CN206440092U - Catalyst Production dryer - Google Patents

Catalyst Production dryer Download PDF

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Publication number
CN206440092U
CN206440092U CN201720045269.0U CN201720045269U CN206440092U CN 206440092 U CN206440092 U CN 206440092U CN 201720045269 U CN201720045269 U CN 201720045269U CN 206440092 U CN206440092 U CN 206440092U
Authority
CN
China
Prior art keywords
container
frame
communicated
catalyst production
teeter chamber
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 - Fee Related
Application number
CN201720045269.0U
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Chinese (zh)
Inventor
李宏
栾浩
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shiyan Yuantong Expensive Environmental Technology Co Ltd
Original Assignee
Shiyan Yuantong Expensive Environmental Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shiyan Yuantong Expensive Environmental Technology Co Ltd filed Critical Shiyan Yuantong Expensive Environmental Technology Co Ltd
Priority to CN201720045269.0U priority Critical patent/CN206440092U/en
Application granted granted Critical
Publication of CN206440092U publication Critical patent/CN206440092U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses Catalyst Production dryer, including outlet pipe and drying chamber, the air pump is arranged on the inside of frame, and air pump is arranged on tracheae, it is described enter tracheae one end be arranged on frame outside communicated with the external world.This kind of Catalyst Production dryer, it is provided with air pump, the moisture of air is separated out by bleed phenomenon in air pressurized decompression process and improves drying effect, it is provided with teeter chamber and heater, the agitating and heating of catalyst is realized by the cooperation of teeter chamber and heater, heating lamp is provided with, further catalyst is dried by heating lamp, aforesaid operations, by PLC control, are a kind of Catalyst Production dryers easy to use.

Description

Catalyst Production dryer
Technical field
The utility model is related to catalyst technical field, specially Catalyst Production dryer.
Background technology
At present, its structure of the mesh belt dryer of in the market disclosure belongs to hot-air seasoning, and vapor is directly discharged so in work As when cause the problem of heat-energy losses are big, drying rate is slow.
Utility model content
The purpose of this utility model is to provide Catalyst Production dryer, to solve what is proposed in above-mentioned background technology Heat-energy losses are big, the problem of drying rate is slow.
To achieve the above object, the utility model provides following technical scheme:Catalyst Production includes air with dryer Pump, the first container, sieve plate, second container, motor, feeding mouth, stirring blade, teeter chamber, heater, discharge nozzle, heating lamp, machine Frame, conveyer belt, baffle plate, water tank, PLC, enter tracheae, outlet pipe, drying chamber, magnetic valve, it is characterised in that:The air Pump is arranged on the inside of frame, and air pump is arranged on tracheae, it is described enter tracheae one end be arranged on the outside of frame with it is outer Boundary is communicated, and is entered the other end of tracheae and communicated with the inside of teeter chamber, and the sieve plate, which is separately mounted to the first container and second, to be held The inside of device, the feeding mouth is arranged in the top side face of frame, and feeding mouth inside teeter chamber with communicating, the stirring blade with Motor is connected, and stirring blade is arranged on the inside of teeter chamber, and the heater is arranged on the outer wall low side surface of teeter chamber, institute One end of discharge nozzle is stated to communicate with the inside of teeter chamber, and the other end of discharge nozzle is communicated with the inside of drying chamber, the heating Lamp is arranged in the inwall top side face of drying chamber, and the conveyer belt is arranged on the inside of drying chamber, and the baffle plate is arranged on frame Outer wall one side on, the inside of the inside of the water tank respectively with the first container, second container is communicated, the PLC On the one side for being arranged on frame outer wall, described outlet pipe one end is communicated with the inside of water tank, and the other end of outlet pipe is set Communicated on the outer wall one side of frame with the external world, the magnetic valve be arranged on outlet pipe on, and magnetic valve be located at outlet pipe with The junction of water tank.
It is preferred that, first container is provided with overflow valve with second container junction.
It is preferred that, the stirring blade is helicoidal structure.
It is preferred that, the sieve plate is set in parallel in the inside of the first container and second container.
It is preferred that, the PLC is electrically connected with motor, heater, heating lamp, conveyer belt, magnetic valve.
Compared with prior art, the beneficial effects of the utility model are:This kind of Catalyst Production dryer, sets free Air pump, the moisture of air is separated out and improves drying effect, be provided with teeter chamber by bleed phenomenon in air pressurized decompression process With heater, the agitating and heating of catalyst is realized by the cooperation of teeter chamber and heater, heating lamp is provided with, passes through heating lamp Further catalyst is dried, aforesaid operations, by PLC control, are that a kind of Catalyst Production easy to use is dried Dry machine.
Brief description of the drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is the utility model overlooking the structure diagram;
Fig. 3 is the utility model left view structure partial schematic diagram;
Fig. 4 is the utility model partial structural diagram.
In figure:Air pump -1;First container -2;Sieve plate -3;Second container -4;Motor -5;Feeding mouth -6;Stirring blade -7; Teeter chamber -8;Heater -9;Discharge nozzle -10;Heating lamp -11;Frame -12;Conveyer belt -13;Baffle plate -14;Water tank -15;PLC is controlled Device -16 processed;Enter tracheae -17;Outlet pipe -18;Drying chamber -19;Magnetic valve -20.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made The every other embodiment obtained, belongs to the scope of the utility model protection.
Fig. 1-4 are referred to, the utility model provides a kind of technical scheme:Catalyst Production dryer, including air pump 1st, the first container 2, sieve plate 3, second container 4, motor 5, feeding mouth 6, stirring blade 7, teeter chamber 8, heater 9, discharge nozzle 10, plus Thermolamp 11, frame 12, conveyer belt 13, baffle plate 14, water tank 15, PLC 16, enter tracheae 17, outlet pipe 18, drying chamber 19, Air pump 1 is arranged on the inside of frame 12, and air pump 1 is arranged on tracheae 17, enters the one end of tracheae 17 installed in frame 12 Outside communicated with the external world, and enter the other end of tracheae 17 and communicated with the inside of teeter chamber 8, sieve plate 3 is separately mounted to the first appearance The inside of device 2 and second container 4, feeding mouth 6 is arranged in the top side face of frame 12, and feeding mouth 6 and the inside phase of teeter chamber 8 Logical, stirring blade 7 is connected with motor 5, and stirring blade 7 is arranged on the inside of teeter chamber 8, and heater 9 is arranged on the outer of teeter chamber 8 On wall low side surface, one end of discharge nozzle 10 is communicated with the inside of teeter chamber 8, and the other end and the drying chamber 19 of discharge nozzle 10 is interior Portion is communicated, and heating lamp 11 is arranged in the inwall top side face of drying chamber 19, and conveyer belt 13 is arranged on the inside of drying chamber 19, baffle plate 14 are arranged on the outer wall one side of frame 12, and the inside of the inside of water tank 15 respectively with the first container 2, second container 4 is communicated, PLC 16 is arranged on the one side of the outer wall of frame 12, and the one end of outlet pipe 18 is communicated with the inside of water tank 15, and outlet pipe 18 other end is arranged on the outer wall one side of frame 12 and communicated with the external world.
In above-described embodiment, specifically, the first container 2 and the junction of second container 4 are provided with overflow valve, overflow valve can be with Ensure that the air pressure in the first container 2 is more than atmospheric pressure;
In above-described embodiment, specifically, stirring blade 7 is helicoidal structure, helicoidal structure can be sufficiently catalyst Smash, shake up and mixed with air;
In above-described embodiment, specifically, sieve plate 3 is set in parallel in the first container 2 and the inside of second container 4, work as air Through be arrangeding in parallel sieve plate 3 when, be easy to the surface of water vapor adsorption sieve plate 3 separated out in air, improve the drying journey of air Degree;
In above-described embodiment, specifically, PLC 16 and motor 5, heater 9, heating lamp 11, conveyer belt 13, electromagnetism Valve 20 is electrically connected with, and is realized by PLC 16 to motor 5, heater 9, heating lamp 11, conveyer belt 13, magnetic valve 20 Control, facilitates staff to operate, and the PLC 16 is Omron singlechip controller.
Operation principle:When using the Catalyst Production dryer, need first to whole Catalyst Production dryer Have the understanding in a structure, when in use, can more easily be used, by feeding mouth 6 and outlet pipe 18 respectively with Corresponding pipeline connection, the device is switched on power, and now PLC 16 enables motor 5, heater 9, heating lamp 11, biography Band 13, magnetic valve 20 are sent, catalyst enters the inside of teeter chamber 8 by feeding mouth 6, and now motor 5 drives 7 turns of stirring blade Dynamic, while motor drives air pump 1 to work, air enters through entering the air inlet pump 1 of tracheae 17, air in the presence of air pump 1 Enter the first container 2, now the overflow valve between the first container 2 and second container 4 plays pressure maintaining effect, make in the first container 2 Air pressure is far longer than atmospheric pressure, and now the water in air is precipitate on sieve plate 3, and water is arrived in the water storage separated out on sieve plate 3 In case 15, the air overflowed from overflow valve enters second container 4, and the air for now entering second container 4 recovers atmospheric pressure cause Decline air themperature, so that the water in air is further precipitate on sieve plate 3, water is arrived in the water storage precipitateing on sieve plate 3 In case 15, the air now more dried enters in teeter chamber 8, and dry air is sufficiently stirred for catalyst, in whipping process Middle heater 9 makes the moisture evaporation in catalyst into air to the heating of teeter chamber 8, and now catalyst passes through discharge nozzle with air 10 fall on the top surface of conveyer belt 13, and the communicated band 13 of the catalyst in conveyer belt top side is transported to the lower section of baffle plate 14, simultaneously The moisture contained in course of conveying in the further volatilization catalyst of heating of the catalyst through adding heating lamp 11, so as to realize baking It is dry.
In summary, although the utility model is described in detail with reference to the foregoing embodiments, for this area For technical staff, it can still modify to the technical scheme described in foregoing embodiments, or to which part Technical characteristic carries out equivalent substitution, all within spirit of the present utility model and principle, any modification for being made, equivalent substitution, Improve etc., it should be included within protection domain of the present utility model.

Claims (5)

1. Catalyst Production dryer, including air pump (1), the first container (2), sieve plate (3), second container (4), motor (5), feeding mouth (6), stirring blade (7), teeter chamber (8), heater (9), discharge nozzle (10), heating lamp (11), frame (12), biography Send band (13), baffle plate (14), water tank (15), PLC (16), enter tracheae (17), outlet pipe (18), drying chamber (19), electricity Magnet valve (20), it is characterised in that:The air pump (1) is arranged on the inside of frame (12), and air pump (1) is arranged on into tracheae (17) on, it is described enter tracheae (17) one end be arranged on the outside of frame (12) and communicated with the external world, and enter the other end of tracheae (17) Communicated with the inside of teeter chamber (8), the sieve plate (3) is separately mounted to the inside of the first container (2) and second container (4), institute Feeding mouth (6) is stated to be arranged in the top side face of frame (12), and feeding mouth (6) inside teeter chamber (8) with communicating, the stirring blade (7) it is connected with motor (5), and stirring blade (7) is arranged on the inside of teeter chamber (8), the heater (9) is arranged on teeter chamber (8) on outer wall low side surface, one end of the discharge nozzle (10) is communicated with the inside of teeter chamber (8), and discharge nozzle (10) is another One end is communicated with the inside of drying chamber (19), and the heating lamp (11) is arranged in the inwall top side face of drying chamber (19), described Conveyer belt (13) is arranged on the inside of drying chamber (19), and the baffle plate (14) is arranged on the outer wall one side of frame (12), institute State inside of the inside of water tank (15) respectively with the first container (2), second container (4) to communicate, the PLC (16) is set On the one side of frame (12) outer wall, described outlet pipe (18) one end is communicated with the inside of water tank (15), and outlet pipe (18) The other end be arranged on the outer wall one side of frame (12) and communicated with the external world, the magnetic valve (20) is arranged on outlet pipe (18) On, and magnetic valve (20) is located at the junction of outlet pipe (18) and water tank (15).
2. Catalyst Production dryer according to claim 1, it is characterised in that:First container (2) and second Container (4) junction is provided with overflow valve.
3. Catalyst Production dryer according to claim 1, it is characterised in that:The stirring blade (7) is helical form Structure.
4. Catalyst Production dryer according to claim 1, it is characterised in that:The sieve plate (3) is set in parallel in The inside of first container (2) and second container (4).
5. Catalyst Production dryer according to claim 1, it is characterised in that:The PLC (16) and electricity Machine (5), heater (9), heating lamp (11), conveyer belt (13), magnetic valve (20) are electrically connected with.
CN201720045269.0U 2017-01-13 2017-01-13 Catalyst Production dryer Expired - Fee Related CN206440092U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720045269.0U CN206440092U (en) 2017-01-13 2017-01-13 Catalyst Production dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720045269.0U CN206440092U (en) 2017-01-13 2017-01-13 Catalyst Production dryer

Publications (1)

Publication Number Publication Date
CN206440092U true CN206440092U (en) 2017-08-25

Family

ID=59634778

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720045269.0U Expired - Fee Related CN206440092U (en) 2017-01-13 2017-01-13 Catalyst Production dryer

Country Status (1)

Country Link
CN (1) CN206440092U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109317072A (en) * 2018-10-19 2019-02-12 山东耀华特耐科技有限公司 Phosphate dihydrogen aluminum solution Preparation equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109317072A (en) * 2018-10-19 2019-02-12 山东耀华特耐科技有限公司 Phosphate dihydrogen aluminum solution Preparation equipment
CN109317072B (en) * 2018-10-19 2020-12-22 山东耀华特耐科技有限公司 Aluminum dihydrogen phosphate solution preparation equipment

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Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170825

Termination date: 20210113

CF01 Termination of patent right due to non-payment of annual fee