim 1, it is characterized in that: described hot oil heater also comprises one end and is fixedly connected with described used oil pipe and the auxiliary exhaust pipe communicated, straight up, the other end communicates with described expansion slot described auxiliary exhaust pipe.
3. modifying asphalt production system according to claim 2, is characterized in that: the mixing tank of described mixed whipping appts is the jacket canister of heat-conducting oil heating.
4. modifying asphalt production system according to claim 3, is characterized in that: described matrix pitch heat riser is two heat exchangers in series of heat-conducting oil heating.
5. modifying asphalt production system according to claim 4, is characterized in that: described angle-inserting type agitator is double-deck hinging type agitator.
6. the modifying asphalt production system according to any one of claim 1 to 5, is characterized in that: the stir shaft of described paddle stirrer is fixedly connected with three layers or four layers of paddle, and every one deck has two or three paddles.
7. the modifying asphalt production system according to any one of claim 1 to 5, is characterized in that: the mill material in described shearing colloidal mill is 17-4 steel alloy.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520038946.7U CN204400908U (en) | 2015-01-21 | 2015-01-21 | A kind of modifying asphalt production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520038946.7U CN204400908U (en) | 2015-01-21 | 2015-01-21 | A kind of modifying asphalt production system |
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| Publication Number | Publication Date |
|---|---|
| CN204400908U true CN204400908U (en) | 2015-06-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520038946.7U Expired - Fee Related CN204400908U (en) | 2015-01-21 | 2015-01-21 | A kind of modifying asphalt production system |
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| Country | Link |
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| CN (1) | CN204400908U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104560087A (en) * | 2015-01-21 | 2015-04-29 | 中化弘润石油化工有限公司 | Modified asphalt production system |
| CN105733284A (en) * | 2016-04-07 | 2016-07-06 | 无锡华通沥青新技术发展有限公司 | Environment-friendly modified asphalt production system |
| CN108219813A (en) * | 2018-03-06 | 2018-06-29 | 国家能源投资集团有限责任公司 | Mesophase pitch and its continuous producing method and system |
-
2015
- 2015-01-21 CN CN201520038946.7U patent/CN204400908U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104560087A (en) * | 2015-01-21 | 2015-04-29 | 中化弘润石油化工有限公司 | Modified asphalt production system |
| CN105733284A (en) * | 2016-04-07 | 2016-07-06 | 无锡华通沥青新技术发展有限公司 | Environment-friendly modified asphalt production system |
| CN105733284B (en) * | 2016-04-07 | 2018-08-10 | 无锡华通沥青新技术发展有限公司 | A kind of environment-friendly modified asphalt production system |
| CN108219813A (en) * | 2018-03-06 | 2018-06-29 | 国家能源投资集团有限责任公司 | Mesophase pitch and its continuous producing method and system |
| CN108219813B (en) * | 2018-03-06 | 2020-08-25 | 国家能源投资集团有限责任公司 | Mesophase pitch and continuous production method and system thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150617 Termination date: 20170121 |