CN2217767Y - Continuous screw-sealing dryer - Google Patents
Continuous screw-sealing dryer Download PDFInfo
- Publication number
- CN2217767Y CN2217767Y CN 95243305 CN95243305U CN2217767Y CN 2217767 Y CN2217767 Y CN 2217767Y CN 95243305 CN95243305 CN 95243305 CN 95243305 U CN95243305 U CN 95243305U CN 2217767 Y CN2217767 Y CN 2217767Y
- Authority
- CN
- China
- Prior art keywords
- spiral conveying
- raw material
- pump
- conveying tube
- continous way
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Abstract
The utility model relates to a continuous spiral sealing dryer which comprises a material stirring drum, a pump, a plurality of spiral conveying pipes which are connected from heads to ends, a plurality of steam chambers, a container, a water storing drum, a charging hopper and a motor, wherein, the interior of the material stirring drum is provided with stirring vanes, and the bottom end is connected with the pump. The pump is connected with the spiral conveying pipes by material conveying pipes. One end of the spiral conveying pipes is provided with the motor for driving and conveying the spiral vanes in the pipes, and thus raw material can move forward to the outlet ends of the spiral conveying pipe. The outlet ends are provided with the charging hopper. The steam chambers are arranged outside the spiral conveying pipes, and one end of each steam chamber is provided with an automatic control valve. One end of the conveying pipes mutually connected is connected with the water storing drum and a vacuum pump connected with a container.
Description
The utility model relates to drying equipment, particularly steam to raw material heating in dry machine.
General common drying machine as shown in Figure 1, is canal drier, mainly comprise a ring body 11, ring body 11 surfaces are provided with several through holes 12, and its inside is provided with passage 13, be provided with conveying ride 14 in passage 13 lower ends, carry installing raw material 15 to be dried on the ride 14.Be provided with heater 16 in ring body 11 outsides, directly the raw material in the ring body 11 15 is heated.This structure will be installed in raw material 15 in advance when implementing and carry on the ride 14, and when treating transport platform 14 by ring body 11,16 pairs of raw materials 15 of heater directly heat, and make raw material 15 reach drying purpose.But this drying machine is to make raw material drying with direct mode of heating, and raw material is to load in mixture carrying on the ride, can produce a part of raw material to be heated, and another part raw material can not be heated, or certain part raw material is heated the shortcoming that another one then can't be heated.And because directly heating, can produce raw material overheated or not heat etc. can't grasp the shortcoming that uneven drying is spared.
Of the present utility model day be to provide a kind of continous way helixseal drying machine.Be provided with a plurality of end to end spiral conveying tubes, the carrier pipe external rings is provided with vaporium, to the transferring raw material indirect; Before raw material enters spiral conveying tube, stir through the raw material mixing drum earlier, raw material is broken up, and pre-Steam Heating; Like that in entering spiral conveying tube heating process spiral constantly overturns, thereby make raw material fully evenly dry.
The technical solution of the utility model is: by the raw material mixing drum, and pump, the spiral conveying tube that several are end to end, several vaporiums, container, water butt, vavuum pump and charging hopper and motor are formed.Wherein be provided with stirring vane in the raw material mixing drum, there are motor and cover in the upper end, and the bottom connects a pump, and raw material is after the pump sucking-off, be delivered to several end to end spiral conveying tubes of upper end, form the continous way transfer pipeline, raw material is delivered to the port of export continuously, the port of export has charging hopper, end at each spiral conveying tube is provided with motor, helical blade is arranged in the pipe, and helical blade is provided with vaporium at raw material mixing drum and spiral conveying tube external rings simultaneously by Motor Drive.In addition, be provided with the automatic pipe valve, connect a vavuum pump and a water butt that joins with container at transfer pipeline one end that is interconnected at an end of spiral conveying tube.
The utility model has the advantages that:
1, before raw material does not enter spiral conveying tube, stir earlier and Steam Heating in advance through the raw material mixing drum, after being broken up, raw material is subjected to heated drying.
2, raw material is constantly overturn by spiral in spiral conveying tube heating process, makes raw material fully evenly dry.
Description of drawings:
Fig. 1 is general canal drier stereogram.
Fig. 2 is a structural representation of the present utility model.
Fig. 3 is a part carrier pipe rotation heat drying schematic diagram of the present utility model.
Label is in the accompanying drawing:
The 1-canal drier, the 11-ring body, the 12-through hole, the 13-passage, 14-carries ride, the 15-raw material, 2-raw material mixing drum, 12-stirring vane, 22-cover, 23-motor, the 3-pump, 30-feed pipe, 31,32,33, the 34-spiral conveying tube, 311,321,331, the 341-helical blade, 35,36,37,38-motor, 4a, 4b, 4c-pipeline, 41,42,43,44,45-vaporium, 451-steam pipe, 5-container, 5a, the 5b-pipeline, 52-suction hose, 6-water butt, 71,72-charging hopper, 73,74-switch, 81,82,83,84-automatic pipe valve, 85,86-Pressure gauge, 9-vavuum pump, 91-thermometer.
The utility model is described in further detail below in conjunction with accompanying drawing, but it must be noted that present embodiment is for illustrative purposes only rather than to restriction of the present utility model.
Embodiment:
Continous way helixseal drying machine of the present utility model comprises: raw material mixing drum 2, pump 3, several end to end spiral conveying tubes 31,32,33,34, several vaporiums 41,42,43,44,45, container 5, water butt 6, vavuum pump 9 and charging hopper 71,72.Wherein, be provided with stirring vane 21 in the raw material mixing drum 2, the upper end is provided with cover 22, cover 22 can supply switch, and raw material is packed into, and its upper end is provided with motor 23 to drive stirring vane 21 work, be peripherally installed with vaporium 45 at mixing drum 2, vaporium 45 feeds steam by steam pipe 451.Raw material mixing drum 2 bottoms are connected with pump 3 with pipeline, pipeline is provided with the flow that magnetic valve flows out with the control raw material, after 3 sucking-offs of raw material process pump, transport to the spiral conveying tube 31 of upper end through feed pipe 30, spiral conveying tube 31 and other spiral conveying tubes 32,33,34 is end to end, form the continous way transfer pipeline, raw material can be delivered to the port of export continuously.At spiral conveying tube 31,32,33,34 one ends are provided with motor 35,36,37,38, and there is helical blade 311,321,331,341 inside, motor 35,36, and 37,38 can drive helical blade 311,321,331,341 helical rotation.In addition below spiral conveying tube 34 ports of export be provided with charging hopper 71,72, be provided with switch 73,74 with the control flow below two charging hoppers 71,72.At helix tube 31,32,33,34 outsides are provided with vaporium 41,42,43,44, each vaporium 41,42,43,44 also is interconnected vaporium 41, steam in 42,43,44 are fed by pipeline 4a, and are derived by pipeline 46, simultaneously also by the road 4c feed cold water with the indoor temperature of steam regulation.In addition, at spiral conveying tube 31,32,33,34 ends are respectively equipped with automatic pipe valve 81,82,83,84, automatic pipe valve 81,82,83,84 connecting line is connected with pipeline 5a, and pipe rule 5a is communicated to container 5, a container 5 and a pipeline 5b are connected to vavuum pump 9, are communicated to water butt 6 with another suction hose 52.The pipeline that automatic pipe valve 81,82,83,84 is connected with pipeline 5a is provided with Pressure gauge 85,86 with the pressure in the pipeline of check regulating pipeline 5a at any time and being connected.Again at spiral conveying tube 31,32,33,34 with vaporium 41,42,43,44 on respectively be provided with thermometer 91 so that check at any time and regulate, control is within the specific limits.
The course of work of the present utility model: earlier raw material is put into raw material mixing drum 2, raw material is stirred through stirring vane 21 be loose condition (of surface), borrow the steam of vaporium 45 to give dry in advance the processing then simultaneously, raw material is sent into the spiral conveying tube 31 of upper end through pump 3 suctions through feed pipe 30, helical blade 311 in the spiral conveying tube 31 drives through motor 35 and rotates, and raw material is delivered to next spiral conveying tube 32, carries successively, enter spiral conveying tube 31 at raw material, in 32,33,34 the course of conveying, be located at spiral conveying tube 31, the vaporium 41 of 32,33,34 outsides, 42,43,44 promptly are full of steam, borrow steam to spiral conveying tube 31,32, raw material in 33,34 carries out indirect, and raw material overturns in the helical rotation process, as shown in Figure 3, each face of raw material can both be heated and even drying.Because raw material is at spiral conveying tube 31,32, in 33,34 course of conveying, reach dry through the heating of continuous vaporium 41,42,43,44, flow to charging hopper 71,72 at last and seal pack.
In addition, in order to prevent raw material in spiral conveying tube 31,32,33,34 through vaporium 41,42, after 43,44 the steam indirect, have part moisture content and condense in the pipeline, so that influence the drying of raw material, the spy establishes a vavuum pump 9 in container 5 outsides, during vavuum pump 9 work, can make pipeline 5a, 5b and the container 5 inner vacuum that form are borrowed automatic pipe valve 81,82, being interconnected of 83,84 control and pipeline, can be at any time with at spiral conveying tube 31, steam in 32,33,34 is evacuated to container 5.5b is to true pump 9 by the road if any part gas, and the water droplet of condensation can 52 flow into water butts 6 dischargings by the road.In addition, be located at spiral conveying tube 31,32,33,34 and the thermometer 91 and the Pressure gauge 85 of vaporium 41,42,43,44,86 can check adjusting at any time, as finding temperature, hypertonia or crossing when low, can feed steam by pipeline 4a, or feed cold water by pipeline 4c and regulate.
Claims (5)
1, a kind of continous way helixseal drying machine comprises: raw material mixing drum (2), pump (3), several end to end spiral conveying tubes (31), (32), (33), (34), several vaporiums (41), (42), (43), (44), (45), container (5), water butt (6), vavuum pump (9) and charging hopper (71), (72) and motor (23), (35), (36), (37), (38), it is characterized in that raw material mixing drum (2), be provided with stirring vane (21) in the tube, external rings is established vaporium (45), and there are motor (23) and cover (22) in the upper end, the bottom connects a pump (3), and pump (3) is connected by feed pipe (30) with spiral conveying tube (31); Spiral conveying tube (31), (32), (33), (34) are end to end, form the continous way transfer pipeline, spiral conveying tube, (31), (32), (33), (34) one ends are provided with motor (35), (36), (37), (38), there are helical blade (311), (321), (331) in inside, (341), external rings is established vaporium (41), (42), (43), (44), below spiral conveying tube (34) port of export be provided with at least one charging hopper (71).
2, continous way helixseal drying machine according to claim 1 is characterized in that spiral conveying tube (31), (32), (33), (34) end is provided with automatic pipe valve (81) respectively, (82), (83), (84), automatic pipe valve (81), (82), (83), (84), connecting line be connected to a container (5) with pipeline (5a).
3, continous way helixseal drying machine according to claim 2 is characterized in that a described container (5) and a pipeline (5a) are connected to vavuum pump (9), are connected to water butt (6) with another suction hose (52).
4, continous way helixseal drying machine according to claim 2 is characterized in that automatic pipe valve (81), (82), (83), the connecting line of (84) is provided with Pressure gauge (85), (86).
5, continous way helixseal drying machine according to claim 2 is characterized in that spiral conveying tube (31), (32), (33), (34) are respectively equipped with thermometer (91) with vaporium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95243305 CN2217767Y (en) | 1995-01-04 | 1995-01-04 | Continuous screw-sealing dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95243305 CN2217767Y (en) | 1995-01-04 | 1995-01-04 | Continuous screw-sealing dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2217767Y true CN2217767Y (en) | 1996-01-17 |
Family
ID=33883936
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 95243305 Expired - Lifetime CN2217767Y (en) | 1995-01-04 | 1995-01-04 | Continuous screw-sealing dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2217767Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100548518C (en) * | 2005-06-08 | 2009-10-14 | 江南环境工程（嘉兴）有限公司 | The compression drying under reduced pressure method of house refuse etc. and compression drying under reduced pressure machine |
| CN102321435A (en) * | 2011-06-07 | 2012-01-18 | 景东力奥林产集团林业化工有限公司 | Rosin residue roasting machine and complete equipment comprising residue roasting machine |
| CN102581980A (en) * | 2011-01-06 | 2012-07-18 | 崔丞钧 | Process for preparing resin composition for molding polypropylene-vegetable residue |
-
1995
- 1995-01-04 CN CN 95243305 patent/CN2217767Y/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100548518C (en) * | 2005-06-08 | 2009-10-14 | 江南环境工程（嘉兴）有限公司 | The compression drying under reduced pressure method of house refuse etc. and compression drying under reduced pressure machine |
| CN102581980A (en) * | 2011-01-06 | 2012-07-18 | 崔丞钧 | Process for preparing resin composition for molding polypropylene-vegetable residue |
| CN102321435A (en) * | 2011-06-07 | 2012-01-18 | 景东力奥林产集团林业化工有限公司 | Rosin residue roasting machine and complete equipment comprising residue roasting machine |
| CN102321435B (en) * | 2011-06-07 | 2013-07-31 | 景东力奥林产集团林业化工有限公司 | Rosin residue roasting machine and complete equipment comprising residue roasting machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |