CN201055805Y - Slant pulverizing and dewatering device capable of corrupting organic refuse - Google Patents
Slant pulverizing and dewatering device capable of corrupting organic refuse Download PDFInfo
- Publication number
- CN201055805Y CN201055805Y CNU2007200508404U CN200720050840U CN201055805Y CN 201055805 Y CN201055805 Y CN 201055805Y CN U2007200508404 U CNU2007200508404 U CN U2007200508404U CN 200720050840 U CN200720050840 U CN 200720050840U CN 201055805 Y CN201055805 Y CN 201055805Y
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- Prior art keywords
- dehydration
- organic waste
- tilting
- chamber
- fragmentation
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- Expired - Fee Related
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- Treatment Of Sludge (AREA)
Abstract
The utility model is an oblique biodegradable organic waste crushing and dehydration device. The device comprises a dehydration chamber. The upper end of the dehydration chamber is equipped with a discharge outlet; the middle of the dehydration chamber is equipped with a feed inlet, and the bottom is equipped with a drainage exit. An axle center at the dehydration chamber is equipped with a rotary shaft which is driven by a driver and is equipped with spiral vanes. The utility model can crush and dehydrate the biodegradable organic waste synchronously, so the materials reach the set moisture content to facilitate the rapid aerobic fermentation. The utility model is characterized by the high working efficiency.
Description
Technical field
The utility model relates to a kind of refuse treatment plant, specifically be a kind of at tilting can rotten organic waste fragmentation and dewater unit.
Background technology
The oxygen consumption sweat of organic waste, its suitable water content is about between the 50%-60%, but water content that can rotten organic waste is too high usually, especially contains melon and fruit class and the more rubbish of kitchen excess.Simultaneously because can rotten organic waste not of uniform size, in order to quicken fermentation, need to bulk can carry out fragmentation by rotten organic matter, make its granularity suitable, be convenient to even fermentation.Plate and frame type filter-press in the market, vacuum-type drum filter, centrifugal drier, belt pressing type filter can both be used in a lot of occasions, but are not suitable for the preliminary treatment as fermented manure.In addition, under the working condition of continuously a small amount of material input, make material dewatering reach needed certain the specific moisture of fermentation, being seen spiral dewaterer still can't be accomplished at present.Therefore need a kind of organic matter fermentation pretreatment unit broken and controlled dehydrating function that has simultaneously.
The utility model content
The purpose of this utility model provides a kind ofly can carry out fragmentation and dehydration by rotten organic waste simultaneously, makes material reach the moisture of setting, the refuse treatment plant of being convenient to carry out quick oxygen consumption fermentation.
The utility model is achieved in that fragmentation and the dewater unit that a kind of tilting can rotten organic waste, comprise the dehydration cavity, described dehydration cavity upper end offers discharging opening, dehydration cavity middle part offers charging aperture, the dehydration cavity bottom is provided with discharge outlet, the axle center that is positioned at the dehydration cavity is provided with rotating shaft, and described rotating shaft is by driver drives, and described rotating shaft is provided with helical blade.
Described dehydration cavity is pencil shape, and dehydration cavity frame tilts to be located on the support, and the dehydration cavity is divided into the cylindric first half and is used to dewater and the dehydration chamber of broken rubbish and the propelling chamber that coniform Lower Half is used for fragmentation and propelling rubbish.
The pitch in the pitch ratio dehydration chamber in described propelling chamber is big, and the pitch in described propelling chamber and dehydration chamber from bottom to top narrows down respectively gradually and the diameter of this place's rotating shaft from bottom to top increases respectively gradually.
Be provided with below the helical blade in described propelling chamber one with the dehydration cavity dumping be used to prevent that waste water from flowing to bearing block and helping waste water and discharge baffle plate outside the dehydration chamber.
Gap between the external diameter of described helical blade and the dehydration cavity wall is 1～5mm.
The inwall of described dehydration cavity is provided with some grooves longitudinally.
Described discharging opening is provided with movable pressure door, and described pressure door one end is connected with spring.
The angle that described dehydration cavity tilts is 30～60 °.
Described driver and feeding gate are controlled by intelligence control system.
Compared with prior art, owing to be provided with rotating shaft in the dehydration cavity, rotating shaft is provided with the spiral leaf.Under the driving of driver, the rubbish in the dehydration cavity is squeezed broken and dehydration under the spiral leaf squeezing action, make material reach the moisture of setting.The utlity model has the characteristics of high efficiency.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is carried out detailed explanation.
As shown in Figure 1, the utility model is made of dehydration cavity, rotating shaft 6, helical blade 2, charging aperture 3, discharging opening 8, discharge outlet 11, actuating unit, intelligence control system and other accessory structure of pencil shape.
Dehydration cavity 1 is closely linked by flange and screw by multistage hollow cylinder or circular cone tube, can segmentation remove or replace during maintenance.
The dehydration cavity, its Lower Half is the hollow cavity of cylindrical shape, in this cavity, organic materials is pushed into and is broken, is called to advance chamber 13; Its first half is conical hollow cavity, and organic materials mainly is broken and extrusion dehydration in this cavity, is called dehydration chamber 1.
The rotating shaft of propelling chamber 13 and dehydration 1 inside, chamber and helical blade structure and shape are variant: advance in the chamber 13, the pitch broad of helical blade 2 narrows down from the bottom to top gradually, and the diameter of rotating shaft 6 increases from the bottom to top gradually; In the dehydration chamber 1, the pitch of helical blade 2 is narrower, narrows down gradually from the bottom to top, and the diameter of rotating shaft 6 dwindles equally from the bottom to top gradually.
Advance helical blade 2 bottoms in the chamber 13 that a baffle plate 4 (cutting dirty plate) that is fixed in cavity is set, cut dirty plate and be fixed in the open circles ring flat-plate that advances in the chamber 13, its inwall closely entangles rotating shaft 6; Cut dirty plate and favour rotating shaft 6 axle center,, can prevent that organic wastewater from flowing to bearing block 5, avoid influence lubricated perpendicular to horizontal plane.
The inwall of dehydration cavity has many grooves longitudinally, and these grooves are made of the many ribs gap that invests cavity inner wall, are uniformly distributed in cavity inner wall, is convenient to let out under the current after fragmentation is dewatered.
The axle core of rotating shaft 6 totally is spindle, and two is little, and the middle and upper part is big, and the pitch between the helical blade 2 is progressively dwindled from the bottom to top.This structure is beneficial to the organic matter that " eating " advances bulk, and when up carrying, the bulk organic matter is broken into fritter by top helical blade 2 and the cavity that narrows, and is squeezed and dewaters.Realize " eat tell greatly little ".
Distance between the external diameter of helical blade 2 and the dehydration cavity is less than 5mm; From the bottom to top, helical blade 2 width (distance of external diameter and internal diameter) dwindle gradually, and its size range is between 30mm-300mm.
Charging aperture 3 be positioned at advance 13 middle and lower parts, chamber towards the sky one side, with dehydration cavity junction the feeding gate of adjustable throttle amount is arranged, run into the instruction that unusual and emergency situation can be accepted intelligence control system, in time close.
Discharging opening 8 is positioned at one side towards ground on dehydration top, chamber, there is pressure door 9 discharging opening 8 outsides, under the effect of both sides, student side spring 15, usually be in closed condition, in the cavity that is subjected to dewatering after certain squeezing action power of material, pressure door 9 is opened, be broken and dewater after organic materials under the gravity effect, discharge, fall into be positioned at its below receiving hopper 14 or conveyer belt.
It is emphasized that: the existence of spindle spiral handspike and pressure door, make continuously a small amount of material be treated as possibility, strengthened dehydrating effect, avoided under the working condition of a small amount of material input the problem that dehydrating effect is difficult to ensure.
Dynamical system is made of a reducing motor 7 and belt pulley set, can regulate the speed of rotation.Under the state of continuous feed, keep slowly running, can cut down the consumption of energy.
Intelligence control system can be controlled the switch of dynamical system and feeding gate, finds that potential safety hazard in time starts guard mode, closes dynamical system and feeding gate.
Can rotten organic waste fragmentation also comprise support 12 and the base 10 that is used to support this device with dewater unit, 45 ° of inclinations of dehydration cavity frame are located on the support 12.
Claims (9)
1. fragmentation and the dewater unit that a tilting can rotten organic waste, it is characterized in that: comprise the dehydration cavity, described dehydration cavity upper end offers discharging opening, dehydration cavity middle part offers charging aperture, the dehydration cavity bottom is provided with discharge outlet, the axle center that is positioned at the dehydration cavity is provided with rotating shaft, and described rotating shaft is by driver drives, and described rotating shaft is provided with helical blade.
2. tilting as claimed in claim 1 can rotten organic waste fragmentation and dewater unit, it is characterized in that, described dehydration cavity is pencil shape, dehydration cavity frame tilts to be located on the support, and the dehydration cavity is divided into the cylindric first half and is used to dewater and the dehydration chamber of broken rubbish and the propelling chamber that coniform Lower Half is used for fragmentation and propelling rubbish.
3. tilting as claimed in claim 1 can rotten organic waste fragmentation and dewater unit, it is characterized in that, the pitch in the pitch ratio dehydration chamber in described propelling chamber is big, and the pitch in described propelling chamber and dehydration chamber from bottom to top narrows down respectively gradually and the diameter of this place's rotating shaft from bottom to top increases respectively gradually.
4. tilting as claimed in claim 1 can rotten organic waste fragmentation and dewater unit, it is characterized in that, be provided with below the helical blade in described propelling chamber one with the dehydration cavity dumping be used to prevent that waste water from flowing to bearing block and helping waste water and discharge baffle plate outside the dehydration chamber.
5. tilting as claimed in claim 1 can rotten organic waste fragmentation and dewater unit, it is characterized in that the gap between the external diameter of described helical blade and the dehydration cavity wall is 1～5mm.
6. tilting as claimed in claim 1 can rotten organic waste fragmentation and dewater unit, it is characterized in that the inwall of described dehydration cavity is provided with some grooves longitudinally.
7. tilting as claimed in claim 1 can rotten organic waste fragmentation and dewater unit, it is characterized in that described discharging opening is provided with movable pressure door, described pressure door one end is connected with spring.
8. tilting as claimed in claim 1 can rotten organic waste fragmentation and dewater unit, it is characterized in that the angle that described dehydration cavity tilts is 30～60 °.
9. tilting as claimed in claim 1 can rotten organic waste fragmentation and dewater unit, it is characterized in that described driver and feeding gate are controlled by intelligence control system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200508404U CN201055805Y (en) | 2007-04-27 | 2007-04-27 | Slant pulverizing and dewatering device capable of corrupting organic refuse |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200508404U CN201055805Y (en) | 2007-04-27 | 2007-04-27 | Slant pulverizing and dewatering device capable of corrupting organic refuse |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201055805Y true CN201055805Y (en) | 2008-05-07 |
Family
ID=39424651
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200508404U Expired - Fee Related CN201055805Y (en) | 2007-04-27 | 2007-04-27 | Slant pulverizing and dewatering device capable of corrupting organic refuse |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201055805Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101907385A (en) * | 2010-09-07 | 2010-12-08 | 戴文育 | Rapid dehydration dryer |
| CN104086060A (en) * | 2014-06-18 | 2014-10-08 | 成都新筑展博环保科技有限公司 | Sludge treatment method |
| CN104083918A (en) * | 2014-06-18 | 2014-10-08 | 成都新筑展博环保科技有限公司 | Screw squeezing dewaterer |
| CN104668070A (en) * | 2015-03-13 | 2015-06-03 | 苏州圣谱拉新材料科技有限公司 | Inclined-shaft grinding device |
| CN107399786A (en) * | 2017-08-24 | 2017-11-28 | 深圳汇呈环保科技有限公司 | A kind of wastewater reuse approach device |
| CN108061431A (en) * | 2017-12-07 | 2018-05-22 | 洪作娟 | Organic fertilizer drying system with dehydrating function |
| CN115127311A (en) * | 2022-08-29 | 2022-09-30 | 南通钇龙玻璃制品有限公司 | Dehydration equipment of raw materials for waste plastic recovery |
-
2007
- 2007-04-27 CN CNU2007200508404U patent/CN201055805Y/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101907385A (en) * | 2010-09-07 | 2010-12-08 | 戴文育 | Rapid dehydration dryer |
| CN101907385B (en) * | 2010-09-07 | 2012-09-26 | 戴文育 | Rapid dehydration dryer |
| CN104086060A (en) * | 2014-06-18 | 2014-10-08 | 成都新筑展博环保科技有限公司 | Sludge treatment method |
| CN104083918A (en) * | 2014-06-18 | 2014-10-08 | 成都新筑展博环保科技有限公司 | Screw squeezing dewaterer |
| CN104668070A (en) * | 2015-03-13 | 2015-06-03 | 苏州圣谱拉新材料科技有限公司 | Inclined-shaft grinding device |
| CN104668070B (en) * | 2015-03-13 | 2017-03-08 | 江苏晨日环保科技有限公司 | A kind of sloping shaft reducing mechanism |
| CN107399786A (en) * | 2017-08-24 | 2017-11-28 | 深圳汇呈环保科技有限公司 | A kind of wastewater reuse approach device |
| CN107399786B (en) * | 2017-08-24 | 2018-05-15 | 黑山北方清源水务有限公司 | A kind of wastewater reuse approach device |
| CN108061431A (en) * | 2017-12-07 | 2018-05-22 | 洪作娟 | Organic fertilizer drying system with dehydrating function |
| CN115127311A (en) * | 2022-08-29 | 2022-09-30 | 南通钇龙玻璃制品有限公司 | Dehydration equipment of raw materials for waste plastic recovery |
| CN115127311B (en) * | 2022-08-29 | 2022-11-29 | 南通钇龙玻璃制品有限公司 | Dehydration equipment of raw materials for waste plastic recovery |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: SHENZHEN DERUN ENVIRONMENTAL PROTECTION INVESTMENT Free format text: FORMER NAME: GUANGZHOU DERUN ENVIRONMENTAL TECHNOLOGY DEVELOPMENT CO. |
|
| CP03 | Change of name, title or address |
Address after: B, 14 floor, SED science and technology building, 1 science Road, Nanshan District Science Park, Guangdong, Shenzhen Province, 518000 Patentee after: Shenzhen Ters Environmental Protection Investment Co., Ltd. Address before: Floor 8, Guoxin building, 363 Dongfeng Dong Road, Guangdong, Guangzhou Province, China: 510000 Patentee before: Derun Environment-Protection Science-Technology Development Co., Ltd., Guangzhou |
|
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 518000 Guangdong city of Shenzhen province Nanshan District South Road four No. 021 high-tech industrial village building R1-B layer Patentee after: Shenzhen Ters Environmental Protection Investment Co., Ltd. Address before: 14, B, 518000 building, SED science and technology building, 1 science Road, Nanshan District Science Park, Guangdong, Shenzhen Patentee before: Shenzhen Ters Environmental Protection Investment Co., Ltd. |
|
| ASS | Succession or assignment of patent right |
Owner name: SHENZHEN HEXU ENVIRONMENTAL INVESTMENT CO.,LTD. Free format text: FORMER OWNER: SHENZHEN TERESA ENVIRONMENTAL SCIENCES + TECHNOLOGIES DEVELOPMENT CO., LTD. Effective date: 20130117 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20130117 Address after: 28 building 518000 unit B2 in Guangdong province Shenzhen city Nanshan District high tech Park high-tech South Road China Technology Development Institute Patentee after: Shenzhen continuous environmental protection investment Co., Ltd. Address before: 518000 Guangdong city of Shenzhen province Nanshan District South Road four No. 021 high-tech industrial village building R1-B layer Patentee before: Shenzhen Ters Environmental Protection Investment Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080507 Termination date: 20150427 |
|
| EXPY | Termination of patent right or utility model |