CN105752692B - Reactor Geldart-D particle feeding system - Google Patents
Reactor Geldart-D particle feeding system Download PDFInfo
- Publication number
- CN105752692B CN105752692B CN201610219711.7A CN201610219711A CN105752692B CN 105752692 B CN105752692 B CN 105752692B CN 201610219711 A CN201610219711 A CN 201610219711A CN 105752692 B CN105752692 B CN 105752692B
- Authority
- CN
- China
- Prior art keywords
- pot type
- type storehouse
- reactor
- discharging opening
- rotary feeder
- 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.)
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- 239000002245 particle Substances 0.000 title claims abstract description 12
- 238000007599 discharging Methods 0.000 claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 14
- 238000006243 chemical reaction Methods 0.000 claims abstract description 9
- 238000005303 weighing Methods 0.000 claims abstract description 7
- 239000000428 dust Substances 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 238000010276 construction Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000000843 powder Substances 0.000 description 7
- 239000007788 liquid Substances 0.000 description 4
- 230000005514 two-phase flow Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000003340 mental effect Effects 0.000 description 1
- 230000004630 mental health Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
- B65G53/24—Gas suction systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/40—Feeding or discharging devices
- B65G53/48—Screws or like rotary conveyors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/60—Devices for separating the materials from propellant gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/66—Use of indicator or control devices, e.g. for controlling gas pressure, for controlling proportions of material and gas, for indicating or preventing jamming of material
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Air Transport Of Granular Materials (AREA)
Abstract
The present invention relates to a kind of reactor Geldart-D particle feeding system, it mainly includes vavuum pump, ton bag feeding station and pot type storehouse, the first rotary feeder is provided with the bottom discharge mouth of the ton bag feeding station, the discharging opening of the rotary feeder is connected by converying feeding tube with the air inlet in pot type storehouse, top in the pot type storehouse is provided with material gas separating device, gas outlet above the pot type storehouse is connected by vacuum tube with vavuum pump, the bottom in the pot type storehouse is provided with cyclone dust collectors, the discharging opening of the cyclone dust collectors is provided with the second rotary feeder, the discharging opening of second rotary feeder is connected with the charging aperture of frequency conversion conveying worm, the discharging opening of the frequency conversion conveying worm is connected with the charging aperture of reactor.The present invention is using automation negative pressure feeding system：Energy consumption is low, simple in construction, easy to operate, weighing precision is high, continuous suction stable, gas discharge meet the requirement of environmental protection.
Description
Technical field
A kind of feeding system of the present invention, more particularly to a kind of reactor Geldart-D particle feeding system.Belong to environment-friendly engineering skill
Art field.
Background technology
It is to be stamped many charge doors on hand stock, reactor that the powder of existing reactor, which adds resourcefulness, in addition
During powder, powder is poured into reactor by a normally open larger charge door by workman from charge door.Existing powder is added
Method has disadvantages that, if powder addition is very big it is necessary to add repeatedly many times, efficiency is very low, and goes easily to make
Into dust pollution, physical and mental health and environment to workman cause harm.In order to devise automatical feeding system, and existing
In feeding system, due to material, from ground feeding to having in the reactor of certain altitude, will mostly be reacted using vavuum pump
Malleation feeding is converted in kettle, and sets feed pump to increase feed pressure.Existing feeding system works as institute due to using malleation feeding
The viscosity of feeding liquid is higher, and during beyond the lift or pressure of design pump, does not reach feeding requirement；When malleation feeding system makes
Easily leaked with flow during thick liquid, be unfavorable for safety；The dirt to air can be caused when positive pressure system is using volatile liquid
Dye, is unfavorable for environmental protection.When corrosive liquids is by malleation flow, the corrosion of flow is easily caused.
The content of the invention
The technical problems to be solved by the invention are to provide a kind of reactor Geldart-D particle feeding for above-mentioned prior art
System, using automation negative pressure feeding system：Energy consumption is low, simple in construction, easy to operate, weighing precision is high, continuous suction stable,
Gas discharges meet the requirement of environmental protection.
The present invention the used technical scheme that solves the above problems is：A kind of reactor Geldart-D particle feeding system, it leads
To include vavuum pump, ton bag feeding station and pot type storehouse, the first rotation is provided with the bottom discharge mouth of the ton bag feeding station
Batcher, the discharging opening of first rotary feeder is connected by converying feeding tube with the air inlet in pot type storehouse, in the pot type
Top in storehouse is provided with material gas separating device, and the gas outlet above the pot type storehouse is connected by vacuum tube with vavuum pump,
The bottom in the pot type storehouse is provided with cyclone separator, and the discharging opening of the cyclone separator is provided with the second rotary feeder,
The discharging opening of second rotary feeder is connected with the charging aperture of frequency conversion conveying worm, and the frequency conversion conveying worm goes out
Material mouth is connected with the charging aperture of reactor.
Preferably, it is provided with deduster at the ton bag feeding station.
Preferably, weighing sensor and level-sensing device are provided with the pot type storehouse.
Compared with prior art, the advantage of the invention is that：
The present invention is using automation negative pressure feeding system：Energy consumption is low, simple in construction, easy to operate, weighing precision is high, continuous
Suction is stable, gas discharge meet the requirement of environmental protection, and suction and conveying material the largest particles can reach 2 centimeters, can arbitrarily adjust material-gas ratio
Concentration, converying feeding tube arrangement is convenient, can arbitrarily turn round.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Wherein：
Vavuum pump 1, ton bag feeding station 2, pot type storehouse 3, deduster 4, the first rotary feeder 5, converying feeding tube 6, material qi leel
From device 7, vacuum tube 8, cyclone separator 9, the second rotary feeder 10, frequency conversion conveying worm 11, reactor 12, weighing and sensing
Device 13, level-sensing device 14.
Embodiment
The present invention is described in further detail below in conjunction with accompanying drawing embodiment.
As shown in figure 1, a kind of reactor Geldart-D particle feeding system in the present embodiment, mainly includes vavuum pump 1, ton bag
Feeding station 2 and pot type storehouse 3, deduster 4 is provided with the ton bag feeding station 2, and it is that airborne dust is excessive to prevent from feeding intake, in the ton
The first wear-resisting rotary feeder 5, the discharging of first rotary feeder 5 are provided with the bottom discharge mouthful of bag feeding station 2
Mouth is connected by converying feeding tube 6 with the air inlet in pot type storehouse 3, and the top in the pot type storehouse 3 is provided with material gas separating device 7,
The converying feeding tube 6 is located at the lower section of material gas separating device 7, and outlet is offered on the pot type storehouse 3 of the top of material gas separating device 7
Mouthful, the gas outlet is connected by vacuum tube 8 with vavuum pump 1, and the bottom in the pot type storehouse 3 is provided with cyclone separator 9, described
The discharging opening of cyclone separator 9 is provided with the second rotary feeder 10, the discharging opening of second rotary feeder 10 and frequency conversion
The charging aperture of conveying worm 10 is connected, and the discharging opening of the frequency conversion conveying worm 11 is connected with the charging aperture of reactor 12.
Weighing sensor 13 and level-sensing device 14 are provided with the pot type storehouse 3, material position in storehouse can be controlled and accurate
Measure the weight of material.
Reactor Geldart-D particle feeding system is used as power source with Roots vaccum pump or high heart blower fan, and pipeline and pot type storehouse are taken out
Into certain vacuum state, facilitate the two phase flow of air inlet formation feed powder pellet and gas under atmospheric pressure, through defeated
Pipeline is sent to input cyclone separator.Two phase flow is in cyclone separator due under high mental and physical efforts and Action of Gravity Field, making most of material
Separated with gas.A small amount of material enters deduster with gas, powder is separated with gas by filter bag effect, gas is discharged into greatly
Gas.
In addition to the implementation, present invention additionally comprises have other embodiment, all use equivalent transformation or equivalent replacements
The technical scheme that mode is formed, all should fall within the scope of the hereto appended claims.
Claims (3)
1. a kind of reactor Geldart-D particle feeding system, it is characterised in that：It mainly includes vavuum pump（1）, ton bag feeding station（2）
With pot type storehouse（3）, in the ton bag feeding station（2）Bottom discharge mouthful at be provided with the first rotary feeder（5）, described first
Rotary feeder（5）Discharging opening pass through converying feeding tube（6）With pot type storehouse（3）Air inlet be connected, in the pot type storehouse（3）It is interior
Top be provided with material gas separating device（7）, in the pot type storehouse（3）The gas outlet of top passes through vacuum tube（8）With vavuum pump（1）
It is connected, in the pot type storehouse（3）Bottom be provided with cyclone separator（9）, the cyclone separator（9）Discharging opening be provided with
Second rotary feeder（10）, second rotary feeder（10）Discharging opening and frequency conversion conveying worm（11）Charging aperture
It is connected, the frequency conversion conveying worm（11）Discharging opening and reactor（12）Charging aperture be connected.
2. a kind of reactor Geldart-D particle feeding system according to claim 1, it is characterised in that：Fed intake in the ton bag
Stand（2）Place is provided with deduster（4）.
3. a kind of reactor Geldart-D particle feeding system according to claim 1 or 2, it is characterised in that：In the pot type
Storehouse（3）On be provided with weighing sensor（13）And level-sensing device（14）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610219711.7A CN105752692B9 (en) | 2016-04-11 | 2016-04-11 | Reactor Geldart-D particle feeding system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610219711.7A CN105752692B9 (en) | 2016-04-11 | 2016-04-11 | Reactor Geldart-D particle feeding system |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| CN105752692A CN105752692A (en) | 2016-07-13 |
| CN105752692B true CN105752692B (en) | 2017-10-03 |
| CN105752692B9 CN105752692B9 (en) | 2017-12-26 |
Family
ID=56333641
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610219711.7A Active CN105752692B9 (en) | 2016-04-11 | 2016-04-11 | Reactor Geldart-D particle feeding system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105752692B9 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106431787A (en) * | 2016-09-28 | 2017-02-22 | 安徽向科化工有限公司 | Talcum powder feeding device and talcum powder feeding method for powdery emulsion explosive |
| CN107226354B (en) * | 2017-07-14 | 2023-04-14 | 湖北民族学院 | Weighing and feeding equipment for salting-out process and using method thereof |
| CN107640594B (en) * | 2017-09-29 | 2023-05-12 | 襄阳市精信催化剂有限责任公司 | Control method of zero-crushing negative-pressure wind power conveying device |
| CN109925967A (en) * | 2019-04-16 | 2019-06-25 | 郑仲新 | A kind of continuous feed, deslagging and slag dumping integration refuse disposal system |
| CN110654899A (en) * | 2019-09-05 | 2020-01-07 | 江阴市高达输送机械科技有限公司 | Vacuum closed feeder and dust-free feeding method |
| CN112551172A (en) * | 2020-04-30 | 2021-03-26 | 章丘丰源机械有限公司 | Environment-friendly pneumatic conveying system |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN105752692A (en) | 2016-07-13 |
| CN105752692B9 (en) | 2017-12-26 |
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| GR01 | Patent grant | ||
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| CI03 | Correction of invention patent |
Correction item: Claims Correct: Correct False: Error Number: 40-01 Page: full text Volume: 33 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Pneumatic conveying and feeding system of reactor Effective date of registration: 20221102 Granted publication date: 20171003 Pledgee: Jiangyin branch of Bank of China Ltd. Pledgor: JIANGYIN GAODA TRANSPORTATION MACHINERY TECHNOLOGY Co.,Ltd. Registration number: Y2022980020473 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20230907 Granted publication date: 20171003 Pledgee: Jiangyin branch of Bank of China Ltd. Pledgor: JIANGYIN GAODA TRANSPORTATION MACHINERY TECHNOLOGY Co.,Ltd. Registration number: Y2022980020473 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Reaction kettle pneumatic conveying and feeding system Effective date of registration: 20230913 Granted publication date: 20171003 Pledgee: Jiangyin branch of Bank of China Ltd. Pledgor: JIANGYIN GAODA TRANSPORTATION MACHINERY TECHNOLOGY Co.,Ltd. Registration number: Y2023980056143 |
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| CP03 | Change of name, title or address |
Address after: 214400 No. 9, Shenjiabang Road, Yunting Street, Jiangyin City, Wuxi City, Jiangsu Province (Business premises: No. 58, Shenjiadang, Nanguo Village, Changjing Town, Jiangyin City) Patentee after: Jiangsu Gaoda Intelligent Equipment Co.,Ltd. Country or region after: China Address before: 214422 Industrial Concentration Zone, Yunting Town, Jiangyin City, Wuxi City, Jiangsu Province Patentee before: JIANGYIN GAODA TRANSPORTATION MACHINERY TECHNOLOGY Co.,Ltd. Country or region before: China |