CN205980689U - Dry device for catalyst - Google Patents

Dry device for catalyst Download PDF

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Publication number
CN205980689U
CN205980689U CN201620987705.1U CN201620987705U CN205980689U CN 205980689 U CN205980689 U CN 205980689U CN 201620987705 U CN201620987705 U CN 201620987705U CN 205980689 U CN205980689 U CN 205980689U
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CN
China
Prior art keywords
drying device
dry
witted
keen
thick
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
CN201620987705.1U
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Chinese (zh)
Inventor
李永霞
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Xinzhou Teachers University
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Xinzhou Teachers University
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Application filed by Xinzhou Teachers University filed Critical Xinzhou Teachers University
Priority to CN201620987705.1U priority Critical patent/CN205980689U/en
Application granted granted Critical
Publication of CN205980689U publication Critical patent/CN205980689U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

The utility model belongs to the catalyst field specifically is a dry device for catalyst, including thick drying device, storage device and smart drying device, thick drying device includes thick drying device box and transmission band, the transmission band runs through thick drying device box, the top of thick drying device box is equipped with circulating fan, be equipped with heater I in the thick drying device box, the last storage device entry that is equipped with of storage device, the end that is the transmission band directly over the storage device entrance, smart drying device includes smart drying device box, 12 departments of smart drying device box height are equipped with smart drying device entry, be equipped with heater II in the smart drying device box, smart drying device entry and storage device export passing through tube coupling, the top and the bottom of smart drying device box all are equipped with the psammitolite. The setting of vacuum apparatus and hot inert gas device can make the catalyst dry under the vacuum state, has reduced drying temperature, has avoided producing the phenomenon of sintering because of the high temperature.

Description

A kind of dry catalyst device
Technical field
The invention belongs to catalyst field, specially a kind of dry catalyst device.
Background technology
In catalyst production process dry run be must one of processing step, the catalyst commonly used at present is dried Mode be catalyst feed to be dried is contained on charging tray after be placed on baking material frame, and sometimes too high baking temperature can make Sintering of catalyst, this brings a lot of troubles to production process, also increases the labor intensity of workman.
Content of the invention
In order to solve above-mentioned technical problem, this utility model provides a kind of dry catalyst device.
The application is realized by following proposal:
A kind of dry catalyst device, including thick drying device, storage device and smart drying device, thick drying device bag Include thick drying device casing and be used for transmitting catalyst transmission belt, transmission belt runs through thick drying device casing, thick drying device case The top of body is provided with circulating fan, is provided with heater I, storage device is provided with storage device entrance in thick drying device casing, Storage device porch just on face the discharge end of transmission belt, smart drying device includes keen-witted and capable dry device box, keen-witted and capable dry It is provided with keen-witted and capable dry device portal at the 1/2 of device box height, in keen-witted and capable dry device box, be provided with heater II, smart drying device Entrance is connected by pipeline with storage device outlet, and the top of keen-witted and capable dry device box and bottom are equipped with core.
Preferably, it is provided with temperature inductor, humidifier and humidity sensor, thick drying device case in thick drying device casing The outside of body is provided with controller and display screen.
Preferably, keen-witted and capable dry device box is provided with watch window.
Preferably, the top of keen-witted and capable dry device box is logical all with wherein the one of four-way with bottom is connected.
Preferably, pipeline and vacuum holding are respectively passed through in the other threeway of the four-way of keen-witted and capable dry device box top and bottom Put, hot inert gas device, waste liquid collector are connected, the pipeline connecting vacuum equipment is provided with vacuum control valve, connect The pipeline of hot inert gas device is provided with gas control valve, and the pipeline connecting waste liquid collector is provided with discharge opeing control valve.
Preferably, waste liquid collector is connected with liquid waste treating apparatus.
The principle of the application is:The catalyst needing dry is put in transmission belt, catalyst is with the movement of transmission belt Reach thick drying device, according to the feature of catalyst, catalyst is set and the condition that need, such as temperature, humidity etc. is dried, to catalysis Agent is slightly dried, and display screen can show the temperature and humidity in thick drying device, the thick drying device of temperature sensor senses In temperature, when the temperature in device is less than design temperature, by signal transmission to controller, controller controls for temperature sensor Heater I, heater I works and device is heated, and when temperature is higher than design temperature, temperature sensor is too high by temperature To controller, controller controls heater to quit work to signal transmission, former with temperature controlled to the principle of device humid control Reason is identical, and when humidity is less than setting value, humidifier is in running order, and device is humidified, when humidity is more than setting value, humidification Device is closed state, and circulating fan is opened and device is dehumidified, and catalyst passes through thick drying device with transmission belt Slightly be dried, after with transmission belt reach storage device carry out keen-witted and capable dry;Keen-witted and capable dry before, vacuum control valve, gas control valve It is in closed mode with discharge opeing control valve, open vacuum control valve, gas control valve successively, by evacuation repeatedly, inertia Gas purging enters line replacement to drying tower, and when being replaced, drying tower is in vacuum state, closes vacuum control valve and gas control Catalyst is transported in smart drying device from storage device by the negative pressure in device and motor by valve processed, and catalyst enters essence In drying device, close keen-witted and capable dry device portal, open vacuum control valve, discharge opeing control valve and heater II, remain in catalysis Water in agent and solvent pass through core and pipeline entrance waste liquid collector, certainly, can be full if only passing through thick drying device The demand that foot is dried to catalyst, then just it need not be carried out keen-witted and capable dry.
Transmission belt is located at the middle and lower part of thick drying box, and heater is located at the top of transmission belt.
Core is core filter plate, has filtration.
This device selects the diameter dimension of storage device pipeline between smart drying device according to the size of catalyst granules, And selecting suitable transmission speed, it is to avoid blocking pipeline, this section of pipeline can be may also be employed using continuously transmitting in transmitting procedure Intermittent transmission mode.
The beneficial effect of the application is:The setting of vacuum equipment and hot inert gas device on smart drying device, can make Catalyst is dried under vacuum conditions, reduces baking temperature, it is to avoid produce the phenomenon of sintering because temperature is too high, and waste liquid is received The setting of acquisition means and liquid waste treating apparatus achieves and is dried and liquid waste processing integration, reduces pollution.
When preparing catalyst, sometimes using high boiling solvent or high boiling point reactant, the design of smart drying device can Meet the demand to high boiling substance.
According to the difference of catalyst, only can be slightly dried under meeting the requirement that catalyst is dried, also can only be entered Row is keen-witted and capable dry, also can keen-witted and capable dry, thick drying all carry out, the range of this device is very wide.
Brief description
Fig. 1 is the structural representation of the application;
In figure, 1, thick drying device casing, 2, storage device, 3, smart drying device slim, 4, heater I, 5, temperature sense Answer device, 6, humidifier, 7, humidity sensor, 8, controller, 9, display screen, 10, circulating fan, 11, transmission belt, 12, storage dress Posting port, 13, core, 14, watch window, 15, four-way, 16, vacuum equipment, 17, hot inert gas device, 18, waste liquid collects Device, 19, liquid waste treating apparatus, 20, vacuum control valve, 21, gas control valve, 22, discharge opeing control valve, 23, valve I, 24, plus Hot device II, 25, valve II, 26, motor I, 27, storage device outlet, 28, motor II, 29, transmission belt mouth, smart drying device enters Mouthful.
Specific embodiment
Embodiment 1
A kind of dry catalyst device, including thick drying device, storage device 2 and smart drying device, thick drying device Transmission belt 11 including thick drying device casing 1 with for transmitting catalyst, transmission belt 11 runs through thick drying device casing 1, slightly The top of drying device casing 1 is provided with circulating fan 10, is provided with heater I 4, storage device 2 sets in thick drying device casing 1 There is storage device entrance 12, the surface at storage device entrance 12 faces the discharge end of transmission belt 11, smart drying device bag Include keen-witted and capable dry device box 3, keen-witted and capable dry device box 3 height 1/2 at be provided with smart drying device and enter 30, keen-witted and capable dry device box It is provided with heater II 24, keen-witted and capable dry device portal 30 is connected by pipeline with storage device outlet 27, keen-witted and capable dry device box in 3 3 top and bottom are equipped with core 13, are provided with temperature sensor 5, humidifier 6 and humidity sensor in thick drying device casing 1 Device 7, the outside of thick drying device casing 1 is provided with controller 8 and display screen 9, and keen-witted and capable dry device box 3 is provided with watch window 14, the top of keen-witted and capable dry device box 3 is logical all with wherein the one of four-way 15 with bottom to be connected, keen-witted and capable dry device box 3 top Other threeway with the four-way 15 of bottom is respectively passed through pipeline and is collected with vacuum equipment 16, hot inert gas device 17, waste liquid Device 18 is connected, and the pipeline connecting vacuum equipment 16 is provided with vacuum control valve 20, connects the pipe of hot inert gas device 17 Road is provided with gas control valve 21, and the pipeline connecting waste liquid collector 18 is provided with discharge opeing control valve 22, waste liquid collector 18 are connected with liquid waste treating apparatus 19.
Motor I 26 is used for driving transmission belt 11, and motor 28 is used for for catalyst being transferred to smart drying device from storage device Interior, valve I 23 is used for controlling the opening and closing of pipeline between waste liquid collector 18 and liquid waste treating apparatus 19 it is clear that thick drying device 1 is provided with the transmission tape entry 29 passing through for transmission belt, and the size of transmission tape entry 21 will can make to put catalysis in transmission belt Can also pass through after agent.

Claims (6)

1. a kind of dry catalyst device is it is characterised in that include thick drying device, storage device and smart drying device, slightly Drying device includes thick drying device casing and the transmission belt for transmitting catalyst, and transmission belt runs through thick drying device casing, The top of thick drying device casing is provided with circulating fan, is provided with heater I, storage device is provided with storage in thick drying device casing Cryopreservation device entrance, the surface of storage device porch faces the discharge end of transmission belt, and smart drying device includes keen-witted and capable dry dress Put casing, keen-witted and capable dry device box height 1/2 at be provided with keen-witted and capable dry device portal, be provided with heater in keen-witted and capable dry device box II, keen-witted and capable dry device portal is connected by pipeline with storage device outlet, and the top of keen-witted and capable dry device box and bottom are equipped with Core.
2. as claimed in claim 1 a kind of dry catalyst device it is characterised in that setting in described thick drying device casing There are temperature inductor, humidifier and humidity sensor, the outside of thick drying device casing is provided with controller and display screen.
3. as claimed in claim 1 a kind of dry catalyst device it is characterised in that setting on described keen-witted and capable dry device box There is watch window.
4. as claimed in claim 1 a kind of dry catalyst device it is characterised in that the top of described keen-witted and capable dry device box Portion is logical all with wherein the one of four-way with bottom to be connected.
5. as claimed in claim 1 a kind of dry catalyst device it is characterised in that described keen-witted and capable dry device box top Pipeline and vacuum equipment, hot inert gas device, waste liquid collector phase are respectively passed through in other threeway with the four-way of bottom Connect, the pipeline connecting vacuum equipment is provided with vacuum control valve, and the pipeline connecting hot inert gas device is provided with gas control Valve processed, the pipeline connecting waste liquid collector is provided with discharge opeing control valve.
6. as claimed in claim 5 a kind of dry catalyst device it is characterised in that described waste liquid collector and waste liquid Processing meanss are connected.
CN201620987705.1U 2016-08-30 2016-08-30 Dry device for catalyst Expired - Fee Related CN205980689U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620987705.1U CN205980689U (en) 2016-08-30 2016-08-30 Dry device for catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620987705.1U CN205980689U (en) 2016-08-30 2016-08-30 Dry device for catalyst

Publications (1)

Publication Number Publication Date
CN205980689U true CN205980689U (en) 2017-02-22

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620987705.1U Expired - Fee Related CN205980689U (en) 2016-08-30 2016-08-30 Dry device for catalyst

Country Status (1)

Country Link
CN (1) CN205980689U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109469818A (en) * 2018-12-10 2019-03-15 中国空分工程有限公司 A kind of device and method for the not parking supplement expanded perlite of large-scale low-temperature storage tank
CN109603686A (en) * 2019-01-29 2019-04-12 连云港清泰化工有限公司 A kind of perfluor hexanone catalyst dewatering process and equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109469818A (en) * 2018-12-10 2019-03-15 中国空分工程有限公司 A kind of device and method for the not parking supplement expanded perlite of large-scale low-temperature storage tank
CN109603686A (en) * 2019-01-29 2019-04-12 连云港清泰化工有限公司 A kind of perfluor hexanone catalyst dewatering process and equipment

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170222

Termination date: 20170830