CN204382569U - Maturation process system sent out in advance by a kind of polystyrene - Google Patents
Maturation process system sent out in advance by a kind of polystyrene Download PDFInfo
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- CN204382569U CN204382569U CN201520021113.XU CN201520021113U CN204382569U CN 204382569 U CN204382569 U CN 204382569U CN 201520021113 U CN201520021113 U CN 201520021113U CN 204382569 U CN204382569 U CN 204382569U
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Abstract
The utility model relates to a kind of polystyrene and sends out maturation process system in advance, belongs to plastic product processing technical field.Comprise prefoam device, fluidizing drying bed and maturation process device; Prefoam device connects fluidizing drying bed by voltage stabilizing blow-off valve, fluidizing drying bed by flood dragon conveyer connection maturation process device; The utility model, by changing existing pre-equipment and slaking chamber structure, simplifies fluidizing drying bed, overcomes the deficiency that high, the fluidizing drying bed drying efficiency of the fluidized drying energy consumption existed in prior art is low, slaking chamber structure complicated and slaking storehouse energy consumption is high.
Description
Technical field
The utility model relates to a kind of polystyrene and sends out maturation process system in advance, belongs to plastic product processing technical field.
Background technology
Existing polystyrene sends out system in advance primarily of prefoam device, prefoam device is connected with fluidizing drying bed, prefoam device is connected with steam boiler, expandable polystyrene raw material is carried out prefoam by prefoam device in steam, and carries out drying, maturation process in fluidizing drying bed for the expandable polystyrene raw material feeding after prefoam.Expandable polystyrene raw material after maturation process send steam to foam.After expandable polystyrene raw material is put into prefoam device, heating expandable polystyrene raw material raw material by leading to steam to prefoam device, thus foam, also needing to pass into compressed air to control to press in prefoam device.Its deficiency existed is: 1, steam utilization is insufficient, and compressed-air actuated passing into can reduce heating-up temperature locally, and therefore the overall energy consumption of equipment is larger; 2, Steam Heating process can produce a large amount of moisture content and enters in expandable polystyrene raw material, extend fluidizing drying bed in the dry processing time, greatly reduce production efficiency; 3, fluidizing drying bed also to be sent out in advance by Steam Heating or heated-air drying after polystyrene foam, still need to consume a large amount of heat energy; 4, maturation process needs to arrange multiple special slaking storehouse, and arrange the power-driven mechanism of more multiple feeding pipe or the conversion of slaking storehouse, therefore system architecture is comparatively complicated, and not only construction cost is high, and maintenance work difficulty.
Such as on 04 16th, 2014, Chinese utility model patent Authorization Notice No. CN 203542965U, maturation process integrated system sent out in advance by disclosed a kind of polystyrene, exactly steam is directly sent in foamed pot, expandable polystyrene raw material containing a large amount of moisture content enters fluidizing drying bed, just need by heated-air drying process, still need to consume a large amount of heat energy, and extend drying time; More than three slaking storehouses need to arrange rotating disc, consume a large amount of power consumptions, and driving mechanism is also comparatively complicated.
Utility model content
The utility model is just for the deficiency that prior art exists, a kind of polystyrene is provided to send out maturation process system in advance, by changing existing pre-equipment and slaking chamber structure, simplify fluidizing drying bed, overcome the deficiency that high, the fluidizing drying bed drying efficiency of the fluidized drying energy consumption existed in prior art is low, slaking chamber structure complicated and slaking storehouse energy consumption is high.
For solving the problem, technical solution adopted in the utility model is as follows:
Maturation process system sent out in advance by a kind of polystyrene, comprises prefoam device, fluidizing drying bed and maturation process device; Prefoam device connects fluidizing drying bed by voltage stabilizing blow-off valve, fluidizing drying bed by flood dragon conveyer connection maturation process device; Described prefoam device is a cylinder tank body having interlayer barrel, and there is lock wind feed hopper side, cylinder tank body top; Cylinder tank body top dome head has the agitating device and forcing pipe that stretch into tank inner chamber, and forcing pipe connects air compressor machine aspirating end; The interlayer outer wall of cylinder tank body top dome head is provided with the steam exhaust pipe being communicated with interlayer, and steam exhaust pipe connects UTILIZATION OF VESIDUAL HEAT IN case; Arrange voltage stabilizing blow-off valve in the side of cylinder tank body lower sleeve wall, the interlayer outer wall of opposite side barrel is provided with the steam inlet duct of connection interlayer; Discharge outlet is also had at the outer tube wall of cylinder tank base interlayer; The discharge gate of described voltage stabilizing blow-off valve stretch into described fluidizing drying bed in; In fluidizing drying bed, be provided with air dispersion pipe, described air dispersion tube-surface is evenly provided with multiple dispersion hole, and described air dispersion pipe one section is closed, and the other end connects described air intake duct; Described maturation process device is made up of vertical traffic cycle, support fixed axis and multiple slaking bucket, and vertical traffic cycle is arranged on by wheel hub and supports on fixed axis, can rotate around support fixed axis; A commutation slip ring also fixed coaxially by the wheel hub of above-mentioned vertical traffic cycle; Receiver is had at the hypomere of vertical traffic cycle; Described multiple slaking bucket is uniformly set on described vertical traffic cycle excircle, and the quarrel of slaking bucket is opened wide by vertical traffic cycle radial direction; Each quarrel is all equipped with photoelectric sensor, and the signal output part of these photoelectric sensors is connected on each movable contact of described commutation slip ring respectively, and the static contact of commutation slip ring connects driver by holding wire; Between the wheel hub of above-mentioned vertical traffic cycle and support fixed axis, electric control brake hoof is housed; Above-mentioned driver connects electric control brake hoof.
Further, described lock wind feed hopper on the blanking channel of hopper, establishes sealing blocking connection first pulsometer to control it open and close.
Further, described UTILIZATION OF VESIDUAL HEAT IN case is for comprising thermal-insulating body, and box house lays coil pipe; The upper surface of thermal-insulating body has two stand pipe of leading in casing, wherein a stand pipe upper end mouth of pipe connects air filtration cap, lower end mouth of pipe straight cutting casing its lowest position, another root stand pipe upper end mouth of pipe connects air compressor machine suction end, and the lower end mouth of pipe communicates with box house highest position; Two pipe ports of described coil pipe extend outside thermal-insulating body, and a pipe port is wherein that air inlet is connected with described steam exhaust pipe, and another pipe port is outside the in line casing in gas outlet.
Further, described voltage stabilizing blow-off valve is made up of pressurization cylinder, valve plug, connecting rod and the second pulsometer; Pressurization cylinder is one end open, and another end is closed and barrel opens the cylinder of side opening; Valve plug is positioned at supercharging cylindrical shell; Through pressurization cylinder end-blocking in the middle part of above-mentioned connecting rod, one end connects valve plug, and another end connects the second pulsometer; The opening of above-mentioned supercharging cylindrical shell is in cylinder tank intracoelomic cavity bottom, and side opening is in cylinder tank external body, and aperture forms discharge gate down.
Compared with prior art, implementation result of the present utility model is as follows:
Maturation process system sent out in advance by polystyrene described in the utility model, heating steam is in the interlayer of prefoam device cylinder tank body, by interlayer heat transfer also agitating heating expandable polystyrene raw material, steam does not directly contact with expandable polystyrene raw material, and the moisture content that Steam Heating process produces can not enter in expandable polystyrene raw material.Thus, enter fluidizing drying bed expandable polystyrene raw material without the need to logical preheated air, greatly shorten fluidizing drying bed in the dry processing time, improve production efficiency; Save heat energy; Described maturation process device is by vertical traffic cycle, and rely on the deadweight of slaking bucket to drive the work of vertical traffic cycle slow circumvolve, do not consume electric energy, driving mechanism is simple, thus reduces construction cost, and is conducive to daily maintenance.
Accompanying drawing explanation
Fig. 1 is that maturation process integrated system structural representation sent out in advance by polystyrene described in the utility model.
Be labeled as in figure: 1 voltage stabilizing blow-off valve; 2 flood dragon conveyers; 3 cylinder tank bodies; 4 lock wind feed hoppers; 5 agitating devices; 6 forcing pipes; 7 air compressor machines; 8 steam exhaust pipes; 9 UTILIZATION OF VESIDUAL HEAT IN casees; 10 steam inlet ducts; 11 discharge outlet; 12 air dispersion pipes; 13 air intake ducts; 14 vertical traffic cycles; 15 support fixed axis; 16 slaking buckets; 17 commutation slip rings; 18 receivers; 19 photoelectric sensors; 20 drivers; 21 sealing blockings; 22 first pulsometers; 23 coil pipes; 24 air filtration caps; 25 pressurization cylinders; 26 valve plugs; 27 connecting rods; 28 second pulsometers.
Detailed description of the invention
Below in conjunction with specific embodiments content of the present utility model is described.
As shown in Figure 1
Maturation process system sent out in advance by a kind of polystyrene, comprises prefoam device, fluidizing drying bed and maturation process device; Prefoam device connects fluidizing drying bed by voltage stabilizing blow-off valve 1, fluidizing drying bedly connects maturation process device by flood dragon conveyer 2; Described prefoam device is a cylinder tank body 3 having interlayer barrel, and there is lock wind feed hopper 4 side, cylinder tank body 3 top; Cylinder tank body 3 top dome head has the agitating device 5 and forcing pipe 6 that stretch into tank inner chamber, forcing pipe 6 connects air compressor machine 7 aspirating end; The interlayer outer wall of cylinder tank body 3 top dome head is provided with the steam exhaust pipe 8 being communicated with interlayer, and steam exhaust pipe 8 connects UTILIZATION OF VESIDUAL HEAT IN case 9; Arrange voltage stabilizing blow-off valve 1 in the side of cylinder tank body 3 bottom barrel, the interlayer outer wall of opposite side barrel is provided with the steam inlet duct 10 of connection interlayer; Bottom cylinder tank body 3, the outer tube wall of interlayer also has discharge outlet 11; The discharge gate of described voltage stabilizing blow-off valve 1 stretch into described fluidizing drying bed in; In fluidizing drying bed, be provided with air dispersion pipe 12, described air dispersion pipe 12 surface uniform is provided with multiple dispersion hole, and described air dispersion pipe 12 1 sections is closed, and the other end connects air intake duct 13; Described maturation process device is made up of vertical traffic cycle 14, support fixed axis 15 and 12 slaking buckets 16, and vertical traffic cycle 14 is arranged on by wheel hub and supports on fixed axis 15, can rotate around support fixed axis 15; A commutation slip ring 17 also fixed coaxially by the wheel hub of above-mentioned vertical traffic cycle 14; Receiver 18 is had at the hypomere of vertical traffic cycle 14; Described multiple slaking bucket 16 is uniformly set on described vertical traffic cycle 14 excircle, and the quarrel of slaking bucket 16 is opened wide by vertical traffic cycle 14 radial direction; Photoelectric sensor 19 is all equipped with in each quarrel, and the signal output part of these photoelectric sensors 19 is connected on each movable contact of described commutation slip ring 17 respectively, and the static contact of commutation slip ring 17 connects driver 20 by holding wire; Between the wheel hub of above-mentioned vertical traffic cycle 14 and support fixed axis 15, electric control brake hoof is housed; Above-mentioned driver 20 connects electric control brake hoof.
Described lock wind feed hopper 4 on the blanking channel of hopper, establishes sealing blocking (21) to connect the first pulsometer (22) control its keying.
Described UTILIZATION OF VESIDUAL HEAT IN case 9 is for comprising thermal-insulating body, and box house lays coil pipe (23); The upper surface of thermal-insulating body has two stand pipe of leading in casing, wherein a stand pipe upper end mouth of pipe connects air filtration cap (24), lower end mouth of pipe straight cutting casing its lowest position, another root stand pipe upper end mouth of pipe connects air compressor machine 7 suction end, and the lower end mouth of pipe communicates with box house highest position; Two pipe ports of described coil pipe (23) extend outside thermal-insulating body, and a pipe port is wherein that air inlet is connected with described steam exhaust pipe 8, and another pipe port is outside the in line casing in gas outlet.
Described voltage stabilizing blow-off valve 1 is made up of pressurization cylinder (25), valve plug (26), connecting rod (27) and the second pulsometer (28); Pressurization cylinder (25) is one end open, and another end is closed and barrel opens the cylinder of side opening; Valve plug (26) is positioned at pressurization cylinder (25) body; Above-mentioned connecting rod (27) middle part is through pressurization cylinder (25) end-blocking, and one end connects valve plug (26), and another end connects the second pulsometer (28); The opening of above-mentioned pressurization cylinder (25) body is in cylinder tank body 3 inner chamber bottom, and it is outside that side opening is in cylinder tank body 3, and aperture forms discharge gate down.
Operation principle of the present utility model is:
Expandable polystyrene raw material enters prefoam device from lock wind feed hopper 4, Sealed lock wind feed hopper 4 and voltage stabilizing blow-off valve 1, in the interlayer of prefoam device, logical high-temperature steam, enters UTILIZATION OF VESIDUAL HEAT IN case 9 from the steam exhaust pipe 8 of cylinder tank body 3 top dome head after high-temperature steam and the heat exchange of prefoam device inner layer wall; Under the effect of agitating device 5, expandable polystyrene raw material is heated by inner layer wall; Then continue to heat and open air compressor machine 7 by pre-warmed air press-in prefoam device supercharging in UTILIZATION OF VESIDUAL HEAT IN case 9, after prefoam device pressure and expandable polystyrene material temperature reach setting value, start voltage stabilizing blow-off valve 1 immediately, under valve plug (26) effect of voltage stabilizing blow-off valve 1, the increase of expandable polystyrene feed pressure is slowed down, then release suddenly, expandable polystyrene raw material enters rapidly fluidizing drying bed with air-flow.In the interlayer of prefoam device, when the condensed water that high-temperature steam produces is too much, discharge can be opened from the outer tube wall discharge outlet 11 of interlayer bottom cylinder tank body 3.
After above-mentioned expandable polystyrene raw material is fluidizing drying bed, the air that air dispersion pipe 12 in fluidizing drying bed is produced by boasting constantly blows high temperature expandable polystyrene raw material, remain in moisture natural evaporation in expandable polystyrene raw material, reach the effect of dry process.
Expandable polystyrene raw material after fluidizing drying bed drying process, send in maturation process device by flood dragon conveyer 2, the slaking bucket 16 be now designed in maturation process device is just right with flood dragon conveyer 2 feed opening, when this slaking bucket 16 is completely expected, photoelectric sensor 19 on slaking bucket 16 sends signal, simultaneously corresponding with on the commutation slip ring 17 that this photoelectric sensor 19 is connected movable contact is lucky and static contact position is just right, the signal of photoelectric sensor 19 is accepted by driver 20, driver 20 sends control signal to electric control brake hoof, electric control brake hoof unclamps, the slaking bucket 16 of material is had compared with the slaking bucket 16 having material in vertical traffic cycle 14, because gravity unbalance starts rotation, what adjust driver 20 unclamps the control time, when making vertical traffic cycle 14 forward next slaking bucket 16 to just to flood dragon conveyer 2 feed opening position, driver 20 is automatic locking electric control brake hoof again, now repeat again to carry charging, this slaking bucket 16 is filled and is turned next slaking bucket 16 again, so circulates, expandable polystyrene raw material stops slaking in slaking bucket 16, and when the slaking bucket 16 of feeding forwards the extreme lower position of vertical traffic cycle 14 to, slaking terminates, and the expandable polystyrene raw material of slaking is discharged to receiver 18 along slaking bucket 16 mouthfuls.
Above content is in conjunction with specific embodiments to the detailed description that the utility model is done, and can not assert that the utility model is specifically implemented to be only limitted to these explanations.For the utility model person of ordinary skill in the field, without departing from the concept of the premise utility, some simple deduction or replace can also be made, all should be considered as the scope belonging to the utility model protection.
Claims (4)
1. a maturation process system sent out in advance by polystyrene, comprises prefoam device, fluidizing drying bed and maturation process device; It is characterized in that: prefoam device connects fluidizing drying bed by voltage stabilizing blow-off valve (1), fluidizing drying bed by flood dragon conveyer (2) connection maturation process device; Described prefoam device is a cylinder tank body (3) having interlayer barrel, and there is lock wind feed hopper (4) cylinder tank body (3) side, top; Cylinder tank body (3) top dome head has the agitating device (5) stretching into tank inner chamber and forcing pipe (6), and forcing pipe (6) connects air compressor machine (7) aspirating end; The interlayer outer wall of cylinder tank body (3) top dome head is provided with the steam exhaust pipe (8) being communicated with interlayer, and steam exhaust pipe (8) connects UTILIZATION OF VESIDUAL HEAT IN case (9); Arrange voltage stabilizing blow-off valve (1) in the side of cylinder tank body (3) bottom barrel, the interlayer outer wall of opposite side barrel is provided with the steam inlet duct (10) of connection interlayer; Discharge outlet (11) is also had at the outer tube wall of cylinder tank body (3) bottom interlayer; The discharge gate of described voltage stabilizing blow-off valve (1) stretch into described fluidizing drying bed in; In fluidizing drying bed, be provided with air dispersion pipe (12), described air dispersion pipe (12) surface uniform is provided with multiple dispersion hole, and described air dispersion pipe (12) sections is closed, and the other end connects air intake duct (13); Described maturation process device is made up of vertical traffic cycle (14), support fixed axis (15) and multiple slaking bucket (16), and vertical traffic cycle (14) is arranged on by wheel hub and supports on fixed axis (15), can rotate around support fixed axis (15); The wheel hub of above-mentioned vertical traffic cycle (14) is also fixed coaxially a commutation slip ring (17); Receiver (18) is had at the hypomere of vertical traffic cycle (14); Described multiple slaking bucket (16) is uniformly set on described vertical traffic cycle (14) excircle, and the quarrel of slaking bucket (16) is opened wide by vertical traffic cycle (14) radial direction; Each quarrel is all equipped with photoelectric sensor (19), the signal output part of these photoelectric sensors (19) is connected on each movable contact of described commutation slip ring (17) respectively, and the static contact of commutation slip ring (17) connects driver (20) by holding wire; Between the wheel hub of above-mentioned vertical traffic cycle (14) and support fixed axis (15), electric control brake hoof is housed; Above-mentioned driver (20) connects electric control brake hoof.
2. maturation process system sent out in advance by a kind of polystyrene according to claim 1, it is characterized in that: described lock wind feed hopper (4) on the blanking channel of hopper, establishes sealing blocking (21) to connect the first pulsometer (22) control its keying.
3. maturation process system sent out in advance by a kind of polystyrene according to claim 1, it is characterized in that: described UTILIZATION OF VESIDUAL HEAT IN case (9) is for comprising thermal-insulating body, and box house lays coil pipe (23); The upper surface of thermal-insulating body has two stand pipe of leading in casing, wherein a stand pipe upper end mouth of pipe connects air filtration cap (24), lower end mouth of pipe straight cutting casing its lowest position, another root stand pipe upper end mouth of pipe connects air compressor machine (7) suction end, and the lower end mouth of pipe communicates with box house highest position; Two pipe ports of described coil pipe (23) extend outside thermal-insulating body, and a pipe port is wherein that air inlet is connected with described steam exhaust pipe (8), and another pipe port is outside the in line casing in gas outlet.
4. maturation process system sent out in advance by a kind of polystyrene according to claim 1, it is characterized in that: described voltage stabilizing blow-off valve (1) is made up of pressurization cylinder (25), valve plug (26), connecting rod (27) and the second pulsometer (28); Pressurization cylinder (25) is one end open, and another end is closed and barrel opens the cylinder of side opening; Valve plug (26) is positioned at pressurization cylinder (25) body; Above-mentioned connecting rod (27) middle part is through pressurization cylinder (25) end-blocking, and one end connects valve plug (26), and another end connects the second pulsometer (28); The opening of above-mentioned pressurization cylinder (25) body is in cylinder tank body (3) inner chamber bottom, and it is outside that side opening is in cylinder tank body (3), and aperture forms discharge gate down.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520021113.XU CN204382569U (en) | 2015-01-13 | 2015-01-13 | Maturation process system sent out in advance by a kind of polystyrene |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520021113.XU CN204382569U (en) | 2015-01-13 | 2015-01-13 | Maturation process system sent out in advance by a kind of polystyrene |
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| CN204382569U true CN204382569U (en) | 2015-06-10 |
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| CN201520021113.XU Expired - Fee Related CN204382569U (en) | 2015-01-13 | 2015-01-13 | Maturation process system sent out in advance by a kind of polystyrene |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114147908A (en) * | 2021-12-09 | 2022-03-08 | 常州顺唯尔材料科技有限公司 | Polystyrene foaming process and foaming system |
| CN114932652A (en) * | 2022-04-11 | 2022-08-23 | 张成基 | Curing equipment for fully curing EPS foam |
-
2015
- 2015-01-13 CN CN201520021113.XU patent/CN204382569U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114147908A (en) * | 2021-12-09 | 2022-03-08 | 常州顺唯尔材料科技有限公司 | Polystyrene foaming process and foaming system |
| CN114932652A (en) * | 2022-04-11 | 2022-08-23 | 张成基 | Curing equipment for fully curing EPS foam |
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Legal Events
| Date | Code | Title | Description |
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| 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: 20150610 Termination date: 20170113 |