CN104589688A - Viscous residue spiral squeeze feeder - Google Patents
Viscous residue spiral squeeze feeder Download PDFInfo
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- CN104589688A CN104589688A CN201510022937.3A CN201510022937A CN104589688A CN 104589688 A CN104589688 A CN 104589688A CN 201510022937 A CN201510022937 A CN 201510022937A CN 104589688 A CN104589688 A CN 104589688A
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- accommodating cavity
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Abstract
The invention provides a viscous residue spiral squeeze feeder, which comprises a machine body and a screw blade, wherein an accommodating cavity is formed in the machine body; the screw blade is arranged in the accommodating cavity; the accommodating cavity comprises a spiral conveying region and a discharging compaction region; the spiral conveying region and the discharging compaction region are arrayed in the conveying direction of materials in sequence; the discharging compaction region is a conical cavity; the cross section of the conical cavity is gradually reduced along the conveying direction of the materials; one section, in the discharging compaction region, of the spiral blade is of a conical spiral structure which is matched with the conical cavity; a water draining region is arranged below the accommodating cavity in the machine body; the accommodating cavity and the water draining region are separated by a partition; the partition is provided with a communicating structure which enables the accommodating cavity and the water draining region to be communicated; lighter viscous biomass residues are squeezed into block shapes by squeeze helixes, the weight of the materials is increased, the materials can fully fall on a boiler furnace bottom to burn, the temperature of the boiler furnace bottom is ensured, and the burning capacity of biomass is increased.
Description
Technical field
A kind of viscous residue screw press of the present invention batcher.
Background technology
Because present biomass electric power plant is at some adhesive biomass residues of burning---during as tealeaf residue, the dregs of a decoction etc., because the density ratio of such residue own is lighter, the siege being not easy to drop to Fluidized Bed Boiler burns, substantially how just to burn clean in the air at boiler, be not easy the temperature ensureing furnace like this, so other fuel must be added---as coal etc. maintains the boiler temperature of siege, so just cause the waste of resource.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of viscous residue screw press batcher, lighter viscosity biomass residue can be squeezed into bulk by propelling worm, increase the weight of material, material can be made so fully to drop in furnace burn, ensure furnace temperature, increase the quantity combusted of living beings.
For solving above-mentioned existing technical problem, the present invention adopts following scheme: viscous residue screw press batcher, comprise body and helical blade, accommodating cavity is provided with in described body, described helical blade is located in accommodating cavity, described accommodating cavity comprises helical feed district and discharging compacting zone, described helical feed district and discharging compacting zone are arranged in order on the throughput direction of material, described discharging compacting zone is conical cavity, and the cross section of described conical cavity is reducing gradually on the throughput direction of material, in discharging compacting zone one section of described helical blade is the cone helical structure coordinated with conical cavity, the below of the inherent accommodating cavity of described body is provided with catchment, separated by barrier between described accommodating cavity and catchment, described barrier has the connectivity structure that accommodating cavity is communicated with catchment.
Viscosity biomass residue enters accommodating cavity from charging aperture, rotated by helical blade and arrive discharging compacting zone through helical feed district successively, viscosity biomass residue is in the compacting of discharging compacting zone, viscosity biomass residue is squeezed into bulk and is discharged by discharging opening, and the waste liquid extruded in viscosity biomass residue is then discharged from catchment.
As preferably, described barrier is grid type grid, and described connectivity structure is the grate opening on grid type grid.Be convenient to draining.
As preferably, described helical blade is varying pitch structure.After adopting varying pitch structure, on the throughput direction of material, the pitch of helical blade is in reducing trend gradually, and material, in course of conveying, can play the effect of preliminary extruding.
As preferably, described catchment comprises collect cavity and is located at the discharge outlet bottom collect cavity.
Beneficial effect:
A kind of viscous residue screw press batcher that the present invention adopts technique scheme to provide, lighter viscosity biomass residue can be squeezed into bulk by propelling worm, increase the weight of material, material can be made so fully to drop in furnace burn, ensure furnace temperature, increase the quantity combusted of living beings.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 be in Fig. 1 A-A to sectional view;
Fig. 3 is left view of the present invention.
Detailed description of the invention
Be a kind of embodiment of viscous residue screw press batcher of the present invention as shown in Figures 1 to 3, it comprises body 1 and helical blade 2, accommodating cavity is provided with in body 1, accommodating cavity is made up of helical feed district 111 and 112 two sections, discharging compacting zone, helical feed district 111 and discharging compacting zone 112 are arranged in order on the throughput direction of material, helical blade is located in accommodating cavity, and helical blade one section is positioned at 111, one section, helical feed district and is positioned at discharging compacting zone 112; Body 1 is provided with charging aperture 12 and discharging opening 13, and charging aperture 12 is positioned at place of helical feed district 111, and discharging opening 13 is positioned at the end of discharging compacting zone 112 and helical blade 2; Helical blade 2 is connected with motor 14, is rotated drive helical blade 2 directional rotating by motor 14.
In the present embodiment, discharging compacting zone 112 is conical cavity, and the cross section of conical cavity is reducing gradually on the throughput direction of material, and in discharging compacting zone 112 one section of helical blade 2 is the cone helical structure matched with conical cavity structure; The below of the inherent accommodating cavity of body 1 is provided with catchment, separated by barrier 3 between accommodating cavity and catchment, barrier 3 has the connectivity structure that accommodating cavity is communicated with catchment, in the present embodiment, barrier 3 adopts grid type grid, and described connectivity structure is the grate opening on grid type grid; Described helical blade 2 is varying pitch structure, and along on the throughput direction of material, the pitch of helical blade 2 reduces gradually, is convenient to, to viscosity biomass residue express material, can make squeezing better effects if.
In the present embodiment, catchment is made up of collect cavity 41 and the discharge outlet 42 be located at bottom collect cavity 41, arranges collect cavity 41 and is convenient to the waste liquid that viscosity biomass residue extrudes after helical blade 2 extrudes and flows out.
The course of work is: viscosity biomass residue enters helical feed district 111 from charging aperture 12, motor 14 drives helical blade to make directional-rotation by reductor, waste liquid in viscosity biomass residue is extruded by viscosity biomass residue under the rotary squeezing of helical blade transmission line, the viscosity biomass residue extracted is discharged from discharging opening 13 in block or pie, the bulk that viscous residue limit is pressed into or pie residue just directly send into electricity generation boiler, discharge after the waste liquid extruded flows to collect cavity 41 from grid type grid from discharge outlet 42.
Claims (4)
1. viscous residue screw press batcher, comprise body (1) and helical blade (2), described body is provided with accommodating cavity in (1), described helical blade is located in accommodating cavity, it is characterized in that: described accommodating cavity comprises helical feed district (111) and discharging compacting zone (112), described helical feed district (111) and discharging compacting zone (112) are arranged in order on the throughput direction of material, described discharging compacting zone (112) is conical cavity, and the cross section of described conical cavity is reducing gradually on the throughput direction of material, in discharging compacting zone (112) one section of described helical blade (2) is the cone helical structure coordinated with conical cavity, the below of described body (1) inherent accommodating cavity is provided with catchment, separated by barrier (3) between described accommodating cavity and catchment, described barrier (3) has the connectivity structure that accommodating cavity is communicated with catchment.
2. viscous residue screw press batcher according to claim 1, is characterized in that: described barrier (3) is grid type grid, and described connectivity structure is the grate opening on grid type grid.
3. viscous residue screw press batcher according to claim 1, is characterized in that: described helical blade (2) is varying pitch structure.
4. viscous residue screw press batcher according to claim 1, is characterized in that: described catchment comprises collect cavity (41) and is located at the discharge outlet (42) of collect cavity (41) bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510022937.3A CN104589688A (en) | 2015-01-16 | 2015-01-16 | Viscous residue spiral squeeze feeder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510022937.3A CN104589688A (en) | 2015-01-16 | 2015-01-16 | Viscous residue spiral squeeze feeder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104589688A true CN104589688A (en) | 2015-05-06 |
Family
ID=53115903
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510022937.3A Pending CN104589688A (en) | 2015-01-16 | 2015-01-16 | Viscous residue spiral squeeze feeder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104589688A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109663396A (en) * | 2019-02-19 | 2019-04-23 | 湖北滴水科技有限公司 | A kind of clean robot sewage water filtration processing unit |
| CN109664540A (en) * | 2019-02-19 | 2019-04-23 | 磐石市富元机械厂 | Stalk de-watering extrusion molding machine |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3938434A (en) * | 1973-03-19 | 1976-02-17 | Cox Clyde H | Sludge dewatering |
| JPS6483398A (en) * | 1987-09-28 | 1989-03-29 | Yoshiro Aoyama | Screw press type hydroextractor |
| JPH11347796A (en) * | 1998-06-11 | 1999-12-21 | Yoshiro Aoyama | Dehydration press |
| CN200970496Y (en) * | 2006-09-06 | 2007-11-07 | 蒋晓 | Variable pitch type conic screw squeezing sucking filter |
| CN202480407U (en) * | 2012-02-14 | 2012-10-10 | 黑龙江省计算中心 | Helical extrusion and separation filtering machine with conical rings |
| CN204398363U (en) * | 2015-01-16 | 2015-06-17 | 浙江中科兴环能设备有限公司 | Viscous residue screw press batcher |
-
2015
- 2015-01-16 CN CN201510022937.3A patent/CN104589688A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3938434A (en) * | 1973-03-19 | 1976-02-17 | Cox Clyde H | Sludge dewatering |
| JPS6483398A (en) * | 1987-09-28 | 1989-03-29 | Yoshiro Aoyama | Screw press type hydroextractor |
| JPH11347796A (en) * | 1998-06-11 | 1999-12-21 | Yoshiro Aoyama | Dehydration press |
| CN200970496Y (en) * | 2006-09-06 | 2007-11-07 | 蒋晓 | Variable pitch type conic screw squeezing sucking filter |
| CN202480407U (en) * | 2012-02-14 | 2012-10-10 | 黑龙江省计算中心 | Helical extrusion and separation filtering machine with conical rings |
| CN204398363U (en) * | 2015-01-16 | 2015-06-17 | 浙江中科兴环能设备有限公司 | Viscous residue screw press batcher |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109663396A (en) * | 2019-02-19 | 2019-04-23 | 湖北滴水科技有限公司 | A kind of clean robot sewage water filtration processing unit |
| CN109664540A (en) * | 2019-02-19 | 2019-04-23 | 磐石市富元机械厂 | Stalk de-watering extrusion molding machine |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150506 |