CN202784851U - Powder conveying system - Google Patents
Powder conveying system Download PDFInfo
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- CN202784851U CN202784851U CN 201220465470 CN201220465470U CN202784851U CN 202784851 U CN202784851 U CN 202784851U CN 201220465470 CN201220465470 CN 201220465470 CN 201220465470 U CN201220465470 U CN 201220465470U CN 202784851 U CN202784851 U CN 202784851U
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- Prior art keywords
- powder
- type pump
- delivery system
- gear
- pressure gas
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Abstract
The utility model relates to powder conveying, in particular to a powder conveying system which comprises a blanking hopper, a gear pump, a mixer, a conveying pipeline, a collecting hopper and a dust remover, wherein the blanking hopper, the gear pump, the mixer, the conveying pipeline and the collecting hopper are sequentially connected; the blanking hopper is connected with a feeding end of the gear pump; the gear pump comprises a shell, a meshing gear set and a power source; the meshing gear set is arranged in the shell and comprises two gears which are meshed with each other; the two gears are respectively and rotatablely connected with the shell; when the meshing gear set rotates, two adjacent teeth arranged on the same gear are matched with the shell in a circulating way, so that a powder conveying cavity can be formed; the mixer is provided with a compressed air inlet; and the dust remover is arranged on the top of the collecting hopper. According to the powder conveying system, the gear pump has the function of isolation when being in charge of rotary feeding; and compressed air is taken as power. Therefore, powder can be conveyed in the closed environment, thus not being diffused into the atmosphere.
Description
Technical field
The utility model relates to powder to be carried, particularly a kind of powder delivery system.
Background technology
Often can use powder in process of production, powder is comprised of many tiny solia particles, does not have fixing shape, possesses certain flowing power, therefore can't directly carry.Existing common practice generally is by the belt conveyor conveying powder materials.But owing to lack interaction between the particulate of composition powder, be easy to be blown in the atmosphere by air-flow, cause dust pollution.Dust pollution is directly threatening people's life, and the environment that especially is in dust pollution can cause multiple cardiovascular, breathing problem etc.Asthma, bronchitis attack rate are typical case's performance of dust pollution aggravation in the constantly Quick higher position in this year, and too much dust grows germ virus easily to healthy totally unfavorable.Also have great harm for skin health.
In addition, dust flies away other raw material that also can cause in the workshop everywhere in the workshop contaminated, perhaps sucked the accidents such as equipment is impaired that cause by miscellaneous equipment.
The utility model content
The utility model provides a kind of powder delivery system, can be in confined space conveying powder materials.
In order to achieve the above object, the technical solution of the utility model is achieved in that
Powder delivery system comprises hopper, gear type pump, mixer, transfer line, aggregate bin and dust exhaustor; Described hopper, described gear type pump, described mixer, described transfer line and described aggregate bin connect successively; Wherein, described hopper is connected with the feed end of described gear type pump;
Described gear type pump comprises shell, be used for that powder is delivered to the engaging tooth wheels of discharge end by the feed end of gear type pump and be used for driving the propulsion source of described engaging tooth wheels; Described engaging tooth wheels are arranged in the described shell, and comprise two pitch wheels; Two described gears all are rotationally connected with described shell, and described shell is divided into feed space and discharge chamber two parts; When described engaging tooth wheels rotate, be positioned at adjacent two teeth on the same described gear and can circulate and cooperate the powder conveyor chamber that is formed for the powder of described feed space is delivered to described discharge chamber with the inwall of described shell;
Be provided with the pressure gas entrance on the described mixer; Described dust exhaustor is arranged on the top of described aggregate bin.
Further, in the aforesaid powder delivery system, be provided with the relief hole that communicates with the engagement place of two described gears on the described shell.
Further, in the aforesaid powder delivery system, also be provided with two cleaning hole that are used for entering the gas that the powder between adjacent two teeth on the same described gear is blown off on the described shell; Two described cleaning hole all communicate with described discharge chamber; The all corresponding described cleaning hole of each described gear; And the projection of described cleaning hole in this gear sagittal plane is positioned at the scope that the path of motion of tooth in the sagittal plane of described gear of this gear covers.
Further, in the aforesaid powder delivery system, described pressure gas entrance and the coaxial setting of described transfer line.
Further, in the aforesaid powder delivery system, described pressure gas entrance is connected with the pressure gas pipeline; Be provided with pressure maintaining valve on the described pressure gas pipeline.
Further, in the aforesaid powder delivery system, also be provided with meter on the described pressure gas pipeline, described meter is between described pressure maintaining valve and described pressure gas entrance.
Further, in the aforesaid powder delivery system, the top of described aggregate bin also is provided with vacuum release valve.
Further, in the aforesaid powder delivery system, the bottom of described aggregate bin is provided with blow-off valve.
Further, in the aforesaid powder delivery system, described hopper is connected with described gear type pump by the top of described gear type pump; Described mixer is connected with described gear type pump by the below of described gear type pump.
Further, in the aforesaid powder delivery system, described transfer line is connected with the top of described aggregate bin.
Compared with prior art, powder delivery system described in the utility model is delivered to mixer with powder from hopper by gear type pump, passes into pressure gas in mixer, and drives powder through transfer line arrival aggregate bin as propulsion source.In this process, because gear type pump has unidirectional conveying function, its feed space and discharge chamber are that constantly engaged gear cluster cuts off, so air-flow can only move to transfer line after pressure gas entered mixer, and then the powder that drives in the mixer moves to transfer line.Overall process middle gear pump is responsible for playing the partition effect when rotation is fed into mixer, prevents that pressure gas from directly flowing to hopper; Pressure gas is as the power that powder is delivered to aggregate bin by mixer.Powder is deposited on the aggregate bin bottom after arriving aggregate bin, and the pressure of pressure gas is discharged by dust exhaustor.Powder can be finished conveying under airtight environment like this, can not be diffused in the atmosphere, and human body or equipment are caused damage.
In addition, powder delivery system provided by the utility model also has following technique effect:
(1) by arrange relief hole can will retain the pressure gas of engagement place of two gears discharge, prevent from that these pressure gass are released to cause behind the feed space to push powder, hinder blanking.
(2) powder that remains between two teeth can be blown off by cleaning hole is set, prevent residual.
(3) by with pressure gas entrance and the coaxial setting of transfer line, pressure gas directly is connect by the pressure gas entrance enter transfer line, can not cause the kinetic energy waste.
(4) can make the pressure of pressure gas more stable by pressure maintaining valve is set, make the pressure in the transfer line keep stable, can be not fluctuated.
(5) volume of the quantity of the upper powder conveyor chamber of the rotating speed by gear type pump, gear and powder conveyor chamber can draw the powder transfer rate of gear type pump as calculated, realizes the accurate measurement to powder; And can measure the used compressed gas scale of construction by meter is set, be convenient to technique and cost control.
(6) can when the aggregate bin internal pressure surpasses the resistance to compression limit, play a protective role by vacuum release valve is set, prevent that dust exhaustor from damaging.
(7) by being set, blow-off valve can discharge from direct that sedimentation is the good powder in aggregate bin bottom.
(8) by transfer line is connected with the top of aggregate bin, can make powder have more space free to be deposited to bottom the aggregate bin, and it is far away to enter the pressure gas of the aggregate bin powder good apart from sedimentation, and it is blown afloat again.
Description of drawings
In order to be illustrated more clearly in the utility model specific embodiment or technical scheme of the prior art, the below will do to introduce simply to the accompanying drawing of required use in the specific embodiment or the description of the Prior Art, apparently, accompanying drawing in the following describes is embodiments more of the present utility model, for those of ordinary skills, under the prerequisite of not paying creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is the structural representation of the utility model embodiment one described powder delivery system;
Fig. 2 is the structural representation of the utility model embodiment two described powder delivery systems.
Reference numeral: 1-hopper, 2-gear type pump, 3-mixer, 4-transfer line, the 5-aggregate bin, 6-dust exhaustor, 7-shell, 8-engaging tooth wheels, 9-feed space, 10-discharge chamber, 11-powder conveyor chamber, 12-pressure gas entrance, 13-cleaning hole, 14-pressure gas pipeline, 15-pressure maintaining valve, 16-meter, the 17-vacuum release valve, 18-blow-off valve, 19-relief hole.
The specific embodiment
For making the purpose of this utility model, technical scheme and advantage clearer; the below will carry out clear, complete description to the technical solution of the utility model; based on the specific embodiment in the utility model; those of ordinary skills are resulting all other embodiments under the prerequisite of not making creative work, all belong to the scope that the utility model is protected.
As shown in Figure 1, embodiment one of the present utility model provides a kind of powder delivery system, comprises hopper 1, gear type pump 2, mixer 3, transfer line 4, aggregate bin 5 and dust exhaustor 6; Hopper 1, gear type pump 2, mixer 3, transfer line 4 and aggregate bin 5 connect successively; Wherein, hopper 1 is connected with the feed end of gear type pump 2;
Hopper 1 is connected with gear type pump 2 by the top of gear type pump 2; Mixer 3 is connected with gear type pump 2 by the below of gear type pump 2;
Be provided with pressure gas entrance 12 on the mixer 3; Dust exhaustor 6 is arranged on the top of aggregate bin 5.
By gear type pump 2 powder is delivered to mixer 3 from hopper 1, in mixer 3, passes into pressure gas, and drive powder through transfer line 4 arrival aggregate bins 5 as propulsion source.In this process, because gear type pump 2 has unidirectional conveying function, its feed space 9 is that constantly engaged gear cluster 8 cuts off with discharge chamber 10, can only move to transfer line 4 so pressure gas enters mixer 3 rear air-flows, and then the powder in the drive mixer 3 is to transfer line 4 motions.Overall process middle gear pump 2 is responsible for playing the partition effect when rotation is fed into mixer 3, prevents that pressure gas from directly flowing to hopper 1; Pressure gas is as the power that powder is delivered to aggregate bin 5 by mixer 3.Be deposited on aggregate bin 5 bottoms at arrival aggregate bin 5 rear powders, the pressure of pressure gas is discharged by dust exhaustor 6.Powder can be finished conveying under airtight environment like this, can not be diffused in the atmosphere, and human body or equipment are caused damage.
As shown in Figure 2, embodiment two of the present utility model provides another kind of powder delivery system, comprises hopper 1, gear type pump 2, mixer 3, transfer line 4, aggregate bin 5 and dust exhaustor 6; Hopper 1, gear type pump 2, mixer 3, transfer line 4 and aggregate bin 5 connect successively; Wherein, hopper 1 is connected with the feed end of gear type pump 2;
Hopper 1 is connected with gear type pump 2 by the top of gear type pump 2; Mixer 3 is connected with gear type pump 2 by the below of gear type pump 2;
Be provided with pressure gas entrance 12 on the mixer 3; Dust exhaustor 6 is arranged on the top of aggregate bin 5.
Because discharge chamber 10 communicates with mixer 3, so the gaseous tension in the discharge chamber 10 can be more much larger than feed space 9.And the position that begins to mesh of intermeshing two gears is positioned at discharge chamber 10 1 sides, the position of finishing engagement is positioned at feed space 9 one sides, so the air pressure of the engagement place of two gears equates with discharge chamber 10, equally greater than feed space 9, when finishing engagement, two gears exist the air pressure of engagement place to discharge like this, powder in the feed space 9 is pushed away gear, because the conveying of gear type pump 2 is endlessly processes, therefore this air pressure can form endlessly thrust prevention powder near gear, cause blanking velocity slow, even cause putty.
In order to prevent that above-mentioned situation from occuring, and is provided with the relief hole 19 that communicates with the engagement place of two described gears on the shell 7.By arrange relief hole 19 can will retain the pressure gas of engagement place of two gears discharge, prevent from that these pressure gass are released to cause behind the feed space 9 to push powder, hinder blanking.
For fear of above-mentioned situation, also be provided with two cleaning hole 13 that are used for entering the gas that the powder between adjacent two teeth on the same described gear is blown off on the shell 7; Two cleaning hole 13 all communicate with discharge chamber 10; The all corresponding cleaning hole 13 of each described gear; And the projection of cleaning hole 13 in this gear sagittal plane is positioned at the scope that the path of motion of tooth in the sagittal plane of described gear of this gear covers.Like this cleaning hole is connected air inlet pipe and just the powder that remains between two teeth can be blown off, prevent residual.
Pressure gas is that the kinetic energy when relying on gas flow drives the powder motion and then reaches the purpose of carrying powder, so the kinetic energy of pressure gas is most important for the conveying of powder.Turning or meeting with the kinetic energy that can lose in a large number pressure gass when blocking, cause the powder fed distance to shorten, speed slows down, and cost increases.
Therefore, pressure gas entrance 12 and transfer line 4 coaxial settings.Pressure gas directly is connect by pressure gas entrance 12 enter transfer line 4, can not cause the kinetic energy waste.
Pressure gas is swiftly flowing high pressure gas, and its inner distribution of pressure is uneven, changes very fast.Carry out the flow velocity inequality that the powder conveying can cause powder if directly make it enter pipeline, and can cause transfer line 4 internal pressure overbalances, cause potential safety hazard.
For fear of the problems referred to above occurring, pressure gas entrance 12 is connected with pressure gas pipeline 14; Be provided with pressure maintaining valve 15 on the pressure gas pipeline 14.Can make the pressure of pressure gas more stable by pressure maintaining valve 15 is set, make the pressure in the transfer line 4 keep stable, can be not fluctuated.
For technology controlling and process and assessing the cost, often need various parameters are monitored in process of production.
The quantity of the rotating speed by gear type pump 2, the upper powder conveyor chamber 11 of gear and the volume of powder conveyor chamber 11 can draw the powder transfer rate of gear type pump 2 as calculated, realize the accurate measurement to powder, and precision can reach more than 98%.In the past gear type pump metering is mainly used in liquid meter.Now can be not residual by cleaning hole 13 rear solid powders are set, thus can realize metering feed to solid materials such as powders, solved in the powder course of conveying problem that the control for amount can't precisely detect in real time.
In order to realize that to the utilization of pressure gas actv., the feeding coal of mate gear pump 2 is monitored the compressed gas scale of construction, also be provided with meter 16 on the pressure gas pipeline 14, meter 16 is between pressure maintaining valve 15 and pressure gas entrance 12.So just, reached to powder with to the used compressed gas scale of construction and measured, be convenient to technique and cost control.
Every equipment has a resistance to compression limit, and equipment will be impaired when inside and outside differential pressure surpasses this limit, even also might cause personnel and property damage.And a lot of links of existence in process of production, these links connect each other, all linked with one another, and any one link goes wrong and all might cause intrasystem pressure to change.In case just can have an accident and pressure exceeds the resistance to compression limit of equipment self.And dust exhaustor 6 itself is exactly the inside and outside equipment of connected system in whole powder delivery system; therefore when changing greatly, internal system pressure is easy to exceed the tolerance range of dust exhaustor 6; if at this moment do not take the safety method dust exhaustor 6 will be impaired even damage, can't continue normal operation.
For fear of the generation of above-mentioned situation, the top of aggregate bin 5 also is provided with vacuum release valve 17.Can when aggregate bin 5 internal pressures surpass the resistance to compression limit, play a protective role like this, prevent that dust exhaustor 6 from damaging.
Because therefore the self-characteristic of powder also should be stored in powder in the airtight space after finishing conveying as far as possible.Aggregate bin 5 itself is one well to be selected, and the powder after the sedimentation can be directly in aggregate bin 5 interior storages.And be provided with blow-off valve 18 by the bottom at aggregate bin 5, can be from aggregate bin 5 bottoms directly powder that sedimentation is good discharge, directly use or pack is sealed up for safekeeping all very convenient.
Because native system is by pressure gas powder to be delivered to aggregate bin 5, pressurized air is also remaining after entering aggregate bin 5 kinetic energy, and this part kinetic energy can continue to act on the interior powder of aggregate bin 5, and it is blown afloat again.
In order to reduce the generation of above-mentioned situation, make as early as possible sedimentation of powder, transfer line 4 is connected with the top of aggregate bin 5.Can make like this powder have more space free to be deposited to aggregate bin 5 bottoms, and it is far away to enter the pressure gas of aggregate bin 5 powder good apart from sedimentation, and it is blown afloat again.
It should be noted that at last: above embodiment and embodiment only in order to the technical solution of the utility model to be described, are not intended to limit; Although with reference to aforementioned embodiments and embodiment the utility model is had been described in detail, those of ordinary skill in the art is to be understood that: it still can be made amendment to the technical scheme that aforementioned embodiments or embodiment put down in writing, and perhaps part technical characterictic wherein is equal to replacement; And these modifications or replacement do not make essence disengaging the utility model embodiment of appropriate technical solution or the spirit and scope of embodiment technical scheme.
Claims (10)
1. powder delivery system is characterized in that: comprise hopper, gear type pump, mixer, transfer line, aggregate bin and dust exhaustor; Described hopper, described gear type pump, described mixer, described transfer line and described aggregate bin connect successively; Wherein, described hopper is connected with the feed end of described gear type pump;
Described gear type pump comprises shell, be used for that powder is delivered to the engaging tooth wheels of discharge end by the feed end of gear type pump and be used for driving the propulsion source of described engaging tooth wheels; Described engaging tooth wheels are arranged in the described shell, and comprise two pitch wheels; Two described gears all are rotationally connected with described shell, and described shell is divided into feed space and discharge chamber two parts; When described engaging tooth wheels rotate, be positioned at adjacent two teeth on the same described gear and can circulate and cooperate the powder conveyor chamber that is formed for the powder of described feed space is delivered to described discharge chamber with the inwall of described shell;
Be provided with the pressure gas entrance on the described mixer; Described dust exhaustor is arranged on the top of described aggregate bin.
2. powder delivery system as claimed in claim 1 is characterized in that: be provided with the relief hole that communicates with the engagement place of two described gears on the described shell.
3. powder delivery system as claimed in claim 1 is characterized in that: also be provided with two cleaning hole that are used for entering the gas that the powder between adjacent two teeth on the same described gear is blown off on the described shell; Two described cleaning hole all communicate with described discharge chamber; The all corresponding described cleaning hole of each described gear; And the projection of described cleaning hole in this gear sagittal plane is positioned at the scope that the path of motion of tooth in the sagittal plane of described gear of this gear covers.
4. such as the described powder delivery system of any one in the claims 1 to 3, it is characterized in that: described pressure gas entrance and the coaxial setting of described transfer line.
5. such as the described powder delivery system of any one in the claims 1 to 3, it is characterized in that: described pressure gas entrance is connected with the pressure gas pipeline; Be provided with pressure maintaining valve on the described pressure gas pipeline.
6. powder delivery system as claimed in claim 5, it is characterized in that: also be provided with meter on the described pressure gas pipeline, described meter is between described pressure maintaining valve and described pressure gas entrance.
7. such as the described powder delivery system of any one in the claims 1 to 3, it is characterized in that: the top of described aggregate bin also is provided with vacuum release valve.
8. such as the described powder delivery system of any one in the claims 1 to 3, it is characterized in that: the bottom of described aggregate bin is provided with blow-off valve.
9. such as the described powder delivery system of any one in the claims 1 to 3, it is characterized in that: described hopper is connected with described gear type pump by the top of described gear type pump; Described mixer is connected with described gear type pump by the below of described gear type pump.
10. such as the described powder delivery system of any one in the claims 1 to 3, it is characterized in that: described transfer line is connected with the top of described aggregate bin.
Priority Applications (1)
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CN 201220465470 CN202784851U (en) | 2012-09-12 | 2012-09-12 | Powder conveying system |
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CN 201220465470 CN202784851U (en) | 2012-09-12 | 2012-09-12 | Powder conveying system |
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CN202784851U true CN202784851U (en) | 2013-03-13 |
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CN 201220465470 Expired - Lifetime CN202784851U (en) | 2012-09-12 | 2012-09-12 | Powder conveying system |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102837968A (en) * | 2012-09-12 | 2012-12-26 | 刘华 | Powder conveying system |
CN103935706A (en) * | 2014-05-06 | 2014-07-23 | 江苏雅仕保鲜产业有限公司 | Garbage collection device for fruit and vegetable waste |
CN104406187B (en) * | 2014-11-05 | 2016-08-24 | 衢州昀睿工业设计有限公司 | A kind of charging gear of coal burner |
CN106561761A (en) * | 2017-01-24 | 2017-04-19 | 林俊广 | Apparatus for coating seasoning on flour cake |
-
2012
- 2012-09-12 CN CN 201220465470 patent/CN202784851U/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102837968A (en) * | 2012-09-12 | 2012-12-26 | 刘华 | Powder conveying system |
CN102837968B (en) * | 2012-09-12 | 2015-10-28 | 刘华 | Powder delivery system |
CN103935706A (en) * | 2014-05-06 | 2014-07-23 | 江苏雅仕保鲜产业有限公司 | Garbage collection device for fruit and vegetable waste |
CN103935706B (en) * | 2014-05-06 | 2016-05-04 | 江苏雅仕保鲜产业有限公司 | For the refuse collector of fruits and vegetables waste material |
CN104406187B (en) * | 2014-11-05 | 2016-08-24 | 衢州昀睿工业设计有限公司 | A kind of charging gear of coal burner |
CN106561761A (en) * | 2017-01-24 | 2017-04-19 | 林俊广 | Apparatus for coating seasoning on flour cake |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20130313 Effective date of abandoning: 20151028 |
|
C25 | Abandonment of patent right or utility model to avoid double patenting |