CN109405515A - A kind of granulated material drier - Google Patents

A kind of granulated material drier Download PDF

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Publication number
CN109405515A
CN109405515A CN201811313442.6A CN201811313442A CN109405515A CN 109405515 A CN109405515 A CN 109405515A CN 201811313442 A CN201811313442 A CN 201811313442A CN 109405515 A CN109405515 A CN 109405515A
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CN
China
Prior art keywords
pipeline
drying box
round table
drying
valve
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Granted
Application number
CN201811313442.6A
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Chinese (zh)
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CN109405515B (en
Inventor
黄有海
周兴旺
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Shenzhen Qintai Industrial Development Co.,Ltd.
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Ma'anshan Muji Information Technology Co Ltd
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Priority to CN201811313442.6A priority Critical patent/CN109405515B/en
Publication of CN109405515A publication Critical patent/CN109405515A/en
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Publication of CN109405515B publication Critical patent/CN109405515B/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/12Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/001Handling, e.g. loading or unloading arrangements
    • F26B25/002Handling, e.g. loading or unloading arrangements for bulk goods
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2200/00Drying processes and machines for solid materials characterised by the specific requirements of the drying good
    • F26B2200/08Granular materials

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

The present invention provides a kind of granulated material driers.It solve material be easy it is over-drying, in cavity the technical issues of residual material, the cooperation that the present invention passes through screw auger and liter expects pipe, it can will be located at the top of the material lifting to dry cavity of dry cavity bottom, the drying process that dry cavity bottom is recycled is dropped back into again from the bottom surface hole Sa Liao of the round table-like pipeline of the upper section of liter expects pipe, the junction of discharge nozzle and round table-like pipeline is equipped with separated material valve, the inner wall of round table-like pipeline is equipped with material mass dryness fraction inductor, corresponding each spill is provided with linkage valve on material hole, the open and-shut mode of separated material valve and linkage valve is opposite, it can prevent over-drying, improve dry mass and drying efficiency.Under the action of cylinder and telescopic rod, the left and right ends of drying box can be swung up and down in certain amplitude, promote material mobile to dry cavity center, be conducive to material and entered in liter expects pipe and recycle remaining dried material in drying box.

Description

A kind of granulated material drier
Technical field
The invention belongs to dry fields, and in particular to a kind of granulated material drier.
Background technique
Existing granulated material drier, it is most of using hot wind is passed through into drying chamber body, it is carried out in conjunction with stirring rod Agitation, comes into full contact with hot wind with material, to improve hot wind utilization efficiency.But such granulated material drier can not and When will meet technique require (aridity) material send out drying chamber it is external, but stop in the cavity with undried material after Continuous agitation rolling and with the further contact drying of hot wind, on the one hand cause material over-drying, on the other hand consume hot wind again, Reduce unit hot wind utilization efficiency.In addition, existing granulated material drier discharging is inconvenient, it is easy to remain in the cavity Material.
Summary of the invention
The present invention provides a kind of granulated material driers, it is intended to solve above-mentioned technical problem.
The granulated material drier includes drying box, heat source, and dry cavity is formed inside the drying box, described The center of top of drying box is equipped with feed pipe, and the dry cavity center is provided with a liter expects pipe, the bottom of described liter of expects pipe with There are feeding cavities between the bottom surface of the drying box.
Screw auger is installed, the screw auger includes helical axis, and the lower end of the helical axis is passed through in described liter of expects pipe It wears the bottom of the drying box and is fixedly connected by shaft coupling with the output shaft for the rotating electric machine being mounted on the base, it is described Helical axis and drying box bottom are cooperated by rolling bearing, are welded with helical blade on the surface of the helical axis.
The middle and lower sections of described liter of expects pipe are circular cylindrical pipe, and upper section is formed by connecting by multistage pipeline of different shapes, including Gradually reducing pipeline, straight round tube and round table-like pipeline, the broadside of the gradually reducing pipeline are fixedly connected with one end of the circular cylindrical pipe, The narrow side of the gradually reducing pipeline is fixedly connected with one end of the straight round tube, and the other end of the straight round tube is fixedly connected with the circle Round table-like pipeline described in the bottom surface of mesa-shaped pipeline and connection.
The top surface of the round table-like pipeline is fixedly connected and one end of one discharge nozzle of connection, and the discharge nozzle is set in described Inside feed pipe, another end surfaces of the discharge nozzle are equipped with connector, and reach outside the feed pipe.
The junction of the discharge nozzle and round table-like pipeline is equipped with separated material valve, and the inner wall of round table-like pipeline is equipped with Material mass dryness fraction inductor, the bottom surface of the round table-like pipeline, which has been evenly arranged, spills material hole, and corresponding each spill is provided with connection on material hole Movable valve, the separated material valve, material mass dryness fraction inductor and linkage valve are all electrically connected with control system.
The two sides of the base upper surface are mounted on cylinder, and a telescopic rod is connected on the cylinder, the telescopic rod A connecting plate is installed at top, and the connecting plate is fixedly connected on the bottom both ends of the drying box.
Discharge port is arranged in the bottom center of the drying box, and discharge valve, the electric rotating is arranged in corresponding discharge outlet Material collection box is installed on the axis body immediately below the discharge valve on the output shaft of machine.
The feeding cavities are the partial size of 4 times of granule materials to be dried.
The connector is connection screw thread.
The connection screw thread connects a hose.
The material mass dryness fraction inductor is 2 or more.
The connecting plate is bolted on the bottom both ends of the drying box.
The heat source is using diversified forms, preferably hot air drying such as electric heating, microwave heating, heat-conducting oil heating or Hot-blast Heatings It is dry.
The adjustable in length of the helical axis or rotating electric machine output shaft is flexible, can extend the screw auger and protrude into In the discharge nozzle.
Temperature sensor is installed inside the drying box.
The material collection box uses conical socket structure, is obliquely installed, and the bottommost of the conical socket, which is equipped with, to gather materials Mouthful, collection material mouth connects a hose.
Compared with prior art, the invention has the following advantages:
The present invention is by screw auger and rises the cooperation of expects pipe, can will be located at the material lifting of dry cavity bottom to drying chamber At the top of body, the drying that dry cavity bottom is recycled is dropped back into again from the bottom surface hole Sa Liao of the round table-like pipeline of the upper section of liter expects pipe Processing, drying effect is good, can be realized to material evenly drying.
The junction of discharge nozzle and round table-like pipeline is equipped with separated material valve, and the inner wall of round table-like pipeline is equipped with material Mass dryness fraction inductor, corresponding each spill are provided with linkage valve on material hole, the open and-shut mode of separated material valve and linkage valve is on the contrary, energy It is enough that dry cavity is discharged in dried material in time, it prevents over-drying, improves dry mass and drying efficiency.
Under the action of cylinder and telescopic rod, the left and right ends of drying box can be swung up and down in certain amplitude, Promote material mobile to dry cavity center, be conducive to material and enter in liter expects pipe, is also beneficial to residual in recycling drying box Dried material.
Discharge nozzle is set in inside feed pipe, and another end surfaces of discharge nozzle are equipped with connector one hose of connection and are conducive to Facilitate collection dried material, and the waste heat of dried material can preheat the wet feed at feed pipe, is conducive to improve heat Utilization efficiency.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of granulated material drier.
Specific embodiment
Referring to Fig. 1, granulated material drier provided in this embodiment, including drying box 1, drying box inside are formed The center of top of dry cavity, the drying box 1 is equipped with feed pipe 11, and the dry cavity center is provided with liter expects pipe 2, rises There are feeding cavities 3 between the bottom of expects pipe 2 and the bottom surface of the drying box 1, and the feeding cavities 3 are at least more than to be dried The partial size of grain material, more than preferably 4 times of partial sizes, so that material is able to enter in liter expects pipe 2.
Screw auger is installed, the screw auger includes helical axis 4, the lower end of the helical axis 4 in described liter of expects pipe 2 Through the drying box 1 bottom and by shaft coupling with the output shaft of rotating electric machine 7 that is mounted on pedestal 6 is fixed connects It connects, the helical axis 4 is cooperated with 1 bottom of drying box by rolling bearing, is welded with helical blade on the surface of the helical axis 4 5.The screw auger cooperation, which rises expects pipe 2, will be located at the top of the material lifting to dry cavity of dry cavity bottom.
The middle and lower sections of described liter of expects pipe 2 are circular cylindrical pipe, and upper section is formed by connecting by multistage pipeline of different shapes, including Gradually reducing pipeline 8, straight round tube 9 and round table-like pipeline 10, the broadside diameter of the gradually reducing pipeline 8 and the diameter of the circular cylindrical pipe Identical, the broadside of gradually reducing pipeline 8 is fixedly connected with one end of the circular cylindrical pipe, the narrow side diameter of the gradually reducing pipeline 8 with The diameter of the straight round tube 9 is identical, and the narrow side of gradually reducing pipeline 8 is fixedly connected with one end of the straight round tube 9, the straight round tube 9 The other end be fixedly connected the round table-like pipeline 10 bottom surface and connection described in round table-like pipeline 10.
The top surface of the round table-like pipeline 10 is fixedly connected and one end of one discharge nozzle 12 of connection, the discharge nozzle 12 are arranged Inside the feed pipe 11, another end surfaces of the discharge nozzle 12 are equipped with connector, such as connection screw thread 22, and stretch out To outside feed pipe 11, a hose can be connected by connection screw thread to facilitate collection dry material.
The junction of the discharge nozzle 12 and round table-like pipeline 10 is equipped with separated material valve 13, the inner wall of round table-like pipeline 10 Face is equipped with material mass dryness fraction inductor 14, the number of the material mass dryness fraction inductor 14 can according to the actual situation depending on, in figure only Show one, but can actually be it is multiple, such as 2 or more, more accurately to detect material drying regime.
The bottom surface of the round table-like pipeline 10, which has been evenly arranged, spills material hole 15, and the aperture for spilling material hole 15 is greater than particulate matter The partial size of material, corresponding each spill are provided with linkage valve on material hole 15.
The separated material valve 13, material mass dryness fraction inductor 14 and linkage valve are all electrically connected with control system.Its interval The open and-shut mode of valve 13 and linkage valve is expected on the contrary, being the separated material valve closure, when linkage valve closes when linkage valve is opened When conjunction, separated material valve is opened.The specific opening and closing of valve passes through the dry materials situation at 14 sense channel of material mass dryness fraction inductor, And will test value in real time and feed back to control system, when detected value meets the predetermined range of dry materials requirement setting, control System issues instruction, opens separated material valve, closes linkage valve;When detected value does not meet the predetermined value of dry materials requirement setting When range, control system issues instruction, opens linkage valve, closes separated material valve.
The two sides of 6 upper surface of pedestal are mounted on cylinder 16, a telescopic rod 17 are connected on the cylinder 16, described in two A connecting plate 18 is installed at the top of telescopic rod 17, and two connecting plates 18 are fixedly connected with (such as being bolted) described dry The bottom both ends of dry cabinet 1.Under the action of cylinder 16 and telescopic rod 17, the left and right ends of drying box 1 can be certain It is swung up and down in amplitude, promotes material mobile to dry cavity center, be conducive to material and enter in liter expects pipe 2.
The granulated material drier further includes for heat source needed for dried material, which can be set described Inside drying box 1, internal heat resource is constituted, also can be set outside the drying box 1, constitute external heat source, heating is dry Dry mode can be using diversified forms, preferably heated-air drying such as electric heating, microwave heating, heat-conducting oil heating, Hot-blast Heatings.
In order to monitor heating state in drying chamber body, temperature sensor 21 is also equipped with inside the drying box 1.
The working method of granulated material drier provided by the present embodiment is as follows: as shown in Figure 1, particulate matter to be dried Material enters dry inside cavity from feed pipe 11, falls on the outer surface of round table-like pipeline 10 and then disperses to fall on dry cavity bottom Portion, material and hot wind come into full contact with drying during the falling process, and screw auger cooperation, which rises expects pipe 2, will be located at dry cavity bottom Material lifting to dry cavity at the top of, dropped back into again from the bottom surface hole Sa Liao 15 of the round table-like pipeline 10 of the upper section of liter expects pipe 2 dry Dry cavity bottom is dried again.When material mass dryness fraction inductor 14 detects that dry materials situation meets dry materials and wants When asking, by control system issue instruct, open separated material valve, close linkage valve, material no longer from spill material hole 15 drop back into drying Cavity bottom, but continued up under the action of screw auger, increase since upward material constantly accumulates, close to out The material of expects pipe 12 moves up under the extruding of screw auger and back material to be discharged by discharge nozzle 12, is received in time by hose The dried material of Ji Chuliaoguanchu.
Phase after the drying depends merely on the upward active force of screw auger and lacks bottom since material is reduced in drying chamber body The extruding force of the material constantly moved upwards, it is difficult to continue to be discharged from discharge nozzle 12 by dried material.It therefore, can be from lower section It makes adjustment in face.
On the one hand, telescopic screw auger can be selected, the length of the output shaft of the helical axis 4 or rotating electric machine 7 Degree is adjustable flexible, can extend screw auger protrude into discharge nozzle 12 when needed.It on the other hand, can also be in drying box 1 bottom center is arranged discharge port, and corresponding discharge outlet is arranged discharge valve 19, in institute on the output shaft of the rotating electric machine 7 It states and material collection box 20 is installed on the axis body immediately below discharge valve 19.
The material collection box 20 uses conical socket structure, is obliquely installed, and the bottommost of the conical socket is equipped with collection Material mouth, collection material mouth can connect hose with the dried material in collection material collection box 20.Due in cylinder 16 and telescopic rod 17 Under the action of, the left and right ends of drying box 1 can be swung up and down in certain amplitude, promote surplus material to drying box 1 Bottom center discharge port it is mobile, to recycle remaining dried material in drying box.
The above description is merely a specific embodiment, but scope of protection of the present invention is not limited thereto, any In the technical scope disclosed by the present invention, any changes or substitutions that can be easily thought of by those familiar with the art, all answers It is included within the scope of the present invention.

Claims (10)

1. a kind of granulated material drier, including drying box (1), heat source, the drying box (1) is internal to form drying chamber Body, which is characterized in that
The center of top of the drying box (1) is equipped with feed pipe (11), and the dry cavity center is provided with a liter expects pipe (2), There are feeding cavities (3) between the bottom of described liter of expects pipe (2) and the bottom surface of the drying box (1);
Screw auger is installed in described liter of expects pipe (2), the screw auger includes helical axis (4), under the helical axis (4) End runs through the bottom of the drying box (1) and by the output shaft of shaft coupling and the rotating electric machine (7) being mounted on pedestal (6) It is fixedly connected, the helical axis (4) and drying box (1) bottom are cooperated by rolling bearing, on the surface of the helical axis (4) It is welded with helical blade (5);
The middle and lower sections of described liter of expects pipe (2) are circular cylindrical pipe, and upper section is formed by connecting by multistage pipeline of different shapes, including gradually Pipe (8), straight round tube (9) and round table-like pipeline (10), the broadside of the gradually reducing pipeline (8) and the one of the circular cylindrical pipe End is fixedly connected, and the narrow side of the gradually reducing pipeline (8) is fixedly connected with one end of the straight round tube (9), the straight round tube (9) The other end is fixedly connected with round table-like pipeline (10) described in the bottom surface of the round table-like pipeline (10) and connection;
The top surface of the round table-like pipeline (10) is fixedly connected and one end of one discharge nozzle of connection (12), discharge nozzle (12) set It is internal to be located at the feed pipe (11), another end surfaces of the discharge nozzle (12) are equipped with connector, and reach it is described into Expects pipe (11) is outside;
The junction of the discharge nozzle (12) and round table-like pipeline (10) is equipped with separated material valve (13), round table-like pipeline (10) Inner wall is equipped with material mass dryness fraction inductor (14), and the bottom surface of the round table-like pipeline (10), which has been evenly arranged, spills material hole (15), Corresponding each spill is provided with linkage valve on material hole (15), the separated material valve (13), material mass dryness fraction inductor (14) and linkage Valve is all electrically connected with control system;
The two sides of pedestal (6) upper surface are mounted on cylinder (16), connect a telescopic rod (17), institute on the cylinder (16) The top installation one connecting plate (18) of telescopic rod (17) is stated, the connecting plate (18) is fixedly connected on the drying box (1) Bottom both ends;
Discharge port, corresponding discharge outlet setting discharge valve (19), the rotation is arranged in the bottom center of the drying box (1) Material collection box (20) are installed on the axis body immediately below the discharge valve (19) on the output shaft of motor (7).
2. granulated material drier according to claim 1, which is characterized in that the feeding cavities (3) are 4 times to dry The partial size of dry granule materials.
3. granulated material drier according to claim 2, which is characterized in that the connector is connection screw thread (22).
4. granulated material drier according to claim 2, which is characterized in that connection screw thread (22) connection one is soft Pipe.
5. granulated material drier according to claim 4, which is characterized in that the material mass dryness fraction inductor (14) is 2 or more.
6. granulated material drier according to claim 1, which is characterized in that the connecting plate (18) is solid by bolt It is scheduled on the bottom both ends of the drying box (1).
7. granulated material drier according to claim 1, which is characterized in that the heat source uses electric heating, microwave The diversified forms, preferably heated-air drying such as heating, heat-conducting oil heating or Hot-blast Heating.
8. granulated material drier according to claim 1, which is characterized in that the helical axis (4) or electric rotating The adjustable in length of machine (7) output shaft is flexible, can extend the screw auger and protrude into the discharge nozzle (12).
9. granulated material drier according to claim 1, which is characterized in that pacify inside the drying box (1) Equipped with temperature sensor (21).
10. granulated material drier according to claim 1, which is characterized in that the material collection box (20) uses Conical socket structure is obliquely installed, and the bottommost of the conical socket is equipped with collection material mouth, and collection material mouth connects a hose.
CN201811313442.6A 2018-11-06 2018-11-06 Granular material drying device Active CN109405515B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811313442.6A CN109405515B (en) 2018-11-06 2018-11-06 Granular material drying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811313442.6A CN109405515B (en) 2018-11-06 2018-11-06 Granular material drying device

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CN109405515A true CN109405515A (en) 2019-03-01
CN109405515B CN109405515B (en) 2020-11-13

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111578676A (en) * 2020-05-29 2020-08-25 魏艳秋 Aggregate fast drying case for hydraulic and hydroelectric engineering concrete detection
CN114383918A (en) * 2022-01-11 2022-04-22 长安大学 ENM aerosol diffusion drying system
CN114963741A (en) * 2022-05-30 2022-08-30 浙江伽能环境工程有限责任公司 Sulfur drying and forming device
CN115751914A (en) * 2022-08-16 2023-03-07 农业农村部南京农业机械化研究所 Vertical internal circulation microwave convection coupling grain drying device and drying method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4373272A (en) * 1980-09-25 1983-02-15 General Electric Company System for controlling spouted bed inlet conditions
CN205897789U (en) * 2016-06-23 2017-01-18 天津市上德富国生物技术有限公司 Fermented feed drying device
CN206094838U (en) * 2016-09-12 2017-04-12 巢湖春友种业科技有限公司 But heat energy cyclic utilization's seed hot air drying device
CN108507338A (en) * 2018-04-10 2018-09-07 陈璐滨 A kind of damping type circular form industrial chemicals drying unit
CN108692555A (en) * 2017-04-07 2018-10-23 程长春 Cereal vacuum dryer

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4373272A (en) * 1980-09-25 1983-02-15 General Electric Company System for controlling spouted bed inlet conditions
CN205897789U (en) * 2016-06-23 2017-01-18 天津市上德富国生物技术有限公司 Fermented feed drying device
CN206094838U (en) * 2016-09-12 2017-04-12 巢湖春友种业科技有限公司 But heat energy cyclic utilization's seed hot air drying device
CN108692555A (en) * 2017-04-07 2018-10-23 程长春 Cereal vacuum dryer
CN108507338A (en) * 2018-04-10 2018-09-07 陈璐滨 A kind of damping type circular form industrial chemicals drying unit

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111578676A (en) * 2020-05-29 2020-08-25 魏艳秋 Aggregate fast drying case for hydraulic and hydroelectric engineering concrete detection
CN111578676B (en) * 2020-05-29 2022-03-11 安徽玉梯建设有限公司 Aggregate fast drying case for hydraulic and hydroelectric engineering concrete detection
CN114383918A (en) * 2022-01-11 2022-04-22 长安大学 ENM aerosol diffusion drying system
CN114383918B (en) * 2022-01-11 2023-06-23 长安大学 ENM aerosol diffusion drying system
CN114963741A (en) * 2022-05-30 2022-08-30 浙江伽能环境工程有限责任公司 Sulfur drying and forming device
CN115751914A (en) * 2022-08-16 2023-03-07 农业农村部南京农业机械化研究所 Vertical internal circulation microwave convection coupling grain drying device and drying method thereof

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