CN203033769U - Phosphate-pulp producing and breaking system - Google Patents
Phosphate-pulp producing and breaking system Download PDFInfo
- Publication number
- CN203033769U CN203033769U CN 201320040972 CN201320040972U CN203033769U CN 203033769 U CN203033769 U CN 203033769U CN 201320040972 CN201320040972 CN 201320040972 CN 201320040972 U CN201320040972 U CN 201320040972U CN 203033769 U CN203033769 U CN 203033769U
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- China
- Prior art keywords
- cone crusher
- crushing cone
- ball grinder
- wet ball
- phosphate
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Abstract
The utility model discloses a phosphate-pulp producing and breaking system. The phosphate-pulp producing and breaking system comprises a coarse crushing cone crusher, a fine crushing cone crusher, a screening device, a wet ball grinder, a belt conveying device and a water supply pipe and is characterized in that the fine crushing cone crusher, the screening device and the wet ball grinder are arranged at the rear of the coarse crushing cone crusher in sequence, the belt conveying device is arranged between the screening device and the fine crushing cone crusher, and the water supply pipe is arranged on the wet ball grinder. By adopting the coarse crushing cone crusher and the fine crushing cone crusher, the crushing efficiency is high, the outlet particle size is stable, and the crushing requirement is met. The measurement and the calculation show that the wet ball grinder has the grinding efficiency of 90%, only 0.41kg of steel balls in each ton of raw ore is consumed, 408 tons of steel balls and millions of capital can be saved annually if 1.2 million of phosphorite is ground annually, the production cost of a product is reduced, the economic benefit is improved.
Description
Technical field
The utility model relates to a kind of phosphoric acid ore pulp and produces the crushing system device.
Background technology
In the production process of phosphoric acid product, the fragmentation of Rock Phosphate (72Min BPL) and ore grinding are important procedures.In the prior production process, " jaw crusher " adopted in coarse crushing more, adopt in small, broken bits " the hammer counterattack is broken " more, this mode crushing efficiency is low, outlet granularity instability, can not guarantee into the mill requirement, causes " wet-type ball mill " grinding efficiency low (65%), and the infringement to grinding machine is big, therefore the ball consumption, is necessary to make improvements up to the 0.75kg/t raw ore.
Summary of the invention
The purpose of this utility model will provide a kind of crushing efficiency height, outlet particle size stable exactly, and guaranteed to go into to grind requirement, make ball mill grinding efficiency height, and the phosphoric acid ore pulp that the infringement to grinding machine is little, the ball consumption is low is produced the crushing system device, it had both avoided the waste of raw ore, had improved the utilization ratio of raw ore again.
The purpose of this utility model is that the following technical scheme that adopts realizes: a kind of phosphoric acid ore pulp is produced the crushing system device, comprise coarse crushing cone crusher, cone crusher in small, broken bits, screening plant, wet-type ball mill, feedback belt dressing, water-supply pipe, it is characterized in that: be arranged in order behind the coarse crushing cone crusher cone crusher in small, broken bits, screening plant and wet-type ball mill are set, and be provided with between screening plant and the cone crusher in small, broken bits and feed back belt dressing and wet-type ball mill is provided with water-supply pipe.
Advantage of the present utility model and beneficial effect are: this technology is paid attention to " heavily broken light mill " principle, after thick, fine crushing used instead " cone crusher ", crushing efficiency height, outlet particle size stable, and guaranteed to go into to grind requirement, through measuring and calculating, " wet-type ball mill " grinding efficiency reaches 90%, the ball consumption is down to the 0.41kg/t raw ore, with 1,200,000 tons of/year flotation of phosphate rock industrial scales, only " the ball consumption descends " annual 408 tons of steel balls, saving money of saving is through millions of units, reduce production cost of products, improved economic benefit.
Description of drawings
Concrete structure of the present utility model is provided by following embodiment and accompanying drawing thereof.
Fig. 1 is structural representation of the present utility model.
Fig. 1 double as Figure of abstract.
Among the figure 1, the coarse crushing cone crusher, 2, cone crusher in small, broken bits, 3, screening plant, 4, wet-type ball mill, 5, feed back belt dressing, 6, water-supply pipe.
Embodiment
By the following examples, the utility model is described in more detail, but as long as in main idea scope of the present utility model, is not limited in following examples.
A kind of phosphoric acid ore pulp is as shown in Figure 1 produced the crushing system device, comprise coarse crushing cone crusher 1, cone crusher in small, broken bits 2, screening plant 3, wet-type ball mill 4, feed back belt dressing 5, water-supply pipe 6, it is characterized in that: be arranged in order behind the coarse crushing cone crusher 1 cone crusher 2 in small, broken bits, screening plant 3 and wet-type ball mill 4 are set, and be provided with between screening plant 3 and the cone crusher in small, broken bits 2 and feed back belt dressing 5 and wet-type ball mill 4 is provided with water-supply pipe 6.
Principle of work of the present utility model is: above-described embodiment only is one of preferred embodiment of the present utility model; be not to limit protection domain of the present utility model with this; so: all equivalences of doing according to shape of the present utility model, structure, principle change, and all should be covered by within the protection domain of the present utility model.
Claims (1)
1. a phosphoric acid ore pulp is produced the crushing system device, comprise coarse crushing cone crusher (1), cone crusher in small, broken bits (2), screening plant (3), wet-type ball mill (4), feed back belt dressing (5), water-supply pipe (6), it is characterized in that: be arranged in order behind the coarse crushing cone crusher (1) cone crusher in small, broken bits (2), screening plant (3) and wet-type ball mill (4) are set, and be provided with between screening plant (3) and the cone crusher in small, broken bits (2) and feed back belt dressing (5) and wet-type ball mill (4) is provided with water-supply pipe (6).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201320040972 CN203033769U (en) | 2013-01-15 | 2013-01-15 | Phosphate-pulp producing and breaking system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201320040972 CN203033769U (en) | 2013-01-15 | 2013-01-15 | Phosphate-pulp producing and breaking system |
Publications (1)
Publication Number | Publication Date |
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CN203033769U true CN203033769U (en) | 2013-07-03 |
Family
ID=48685906
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201320040972 Expired - Lifetime CN203033769U (en) | 2013-01-15 | 2013-01-15 | Phosphate-pulp producing and breaking system |
Country Status (1)
Country | Link |
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CN (1) | CN203033769U (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103418479A (en) * | 2013-07-31 | 2013-12-04 | 周其锋 | Calcite crushing process |
CN103418481A (en) * | 2013-07-31 | 2013-12-04 | 安徽省司尔特肥业股份有限公司 | Equipment for crushing raw material phosphorus ore |
CN103418480A (en) * | 2013-07-31 | 2013-12-04 | 周其锋 | Calcite powder production process |
CN105129754A (en) * | 2015-07-08 | 2015-12-09 | 安徽新中远化工科技有限公司 | Ore supply system used for preparation of phosphoric acid from fine ores |
CN105709918A (en) * | 2015-12-29 | 2016-06-29 | 荆门新洋丰中磷肥业有限公司 | Production process of high-concentration floating separation of phosphorite |
-
2013
- 2013-01-15 CN CN 201320040972 patent/CN203033769U/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103418479A (en) * | 2013-07-31 | 2013-12-04 | 周其锋 | Calcite crushing process |
CN103418481A (en) * | 2013-07-31 | 2013-12-04 | 安徽省司尔特肥业股份有限公司 | Equipment for crushing raw material phosphorus ore |
CN103418480A (en) * | 2013-07-31 | 2013-12-04 | 周其锋 | Calcite powder production process |
CN105129754A (en) * | 2015-07-08 | 2015-12-09 | 安徽新中远化工科技有限公司 | Ore supply system used for preparation of phosphoric acid from fine ores |
CN105709918A (en) * | 2015-12-29 | 2016-06-29 | 荆门新洋丰中磷肥业有限公司 | Production process of high-concentration floating separation of phosphorite |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term |
Granted publication date: 20130703 |
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CX01 | Expiry of patent term |