CN1060689C - Sorting and processing of ferro-phosphorus, and method of application - Google Patents
Sorting and processing of ferro-phosphorus, and method of application Download PDFInfo
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- CN1060689C CN1060689C CN97119884A CN97119884A CN1060689C CN 1060689 C CN1060689 C CN 1060689C CN 97119884 A CN97119884 A CN 97119884A CN 97119884 A CN97119884 A CN 97119884A CN 1060689 C CN1060689 C CN 1060689C
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Abstract
The present invention discloses a ferro-phosphorus sorting, processing and applying method. A grid is arranged at the upper part of a bunker, a cylindrical sieve adopted by the present invention is divided into five sections, and then a finished product 3 or 2 is fed into a fine-material crusher so as to get further processed and crushed; the grain size of the outlet of the fine-material crusher is controlled to be below 10 millimeters, and then finished product 3 or 2 is fed back into an inlet chute of the cylindrical sieve by a bucket type elevator for being sieved once again; a finished product 4 or 5 is fed into an inlet hopper of a pulverizer by a fine-material bucket type elevator, a feeder uniformly feeds materials into the pendulous pulverizer, and finely-pulverized powder that is smaller than 80 meshes is blown toward a big cyclone collector via an analyzer after analyzed by the analyzer. The products sorted in the present invention has wide application to industrial production, particularly metallurgical production.
Description
The present invention relates to the technical field that ferrophosphorus is produced, particularly relate to the fragmentation processing of ferrophosphorus.
Ferrophosphorus is a main additive during iron and steel is produced, and in industries such as building, metallurgy, auto parts machinery, sanitary apparatus extensive use is arranged all simultaneously, and its purposes difference is also inequality to the requirement of ferrophosphorus granularity.But,, be difficult for being processed into the product of different brackets because ferrophosphorus is hard and crisp; And the ferrophosphorus autoignition temperature is 260 ℃, as fine grinding because spontaneous combustion then can take place in hot-spot, easy firing more when heating up, even blast especially.This is a unresolved always difficult problem in the ferrophosphorus processing.
The objective of the invention is at the deficiencies in the prior art part, provide a kind of technology reasonable, safe and reliable, can process different brackets, especially can produce the processing method of granularity less than 80 order finished products.
Purpose of the present invention can be achieved by adopting following process:
1, bulk ferrophosphorus engineering dump truck, the direct feed bin of transporting to batcher from phosphorus stove factory building;
2, feed bin top is provided with a grid, and the grid hole dimension is 200 * 200 millimeters, granularity greater than 200 millimeters ferrophosphorus piece by manually knocking coarse crushing;
3, granularity falls into feed bin less than 200 millimeters ferrophosphorus piece, and is evenly reinforced to the coarse fodder disintegrating machine by batcher, and particle size after cracking is controlled at below 75 millimeters (3 ");
4, coarse fodder disintegrating machine discharging opening granularity is delivered to drum sieve inlet chute less than the material piece of 75 millimeters (3 ") with belt conveyer, enters drum sieve by gravity;
5, drum sieve is divided into five sections, and first section is the finished product V less than 3 millimeters (1/8 "); Second section is less than 9.5 millimeters (3/8 "), greater than the finished product IV of 3 millimeters (1/8 "); The 3rd section is less than 50 millimeters (2 "), greater than the finished product III of 9.5 millimeters (3/8 "); The 4th section is less than 75 millimeters (3 "), greater than the finished product II of 50 millimeters (2 "); The 5th section is greater than the returning charge (quantity seldom) of 75 millimeters (3 "), sends the batcher feed bin back to handcart;
6, can as required finished product III or II be sent into the fines disintegrating machine, be broken for the finished product of size between 9.5 millimeters of 3 millimeters (1/8 ")----(3/8 ") with further processing, the outlet granularity of fines disintegrating machine is controlled at below 10 millimeters, send drum sieve inlet chute, screening once more back to bucket elevator;
7, can as required finished product IV or finished product V be delivered to flour mill inlet hopper with the fines bucket elevator less than 80 purpose finished product VI, evenly reinforced to the pendulum-type flour mill with batcher, levigate powder is machine by analysis, falls greater than 80 purpose materials, continues levigate; Less than 80 purpose fineves by analysis machine blow to the willy-willy gatherer, can pack.
8, less than the finished product I of 150 millimeters (6 "), on 150 * 150 millimeters grid, can pack as required by hand breaking.
The varigrained ferrophosphorus product of the present invention's processing can be widely used in oil exploitation, building, auto parts machinery, sanitary apparatus, especially as a kind of important additives, can fully satisfy and smelt the multiple needs of producing.For example:
1. finished product I: granularity is not more than 150 millimeters (6 "), is used for blast furnace, big iron-smelting furnace or electric furnace;
2. finished product II: granularity is 50-75 millimeter (2-3 "), is used for little iron-smelting furnace, electric arc furnaces and electric induction furnace;
3. finished product III: granularity is 9.5-50 millimeter (3/8-2 "), is used for little iron-smelting furnace, electric arc furnaces and electric induction furnace;
4. finished product IV: granularity is 3-9.5 millimeter (1/8-3/8 "), is used for electric induction furnace, duplex electric furnace or big ladle;
5. finished product V: granularity is used for little ladle less than 3 millimeters (0-1/8 ");
6. finished product VI: granularity has special special purpose less than 80 orders (0.175 millimeter), as is used for oil well, oil field etc.
Compared with prior art, the present invention has following outstanding advantage:
Ferrophosphorus is carried out classification processing, can utilize phosphate rock resource fully, avoid the waste of natural resources.Ferrophosphorus has extensive use, and it is carried out strict classification processing, helps developing the purposes of ferrophosphorus in different field.The present invention adopts the pendulum-type flour mill, carries out grinding under negative pressure, can not pollute air, helps environmental protection.The present invention to less than 80 purpose fineves by analysis machine blow to the willy-willy gatherer, be skillfully constructed the spontaneous combustion that hot-spot causes when successfully having solved the ferrophosphorus fine grinding even the technical barrier of blast.
Fig. 1 is a process flow diagram of the present invention.
The present invention is the concrete condition according to ferrophosphorus, adopts flow process 1 shown in the drawings, flow process 2 or flow process 3 to process respectively.Below in conjunction with accompanying drawing and embodiment shown in the drawings, content of the present invention is done concrete description, but content of the present invention is not limited to shown in the accompanying drawing.
Embodiment:
With iron-holder 68%, phosphorus content 23-29% contains minor amount of silicon, magnesium, sulphur, table density 6t/m
3, bulk density 3-4t/m
3Fosfosiderite adopt following technology to do classification processing to handle:
1, bulk ferrophosphorus engineering dump truck, the direct feed bin of transporting to batcher from phosphorus stove factory building;
2, feed bin top is provided with a grid, and the grid hole dimension is 200 * 200 millimeters, granularity greater than 200 millimeters ferrophosphorus piece by manually knocking coarse crushing;
3, granularity falls into feed bin less than 200 millimeters ferrophosphorus piece, and is evenly reinforced to the coarse fodder disintegrating machine by batcher, and particle size after cracking is controlled at below 75 millimeters (3 ");
4, coarse fodder disintegrating machine discharging opening granularity is delivered to drum sieve inlet chute less than the material piece of 75 millimeters (3 ") with belt conveyer, enters drum sieve by gravity;
5, drum sieve is divided into five sections, and first section is the finished product V less than 3 millimeters (1/8 "); Second section is less than 9.5 millimeters (3/8 "), greater than the finished product IV of 3 millimeters (1/8 "); The 3rd section is less than 50 millimeters (2 "), greater than the finished product III of 9.5 millimeters (3/8 "); The 4th section is less than 75 millimeters (3 "), greater than the finished product II of 50 millimeters (2 "); The 5th section is greater than the returning charge (quantity seldom) of 75 millimeters (3 "), sends the batcher feed bin back to handcart;
6, can as required finished product III or II be sent into the fines disintegrating machine, be broken for the finished product of size between 9.5 millimeters of 3 millimeters (1/8 ")----(3/8 ") with further processing, the outlet granularity of fines disintegrating machine is controlled at below 10 millimeters, send drum sieve inlet chute, screening once more back to bucket elevator;
7, can as required finished product IV or finished product V be delivered to flour mill inlet hopper with the fines bucket elevator less than 80 purpose finished product VI, evenly reinforced to the pendulum-type flour mill with batcher, levigate powder is machine by analysis, falls greater than 80 purpose materials, continues levigate; Less than 80 purpose fineves by analysis machine blow to the willy-willy gatherer, can pack;
8, less than the finished product I of 150 millimeters (6 "), on 150 * 150 millimeters grid, can pack as required by hand breaking.
In the above-mentioned operation, the maximum appearance and size of feed size is controlled to be 210mm when slightly broken, and the maximum appearance and size of feed size is controlled to be 100mm when carefully broken, and the maximum appearance and size of the feed size during the grinding ferrophosphorus is controlled to be 15mm.
Claims (2)
1, a kind of classification processing method of ferrophosphorus is characterized in that adopting following processing step:
1. bulk ferrophosphorus engineering dump truck is directly transported to the feed bin of batcher from phosphorus stove factory building;
2. feed bin top is provided with a grid, and the grid hole dimension is 200 * 200 millimeters, granularity greater than 200 millimeters ferrophosphorus piece by manually knocking coarse crushing;
3. granularity falls into feed bin less than 200 millimeters ferrophosphorus piece, and is evenly reinforced to the coarse fodder disintegrating machine by batcher, and particle size after cracking is controlled at below 75 millimeters (3 ");
4. coarse fodder disintegrating machine discharging opening granularity is delivered to drum sieve inlet chute less than the material piece of 75 millimeters (3 ") with belt conveyer, enters drum sieve by gravity;
5. drum sieve is divided into five sections, and first section is the finished product V less than 3 millimeters (1/8 "); Second section is less than 9.5 millimeters (3/8 "), and greater than the finished product IV of 3 millimeters (1/8 "), the 3rd section is less than 50 millimeters (2 "), greater than the finished product III of 9.5 millimeters (3/8 "); The 4th section is less than 75 millimeters (3 "), greater than the finished product II of 50 millimeters (2 "); The 5th section is greater than the returning charge (quantity seldom) of 75 millimeters (3 "), sends the batcher feed bin back to handcart;
6. can as required finished product III or II be sent into the fines disintegrating machine, be broken for the finished product of size between 9.5 millimeters of 3 millimeters (1/8 ")----(3/8 ") with further processing, the outlet granularity of fines disintegrating machine is controlled at below 10 millimeters, send drum sieve inlet chute, screening once more back to bucket elevator;
7. can as required finished product IV or finished product V be delivered to flour mill inlet hopper with the fines bucket elevator less than 80 purpose finished product VI, evenly reinforced to the pendulum-type flour mill with batcher, levigate powder is machine by analysis, falls greater than 80 purpose materials, continues levigate; Less than 80 purpose fineves by analysis machine blow to the willy-willy gatherer, can pack.
8. less than the finished product I of 150 millimeters (6 "), on 150 * 150 millimeters grid, can pack as required by hand breaking.
2, processing method according to claim 1, the maximum appearance and size of feed size is controlled to be 210mm when it is characterized in that slightly breaking, the maximum appearance and size of feed size is controlled to be 100mm during thin breaking, and the maximum appearance and size of feed size is controlled to be 15mm during the grinding ferrophosphorus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97119884A CN1060689C (en) | 1997-12-31 | 1997-12-31 | Sorting and processing of ferro-phosphorus, and method of application |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97119884A CN1060689C (en) | 1997-12-31 | 1997-12-31 | Sorting and processing of ferro-phosphorus, and method of application |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1192386A CN1192386A (en) | 1998-09-09 |
| CN1060689C true CN1060689C (en) | 2001-01-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN97119884A Expired - Fee Related CN1060689C (en) | 1997-12-31 | 1997-12-31 | Sorting and processing of ferro-phosphorus, and method of application |
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| CN (1) | CN1060689C (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103157543A (en) * | 2011-12-13 | 2013-06-19 | 洛阳宇航重工机械有限公司 | Alumina crust block crushing process and production line thereof |
| CN103397126B (en) * | 2013-08-01 | 2016-01-20 | 河南豫中铁合金有限公司 | A kind of ferrophosphorus and preparation method thereof |
| CN106733669B (en) * | 2017-01-16 | 2019-04-19 | 贵州开磷有限责任公司 | A kind of dry mine sand processing technology and device |
| CN108325714A (en) * | 2018-03-30 | 2018-07-27 | 宁夏天元锰业有限公司 | A kind of breaking method of metal manganese ingot |
| CN114032439B (en) * | 2021-11-23 | 2022-04-01 | 河南豫中新材料有限公司 | Material and refining method for refining ferrophosphorus |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1149631A (en) * | 1995-11-03 | 1997-05-14 | 朱培基 | Method for preparing ferro-phosphorus from corundum slag |
| CN1154418A (en) * | 1996-01-11 | 1997-07-16 | 牟品文 | Process for producing ferro-phosphorus |
-
1997
- 1997-12-31 CN CN97119884A patent/CN1060689C/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1149631A (en) * | 1995-11-03 | 1997-05-14 | 朱培基 | Method for preparing ferro-phosphorus from corundum slag |
| CN1154418A (en) * | 1996-01-11 | 1997-07-16 | 牟品文 | Process for producing ferro-phosphorus |
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| Publication number | Publication date |
|---|---|
| CN1192386A (en) | 1998-09-09 |
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