CN104307814A - On-line clearing method of dilute acid pipe scales in phosphate ore magnesium-removing and ore-dressing production - Google Patents

On-line clearing method of dilute acid pipe scales in phosphate ore magnesium-removing and ore-dressing production Download PDF

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Publication number
CN104307814A
CN104307814A CN201410434644.1A CN201410434644A CN104307814A CN 104307814 A CN104307814 A CN 104307814A CN 201410434644 A CN201410434644 A CN 201410434644A CN 104307814 A CN104307814 A CN 104307814A
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CN
China
Prior art keywords
ore
magnesium
dilute acid
diluted acid
line clearing
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
CN201410434644.1A
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Chinese (zh)
Inventor
赵锋先
廖世宏
刘维
史进平
张生鹏
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GANSU WENGFU CHEMICAL CO Ltd
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GANSU WENGFU CHEMICAL 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 GANSU WENGFU CHEMICAL CO Ltd filed Critical GANSU WENGFU CHEMICAL CO Ltd
Priority to CN201410434644.1A priority Critical patent/CN104307814A/en
Publication of CN104307814A publication Critical patent/CN104307814A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00Cleaning hollow articles by methods or apparatus specially adapted thereto 
    • B08B9/02Cleaning pipes or tubes or systems of pipes or tubes
    • B08B9/027Cleaning the internal surfaces; Removal of blockages
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/04Cleaning involving contact with liquid
    • B08B3/08Cleaning involving contact with liquid the liquid having chemical or dissolving effect
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B2203/00Details of cleaning machines or methods involving the use or presence of liquid or steam
    • B08B2203/007Heating the liquid

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention aims to provide an on-line clearing method of dilute acid pipe scales in phosphate ore magnesium-removing and ore-dressing production and solves the problem in the prior art that the manual cleaning of a dilute acid pipe is time-consuming and labor-consuming in the phosphate ore magnesium-removing and ore-dressing production. The on-line clearing method comprises the following steps: configuring cleaning liquid composed of sulfuric acid and water in a dilute acid configuration tank, wherein the volume ratio of the sulfuric acid to the water is 1:(5-20); then introducing low-pressure steam in the dilute acid configuration tank to heat; conveying the heated cleaning liquid into a dilute acid pipe by using a conveying pump to clean under the situation of no parking. The on-line clearing method has the benefits that the on-line clearing of the scales is realized, no pipe needs to be disassembled, no investment is required, the maneuverability is realized, and no extra equipment needs to be arranged; the scale removal is more obvious, the cleaning is required once a month, and time and labor are saved.

Description

The online sweep-out method of diluted acid pipeline scale in a kind of removal of magnesium from phosphorous ore mineral processing production
Technical field
The present invention relates to beneficiated phosphate ore field, be specifically related to the online sweep-out method of diluted acid pipeline scale in a kind of removal of magnesium from phosphorous ore mineral processing production.
Background technology
Beneficiated phosphate ore demagging is one of main beneficiation method of modern phosphorus ammonium production industry.Beneficiation method adopts usually " reverse flotation ", and method carries out ore dressing, ore dressing uses gypsum stack backwater dilute sulphuric acid as floatation regulator ore dressing, and containing a large amount of foreign ion such as a large amount of Ca, Mg, Fe, Al, Si etc. in gypsum stack backwater, generate complicated double salt with sulfuric acid reaction and be attached to duct wall, cause serious scale in pipeline, cause adjusting agent changes in flow rate, affect flotation effect.In order to remove fouling, traditional way is that pipeline is dismantled off-line, manually removes, obvious this method time and effort consuming.
Summary of the invention
The object of this invention is to provide the online sweep-out method of diluted acid pipeline scale in a kind of removal of magnesium from phosphorous ore mineral processing production, diluted acid pipeline manual cleaning in removal of magnesium from phosphorous ore mineral processing production be time-consuming to solve in prior art, the problem of effort.
For this reason, the present invention adopts following technical scheme: the online sweep-out method of diluted acid pipeline scale in a kind of removal of magnesium from phosphorous ore mineral processing production, comprises the steps:
A, in diluted acid configured slot, configure the cleaning fluid be made up of sulfuric acid, water, its sulfuric acid: the volume ratio of water is 1:5 ~ 20;
Low-pressure steam heating is passed in B, diluted acid configured slot in step;
C, when not stopping, step B gained cleaning fluid delivery pump being sent into diluted acid pipeline and cleans.
Further, the pressure of described step B low pressure steam is 0.3 ~ 0.5Mpa, and heating-up temperature is 40 ~ 60 DEG C.
Further, in described step C, scavenging period is 12 ~ 26h.
The invention has the beneficial effects as follows: realize removing fouling online, need not pipeline be dismantled, without investment, maneuverability, without the need to increasing equipment; Scale removal is comparatively obvious, monthly only need clean once, time saving and energy saving.
Accompanying drawing explanation
Fig. 1 is schematic flow sheet of the present invention.
In figure: 1, diluted acid configured slot, 2, delivery pump, 3, diluted acid pipeline.
Detailed description of the invention
Below in conjunction with embodiment, the present invention is described in further details.
Embodiment 1
An online sweep-out method for diluted acid pipeline scale in removal of magnesium from phosphorous ore mineral processing production, the cleaning fluid that configuration is 98% by mass fraction in diluted acid configured slot 1 sulfuric acid, water form, its sulfuric acid: the volume ratio of water is 1:5; Then in diluted acid configured slot 1, pass into the low-pressure steam heating that pressure is 0.3 Mpa, heating-up temperature is 40 DEG C; When not stopping, the cleaning fluid delivery pump 2 after heating is sent into diluted acid pipeline 3 and cleans, scavenging period is 20 h.
Embodiment 2
An online sweep-out method for diluted acid pipeline scale in removal of magnesium from phosphorous ore mineral processing production, the cleaning fluid that configuration is 98% by mass fraction in diluted acid configured slot 1 sulfuric acid, water form, its sulfuric acid: the volume ratio of water is 1:15; Then in diluted acid configured slot 1, pass into the low-pressure steam heating that pressure is 0.4 Mpa, heating-up temperature is 50 DEG C; When not stopping, the cleaning fluid delivery pump 2 after heating is sent into diluted acid pipeline 3 and cleans, scavenging period is 22 h.
Embodiment 3
An online sweep-out method for diluted acid pipeline scale in removal of magnesium from phosphorous ore mineral processing production, the cleaning fluid that configuration is 98% by mass fraction in diluted acid configured slot 1 sulfuric acid, water form, its sulfuric acid: the volume ratio of water is 1:20; Then in diluted acid configured slot 1, pass into the low-pressure steam heating that pressure is 0.5 Mpa, heating-up temperature is 60 DEG C; When not stopping, the cleaning fluid delivery pump 2 after heating is sent into diluted acid pipeline 3 and cleans, scavenging period is 18 h.
The 800000 tons/year of phosphorus concentrate flotation of ore dressing subsidiary factory of Gansu Gengfu Chemistry Co., Ltd. are produced, and before not adopting this method to clean, diluted acid pipeline flow can only reach 15M 3/ h, after adopting this method to ore-dressing plant diluted acid pipeline, cleaning performance statistics is as shown in Table 1,
Table one
Table one shows, and after using this method, diluted acid pipeline flow reaches original about 2 times, substantially reduces clearance time.

Claims (3)

1. the online sweep-out method of diluted acid pipeline scale in removal of magnesium from phosphorous ore mineral processing production, is characterized in that comprising the steps:
A, in diluted acid configured slot, configure the cleaning fluid be made up of sulfuric acid, water, its sulfuric acid: the volume ratio of water is 1:5 ~ 20;
Low-pressure steam heating is passed in B, diluted acid configured slot in step;
C, when not stopping, step B gained cleaning fluid delivery pump being sent into diluted acid pipeline and cleans.
2. the online sweep-out method of diluted acid pipeline scale in a kind of removal of magnesium from phosphorous ore mineral processing production as claimed in claim 1, is characterized in that: the pressure of described step B low pressure steam is 0.3 ~ 0.5Mpa, and heating-up temperature is 40 ~ 60 DEG C.
3. the online sweep-out method of diluted acid pipeline scale in a kind of removal of magnesium from phosphorous ore mineral processing production as claimed in claim 1, is characterized in that: in described step C, scavenging period is 12 ~ 26 h.
CN201410434644.1A 2014-08-29 2014-08-29 On-line clearing method of dilute acid pipe scales in phosphate ore magnesium-removing and ore-dressing production Pending CN104307814A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410434644.1A CN104307814A (en) 2014-08-29 2014-08-29 On-line clearing method of dilute acid pipe scales in phosphate ore magnesium-removing and ore-dressing production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410434644.1A CN104307814A (en) 2014-08-29 2014-08-29 On-line clearing method of dilute acid pipe scales in phosphate ore magnesium-removing and ore-dressing production

Publications (1)

Publication Number Publication Date
CN104307814A true CN104307814A (en) 2015-01-28

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CN201410434644.1A Pending CN104307814A (en) 2014-08-29 2014-08-29 On-line clearing method of dilute acid pipe scales in phosphate ore magnesium-removing and ore-dressing production

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105234133A (en) * 2015-11-05 2016-01-13 广东溢达纺织有限公司 Cleaning method and system of chemical material device and chemical material device with automatic cleaning function
CN107900000A (en) * 2017-11-09 2018-04-13 山东中烟工业有限责任公司 A kind of cigarette process air-conditioning Air-water Humidifying nozzle quick descaling method
CN113385492A (en) * 2020-06-12 2021-09-14 湖北大峪口化工有限责任公司 Cleaning method for phosphogypsum slag yard water return pipeline

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004321119A (en) * 2003-04-28 2004-11-18 Orion Mach Co Ltd Mechanism for cleaning pipeline of milking apparatus
CN101476128A (en) * 2008-12-24 2009-07-08 瓮福(集团)有限责任公司 Method for descaling phosphoric acid conveying pipeline
CN102808193A (en) * 2012-08-30 2012-12-05 贵州开磷(集团)有限责任公司 Cleaning method of phosphoric acid delivery pipeline
EP2612714A1 (en) * 2010-08-30 2013-07-10 Mitsubishi Heavy Industries Food & Packaging Machinery Co., Ltd. Instrument-cleaning method that uses soaking with nanobubble water
CN103303890A (en) * 2013-07-04 2013-09-18 瓮福(集团)有限责任公司 Online reflux rinsing method for tubular reactor
CN203425679U (en) * 2013-08-30 2014-02-12 晶旺光电(徐州)有限公司 Ammonia gas washing tower facilitating cleaning of internal gas pipelines

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004321119A (en) * 2003-04-28 2004-11-18 Orion Mach Co Ltd Mechanism for cleaning pipeline of milking apparatus
CN101476128A (en) * 2008-12-24 2009-07-08 瓮福(集团)有限责任公司 Method for descaling phosphoric acid conveying pipeline
EP2612714A1 (en) * 2010-08-30 2013-07-10 Mitsubishi Heavy Industries Food & Packaging Machinery Co., Ltd. Instrument-cleaning method that uses soaking with nanobubble water
CN102808193A (en) * 2012-08-30 2012-12-05 贵州开磷(集团)有限责任公司 Cleaning method of phosphoric acid delivery pipeline
CN103303890A (en) * 2013-07-04 2013-09-18 瓮福(集团)有限责任公司 Online reflux rinsing method for tubular reactor
CN203425679U (en) * 2013-08-30 2014-02-12 晶旺光电(徐州)有限公司 Ammonia gas washing tower facilitating cleaning of internal gas pipelines

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105234133A (en) * 2015-11-05 2016-01-13 广东溢达纺织有限公司 Cleaning method and system of chemical material device and chemical material device with automatic cleaning function
CN107900000A (en) * 2017-11-09 2018-04-13 山东中烟工业有限责任公司 A kind of cigarette process air-conditioning Air-water Humidifying nozzle quick descaling method
CN113385492A (en) * 2020-06-12 2021-09-14 湖北大峪口化工有限责任公司 Cleaning method for phosphogypsum slag yard water return pipeline

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Application publication date: 20150128

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