CN104192514B - A kind of high mass dryness fraction device for transporting objects - Google Patents
A kind of high mass dryness fraction device for transporting objects Download PDFInfo
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- CN104192514B CN104192514B CN201410409701.0A CN201410409701A CN104192514B CN 104192514 B CN104192514 B CN 104192514B CN 201410409701 A CN201410409701 A CN 201410409701A CN 104192514 B CN104192514 B CN 104192514B
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- roller
- agitating shaft
- stirring vane
- plenum
- discharging opening
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Abstract
The present invention relates to filter press materials-handling technology field, and in particular to a kind of high mass dryness fraction device for transporting objects, including roller, agitating shaft, stirring vane and drive device；Roller is provided with charging aperture and discharging opening, and charging aperture is located at roller one end, and charging aperture is provided with hopper；Side end of the discharging opening located at the other end of roller；Agitating shaft is connected in roller with drive device, is driven by driver；Stirring vane is fixed on the surface of agitating shaft in the shape of a spiral.The present invention passes through above structure, power is provided by drive mechanism, drive agitating shaft rotation, the fixed stirring vane with agitating shaft constantly rotates, promote material to be delivered to filter press, material be moisture content in the case of 60% 80% high mass dryness fraction, the ability with high-pressure delivery, it is hardly damaged or blocks, makes the material density into filter press uniform.
Description
Technical field
The present invention relates to filter press materials-handling technology field, and in particular to a kind of high mass dryness fraction device for transporting objects.
Background technology
The device for transporting objects of filter press is usually high-pressure pump, and material is delivered into press filtration with high voltage style using high-pressure pump
The filter chamber of machine, and continue pressurize, material is realized that the moisture in separation of solid and liquid, material passes through filter cloth mistake in the presence of high pressure
Filter and discharge.The advantage of high-pressure pump is to continue to export constant pressure, prevents material from revealing, and is most common filter press
Device for transporting objects.
But high-pressure pump is usually applicable only to the situation of material water ratio more than 90%, if material is moisture content 60%-
80% high mass dryness fraction material, high-pressure pump can not be then applicable, and easily blocked and even damaged high-pressure pump, but also it is defeated to reduce high-pressure pump
The pressure of material is sent, causes filter press to reduce the performance of separation of solid and liquid.
The content of the invention
It is an object of the invention to for weak point of the prior art there is provided a kind of high mass dryness fraction device for transporting objects,
In the case of high mass dryness fraction of the material for moisture content 60%-80%, the ability with high-pressure delivery is hardly damaged or blocked,
Make the material density into filter press uniform.
To reach above-mentioned purpose, the present invention is achieved through the following technical solutions.
A kind of high mass dryness fraction device for transporting objects, including roller, agitating shaft, stirring vane and drive device；
The roller is provided with charging aperture and discharging opening, and the charging aperture is located at described roller one end, and the charging aperture is provided with
Hopper；Side end of the discharging opening located at the other end of the roller；
The agitating shaft is connected in the roller with the drive device, is driven by the driver
It is dynamic；
The stirring vane is fixed on the surface of the agitating shaft in the shape of a spiral.
From the feed inlet end to the discharge port end, the roller is respectively equipped with feeder, plenum and discharging portion；From
The feeder is to the discharging portion, and the sectional area of the roller is from large to small.
The sectional area of the feeder, plenum and discharging portion is stepped to be gradually reduced.
The sectional area of the feeder, plenum and discharging portion is gradually reduced in stepless shape.
The discontinuous state of the stirring vane in the feeder, described in the plenum and the discharging portion
Stirring vane is continuous state.
In the discharging portion, from one end of the plenum to described discharging opening one end, the stirring vane with it is described
The pivot angle of agitating shaft is gradually reduced.
In the discharging portion, the stirring vane is in the rotation of one end close to the discharging opening and the agitating shaft
The heart is parallel, and vertical with the discharging opening.
In the plenum, the stirring number of axle is two or more, and is parallel to each other between the agitating shaft.
The stirring vane is two or a plurality of spaced spiral blade.
From one end of the charging aperture to one end of the discharging opening, the spacing of the spiral helicine stirring vane gradually becomes
Reduce.
The present invention provides power by above structure by drive mechanism, drives agitating shaft rotation, and fixation is stirred with agitating shaft
Mix blade constantly to rotate, promote material to be delivered to filter press, in the case of high mass dryness fraction of the material for moisture content 60%-80%,
Ability with high-pressure delivery, is hardly damaged or blocks, and makes the material density into filter press uniform.
Brief description of the drawings
Fig. 1 is a kind of cross section structure schematic diagram of example of the present invention.
Fig. 2 is the cross section structure schematic diagram of another example of the present invention.
Wherein：Roller 1, charging aperture 11, discharging opening 12, hopper 13, feeder 14, plenum 15, discharging portion 16, agitating shaft
2nd, stirring vane 3, drive mechanism 4
Embodiment
The invention will be further described with the following Examples.
As depicted in figs. 1 and 2, a kind of high mass dryness fraction device for transporting objects, including roller 1, agitating shaft 2, stirring vane 3 and drive
Dynamic device 4；
The roller 1 be provided with charging aperture 11 and discharging opening 12, the charging aperture 11 be located at described one end of roller 1, it is described enter
Material mouth 11 is provided with hopper 13；Side end of the discharging opening 12 located at the other end of the roller 1；
The agitating shaft 2 is connected in the roller 1 with the drive device 4, by the driver
3 drivings；
The stirring vane 3 is fixed on the surface of the agitating shaft 2 in the shape of a spiral.
From the end of charging aperture 11 to the end of discharging opening 12, the roller 1 is respectively equipped with feeder 14, the and of plenum 15
Discharging portion 16；From the feeder 14 to the discharging portion 16, the sectional area of the roller 1 from large to small, when material is described
Promoted, be moved at heavy in section at small bore by the stirring vane 3 in roller 1, play the effect of supercharging, improve material from
The pressure when discharging opening 12 is exported, when material water ratio is relatively low, improves the conveying capacity of material.
The sectional area of the feeder 14, plenum 15 and discharging portion 16 is stepped to be gradually reduced.The feeder 14,
Plenum 15 and discharging portion 16 can be processed respectively, then assemble the roller 1, be easy to processing, reduce cost.
The sectional area of the feeder 14, plenum 15 and discharging portion 16 is gradually reduced in stepless shape.Inorganic shape gradually contracts
It is small, resistance when material is conveyed in the roller 1 can be reduced, the decay of discharge pressure is reduced.
The discontinuous state of the stirring vane 3 in the feeder 14, in the plenum 15 and the discharging portion
16 stirring vane 3 is continuous state, is used to stir in the stirring vane 3 of the feeder 14, in the plenum 15
It is used to release material with the stirring vane 3 of the discharging portion 16.
In the discharging portion 16, from one end of the plenum 15 to described one end of discharging opening 12, the stirring vane 3
It is gradually reduced with the pivot angle of the agitating shaft 2, makes the material from its density after the discharging opening 12 output
Uniformly.
In the discharging portion 16, the stirring vane 3 is in one end close to the discharging opening 12 and the agitating shaft 2
Pivot is parallel, and vertical with the discharging opening 12, the efficiency of packing materials conveying.
As shown in Fig. 2 in the plenum 15, the quantity of agitating shaft 2 is two or more, and the agitating shaft 2
Between be parallel to each other, preferably material stirring can be made uniform.
The stirring vane 3 is two or a plurality of spaced spiral blade, preferably material stirring can be made equal
It is even.
From one end of the charging aperture 11 to one end of the discharging opening 12, the spacing of the spiral helicine stirring vane 3
Gradually become and reduce, for increasing pressure when releasing material.
The present invention provides power by above structure by above structure, the present invention by drive mechanism, drives agitating shaft rotation
Turn, the fixed stirring vane with agitating shaft constantly rotates, and promotes material to be delivered to filter press, be moisture content 60%- in material
In the case of 80% high mass dryness fraction, the ability with high-pressure delivery is hardly damaged or blocked, and makes the material into filter press close
Degree is uniform.
Finally it should be noted that above example is merely to illustrate technical scheme rather than to present invention protection
The limitation of scope, although being explained in detail with reference to preferred embodiment to the present invention, one of ordinary skill in the art should manage
Solution, technical scheme can be modified or equivalent substitution, without departing from technical solution of the present invention essence and
Scope.
Claims (1)
1. a kind of high mass dryness fraction device for transporting objects, it is characterised in that：Including roller, agitating shaft, stirring vane and drive device；
The roller is provided with charging aperture and discharging opening, and the charging aperture is located at described roller one end, and the charging aperture is provided with hopper；
Side end of the discharging opening located at the other end of the roller；
The agitating shaft is connected in the roller with the drive device, is driven by the drive device；
The stirring vane is fixed on the surface of the agitating shaft in the shape of a spiral；
From the feed inlet end to the discharge port end, the roller is respectively equipped with feeder, plenum and discharging portion；From described
Feeder is to the discharging portion, and the sectional area of the roller is from large to small；
In the discharging portion, from one end of the plenum to described discharging opening one end, the stirring vane and the stirring
The pivot angle of axle is gradually reduced；
The sectional area of the feeder, plenum and discharging portion is stepped to be gradually reduced；
Or, the sectional area of the feeder, plenum and discharging portion is gradually reduced in stepless shape；
The discontinuous state of the stirring vane in the feeder, in the stirring of the plenum and the discharging portion
Blade is continuous state；
In the discharging portion, the stirring vane is put down in the pivot of one end close to the discharging opening and the agitating shaft
OK, it is and vertical with the discharging opening；
In the plenum, the stirring number of axle is two or more, and is parallel to each other between the agitating shaft；
The stirring vane is two or a plurality of spaced spiral blade；
From one end of the charging aperture to one end of the discharging opening, the spacing of the spiral helicine stirring vane gradually becomes contracting
It is small.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410409701.0A CN104192514B (en) | 2014-08-19 | 2014-08-19 | A kind of high mass dryness fraction device for transporting objects |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410409701.0A CN104192514B (en) | 2014-08-19 | 2014-08-19 | A kind of high mass dryness fraction device for transporting objects |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104192514A CN104192514A (en) | 2014-12-10 |
| CN104192514B true CN104192514B (en) | 2017-08-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410409701.0A Active CN104192514B (en) | 2014-08-19 | 2014-08-19 | A kind of high mass dryness fraction device for transporting objects |
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| CN (1) | CN104192514B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108910427A (en) * | 2018-07-18 | 2018-11-30 | 广州薪光合环保技术有限公司 | Screw conveyor and biomass gasification system |
| CN109969705B (en) * | 2019-04-24 | 2024-03-19 | 福建南方路面机械股份有限公司 | Mixed thread screw conveyer |
| RU2744225C1 (en) * | 2020-07-22 | 2021-03-03 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Белгородский государственный технологический университет им. В.Г. Шухова | Method of low-temperature processing of organic solid municipal waste and installation for its implementation |
| CN117142064B (en) * | 2023-10-30 | 2024-01-02 | 华能左权煤电有限责任公司 | Coal pile is with buggy conveyer |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201871360U (en) * | 2010-08-24 | 2011-06-22 | 中国石油化工股份有限公司 | Grinding and bulking machine |
| CN202061567U (en) * | 2011-05-16 | 2011-12-07 | 山东赤城建材有限公司 | Stirrer used for fly ash brick making |
| CN103159012B (en) * | 2011-12-09 | 2015-05-27 | 中粮营养健康研究院有限公司 | Screw feeder |
| JP6214870B2 (en) * | 2013-01-08 | 2017-10-18 | 研機株式会社 | Screw conveyor |
| CN203558460U (en) * | 2013-10-30 | 2014-04-23 | 煤炭科学研究总院 | Special pipe wall screw conveyor |
| CN203667447U (en) * | 2013-12-09 | 2014-06-25 | 攀枝花钢城集团有限公司 | Spirally horizontal feeding machine |
| CN103950695B (en) * | 2014-04-11 | 2016-08-24 | 武汉凯迪工程技术研究总院有限公司 | A kind of biomass material anti-backfire continuous feeding system |
| CN203975810U (en) * | 2014-08-19 | 2014-12-03 | 佛山市金凯地过滤设备有限公司 | A kind of high mass dryness fraction device for transporting objects |
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| CN104192514A (en) | 2014-12-10 |
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| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 528000 south of Jihua Road, Nanzhuang Town, Chancheng District, Foshan City, Guangdong Province Patentee after: Guangdong jinkaidi filtration equipment Co.,Ltd. Address before: Two street Chancheng water district Jiangwan road 528000 Guangdong Province, Foshan City No. 23 Hui Hua Ming court B block 509 Patentee before: FOSHAN JINKAIDI FILTRATION EQUIPMENT Co.,Ltd. |
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