CN1532012A - Method of pelletizing high temperature alloy liquid - Google Patents

Method of pelletizing high temperature alloy liquid Download PDF

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Publication number
CN1532012A
CN1532012A CNA031175252A CN03117525A CN1532012A CN 1532012 A CN1532012 A CN 1532012A CN A031175252 A CNA031175252 A CN A031175252A CN 03117525 A CN03117525 A CN 03117525A CN 1532012 A CN1532012 A CN 1532012A
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CN
China
Prior art keywords
alloy liquid
high temperature
temperature alloy
granulation
turntable
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
CNA031175252A
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Chinese (zh)
Inventor
李昆东
乔佩
周秋林
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.)
KUNYANG PHOSPHORUS FERTILIZER PLANT YUNAN PROV
Original Assignee
KUNYANG PHOSPHORUS FERTILIZER PLANT YUNAN PROV
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Publication date
Application filed by KUNYANG PHOSPHORUS FERTILIZER PLANT YUNAN PROV filed Critical KUNYANG PHOSPHORUS FERTILIZER PLANT YUNAN PROV
Priority to CNA031175252A priority Critical patent/CN1532012A/en
Publication of CN1532012A publication Critical patent/CN1532012A/en
Pending legal-status Critical Current

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Abstract

The present invention relates to a kind of pelletizing high temperature alloy liquid. The production process includes pelletizing in rotary table as one a rotation part and water quenching the pellets. The production process is simple and has alloy temperature of 200-2000 deg.c, stable alloy pellet size of 0.5-5 mm, low investment in equipment, low power consumption and low cost.

Description

High temperature alloy liquid granulating method
Technical field
The present invention relates to a kind of high temperature alloy liquid granulating method, particularly in air, be difficult for oxidation, when shrend, be difficult for the granulating method of the alloy liquid of chemical reaction.
Technical background
At present; the method of high temperature alloy liquid granulation generally is to utilize heating means that the granulation hopper is carried out outer insulation; make high temperature alloy liquid carry out granulation, then metallic particles is carried out shrend after by water leg cooling and air cold shock and obtain product by the granulation hopper.Being incubated for the granulation hopper needs consumes energy; Insulation needs to increase corresponding facility, with water leg the total cost of entire equipment is increased, and causes production cost to rise; Granulation speed in the granulation hopper is relatively also slower.
Summary of the invention
Technical problem to be solved by this invention provides a kind ofly carries out the method for granulation to high temperature alloy liquid, and it can improve granulation speed, and can cut down the consumption of energy and production cost.
Solving the scheme that technical problem of the present invention adopts is: alloy liquid is dripped granulation to the rotary turntable, and turntable places watch-quench tank, and alloying pellet drops down onto watch-quench tank again, directly cool off product.
Technical scheme of the present invention also comprises following proposal: the temperature that liquid high temperature alloy oozes from the granulation hopper outlet is 200 ℃~2000 ℃, leave involute formula shallow slot on the rotary turntable, groove width 2mm~10mm, groove depth 0.5mm~2mm, its rotary speed is 50 rev/mins~300 rev/mins; Alloy liquid is to drip to rotary turntable by the rectangle outlet of middle hopper, and the bore of outlet is wide to be 100 * 4mm~100 * 10mm.
Because alloy granulation of the present invention is to carry out on rotating movement parts, can simplify the structure of original granulation hopper greatly, does not need hopper is incubated in granulation, can save energy, and granulation is speeded up; In the shrend process,, do not need conventional water leg and cold shock air to cool off, so production cost is lower because alloying pellet directly falls into watch-quench tank.
Description of drawings
Fig. 1 is a facility schematic diagram of the present invention;
Fig. 2 is the turntable schematic diagram of facility of the present invention;
Each label is represented successively among the figure: granulation hopper 1, buncher 2, axle 3, turntable 4, cooling water pipe 5, watch-quench tank 6, water inlet 7, feed opening 8, pan tank 9, involute groove 10.
The specific embodiment
See Fig. 1; pour alloy liquid into granulation hopper 1; alloy liquid drops on the rotary turntable 4 from the rectangle outlet; temperature during drippage is 1000 ℃; rotary turntable 4 is circular; have involute groove 10 on it; groove width 2mm~10mm; groove depth 0.5mm~2mm; rotary turntable 4 drives with 75 rev/mins~200 rev/mins speed rotations through axle 3 under the control of buncher 2; alloy is being shaped by involute groove 10 granulations on it on the rotary turntable 4; the size of alloying pellet is by the speed of rotary turntable 4; the size of involute shallow slot; the size control of the height of granulation hopper 1 and the outlet of granulation hopper rectangle; alloying pellet falls into watch-quench tank 6; obtain product by feed opening 8 to pan tank 9 after the cooling water shrend, concrete parameter is face table 1 and table 2 as follows.
Table 1 double centner alloy granule chemical industry condition
Table 2 size distribution

Claims (4)

1, a kind of high temperature alloy liquid granulating method is characterized in that processing step is as follows, and alloy liquid is dripped granulation to the rotary turntable, and turntable places watch-quench tank, and alloying pellet drops down onto watch-quench tank again, directly cool off product.
2, by the described high temperature alloy liquid of claim 1 granulating method, the temperature that it is characterized in that high temperature alloy liquid is at 200 ℃~2000 ℃.
3, by the described high temperature alloy liquid of claim 2 granulating method, it is characterized in that having on the rotary turntable involute formula shallow slot, groove width 2mm~10mm, groove depth 0.5mm~2mm, its rotary speed is 50 rev/mins~300 rev/mins.
4, by the described high temperature alloy liquid of claim 2 granulating method, it is characterized in that alloy liquid is to drip to rotary turntable by the rectangle outlet of middle hopper, the bore of outlet is wide to be 100 * 4mm~100 * 10mm.
CNA031175252A 2003-03-20 2003-03-20 Method of pelletizing high temperature alloy liquid Pending CN1532012A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA031175252A CN1532012A (en) 2003-03-20 2003-03-20 Method of pelletizing high temperature alloy liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA031175252A CN1532012A (en) 2003-03-20 2003-03-20 Method of pelletizing high temperature alloy liquid

Publications (1)

Publication Number Publication Date
CN1532012A true CN1532012A (en) 2004-09-29

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Family Applications (1)

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CNA031175252A Pending CN1532012A (en) 2003-03-20 2003-03-20 Method of pelletizing high temperature alloy liquid

Country Status (1)

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CN (1) CN1532012A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102218539A (en) * 2011-05-26 2011-10-19 江苏科技大学 Method for preparing ultrafine silver powder
CN102328092A (en) * 2011-08-04 2012-01-25 东北大学 Ferroalloy granulating device and granulating method
CN102974781A (en) * 2012-12-08 2013-03-20 太原理工大学 Method for manganese alloy continuous casting and moulding granulating
CN103088254A (en) * 2011-10-27 2013-05-08 上海中河金属加工有限公司 Nickel steel bean production method
CN105612016A (en) * 2013-09-05 2016-05-25 尤万控股股份公司 Granulation of molten material
CN106102969A (en) * 2014-04-03 2016-11-09 尤万控股股份公司 The pelletize of melted ferrochrome
CN106694896A (en) * 2016-12-30 2017-05-24 西安交通大学青岛研究院 Atomization preparation device for TiAl powder
CN106735278A (en) * 2016-12-30 2017-05-31 西安交通大学青岛研究院 A kind of atomization preparing apparatus of TiAl powder
CN110125426A (en) * 2019-05-09 2019-08-16 辽宁科技大学 A kind of ferroalloy granulating device and method

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102218539A (en) * 2011-05-26 2011-10-19 江苏科技大学 Method for preparing ultrafine silver powder
CN102328092A (en) * 2011-08-04 2012-01-25 东北大学 Ferroalloy granulating device and granulating method
CN102328092B (en) * 2011-08-04 2014-06-04 东北大学 Ferroalloy granulating device and granulating method
CN103088254A (en) * 2011-10-27 2013-05-08 上海中河金属加工有限公司 Nickel steel bean production method
CN102974781A (en) * 2012-12-08 2013-03-20 太原理工大学 Method for manganese alloy continuous casting and moulding granulating
CN102974781B (en) * 2012-12-08 2014-05-14 太原理工大学 Method for manganese alloy continuous casting and moulding granulating
CN105612016A (en) * 2013-09-05 2016-05-25 尤万控股股份公司 Granulation of molten material
CN105612016B (en) * 2013-09-05 2018-03-27 尤万控股股份公司 The granulation of melted material
US10618112B2 (en) 2013-09-05 2020-04-14 Uvan Holding Ab Granulation of molten material
CN106102969A (en) * 2014-04-03 2016-11-09 尤万控股股份公司 The pelletize of melted ferrochrome
CN106102969B (en) * 2014-04-03 2018-09-18 尤万控股股份公司 Melt the granulation of ferrochrome
CN106694896A (en) * 2016-12-30 2017-05-24 西安交通大学青岛研究院 Atomization preparation device for TiAl powder
CN106735278A (en) * 2016-12-30 2017-05-31 西安交通大学青岛研究院 A kind of atomization preparing apparatus of TiAl powder
CN106735278B (en) * 2016-12-30 2018-09-18 西安交通大学青岛研究院 A kind of atomization preparing apparatus of TiAl powder
CN110125426A (en) * 2019-05-09 2019-08-16 辽宁科技大学 A kind of ferroalloy granulating device and method

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