CN202207551U - Mixed powder material production line - Google Patents

Mixed powder material production line Download PDF

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Publication number
CN202207551U
CN202207551U CN2011202588433U CN201120258843U CN202207551U CN 202207551 U CN202207551 U CN 202207551U CN 2011202588433 U CN2011202588433 U CN 2011202588433U CN 201120258843 U CN201120258843 U CN 201120258843U CN 202207551 U CN202207551 U CN 202207551U
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CN
China
Prior art keywords
production line
mixed powder
outlet
powder material
mixer
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Expired - Lifetime
Application number
CN2011202588433U
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Chinese (zh)
Inventor
徐巍
张国勤
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Shanghai Lianye Agricultural Science & Technology Co Ltd
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Shanghai Lianye Agricultural Science & Technology Co Ltd
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Priority to CN2011202588433U priority Critical patent/CN202207551U/en
Application granted granted Critical
Publication of CN202207551U publication Critical patent/CN202207551U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model provides a mixed powder material production line which is characterized by comprising screening equipment, a weighting silo, a mixing machine, material conveying equipment and a packer connected in sequence, and further comprising crushing equipment, wherein material outlets of the screening equipment and the crushing equipment are positioned above an inlet of the weighting silo; an inlet of the mixing machine is positioned below an outlet of the weighting silo; an inlet of the material conveying equipment is connected with an outlet of the mixing machine; and an outlet of the material conveying equipment is positioned above an inlet of the packer. The production line, provided by the utility model, can solve the problem of particle uniformity of material, and achieves the particle uniformity of produced mixed powder material; and a pneumatic drying system is used to dry the mixed powder material in finishing the material conveying and lifting functions, so that the manpower and the material handling loss can be greatly saved.

Description

A kind of mixed powder material production line
Technical field
The utility model relates to a kind of powder material plant-scale equipment line, relates in particular to a kind of powder material production line with the mixing of materials function.
Background technology
In the production of mixed powder material, the processing method that generally all can adopt various raw materials to separate for multiple powder material.Particle and character for powder material are taked different processing methods, can be so that the production material uniform particles still adopt the processing method of suiting measures to local conditions can increase the technology of production, and producing required equipment and manual work etc. also increases to some extent.In the production of powder material, processing step just should reduce and reduce.The operation in each step all can produce dust pollution in various degree, and these health of polluting for the direct labor have very big influence.Because it is individual processing that the raw material in each stage is handled, each several part all can take bigger place.And handle in the mixed powder material, energy consumption of equipment is also bigger.
If can under the situation that does not increase the production difficulty, solve the uneven problem of powder material particle, and can not increase dust pollution question, that will help the production of powder material.
The utility model content
The purpose of the utility model provides a kind of mixed powder material production line; To need screening, pulverizing raw materials for production preprocessing process to combine respectively; Reduce the mixed powder production technology; Practice thrift the loss of artificial and material handling greatly, realize that simultaneously granular material is carried and dry carrying out synchronously.
To achieve these goals; The technology that the utility model adopts is a kind of mixed powder material production line; It is characterized in that; Comprise the screening plant, the feed bin of weighing, mixer, material transfer equipment and the packing machine that link to each other successively, also comprise disintegrating apparatus, the material outlet of said screening plant and disintegrating apparatus is positioned at the feed bin import top of weighing; Said mixer import is positioned at the outlet below of the feed bin of weighing; Said material transfer equipment import is connected with the mixer outlet, and the material transfer equipment outlet is positioned at packing machine import top.
In the mixed powder material production line that the utility model provides, according to the particle and the different in kind of powder material, large granular materials is separated with pulverizing through screening earlier, put the granular powder material after separating into weigh bin and carry out weighing.Preferably, between disintegrating apparatus and screening plant, be provided with the material interface channel, sieving isolated larger particles raw material can also be through pulverizing in this interface channel entering disintegrating apparatus.On weigh bin, also be provided with the auxiliary material import, be used to need not pretreated auxiliary material and get into weigh bin.After weighing finished, multiple granular material got into mixer and accomplishes mixing, and mixer is preferably cone-type mixer.Material transfer equipment preferably adopts the pneumatic conveying drying system.After finishing, mixing of materials gets in the pipeline of pneumatic conveying drying system.Under the effect of air-flow, material is transported to the packing machine top, and after packing machine started bottom waiting, material fell into packing machine and packs.Between pneumatic conveying drying system and packing machine, preferably also be provided with the material temporary storing bin.Below packing machine, also be provided with conveyer belt, be used for the packed pulverulent mixture material of producing is sent to the warehouse.
Compared with prior art; The production line that the utility model provides can solve the particle problem of non-uniform of material; The mixed powder material particles that realization is produced is even; Utilize the pneumatic conveying drying system accomplishing the effect that promotes material of carrying in addition, also drying is carried out in mixing simultaneously, can practice thrift the loss of artificial and material handling greatly.
Description of drawings
Fig. 1 is that the mixed powder material that the utility model provides produces the line flow chart.
The specific embodiment
The utility model provides a kind of mixed powder material production line; Original substep is combined with conventional powder material production to screening and the pulverizing preliminary treatment that raw material carries out, in conjunction with forming a kind of production line that processes such as screening, pulverizing, weighing, premixed, conveying drying, packing are combined.Production line mainly is made up of equipment such as vibratory sieve, pulverizer, weigh bin, cone-type mixer, pneumatic conveying drying system and packing machines.
The drying means of conventional granular material is to use fluid bed to carry out drying, and has air-flow to carry drying system in the present invention, carries out drying when can be implemented in the material transportation synchronously.Air-flow carries drying system to be made up of pressure fan, vapor heat exchanger, cyclone separator and air-introduced machine.Vapor heat exchanger, cyclone separator and air-introduced machine are connected through pipeline successively, and the air-introduced machine exhaust outlet links to each other with the import of vapor heat exchanger through circulating line, thereby make air-flow conveying drying system be an airflow line circulatory system.The air outlet of pressure fan is connected with the air inlet of vapor heat exchanger, and pressure fan is positioned at being connected on the pipeline of air-introduced machine and vapor heat exchanger, is used for input air.In the pipeline between vapor heat exchanger and cyclone separator material inlet is set, is used for carrying drying system to add powder material to energy-saving air-flow.
Adopt the different disposal method according to powder material particle and different in kind.To have large granular materials and caking capacity material to sieve through screening machine earlier, the material that accords with production needs gets into weigh bin again and weighs.Powder for large granular materials need be pulverized is ground into the granular material that accords with production requires with pulverizer, reinstalls in the weigh bin and weighs.The weighing induction installation is housed in the weigh bin, can demonstrates the weight that adds material.Multiple granular material gets into from weigh bin in the cone-type mixer, under agitation accomplishes the mixing of powder material.After granular material mixes end, get into the pneumatic conveying drying system.Under the effect of air-flow, powder-material is transported in the temporary feed bin in packing machine top, and the moisture in the granular material also is removed simultaneously.After treating the packing machine startup of temporary feed bin bottom, material falls into packing machine and packs.
Embodiment 1
As shown in Figure 1, pour granular material A into screening machine 1 and carry out material screening according to product requirement, the granular material A that meets product requirement gets into weigh bin 3 through the pipeline between screening machine 1 and the weigh bin 3.After weighing was intact, material A got in the cone-type mixer 4 to be mixed.Solid material B pours pulverizer 2 into, solid material B is ground into the granular material B that closes product requirement with pulverizer 2.Granular material B gets into weigh bin 3 through the pipeline between pulverizer 2 and the weigh bin 3.Weigh bin 3 is carried out weighing for the material B that gets into, and the intact back of weighing material B gets in the cone-type mixer 4 again.Start cone-type mixer 4, wherein material A and B fully mixed.Open cone-type mixer 4 switches afterwards, the mixed powder thing falls into gas-drying system 5.Utilize 5 pairs of mixed powder things of pneumatic conveying drying system to carry out drying, and the mixed powder thing is transported to the port of export place of gas-drying system 5.Through the port of export of gas-drying system 5, the mixed powder thing gets into and is transported in the temporary hopper 6 in top.When the packing machine 7 that is positioned at temporary hopper 6 belows is started working, carry out material package in the small feed bin on the mixed powder material entering packing machine 7.After packing machine 7 packing, mix granular material be packaged into packed, and by the transportation conveyer belt on the packing machine with packaged packed mixed powder mass transport to the warehouse.
Embodiment 2
Present embodiment with process identical, through weigh bin 3 upper sheds, the granular material C that need not to sieve and pulverize is directly added in the weigh bin 3.After material C accomplishes in weigh bin 3 and weighs, get in the cone-type mixer 4 and together mix with material A and material B.
The production line that the utility model provides can solve the particle problem of non-uniform of material, realizes that the mixed powder material particles is even.In addition, utilize the pneumatic conveying drying system, also the mixed powder material is carried out drying, can practice thrift the loss of artificial and material handling greatly accomplishing the effect while of carrying the lifting material.
More than the specific embodiment of the utility model is described in detail, but it is as example, the utility model is not restricted to the specific embodiment of above description.To those skilled in the art, any equivalent modifications that this practicality is carried out with substitute also all among the category of the utility model.Therefore, impartial conversion and the modification under spirit that does not break away from the utility model and scope, done all should be encompassed in the scope of the utility model.

Claims (7)

1. mixed powder material production line; It is characterized in that; Comprise the screening plant, the feed bin of weighing, mixer, material transfer equipment and the packing machine that link to each other successively, also comprise disintegrating apparatus, the material outlet of said screening plant and disintegrating apparatus is positioned at the feed bin import top of weighing; Said mixer import is positioned at the outlet below of the feed bin of weighing; Said material transfer equipment import is connected with the mixer outlet, and the material transfer equipment outlet is positioned at packing machine import top.
2. production line according to claim 1 is characterized in that said weigh bin is provided with the auxiliary material import.
3. production line according to claim 1 is characterized in that, said mixer is a cone-type mixer.
4. production line according to claim 1 is characterized in that, also is provided with the material temporary storing bin between said material transfer equipment and the packing machine.
5. production line according to claim 1 is characterized in that, said packing machine below also is provided with conveyer belt.
6. production line according to claim 1 is characterized in that, is provided with the material interface channel between said pulverizer and the screening plant.
7. production line according to claim 1 is characterized in that, said material transfer equipment adopts the pneumatic conveying drying system.
CN2011202588433U 2011-07-21 2011-07-21 Mixed powder material production line Expired - Lifetime CN202207551U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011202588433U CN202207551U (en) 2011-07-21 2011-07-21 Mixed powder material production line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011202588433U CN202207551U (en) 2011-07-21 2011-07-21 Mixed powder material production line

Publications (1)

Publication Number Publication Date
CN202207551U true CN202207551U (en) 2012-05-02

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Application Number Title Priority Date Filing Date
CN2011202588433U Expired - Lifetime CN202207551U (en) 2011-07-21 2011-07-21 Mixed powder material production line

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CN (1) CN202207551U (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103111210A (en) * 2013-02-26 2013-05-22 杭州海虹精细化工有限公司 Technology for modifying ADC foaming agent
CN105617942A (en) * 2016-03-30 2016-06-01 临沂远博化工有限公司 Raw material feeding device for nitromethane synthesis reaction and method of raw material feeding device
CN105837271A (en) * 2016-03-31 2016-08-10 登封快丰收农业发展有限公司 Granular organic fertilizer production line
CN106276316A (en) * 2016-08-29 2017-01-04 云南冶金新立钛业有限公司 The system and method that powder is pulverized
CN108905670A (en) * 2018-07-18 2018-11-30 广东心宝药业科技有限公司 mixed powder preparation system and method
CN114728246A (en) * 2020-02-10 2022-07-08 日本斯频德制造株式会社 Dispersing device and powder supply member

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103111210A (en) * 2013-02-26 2013-05-22 杭州海虹精细化工有限公司 Technology for modifying ADC foaming agent
CN105617942A (en) * 2016-03-30 2016-06-01 临沂远博化工有限公司 Raw material feeding device for nitromethane synthesis reaction and method of raw material feeding device
CN105837271A (en) * 2016-03-31 2016-08-10 登封快丰收农业发展有限公司 Granular organic fertilizer production line
CN106276316A (en) * 2016-08-29 2017-01-04 云南冶金新立钛业有限公司 The system and method that powder is pulverized
CN106276316B (en) * 2016-08-29 2018-11-27 云南冶金新立钛业有限公司 The system and method that powder crushes
CN108905670A (en) * 2018-07-18 2018-11-30 广东心宝药业科技有限公司 mixed powder preparation system and method
CN114728246A (en) * 2020-02-10 2022-07-08 日本斯频德制造株式会社 Dispersing device and powder supply member

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CX01 Expiry of patent term

Granted publication date: 20120502

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