CN201203561Y - On-line automatic dynamic density analyzer for flotation pulp foam - Google Patents

On-line automatic dynamic density analyzer for flotation pulp foam Download PDF

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Publication number
CN201203561Y
CN201203561Y CNU2008200131633U CN200820013163U CN201203561Y CN 201203561 Y CN201203561 Y CN 201203561Y CN U2008200131633 U CNU2008200131633 U CN U2008200131633U CN 200820013163 U CN200820013163 U CN 200820013163U CN 201203561 Y CN201203561 Y CN 201203561Y
Authority
CN
China
Prior art keywords
foam
force sensor
line automatic
automatic dynamic
liquid crystal
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 - Lifetime
Application number
CNU2008200131633U
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Chinese (zh)
Inventor
商宏伟
聂家龙
张峰
滕勇
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.)
Angang Group Mining Co Ltd
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Angang Group Mining 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 Angang Group Mining Co Ltd filed Critical Angang Group Mining Co Ltd
Priority to CNU2008200131633U priority Critical patent/CN201203561Y/en
Application granted granted Critical
Publication of CN201203561Y publication Critical patent/CN201203561Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/02Froth-flotation processes
    • B03D1/028Control and monitoring of flotation processes; computer models therefor

Abstract

The utility model belongs to an on-line automatic dynamic density analyzer of flotation mineral slurry foam composed of a detecting device, a spiral elevating device and a control device, the detecting device is composed of a counterweight detector, steel wires connected with the counterweight detector and a tensile force sensor, a lower end of the spiral elevating device is connected with the tensile force sensor, the control device is mounted in the control box body and is composed of a switch power supply, a PLC formwork, a terminal bar and a liquid crystal touch screen, the PLC formwork is respectively connected with the liquid crystal touch screen and the terminal bar, the terminal bar is respectively connected with the tensile force sensor and the spiral elevating device box. Adopting the utility model can implement on-line automatic dynamic density analysis, microscopic variation of the on-site foam can be intuitively displayed, the thickness and the quality of the foam can be displayed by trend variation of the foam analyzer, the efficiency and the quality of flotation operation are increased, the utility model is suitable for various metallurgy concentration plants and can help the concentration plant to implement production automation.

Description

The on-line automatic dynamic density analyser of flotation pulp foam
Technical field
The utility model belongs to the ore separators auxiliary device, the on-line automatic dynamic density analyser of particularly a kind of flotation pulp foam.
Background technology
In ore dressing flotation production run, the quality of ore pulp froth bed thickness and foam is that technology is adjusted very important parameter in the flotation cell.Up to the present, owing to there is not effective detection method, operating personnel can only be by the on-site experience analysis, very inaccurate, cause maloperation easily, adopt ultrasonic level gage, radar level gauge and floating ball lever meter to detect mineral pulp level in the flotation cell in the world, but be used for ultrasonic level gage, the radar level gauge transmitted wave can't penetrate froth bed, measure inaccurately, floating ball lever meter can't overcome pulp density and change influence to measuring liquid level, measures inaccurate.Because present neither one is in the world measured the quality effective ways of interior ore pulp froth bed thickness of flotation cell and foam, so all ore dressing plant flotation flowsheets still can not realize the whole process closed-loop control in the world.
Summary of the invention
The purpose of this utility model provides the on-line automatic dynamic density analyser of a kind of flotation pulp foam, intuitively show by the micro-variations of foam analysis instrument on-the-spot foam, the thickness, the quality that show foam, carry out trend analysis, that further judges each section operation scrapes the blister attitude, so that carry out technological operation, improve flotation operation efficient and quality.
The purpose of this utility model realizes by following technical proposals:
According to the on-line automatic dynamic density analyser of flotation pulp froth bed of the present utility model, it is characterized in that by sniffer, the spiral lift device that is connected of sniffer therewith, with sniffer therewith respectively, the control device that spiral lift device is connected is formed, described sniffer is by the counterweight detector, the steel wire that is connected of counterweight detector-pulling force sensor is formed therewith, this steel wire-pulling force sensor is connected with the lower end of spiral lift device, described control device is by the Switching Power Supply that is contained in the control casing, the PLC template, terminal row and liquid crystal touch screen are formed, the PLC template is connected with terminal row with liquid crystal touch screen respectively, terminal row respectively with described pulling force sensor, spiral lift device connects.
Described spiral lift device is by helical screw, the speed gear that is connected of helical screw therewith, and the uniform speed electric motor that is connected of speed gear and the limit protection device that is located on this uniform speed electric motor are formed therewith.
Described liquid crystal touch screen is contained on the door of control box.
Adopt the utility model can realize online automatic dynamic density analysis, trend by the foam analysis instrument changes, can the micro-variations of on-the-spot foam be shown intuitively, the thickness and the quality that show foam, improve flotation operation efficient and quality, be applicable to various technics of metallurgy mineral dressing factory, help the ore dressing plant to realize the production automation.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
Below in conjunction with description of drawings embodiment of the present utility model.
As shown in Figure 1, according to the on-line automatic dynamic density analyser of flotation pulp froth bed of the present utility model, it is characterized in that by sniffer, the spiral lift device that is connected of sniffer therewith, with sniffer therewith respectively, the control device that spiral lift device is connected is formed, described sniffer is by counterweight detector 1, the steel wire 2 that is connected of counterweight detector 1 therewith, pulling force sensor 3 is formed, this connects pulling force sensor 3 and is connected with the lower end of spiral lift device 8, described control device is by the Switching Power Supply 11 that is contained in control box 10 bodies, PLC template 12, terminal row 13 and liquid crystal touch screen 9 are formed, PLC template 12 is connected with terminal row 13 with liquid crystal touch screen 9 respectively, terminal row 13 respectively with described pulling force sensor 3, spiral lift device 8 connects.
Described spiral lift device is by helical screw 4, the speed gear 5 that is connected of helical screw 4 therewith, and the uniform speed electric motor 6 that is connected of speed gear 5 and the limit protection device 7 that is located on this uniform speed electric motor 6 are formed therewith.The limit protection device 7 couples of uniform speed electric motors 6 shield.
Described liquid crystal touch screen 9 is contained on the door 14 of control box 10.
When adopting the utility model, at first connect the Switching Power Supply in the control casing, the PLC template brings into operation, uniform speed electric motor in the control spiral cabinet just changes, the uniform speed electric motor drives the helical screw rotation by speed gear, the counterweight detector that helical screw drives on pulling force sensor and the connected steel wire at the uniform velocity enters froth bed from flotation cell foam top, and enter the ore pulp layer from froth bed, set the just commentaries on classics time of spiral lift device by the PLC template, the degree of depth that control enters the ore pulp layer, control the counter-rotating of spiral lift device behind the arrival set point by the PLC template, the counterweight detector enters froth bed by the ore pulp layer, top from the froth bed to the foam, the PLC template is back and forth carried out said procedure.In counterweight detector to-and-fro movement process, in time the pulling force signal is sent to the PLC template by pulling force sensor, carry out computing by the PLC template, pulling force is transformed into density value, the PLC template root point position that motor travelling speed, rotating working time and the automatic computing of operation stroke are measured of crouching simultaneously, signal is sent to liquid crystal touch screen, the trend that demonstrates thickness, amount of densities and the foam density of foam on liquid crystal touch screen changes, operating personnel just can in time understand the online dynamic density of flotation pulp froth bed, so that instruct production.

Claims (3)

1, the on-line automatic dynamic density analyser of a kind of flotation pulp froth bed, it is characterized in that by sniffer, the spiral lift device that is connected of sniffer therewith, with sniffer therewith respectively, the control device that spiral lift device is connected is formed, described sniffer is by the counterweight detector, the steel wire that is connected of counterweight detector-pulling force sensor is formed therewith, this pulling force sensor is connected with the lower end of spiral lift device, described control device is by the Switching Power Supply that is contained in the control casing, the PLC template, terminal row and liquid crystal touch screen are formed, the PLC template is connected with terminal row with liquid crystal touch screen respectively, terminal row respectively with described pulling force sensor, spiral lift device connects.
2, the on-line automatic dynamic density analyser of flotation pulp froth bed according to claim 1; it is characterized in that described spiral lift device is by helical screw; the speed gear that is connected of helical screw therewith, the uniform speed electric motor that is connected of speed gear and the limit protection device that is located on this uniform speed electric motor are formed therewith.
3, the on-line automatic dynamic density analyser of flotation pulp froth bed according to claim 1 is characterized in that described liquid crystal touch screen is contained on the door of control box.
CNU2008200131633U 2008-05-26 2008-05-26 On-line automatic dynamic density analyzer for flotation pulp foam Expired - Lifetime CN201203561Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008200131633U CN201203561Y (en) 2008-05-26 2008-05-26 On-line automatic dynamic density analyzer for flotation pulp foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008200131633U CN201203561Y (en) 2008-05-26 2008-05-26 On-line automatic dynamic density analyzer for flotation pulp foam

Publications (1)

Publication Number Publication Date
CN201203561Y true CN201203561Y (en) 2009-03-04

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Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008200131633U Expired - Lifetime CN201203561Y (en) 2008-05-26 2008-05-26 On-line automatic dynamic density analyzer for flotation pulp foam

Country Status (1)

Country Link
CN (1) CN201203561Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102539280A (en) * 2010-12-10 2012-07-04 中国石油化工股份有限公司 Temperature increasing and pressurizing foam cement slurry density testing device
CN103676989A (en) * 2013-12-29 2014-03-26 金堆城钼业股份有限公司 Liquid level automatic control system and method for small-sized flotation machine
CN114383985A (en) * 2021-12-24 2022-04-22 鞍钢集团矿业有限公司 Flotation concentrate grade detection method based on multi-parameter feature fusion

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102539280A (en) * 2010-12-10 2012-07-04 中国石油化工股份有限公司 Temperature increasing and pressurizing foam cement slurry density testing device
CN102539280B (en) * 2010-12-10 2013-11-13 中国石油化工股份有限公司 Temperature increasing and pressurizing foam cement slurry density testing device
CN103676989A (en) * 2013-12-29 2014-03-26 金堆城钼业股份有限公司 Liquid level automatic control system and method for small-sized flotation machine
CN114383985A (en) * 2021-12-24 2022-04-22 鞍钢集团矿业有限公司 Flotation concentrate grade detection method based on multi-parameter feature fusion
CN114383985B (en) * 2021-12-24 2023-09-15 鞍钢集团矿业有限公司 Flotation concentrate grade detection method based on multi-parameter feature fusion

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C53 Correction of patent for invention or patent application
CB03 Change of inventor or designer information

Inventor after: Ma Liancheng

Inventor after: Xu Honggang

Inventor after: Sun Changsheng

Inventor after: Bai Yuansheng

Inventor before: Shang Hongwei

Inventor before: Nie Jialong

Inventor before: Zhang Feng

Inventor before: Teng Yong

COR Change of bibliographic data

Free format text: CORRECT: INVENTOR; FROM: SHANG HONGWEI NIE JIALONG ZHANG FENG TENG YONG TO: MA LIANCHENG XU HONGGANG SUN ZHANGSHENG BAI YUANSHENG

C56 Change in the name or address of the patentee
CP01 Change in the name or title of a patent holder

Address after: 114001 Anshan District, Liaoning, No. 219 Road, No. 39, Tiedong

Patentee after: Anshan Iron and Steel Group Mining Co., Ltd.

Address before: 114001 Anshan District, Liaoning, No. 219 Road, No. 39, Tiedong

Patentee before: Anshan Iron & Steel Group Mining Co., Ltd.

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20090304