CN208312933U - A kind of wet molybdenum concentrate is dry and miberal powder collection system - Google Patents
A kind of wet molybdenum concentrate is dry and miberal powder collection system Download PDFInfo
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- CN208312933U CN208312933U CN201820830452.6U CN201820830452U CN208312933U CN 208312933 U CN208312933 U CN 208312933U CN 201820830452 U CN201820830452 U CN 201820830452U CN 208312933 U CN208312933 U CN 208312933U
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- molybdenum concentrate
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- 239000000843 powder Substances 0.000 title claims abstract description 27
- ZOKXTWBITQBERF-UHFFFAOYSA-N molybdenum Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 229910052750 molybdenum Inorganic materials 0.000 title claims abstract description 21
- 239000011733 molybdenum Substances 0.000 title claims abstract description 21
- 239000012141 concentrate Substances 0.000 title claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 24
- 238000011068 load Methods 0.000 claims abstract description 16
- 238000002485 combustion reaction Methods 0.000 claims abstract description 12
- 239000000428 dust Substances 0.000 claims abstract description 8
- 239000003345 natural gas Substances 0.000 claims abstract description 7
- 210000003128 Head Anatomy 0.000 claims description 13
- 238000001035 drying Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000001354 calcination Methods 0.000 abstract description 2
- 238000006297 dehydration reaction Methods 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 235000021050 feed intake Nutrition 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- CYRPECJLOQEQDX-UHFFFAOYSA-N oxo(sulfanylidene)molybdenum Chemical group 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Abstract
A kind of wet molybdenum concentrate it is dry and and miberal powder collection system, including three drum driers, the feed inlet of three drum driers is connect with screw(-type) feeder, the feed inlet of screw(-type) feeder is connect with feed bin a, the hot-wind inlet and combustion chamber of three drum drier, the air-vent and air inlet of the combustion chamber are connected separately with air blower and natural gas air inlet pipe road；The discharge port of three drum drier is connected with vibrating screen in turn by pipeline, bucket mentions, feed bin b, storehouse pump and loading head, the material outlet of the loading head connect feed bin c by pipeline；The powder entrance of the feed bin c is connected with bagroom by pipeline, and the dust outlet of the loading head is connected by pipeline with the powder entrance of bagroom.Advantage is: the system can make wet molybdenum concentrate reach dehydration deoiling effect well, crush dough, improve the dispersibility of molybdenum concentrate, improve calcination procedure product index；And the system automation degree is high, saves manpower, improves production efficiency, protects environment.
Description
Technical field
The utility model relates to a kind of wet molybdenum concentrate drying and miberal powder collection systems.
Background technique
The molybdenum concentrate obtained by flotation, although have passed through certain filtering, filters pressing, moisture content therein, kerosene contain
It measures still very high.Traditional deoiling, dewatering technique be concentration-filtering-drying process, with equipment be mostly center drive concentrator,
Outside filtering type drum vacuumfilter and steam helicoid screw dryer, due to the limitation of dewatering process and appointed condition, the molybdenum essence of production
Dormant oil water content is higher, has balling, caking phenomenon after mixing pack, causes roasting process half-cooked, molybdenum oxide sulfur-bearing is exceeded.Tradition
In operating process, feed intake, splicing, charging are manual operation, dust from flying, environmental pollution, and mineral leakage is serious.
Summary of the invention
The technical problem to be solved by the present invention is to provide a kind of wet molybdenum concentrate drying and miberal powder collection system, the systems
Wet molybdenum concentrate can be made to reach dehydration deoiling effect well, crush dough, improve the dispersibility of molybdenum concentrate, calcination procedure is improved and produce
Product index；And the system automation degree is high, saves manpower, improves production efficiency, protects environment.
The utility model is realized in this way:
A kind of wet molybdenum concentrate it is dry and and miberal powder collection system, be characterized in that, including three drum driers, three are dry
The feed inlet of dry machine is connect with screw(-type) feeder, and the feed inlet of screw(-type) feeder is connect with feed bin a, the heat of three drum drier
Wind entrance and combustion chamber, the air-vent and air inlet of the combustion chamber are connected separately with air blower and natural gas air inlet pipe
Road；The discharge port of three drum drier is connected with vibrating screen in turn by pipeline, bucket mentions, feed bin b, storehouse pumps and loading head, institute
The material outlet for stating loading head connects feed bin c by pipeline；The upper end feed bin c is equipped with bagroom, and the powder of bagroom
Material outlet is connected with the powder entrance of feed bin c by pipeline, and the dust outlet of the loading head passes through pipeline and bag collection
The powder entrance of device is connected.
Further, it is equipped with air compressor in storehouse pump steam inlet, air compressor provides power, the material after making drying
Feed bin c is remotely delivered to by pipeline by storehouse pump.
Further, valve is equipped on the pipeline between the powder outlet of bagroom and the powder entrance of feed bin c,
In waiting bin after material sedimentation, opens valve and transfer the material in bagroom to feed bin c.
The beneficial effects of the utility model are:
Wet molybdenum concentrate enters the drying of three drum driers after being heated by screw(-type) feeder, wet molybdenum concentrate can be made to reach good
It is dehydrated deoiling effect, is sent into Vibration Screen sub-material group later, improves the dispersibility of molybdenum concentrate, improves roasting technique technical indicator；
System automation degree is high, it is dry after molybdenum concentrate can by struggle against mention, storehouse pumps the feeding warehouse-of automatic transportation to rotary kiln
Feed bin c saves manpower, makes the equipment integration such as dry molybdenum concentrate de-oiling, screening, transport, is not necessarily to hand haulage's material, reduces
Manpower improves production efficiency, and environmental-friendly, and loss of material rate is low.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
In figure: the combustion chamber 1- feed bin a, 2-, 3- air blower, 4- screw(-type) feeder, tri- drum drier of 5-, 6- vibrating screen, 7-
Bucket mentions, the 8- feed bin storehouse b, 9- pump, 10- air compressor, 11- feed bin c, 12- bagroom, 13- natural gas air inlet pipe road,
14- valve, 15- loading head, 1501- dust outlet, 1502- material outlet.
Specific embodiment
As shown in Figure 1, the wet molybdenum concentrate is dry and conveys efficient joint device, including three drum driers 5, three drum driers
5 feed inlet is connect with screw(-type) feeder 4 by pipeline, and the feed inlet of screw(-type) feeder 4 is connect with feed bin a1 by pipeline, institute
The hot-wind inlet for stating three drum driers 5 is connected with combustion chamber 2 by pipeline, the air-vent and air inlet point of the combustion chamber 2
It is not connected with air blower 3 and natural gas air inlet pipe road 13；Fresh air is conveyed from air blower 3 from air-vent to combustion chamber 2, by day
Right gas air inlet pipeline 13 conveys natural gas to combustion chamber 2 by air inlet, and fresh air mixes combustion with natural gas by a certain percentage
It burns, heat is delivered to screw(-type) feeder 4, heats to material.
The discharge port of three drum driers 5 is connected with vibrating screen 6 in turn by pipeline, bucket mentions 7, feed bin b8, storehouse pumps 9 and gathers materials
The material outlet 1502 of device 15, the loading head 15 connects feed bin c11 by pipeline；The upper end feed bin c11 is equipped with bagroom
12, and the powder outlet of bagroom 12 is connected with the powder entrance 1102 of feed bin c11 by pipeline, the loading head 15
Dust outlet 1501 be connected by pipeline with the powder entrance of bagroom.Go out in the powder of the bagroom 12
Pipeline between mouth and the powder entrance of feed bin c11 is equipped with valve 14
9 air inlets are pumped in storehouse, air compressor 10 is connected by pipeline, power is provided by air compressor 10, after dry
Material loading head 15 9 is delivered to through the material inlet of loading head 15 by pipeline by storehouse pump；Dust is flown upward in loading head 15
(the lesser material of particle) enters bagroom 12 through dust outlet 1501 with air, settles to material in bagroom 12
Afterwards, valve 14 is opened to transfer the material powder of the collection in bagroom 12 to feed bin c11；The biggish material of particle sinks to collection
After glassware 15, the material outlet 1502 through loading head 15 is sent into storehouse c11, and the material in feed bin c11 is sent by discharge port to rotary kiln
It is produced.
Claims (3)
1. a kind of wet molybdenum concentrate drying and miberal powder collection system, it is characterized in that: including three drum driers, the charging of three drum driers
Mouth is connect with screw(-type) feeder, and the feed inlet of screw(-type) feeder is connect with feed bin a, the hot-wind inlet of three drum drier and combustion
It burns room to be connected, the air-vent and air inlet of the combustion chamber are connected separately with air blower and natural gas air inlet pipe road；Described three
The discharge port of drum drier is connected with vibrating screen in turn by pipeline, bucket mentions, feed bin b, storehouse pumps and loading head, the loading head
Material outlet connects feed bin c by pipeline；The upper end feed bin c is equipped with bagroom, and the powder outlet and material of bagroom
The powder entrance of storehouse c is connected by pipeline, and the dust outlet of the loading head is entered by the powder of pipeline and bagroom
Mouth is connected.
2. wet molybdenum concentrate drying according to claim 1 and miberal powder collection system, it is characterized in that: being equipped in storehouse pump steam inlet
Air compressor.
3. wet molybdenum concentrate drying according to claim 1 and miberal powder collection system, it is characterized in that: in the powder of bagroom
Pipeline between material outlet and the powder entrance of feed bin c is equipped with valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820830452.6U CN208312933U (en) | 2018-05-25 | 2018-05-25 | A kind of wet molybdenum concentrate is dry and miberal powder collection system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820830452.6U CN208312933U (en) | 2018-05-25 | 2018-05-25 | A kind of wet molybdenum concentrate is dry and miberal powder collection system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208312933U true CN208312933U (en) | 2019-01-01 |
Family
ID=64715823
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820830452.6U Active CN208312933U (en) | 2018-05-25 | 2018-05-25 | A kind of wet molybdenum concentrate is dry and miberal powder collection system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208312933U (en) |
-
2018
- 2018-05-25 CN CN201820830452.6U patent/CN208312933U/en active Active
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