CN108147154A - A kind of closed silo isolation cycle discharge control method - Google Patents

A kind of closed silo isolation cycle discharge control method Download PDF

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Publication number
CN108147154A
CN108147154A CN201810037044.XA CN201810037044A CN108147154A CN 108147154 A CN108147154 A CN 108147154A CN 201810037044 A CN201810037044 A CN 201810037044A CN 108147154 A CN108147154 A CN 108147154A
Authority
CN
China
Prior art keywords
hopper
valve
discharge
inlet valve
outlet valve
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.)
Pending
Application number
CN201810037044.XA
Other languages
Chinese (zh)
Inventor
高冬冬
任卫东
李君琪
吕品
张晓峰
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.)
Handan Handan Iron And Steel Group Xinda Technology Co Ltd
Original Assignee
Handan Handan Iron And Steel Group Xinda 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 Handan Handan Iron And Steel Group Xinda Technology Co Ltd filed Critical Handan Handan Iron And Steel Group Xinda Technology Co Ltd
Priority to CN201810037044.XA priority Critical patent/CN108147154A/en
Publication of CN108147154A publication Critical patent/CN108147154A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G65/00Loading or unloading
    • B65G65/30Methods or devices for filling or emptying bunkers, hoppers, tanks, or like containers, of interest apart from their use in particular chemical or physical processes or their application in particular machines, e.g. not covered by a single other subclass
    • B65G65/34Emptying devices
    • B65G65/40Devices for emptying otherwise than from the top
    • B65G65/42Devices for emptying otherwise than from the top using belt or chain conveyors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G43/00Control devices, e.g. for safety, warning or fault-correcting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G2203/00Indexing code relating to control or detection of the articles or the load carriers during conveying
    • B65G2203/02Control or detection

Abstract

The present invention is a kind of closed silo isolation cycle discharge control method, particularly have flue gas by discharge device autocontrol method, belong to discharge automatic control technology field.Technical solution is:Same two feed bins of hopper Corresponding matching by controlling the opening and closing of hopper feed valve and outlet valve, and then control the material conveying of feed bin;Low material position trigger switch L is equipped in the hopperbWith high charge level trigger switch La, inlet valve include inlet valve Va and inlet valve Vb, outlet valve be outlet valve Vc.Beneficial effects of the present invention:Have a very strong versatility, and can directly monitoring and display current valve equipment open and-shut mode, operating personnel can be easily controlled system equipment and reduce accident;The number of withdrawal rate is estimated that by the on-off times of valve, the condition of production is had gained some understanding and controlled indirectly, can be optimized, makes full use of resource, avoids wasting.

Description

A kind of closed silo isolation cycle discharge control method
Technical field
The present invention is a kind of closed silo isolation cycle discharge control method, particularly have flue gas by discharge fill The autocontrol method put belongs to discharge automatic control technology field.
Background technology
At present, during the materials such as industrial material conveying, hopper feed bin discharge convey, material is generally stored inside big In feed bin, then by hopper control material falling speed, discharge quantity to belt feeder conveying and blanking, so as to reach the conveying of material Or the purpose of discharge.The common design of prior art is that a feed bin corresponds to a hopper, the then conveying of control material.This Kind design is more popular simple, and shortcoming is that equipment occupation space is larger, and mechanical equipment, instrumentation, electrical equipment exist certain Repetition amount so as to cause a large amount of wasting of resources.At the same time, have flue gas by the usually entire technique mistake of discharge device Range request is closed, cannot have flue gas intersection in the transmission process for carrying out material between feed bin, for this discharge work Skill just needs post personnel continuously to grasp material real-time condition, once carelessness is likely to result in equipment damage or personnel's thing Therefore there is certain blind area and hidden danger.
Invention content
The object of the present invention is to provide a kind of closed silo isolation cycle discharge control methods, utilize PLC and DCS systems The closed material bin isolation cycle discharge that system is realized designs different discharge devices and discharge control for discharge situation not of the same race Method processed, uses manpower and material resources sparingly, and eliminates safe hidden trouble, and solves the above problem in the presence of background technology.
The technical scheme is that:
A kind of closed silo isolation cycle discharge control method, same two feed bins of hopper Corresponding matching, passes through control The opening and closing of hopper feed valve and outlet valve, and then control the material conveying of feed bin;Low material position trigger switch is equipped in the hopper LbWith high charge level trigger switch La, inlet valve include inlet valve Va and inlet valve Vb, outlet valve be outlet valve Vc;
The top of inlet valve Va and inlet valve Vb, inlet valve Va and inlet valve Vb for being equipped with parallel arrangement above hopper connect respectively Respective feed bin, hopper lower section are equipped with outlet valve Vc;Material transmission process in hopper:When inlet valve Va or inlet valve Vb is opened Material is into material bin, material discharge hopper when outlet valve Vc is opened;During discharge, valve Va or inlet valve Vb and discharging are expected Valve is that cycle discontinuity performs opening and closing order;Control process is:When inlet valve Va is opened, inlet valve Vb and outlet valve Vc is closed;When inlet valve Vb is opened, inlet valve Va and outlet valve Vc are closed;When outlet valve Vc is opened, inlet valve Va and into Expect that valve Vb is closed.
The control mode of the present invention causes hopper in synchronization only there are one inlet valve opening, in the hopper for containing gas Or in the discharging process of feed bin, gas medium will not be caused to diffuse to other devices by hopper, so as between different feed bins Play buffer action;The opening time needs of inlet valve are set according to corresponding technique actual conditions, and when hopper High charge level trigger switch LaDuring action, all inlet valves are closed;The opening time of outlet valve also need according to actual conditions into Row setting, as low material position trigger switch LbDuring action, discharge valve is closed.
According to different process conditions, the arrangement mode of hopper is divided into two kinds of column and matrix form;
The control process of column hopper:When there are two or during more than two hopper, each hopper matches two feed bins, multiple material Bucketline formula arranges, and the outlet valve of each hopper shares same belt conveyor.
The control process of column hopper is:Control the discharging sequence of hopper and the belt conveyor rotation direction phase of institute blanking It is inverse;Hopper outlet valve is opened for order request formula, and after having the order that any one material inlet valve performs charging, discharging is asked It asks and is triggered, outlet valve waits for discharging sequence and then can perform discharge order;This process needs to calculate each hopper in skin The run time of next hopper is run to the discharging point on conveyer, this time is the stand-by period;The process of discharge is cycle , if hopper does not have discharge request, the discharge that this hopper carries out next hopper is skipped, the last one hopper discharge is completed Afterwards, it needs to wait for this hopper corresponding stand-by period, then starts the cycle of next discharge.
The arrangement of matrix form hopper:When meet complicated technology demand or there are equipment place use space limitation when, The arrangement of hopper is matrix arrangement, and such mode can improve space utilization and improve material transfer efficiency;There are two Or during two or more hopper, each hopper matches two feed bins, several hopper elder generation column arrangements, the hopper of each column shares together One feeding pipe;Multiple row is arranged, the feeding pipe of each column shares same belt conveyor.
The control process of matrix form hopper is divided into two kinds:A kind of is the control method according to the discharge of column hopper to matrix Formula material bin hopper is organized into groups, then converting putting in order for hopper according to the demand of production technology carries out discharge, Ci Zhongfang The feed bin of discharge can be freely combined in formula, have very strong operability;Another way is according in actual items matrix Columns, cycle discharge can be carried out at the same time by adjusting the aperture of all outlet valves so as to reach the hopper of all row, and can be with The different group of different behaviors is combined as arrangement, such mode can greatly improve discharge efficiency.
Beneficial effects of the present invention:There is very strong versatility, and being capable of directly monitoring and the equipment opening and closing of display current valve State, operating personnel can be easily controlled system equipment and reduce accident;It is estimated that by the on-off times of valve The number of withdrawal rate, has gained some understanding and controls to the condition of production indirectly, can optimize, make full use of resource, avoid wasting.
Description of the drawings
Fig. 1 hopper discharge control logic schematic diagrames of the present invention;
Fig. 2 is hopper schematic diagram of the present invention;
Fig. 3 is one column hopper discharge schematic diagram of the embodiment of the present invention;
Fig. 4 is the more hopper schematic diagrames of two matrix form of the embodiment of the present invention.
Specific embodiment
Below in conjunction with attached drawing, by embodiment, the present invention will be further described.
A kind of closed silo isolation cycle discharge control method, same two feed bins of hopper Corresponding matching, passes through The opening and closing of hopper feed valve and outlet valve is controlled, and then controls the material conveying of feed bin;Low material position is equipped in the hopper to trigger Switch LbWith high charge level trigger switch La, inlet valve include inlet valve Va and inlet valve Vb, outlet valve be outlet valve Vc;
The top of inlet valve Va and inlet valve Vb, inlet valve Va and inlet valve Vb for being equipped with parallel arrangement above hopper connect respectively Respective feed bin, hopper lower section are equipped with outlet valve Vc;Material transmission process in hopper:When inlet valve Va or inlet valve Vb is opened Material is into material bin, material discharge hopper when outlet valve Vc is opened;During discharge, valve Va or inlet valve Vb and discharging are expected Valve is that cycle discontinuity performs opening and closing order;Control process is:When inlet valve Va is opened, inlet valve Vb and outlet valve Vc is closed;When inlet valve Vb is opened, inlet valve Va and outlet valve Vc are closed;When outlet valve Vc is opened, inlet valve Va and into Expect that valve Vb is closed.
The control mode of the present invention causes hopper in synchronization only there are one inlet valve opening, in the hopper for containing gas Or in the discharging process of feed bin, gas medium will not be caused to diffuse to other devices by hopper, so as between different feed bins Play buffer action;The opening time needs of inlet valve are set according to corresponding technique actual conditions, and when hopper High charge level trigger switch LaDuring action, all inlet valves are closed;The opening time of outlet valve also need according to actual conditions into Row setting, as low material position trigger switch LbDuring action, discharge valve is closed.
According to different process conditions, the arrangement mode of hopper is divided into two kinds of column and matrix form;
Embodiment one, with reference to attached drawing 3, the control process of column hopper:When there are two or during more than two hopper, each hopper Two feed bins, multiple hopper column arrangements are matched, the outlet valve of each hopper shares same belt conveyor.
The control process of column hopper is:Control the discharging sequence of hopper and the belt conveyor rotation direction phase of institute blanking It is inverse;Hopper outlet valve is opened for order request formula, and after having the order that any one material inlet valve performs charging, discharging is asked It asks and is triggered, outlet valve waits for discharging sequence and then can perform discharge order;This process needs to calculate each hopper in skin The run time of next hopper is run to the discharging point on conveyer, this time is the stand-by period;The process of discharge is cycle , if hopper does not have discharge request, the discharge that this hopper carries out next hopper is skipped, the last one hopper discharge is completed Afterwards, it needs to wait for this hopper corresponding stand-by period, then starts the cycle of next discharge.
With reference to attached drawing 3, determine that hopper discharge sequence is B3-B2-B1 according to the rotation direction of belt conveyor, feed bin passes through Inlet valve is to hopper discharge.According to actual production technology Calculation drain time length, inlet valve Va3 or Vb3, which are performed, opens life Enable, complete charging period or hopper B3 have high charge level signal La triggering, then inlet valve close, outlet valve Vc3 is touched at this time The response of hair request discharge waits for discharge sequence.After Vc3 performs discharge order, the process of discharge is completed, at this time hopper discharge Sequence is directed toward Vc2, if B2 storehouses have the process for having charging after this cycle starts, and Vc2 has the request of discharge, then Vb2 Discharge order is performed, if B2 storehouses, without the process of charging, discharge sequence is directed toward Vc1, feed bin B1 is carried out such as the judgement of B2, So that it is determined that whether Vc1 performs discharge order.If Vc2, which completes discharge order rear hopper B1, does not have discharge demand, cycle etc. Treat stand-by period of the time corresponding to B2 hoppers.If Vc1 finally completes discharging process, the stand-by period is recycled as B1 hoppers The corresponding stand-by period, the stand-by period finishes starts next cycle later.The control logic side when there is multiple feed bin hoppers Formula similarly, so control of the discharge of column feed bin hopper in order to control.
Embodiment two, with reference to attached drawing 4, the arrangement of matrix form hopper:When meeting complicated technology demand or there are equipment fields When ground uses the limitation in space, the arrangement of hopper is matrix arrangement, and such mode can improve space utilization and improve object Expect transfer efficiency;When there are two or during more than two hopper, each hopper matches two feed bins, several hopper elder generations column row Row, the hopper of each column share same feeding pipe;Multiple row is arranged, the feeding pipe of each column shares same belt conveyor.
The control process of matrix form hopper is divided into two kinds:A kind of is the control method according to the discharge of column hopper to matrix Formula material bin hopper is organized into groups, then converting putting in order for hopper according to the demand of production technology carries out discharge, Ci Zhongfang The feed bin of discharge can be freely combined in formula, have very strong operability;Another way is according in actual items matrix Columns, cycle discharge can be carried out at the same time by adjusting the aperture of all outlet valves so as to reach the hopper of all row, and can be with The different group of different behaviors is combined as arrangement, such mode can greatly improve discharge efficiency.
With reference to attached drawing 4, according to the transmission direction of the arrangement mode of hopper and belt conveyor, the cycle of hopper discharge is suitable Sequence is B6-B5-B4-B3-B2-B1-B6, and discharge priority is followed successively by from high to low:Va6-Va5-Va4-Va3-Va2-Va1, tool The control method of body can refer to the control method of the discharge of column material bin hopper.Another control mode is B6-B5-B4- B6 and B3-B2-B1-B3 are carried out at the same time, but need to adjust the aperture of outlet valve to adapt to the bearing capacity of lower floor's belt conveyor.
The control method of the present invention comprises the following steps:
Determine the design of material bin hopper.The design method of material bin is a kind of using that in Project design, determines to choose that one kind Control method controls.
Determine the instrument control device of material bin hopper.Hopper whether using height material position, whether have pressure control, whether Whether reversely charging gas medium, material thereby determine that the chained approach of valve along with gas medium etc..
Discharge circular order is determined by the rotation direction of belt conveyor.The rotation direction of belt feeder and material bin hopper Cycle discharge direction contrary can preferably ensure the normal operation of discharge.
Determine that discharging point of each material bin hopper on belt conveyor is transported to the run time of subordinate equipment, this time For the stand-by period, and calculate according to process condition the aperture of valve.Each stand-by period is the interval time recycled every time.
According to the control logic of above step editor's material bin hopper.Used PLC and DCS is combined according to control logic System writes control program.
Control program is debugged, is optimized with reference to actual conditions.

Claims (3)

1. a kind of closed silo isolation cycle discharge control method, it is characterised in that:Same hopper Corresponding matching two Feed bin by controlling the opening and closing of hopper feed valve and outlet valve, and then controls the material conveying of feed bin;It is equipped in the hopper low Material position trigger switch LbWith high charge level trigger switch La, inlet valve include inlet valve Va and inlet valve Vb, outlet valve is outlet valve Vc;
The top of inlet valve Va and inlet valve Vb, inlet valve Va and inlet valve Vb for being equipped with parallel arrangement above hopper connect respectively Respective feed bin, hopper lower section are equipped with outlet valve Vc;Material transmission process in hopper:When inlet valve Va or inlet valve Vb is opened Material is into material bin, material discharge hopper when outlet valve Vc is opened;During discharge, valve Va or inlet valve Vb and discharging are expected Valve is that cycle discontinuity performs opening and closing order;Control process is:When inlet valve Va is opened, inlet valve Vb and outlet valve Vc is closed;When inlet valve Vb is opened, inlet valve Va and outlet valve Vc are closed;When outlet valve Vc is opened, inlet valve Va and into Expect that valve Vb is closed.
2. a kind of closed silo isolation cycle discharge control method according to claim 1, it is characterised in that:When having During two or more hoppers, each hopper matches two feed bins, multiple hopper column arrangements, the outlet valve of each hopper Share same belt conveyor;The control process of column hopper is:Control the discharging sequence of hopper and the Belt Conveying of institute blanking Machine rotation direction contrary;Hopper outlet valve is opened for order request formula, when the life for having any one material inlet valve to perform charging After order, the request of discharging is triggered, and outlet valve waits for discharging sequence and then can perform discharge order;This process needs to calculate every Discharging point of one hopper on belt conveyor runs to the run time of next hopper, and this time is the stand-by period;Discharge Process be cycle, if hopper does not have discharge request, skip the discharge that this hopper carries out next hopper, the last one material It struggles against after the completion of discharge, needs to wait for this hopper corresponding stand-by period, then start the cycle of next discharge.
3. a kind of closed silo isolation cycle discharge control method according to claim 1, it is characterised in that:When having During two or more hoppers, each hopper matches two feed bins, several hopper elder generation column arrangements, the hopper of each column is total to With same feeding pipe;Multiple row is arranged, the feeding pipe of each column shares same belt conveyor.
CN201810037044.XA 2018-01-15 2018-01-15 A kind of closed silo isolation cycle discharge control method Pending CN108147154A (en)

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Application Number Priority Date Filing Date Title
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109761004A (en) * 2019-03-25 2019-05-17 广东洁冠能源科技有限公司 Device for transporting objects, component and method

Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1420407A (en) * 1972-03-06 1976-01-07 Wurth Anciens Ets Paul Supply of charge material to shaft furnaces particularly blast furnaces
JPH0291708A (en) * 1988-08-10 1990-03-30 K Tron Internatl Inc Self-tuning type stochastic control and weighing supply system using weight and actuator measured value
US6059641A (en) * 1997-05-30 2000-05-09 Kyoei Inc. Powder/granule feeder and its application apparatus
US20040016684A1 (en) * 2002-07-24 2004-01-29 Braginsky Mark B. Synchronous semi-automatic parallel sorting
US20090260896A1 (en) * 2005-09-21 2009-10-22 Ishida Co., Ltd. Combination weighing apparatus
CN201703872U (en) * 2010-06-03 2011-01-12 合肥天焱绿色能源开发有限公司 Biomass powder body high-pressure continuous dense phase conveyer capable of regulating height of sending outlet
CN202018244U (en) * 2011-04-08 2011-10-26 浏阳市青草烟花制造有限公司 Automatic gunpowder mixing device
CN202136927U (en) * 2010-12-27 2012-02-08 山东信发金属粉末有限公司 Pneumatic continuous powder mixing device
CN202369108U (en) * 2011-11-22 2012-08-08 中国铝业股份有限公司 Feed divider
CN102756923A (en) * 2012-07-26 2012-10-31 中国神华能源股份有限公司 Port coal transshipment method and coal port
CN103009485A (en) * 2012-11-16 2013-04-03 三一重工股份有限公司 Discharging control system and discharging control method
KR20130052058A (en) * 2011-11-11 2013-05-22 주식회사 포스코 Method for parallel injection of feed hoppers in pulverized coal facilities
JP3199449U (en) * 2015-06-12 2015-08-20 株式会社東京共栄商会 Hopper
CN204675141U (en) * 2015-06-05 2015-09-30 江阴中南重工有限公司 A kind of Double-port moulding mixture storehouse
CN205027709U (en) * 2015-06-01 2016-02-10 中国石油天然气股份有限公司 ONLINE CHROMATOGRAM sampling device
US20160096692A1 (en) * 2014-10-01 2016-04-07 Shell Oil Company Systems and methods for providing feed material to a pressurized system

Patent Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1420407A (en) * 1972-03-06 1976-01-07 Wurth Anciens Ets Paul Supply of charge material to shaft furnaces particularly blast furnaces
JPH0291708A (en) * 1988-08-10 1990-03-30 K Tron Internatl Inc Self-tuning type stochastic control and weighing supply system using weight and actuator measured value
US6059641A (en) * 1997-05-30 2000-05-09 Kyoei Inc. Powder/granule feeder and its application apparatus
US20040016684A1 (en) * 2002-07-24 2004-01-29 Braginsky Mark B. Synchronous semi-automatic parallel sorting
US20090260896A1 (en) * 2005-09-21 2009-10-22 Ishida Co., Ltd. Combination weighing apparatus
CN201703872U (en) * 2010-06-03 2011-01-12 合肥天焱绿色能源开发有限公司 Biomass powder body high-pressure continuous dense phase conveyer capable of regulating height of sending outlet
CN202136927U (en) * 2010-12-27 2012-02-08 山东信发金属粉末有限公司 Pneumatic continuous powder mixing device
CN202018244U (en) * 2011-04-08 2011-10-26 浏阳市青草烟花制造有限公司 Automatic gunpowder mixing device
KR20130052058A (en) * 2011-11-11 2013-05-22 주식회사 포스코 Method for parallel injection of feed hoppers in pulverized coal facilities
CN202369108U (en) * 2011-11-22 2012-08-08 中国铝业股份有限公司 Feed divider
CN102756923A (en) * 2012-07-26 2012-10-31 中国神华能源股份有限公司 Port coal transshipment method and coal port
CN103009485A (en) * 2012-11-16 2013-04-03 三一重工股份有限公司 Discharging control system and discharging control method
US20160096692A1 (en) * 2014-10-01 2016-04-07 Shell Oil Company Systems and methods for providing feed material to a pressurized system
CN205027709U (en) * 2015-06-01 2016-02-10 中国石油天然气股份有限公司 ONLINE CHROMATOGRAM sampling device
CN204675141U (en) * 2015-06-05 2015-09-30 江阴中南重工有限公司 A kind of Double-port moulding mixture storehouse
JP3199449U (en) * 2015-06-12 2015-08-20 株式会社東京共栄商会 Hopper

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
彭乃文;: "袋式除尘器在20t/h锅炉除尘器改造中的应用", 能源环境保护, no. 03 *
朱联东;李海波;朱旭;王钪;熊欣;张晓娟;黄道成;: "铁合金行业工业粉尘无组织排放问题探讨", 云南冶金, no. 03, pages 183 - 184 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109761004A (en) * 2019-03-25 2019-05-17 广东洁冠能源科技有限公司 Device for transporting objects, component and method

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