CN203545145U - Double pressure feed conveying system - Google Patents
Double pressure feed conveying system Download PDFInfo
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- CN203545145U CN203545145U CN201320548696.2U CN201320548696U CN203545145U CN 203545145 U CN203545145 U CN 203545145U CN 201320548696 U CN201320548696 U CN 201320548696U CN 203545145 U CN203545145 U CN 203545145U
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Abstract
The utility model discloses a double pressure feed conveying system and relates to the field of solid material conveying technologies. The system comprises a double pressure feed conveying vehicle, and a material receiving device or a material discharging device which is connected with the double pressure feed conveying vehicle. The double pressure feed conveying vehicle comprises a chassis and a main material tank which is arranged on the chassis; a cyclone separator, at least one filtering and dust removing device and a fluidization device are arranged on the main material tank; the fluidization device is used for fully mixing material and air and provided with at least one air compressor; the cyclone separator is arranged at an inlet of the main material tank and connected with the material receiving device; and the fluidization device is arranged at an outlet of the main material tank and connected with the material discharging device. Through the double pressure feed conveying system, the problems of same physical volume, maximum effective volume or maximum effective loading volume are solved; the double pressure feed conveying system is convenient to process, manufacture, mount and integrate, short in manufacture period and low in cost; space is greatly improved; filtering efficiency is improved; discharging concentration is reduced; a conveying vehicle is more environmental-friendly in work; and meanwhile, time for repairing and maintaining is saved and cost is also saved.
Description
Technical field
The utility model relates to the device in a kind of solid material conveying technology field, specifically a kind of pair of force feed delivery system.
Background technology
Two pressure bull ladles send two kinds of formulas containing pressure sending type and suction, and positive-pressure pneumatic is carried and negative-pressure pneumatic mode of movement, send equipment to be jointly arranged on a truck chassis conveying batch can and force feed, suction and have just formed force feed tank car, as bulk cement carrier; Inhale tank sending car, as dust collector automobile and two pressure waggon, they can realize remote clean the transporting of bulk cargo within the specific limits.
Force feed tank car mode is loose unpacked material to be fallen into conveying batch can naturally from eminence accepting material end (storage end), then garage is sailed to and discharge material end (exhaust end), connect flexible pipe, material is entered in the sealing feed bin with dust exhaustor by pressurized air.This mode, because storage end is unlimited open to atmosphere, easily causes airborne dust and pollution.
Inhaling tank sending car mode is vacuum pump, engine installation and the isolated by filtration system etc. of using dust collector automobile to carry, utilize negative pressure, by flexible pipe, the loose unpacked material of storage end is sucked and carries batch can, then garage is sailed to discharge place, open tail-gate, material is toppled over and drawn off, and this mode can cause secondary pollution when discharge.
Two pressure waggons are to integrate above-mentioned two kinds of modes, utilize pressurized air that the transmitting bulk material of storage end is arrived to batch can, then garage are sailed to exhaust end, connect flexible pipe, and material is entered in the sealing feed bin with dust exhaustor by pressurized air.This mode has solved the secondary pollution problem of above-mentioned two kinds of modes, but because equipment is complicated, expensive, popularize and acquire a certain degree of difficulty.
The whole working processs of two pressure waggons carry out under fully enclosed state, and do not run and emit, drop, be the necessary equipment of factory's cleaner production.Suction vehicle application is very extensive, in steel plant, and cement mill, chemical plant, mining sites etc. are located widespread use, apply the most ripe steel plant that surely belong to.The environment at position and the particulate dust transhipment work of craft dust removal ash such as suction vehicle is mainly under the blast furnace gravity, dry method, stokehold, groove of acknowledgement of consignment steel plant ironmaking, sintering, steel-making, coking.When vehicle arrives filler bin, start vehicle unit of vacuum material-suction system, the Feed system by surface facility sucks material in vehicle-mounted carrying tank; When vehicle arrives while connecting material storehouse, start vehicle pressure system, the system that connects material by surface facility by the material pressure in vehicle-mounted carrying tank body in the storehouse that connects material.The processes such as whole suction, transportation, discharge are all carried out under airtight condition, and dust does not leak and flies upward, and save the energy, meet International Environmental Protection standard.
Through the inspection of prior art is found, Chinese patent literature CN1807208B, open day 2006-07-26, discloses a kind of double-pressurized delivery vehicle mounted pneumatic delivery method and equipment thereof, and this technology packs material in airtight container into; Adopt pressurized air under sealing state by material from airtight container is sent to the major ingredient tank of carrying tank car, in tank, carry out material and air separation process; Transfer pot garage is sailed to exhaust end; Under sealing state, by pressurized air, material is entered in the sealing feed bin with dust exhaustor.Equipment comprises conveying tank car, carry tank car to there is car chassis and be arranged at major ingredient tank above it, by filter chamber's access valve and the tank connected filter chamber of major ingredient, manifold valve block, be arranged at the fluidizer of major ingredient tank tail end and supply compressed-air actuated air compressor, major ingredient tank is connected with feeding equipment by flexible pipe, and fluidizer is connected with discharge apparatus by discharge flexible pipe.But this technology waggon bag dust collector, filter efficiency is lower, and concentration of emission is high, and maintenance and maintenance intervals are long, and expense is high; Waggon has major ingredient chamber, cloth bag chamber (or auxiliary material chamber) to form complex structure, processing and manufacturing and installation integrated complex, manufacturing cycle is long, and cost is high, and lower because have major ingredient chamber, cloth bag chamber (or auxiliary material chamber), auxiliary tank to form effective volume or the internal dimensions of the loading space of main tank.
Utility model content
The utility model is for prior art above shortcomings, a kind of pair of force feed delivery system proposed, integral structure, simple in structure, solve same physical volume and there is maximum effective volume or maximum internal dimensions of the loading space problem, make processing and manufacturing and integrated convenience is installed, the manufacturing cycle is short, and cost is low; Simultaneously greatly saved space and improved filter efficiency, reduced concentration of emission, the waggon environmental protection more that works together, has saved maintenance and maintenance time simultaneously and has also saved expense.
The utility model is achieved through the following technical solutions:
The utility model relates to a kind of pair of force feed delivery system, comprising: two force feed waggons and the feeding equipment being attached thereto or discharge apparatus.
Described two force feed waggons comprise: chassis, be arranged at the major ingredient tank on chassis, this major ingredient tank is provided with cyclone, at least one dust removal by filtration device and for by material and the well-mixed fluidizer with at least one air compressor of air, wherein: cyclone is arranged at the entrance of major ingredient tank and is connected with feeding equipment, fluidizer is arranged at the outlet of major ingredient tank and is connected with discharge apparatus.
Described feeding equipment comprises: with the receiver bin pump of material feeding valve and blow-off valve, wherein: blow-off valve is arranged on pump top, storehouse, material feeding valve is arranged at the lower part outlet of receiver bin pump, the exit end of material feeding valve is connected with the entrance of major ingredient tank, and the top of receiver bin pump is connected and accepts pressurized air with the air compressor on major ingredient tank.
Described discharge apparatus comprises: several are with the discharge bin of filter collector, and the top of this filter collector and the outlet of major ingredient tank are connected to realize the discharge of waggon car.
Technique effect
Compared with prior art, the utility model technique effect comprises:
1) solve same physical volume and there is maximum effective volume or maximum internal dimensions of the loading space problem, make processing and manufacturing and integrated convenience is installed, manufacturing cycle is short, and cost is low, and whole car is not because having cloth bag chamber and auxiliary material chamber to bear malleation for tank body and negative pressure is more reasonable.Because there is no cloth bag chamber (or auxiliary material chamber) or waggon without auxiliary tank, the effective volume of car load is improved greatly, generally can improve 20% effective volume, in other words than general more than enough 20% the material that fills of car energy, the cost of the client's who saves unit time, raises the efficiency that to reduce costs be the great advantage of this car.Because there is no cloth bag chamber (or auxiliary material chamber) thereby or waggon without auxiliary tank alleviated deadweight make car load can load more material.
2) filter collector rather than with bag dust collector for waggon, has greatly saved space and has improved filter efficiency, has reduced concentration of emission, and the waggon environmental protection more that works together, has saved maintenance and maintenance time simultaneously and also saved expense;
3), because storage end and exhaust end have all been realized fully enclosed pneumatic conveying mode, therefore there is no secondary pollution problem;
4) two pressure conveying vehicles only need to provide for oneself an air compressor, can obtain the strength of accepting material and discharging material process and carry propulsion source, have simplified propulsion source equipment, have reduced cost;
5) owing to having cancelled a complete set of vacuum apparatus, save space, can use same car chassis, made the conveying batch can of larger volume, improved user's work efficiency;
6) owing to not using vacuum pump, can carry the material of higher temperature;
7), owing to adopting automobile as transfer transport, bulk cargo can be transported to remote or other unapproachable a plurality of material feedings places arbitrarily;
8) avoided pipeline airvey system length apart from hidden danger such as laying conveying pipes and pipe chokings.
Accompanying drawing explanation
Fig. 1 is the two pressure waggon schematic diagrams of the utility model;
Fig. 2 is the structural representation of two pressure transportation devices;
In figure, equipment is in material feeding state;
Fig. 3 is the structural representation of two pressure transportation devices;
In figure, equipment is in discharge state;
Fig. 4 is the material feeding schematic diagram of two pressure transportation devices;
In figure, equipment is in material feeding state;
Fig. 5 is the discharge schematic diagram of two pressure transportation devices;
In figure, equipment is in discharge state;
In figure: chassis 1, main hydraulic cylinder 2, air compressor 3, control housing 4, manifold valve block 5, fluidizer 6, discharge gate 7, major ingredient tank 8, material inlet 9, access valve 10, cyclone 11, safety valve 12, temperature measuring equipment 13, material level detector 14, device for pressure measurement 15, dust removal by filtration device 16, dust removal by filtration element 17, outlet valve assembly 18, storehouse pump blowing flexible pipe 19, the material feeding valve 20 of pump bottom, storehouse, receiver bin pump 21, receiver bin blow-off valve 22, pressurized air appendix 23, discharge flexible pipe 24, discharge bin 25, filter collector 26, material 27, air 28, LOAD CELLS 29, cylinder support 30, subframe 31.
Fig. 6 is the delivery technology schematic flow sheet of described in the utility model pair of pressure transportation device.
The specific embodiment
Below embodiment of the present utility model is elaborated; the present embodiment is implemented take technical solutions of the utility model under prerequisite; provided detailed embodiment and concrete operating process, but protection domain of the present utility model is not limited to following embodiment.
Embodiment 1
As depicted in figs. 1 and 2, the present embodiment comprises: two force feed waggons and the feeding equipment being attached thereto or discharge apparatus.
Described two force feed waggons comprise: chassis 1, be arranged at the One On The Chassis control housing 4 and with the major ingredient tank 8 of cyclone 11 and at least one dust removal by filtration device 16, wherein: cyclone 11 is connected with the material inlet 9 that is provided with access valve 10, major ingredient tank 8 is connected to realize two conveyings of pressing with feeding equipment or discharge apparatus respectively.
Described two force feed waggons are preferably provided with for by material and the well-mixed fluidizer 6 with at least one air compressor 3 of air, fluidizer 6 is connected with discharge apparatus by discharge flexible pipe 24, and air compressor 3 connects the tracheae of the rear connection receiver bin of manifold valve block 5 and discharge bin 26.
Described air compressor 3 is arranged on two pressure waggons or is directly placed in ground.
Described fluidizer 6 is achieved by the connecting device of major ingredient tank 8 afterbodys.
The entrance of described major ingredient tank 8 is realized by the access valve 10 being arranged on cyclone 11; The outlet of major ingredient tank 8 realizes by the discharge gate 7 being arranged on fluidizer 6.
Described major ingredient tank 8 is provided with the safety valve 12 for overvoltage protection.
Described major ingredient tank 8 is provided with temperature measuring equipment 13 and device for pressure measurement 15, its role is to measure temperature of charge, pressure and warning.
On described major ingredient tank 8, be also provided with material level detector 14, to survey the position of material, on subframe 31, cylinder support 30 be installed simultaneously, on cylinder support 30, LOAD CELLS is installed to weigh warning.
Described material level detector 14 is achieved by the connecting device of major ingredient tank 8 upper ends.
As shown in Figure 2 and Figure 4, described feeding equipment comprises: with the receiver bin pump 21 of material feeding valve 20 and blow-off valve 22, wherein: blow-off valve 22 is arranged on pump top, storehouse, material feeding valve 20 is arranged at the lower part outlet of receiver bin pump 21, access valve 10 on the major ingredient tank 8 of the exit end of material feeding valve 20 and two force feed tank cars is connected, and the top of receiver bin pump 21 is connected and accepts pressurized air with the air compressor 3 on major ingredient tank 8.
As shown in Figure 3 and Figure 5, described discharge apparatus comprises: several are with the discharge bin 25 of filter collector 26, and the top of this filter collector 26 and the outlet of major ingredient tank 8 are connected to realize the discharge of waggon car.
In the present embodiment, related system only adopts major ingredient tank 8 as unique volume of loaded material, and major ingredient tank 8 can not have auxiliary material chamber or cloth bag chamber, also can have auxiliary material chamber or cloth bag chamber.
When two force feed waggons adopt a plurality of major ingredient tank 8, wherein some auxiliary material chamber or cloth bag chambers can be used as are used.
The built-in dust removal by filtration element 17 of described dust removal by filtration device 16, this dust removal by filtration element 17 is breaker plate, sintered plate, perforated tube, moulds and burn pipe, sintered plate or sintering tubular type filtration replacement conventional cloth bag.
As shown in Figure 3, described chassis 1 adopts PTO mode connect and be with engine-driven air compressor 3, and for two force feed tank cars provide enough pressurized airs, meanwhile, car chassis also drives a Hydraulic Pump (not shown), and the hydraulic power of equipment is provided.
The present embodiment relates to the carrying method of said apparatus, comprises the following steps:
1, at storage end, pack material into airtight container, in receiver bin pump 21;
2, adopt pressurized air under sealing state by material from receiver bin pump 21 is sent to the major ingredient tank 8 of carrying tank car.
3, carry tank car after accepting bulk cargo, material is by cyclone settling, the dilatation of the cyclone 11 in major ingredient tank 8, most of material 27 sinks in major ingredient tank 8, gas 28 and a small amount of material 27 directly enter dust removal by filtration element 17, realization separates air and material, material is deposited in car body major ingredient tank 8, and clean air is discharged into atmosphere by outlet valve assembly 18.After material is filled, close the blow-off valve 20 of pump bottom, storehouse, stop blowing, take storehouse pump blowing flexible pipe 19 and pressurized air appendix 23 apart, finish charging process, car is reached to exhaust end;
4, transfer pot garage is sailed to exhaust end;
5,, under sealing state, by pressurized air, material is once entered in the sealing discharge bin 25 with filter collector 26, because there is no cloth bag chamber, auxiliary material chamber, auxiliary tank, as long as the material of drained major ingredient tank all materials that has been exactly drained.
6, transfer pot garage is sailed to storage end.
Described storage end refers to: original position of depositing loose unpacked material, and what equipment received material accepts material end, and receiver bin pump 21.
Described exhaust end refers to: the position of equipment exhausting material, discharge bin 25.
It is to open storehouse pump top material feeding valve 20 that described pressurized air presses down at sealing state the step of delivering to two force feed tank cars by material, and the bulk cargo in material storehouse is discharged in receiver bin pump 21, closes receiver bin blow-off valve 22; In the pump of storehouse, inflate, air pressure reaches specified value, after 1.5-2Kg/cm2, opens the material feeding valve 20 of pump bottom, storehouse, and bulk cargo in storehouse is sent in the major ingredient tank 8 of carrying tank car by storehouse pump blowing flexible pipe 19.
Material is entered in the sealing discharge bin 25 with filter collector 26 and being referred to by pressurized air described in step 5: adopt air compressor 3 to provide pressurized air to car body major ingredient tank 8 and fluidizer 6, this fluidizer 6 is that material and air are fully mixed, the special purpose device that solid material is become and can " be flowed " in pipeline, material in car is sent in the discharge bin 25 of sealing, clean air inherent filtration dust exhaustor 26 exhaust outlets are discharged, dust removal by filtration material by filter collector 26 is stayed in discharge bin, all everything is all to complete in major ingredient tank 8, do not pass through auxiliary material chamber, cloth bag chamber or auxiliary tank, complete the overall process of convey materials.
During work, first open feeding equipment top blow-off valve 22, after bulk cargo is discharged in the pump of storehouse, close top blow-off valve; Recycling pressurized air appendix 23 is to 21 inflations of receiver bin pump, and air pressure reaches after specified value, opens the material feeding valve 20 of pump bottom, storehouse, storehouse pump blowing flexible pipe 19 is sent in the major ingredient tank 8 of two force feed tank cars.
Described conveying tank car is when accepting bulk cargo, material is deposited in material in car body batch can by cyclone 11 whirlwind, dilatation sedimentation and dust removal by filtration device 16, clean air is entered to atmosphere by outlet valve assembly 18, and all are all to complete in main tank.After material is filled, close storehouse pump bottom discharge valve 20, stop blowing, take blowing flexible pipe and air supply pipe apart, finish charging process.Car is reached to exhaust end.
While receiving material, the air that air compressor 3 provides enters cyclone 11 from material inlet 9 by the access valve 10 of opening with material, fall into again major ingredient tank 8, material level detector 14 will check that material level carries out one-level warning at any time, and the LOAD CELLS weight that is greater than regulation when material of weighing is carried out secondary warning.In dust removal by filtration device 16, there are some dust removal by filtration elements 17, keep enough open areas, while carrying the air process dust removal by filtration element 17 of material, 17 of dust removal by filtration elements allow air to pass through, filtering also leaves remaining whole material, cleaned air enters dust removal by filtration device 16 through dust removal by filtration element 17, then discharges from outlet valve assembly 18.All everything is all to complete in major ingredient tank 8.
While discharging material, access valve 10 and outlet valve assembly 18 are and close, the pressurized air that air compressor 3 provides is to the interior pressurising of major ingredient tank 8, pressure reaches specified value, as distributed pressurized air by manifold group 5 after 1.5-2Kg, material is discharged to discharge apparatus by fluidizer 6 and discharge gate 7.While discharging material, must utilize main hydraulic cylinder 2 that the anterior Automatic continuous of major ingredient tank 8 is lifted to the highest, to thoroughly discharge material.
During work, after air compressor 3 starts, by manifold valve block 5, to tank body and fluidizer, provide pressurized air, by pressurized air, material in car is sent to and is received in feed bin, clean air is discharged through filter collector 26 exhaust outlets in major ingredient tank 8, and material is filtered separation and stays in reception feed bin.Complete the overall process of convey materials.
The present embodiment relates to two pressure conveying vehicle carrying methods and equipment thereof.Be more than the preferred forms of the present embodiment, according to the disclosed content of the present embodiment, some identical, replacement schemes that those of ordinary skill in the art can expect apparently, all should fall into the scope that the present embodiment is protected.As the modes of emplacement at dust removal by filtration element 17 and placement location, as dust removal by filtration element 17 adopts breaker plate, sintered plate, perforated tube, moulds and burn pipe, sintered plate, sintered pipes etc., can further reduce costs.
Claims (10)
1. two force feed delivery systems, is characterized in that, comprising: two force feed waggons and the feeding equipment being attached thereto or discharge apparatus;
Described two force feed waggons comprise: chassis, be arranged at the major ingredient tank on chassis, this major ingredient tank is provided with cyclone, at least one dust removal by filtration device and for by material and the well-mixed fluidizer with at least one air compressor of air, wherein: cyclone is arranged at the entrance of major ingredient tank and is connected with feeding equipment, fluidizer is arranged at the outlet of major ingredient tank and is connected with discharge apparatus;
The built-in dust removal by filtration element of described dust removal by filtration device, this dust removal by filtration element is breaker plate, sintered plate, perforated tube, moulds and burn pipe, sintered plate or sintering tubular type filtration replacement conventional cloth bag.
2. system according to claim 1, it is characterized in that, described feeding equipment comprises: with the receiver bin pump of material feeding valve and blow-off valve, wherein: blow-off valve is arranged on pump top, storehouse, material feeding valve is arranged at the lower part outlet of receiver bin pump, the exit end of material feeding valve is connected with the entrance of major ingredient tank, and the top of receiver bin pump is connected and accepts pressurized air with the air compressor on major ingredient tank.
3. system according to claim 1, is characterized in that, described discharge apparatus comprises: several are with the discharge bin of filter collector, and the top of this filter collector and the outlet of major ingredient tank are connected to realize the discharge of waggon car.
4. system according to claim 1, is characterized in that, described fluidizer is connected with discharge apparatus by discharge flexible pipe, connects the tracheae of receiver bin and discharge bin after air compressor connection manifold valve block.
5. according to the system described in claim 2 or 4, it is characterized in that, described air compressor is arranged on two pressure waggons or is directly placed in ground.
6. system according to claim 4, is characterized in that, described fluidizer is achieved by the connecting device of major ingredient tank afterbody.
7. system according to claim 1, is characterized in that, the entrance of described major ingredient tank is realized by the access valve being arranged on cyclone; The outlet of major ingredient tank realizes by the discharge gate being arranged on fluidizer.
8. according to the system described in claim 1 or 7, it is characterized in that, described major ingredient tank is provided with the safety valve for overvoltage protection.
9. according to the system described in claim 1 or 7, it is characterized in that, described major ingredient tank is provided with material level detector, LOAD CELLS, temperature measuring equipment and device for pressure measurement, so as to survey material position, weigh, measure temperature of charge, pressure and warning.
10. system according to claim 1, is characterized in that, described chassis adopts PTO mode connect and be with engine-driven air compressor, for two force feed tank cars provide enough pressurized airs.
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CN201320548696.2U CN203545145U (en) | 2013-09-04 | 2013-09-04 | Double pressure feed conveying system |
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CN201320548696.2U CN203545145U (en) | 2013-09-04 | 2013-09-04 | Double pressure feed conveying system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN115159125A (en) * | 2022-09-05 | 2022-10-11 | 东营市东达机械制造有限责任公司 | Polymer dry powder transportation, storage and feeding device and method |
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2013
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN115159125A (en) * | 2022-09-05 | 2022-10-11 | 东营市东达机械制造有限责任公司 | Polymer dry powder transportation, storage and feeding device and method |
CN115159125B (en) * | 2022-09-05 | 2022-12-09 | 东营市东达机械制造有限责任公司 | Polymer dry powder transportation, storage and feeding device and method |
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TR01 | Transfer of patent right |
Effective date of registration: 20160401 Address after: 201906 Baoshan District, Gu village, an industrial park, No. 1 Fu Road, No. 758, Shanghai Patentee after: Special Aviation Vehicles Co.,Ltd. Shanghai Address before: 200092 Shanghai city Yangpu District Guokang Road No. 100 room 402 Patentee before: SHANGHAI TECHNOLOGY CENTER, NANJING AVIC SPECIAL EQUIPMENT CO.,LTD. |
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140416 Termination date: 20210904 |
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CF01 | Termination of patent right due to non-payment of annual fee |