CN203143694U - Conveying system for finished products of anhydrous sodium sulphate - Google Patents

Conveying system for finished products of anhydrous sodium sulphate Download PDF

Info

Publication number
CN203143694U
CN203143694U CN 201320068152 CN201320068152U CN203143694U CN 203143694 U CN203143694 U CN 203143694U CN 201320068152 CN201320068152 CN 201320068152 CN 201320068152 U CN201320068152 U CN 201320068152U CN 203143694 U CN203143694 U CN 203143694U
Authority
CN
China
Prior art keywords
communicated
nitre
anhydrous sodium
finished product
sodium sulphate
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.)
Expired - Fee Related
Application number
CN 201320068152
Other languages
Chinese (zh)
Inventor
张春太
张云照
何军
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.)
SC HONGYA QINGYIJIANG SODIUM SULPHATE CO Ltd
Original Assignee
SC HONGYA QINGYIJIANG SODIUM SULPHATE CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SC HONGYA QINGYIJIANG SODIUM SULPHATE CO Ltd filed Critical SC HONGYA QINGYIJIANG SODIUM SULPHATE CO Ltd
Priority to CN 201320068152 priority Critical patent/CN203143694U/en
Application granted granted Critical
Publication of CN203143694U publication Critical patent/CN203143694U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The utility model discloses a conveying system for finished products of anhydrous sodium sulphate and relates to a conveying device for powder products. The conveying system comprises a drying device, a conveying device, a pneumatic elevator, a nitrate storage bin and a bag-type dust collector which are connected sequentially, an anhydrous sodium sulphate outlet of the drying device is communicated with the conveying device, an anhydrous sodium sulphate outlet of the conveying device is communicated with the pneumatic elevator, an anhydrous sodium sulphate outlet of the pneumatic elevator is communicated with the storage bin, and the storage bin is provided with an air outlet which is communicated with the bag-type dust collector. The conveying system for the finished products of the anhydrous sodium sulphate is stable in device operation, high in production efficiency, small in occupied space, capable of achieving fine nitrate recycling, convenient to operate, high in regulation performance and novel.

Description

A kind of glauber salt finished product delivery system
Technical field
The utility model relates to a kind of feedway of powder-product.
Background technology
In the prior art, the method that adopts usually for the conveying of finished product nitre is: dry cooled finished product nitre is delivered to the finished product warehouse through the band conveyor trestle, then the packing warehouse-in.Be specially: nitre is through centrifuge dewatering, and by pneumatic conveying drying, dried nitre is stored in the dried nitre storehouse; The nitre that is stored in the dried nitre storehouse passes through the band conveyor trestle, is sent to the finished product nitre warehouse in finished product packing workshop by pumper; After dried nitre is sent to the finished product warehouse, by delivery machine discharge packing warehouse-in.Wherein, belt conveyer is a kind of friction-driven machinery of transported material in a continuous manner.Mainly formed by frame, belt conveyor, belt roller, tightening device, driving device etc.It can put the conveying flow process that forms a kind of material between final emptying point from initial feed with material on certain travel line.
Though it is big to adopt the band conveyor trestle to have fed distance, and very big advantage is arranged in the production technology for remote horizontal feed, there are numerous shortcomings in the wideer advantage of suitable application area of belt conveyor bridge conveying simultaneously for the conveying of finished product nitre:
1, adopt the band conveyor trestle to carry finished product nitre, occupation area of equipment is big, and equipment cost is higher;
2, the belt in the band conveyor trestle is easy to wear aging in operation, and the easy sideslip of belt, belt roller are tied nitre dirt 3, the back rotating effect is bad, and effect is carried in influence, has improved accident rate, and maintenance cost is higher;
4, the thin easy contaminated environment of nitre dust in the transport process of dry nitre causes the wasting of resources simultaneously easily;
5, adopt the band conveyor trestle to carry finished product nitre, the regulation and control of its operational throughput size have certain restriction, and delivery speed also has certain restriction.
The utility model content
The purpose of this utility model is: a kind of stable equipment operation is proposed, and the production efficiency height, the occupation of land space is little, and thin nitre is recyclable, simple operation, the novel glauber salt finished product delivery system that Modulatory character is strong.
The purpose of this utility model realizes by following technical proposals:
A kind of glauber salt finished product delivery system, comprise the airer that connects successively, feedway, Pneumatic lift, storage nitre storehouse and bag dust collector, the glauber salt outlet of described airer is communicated to described feedway, and the glauber salt outlet of described feedway is communicated to described Pneumatic lift, the glauber salt outlet of described Pneumatic lift is communicated to described storage bin, and described storage bin is provided with gas vent and is communicated to described bag dust collector.
As optimal way, described airer is fluid bed.
In the such scheme, fluid bed is in order to dry finished product nitre, and the strength of Pneumatic lift is carried after being convenient to.
As optimal way, described feedway is conveyor screw.
In the such scheme, conveyor screw is in order to send into dry finished product nitre in the Pneumatic lift, and the strength of being convenient to Pneumatic lift is carried.
As optimal way, described gas vent is located at described storage bin top.
In the such scheme, fall to carrying out final gas solid separation according to rising naturally of air-flow and material.
The effect of each part is as follows in the utility model:
Air lift mud pump belongs to a kind of low-pressure air convey materials equipment (Pneumatic ash conveying pump), is applicable to continuously, and the dry powdery material is carried in vertical-lift equably, and its traffic capacity is big and hoisting depth is higher.The air lift mud pump delivery system is mainly by the pump housing, delivery duct and source of the gas three parts are formed, it is little that it has floor area, easy for installation, reliable, simple to operation, equipment itself does not almost have wearing and tearing in operational process, the inner no pressure of pump housing during work is not so its top feed pipeline needs airlock; And lift pump can also overcome the inhomogeneous feed wave phenomenon that causes of feeding equipment moment feeding.
Adopt Pneumatic lift to carry the advantage of finished product nitre:
Floor area is big when 1, at first adopting the Pneumatic lift conveying to overcome the conveying of band conveyor trestle, the shortcoming that equipment has high input;
2, secondly, Pneumatic lift does not have movable parts, and is non-maintaining, and capacity and flow are reconciled by the pressure demodulator, remedied in the production of band conveyor trestle easily to wear out defectives such as easy sideslip;
3, source of the gas provides the power material directly to transmit in delivery pipe in the Pneumatic lift conveying finished product nitre process, and thin nitre can be recycled by bag dust collector, has also avoided thin nitre dust polluting environment simultaneously;
4, adopt Pneumatic lift to carry, in actual production process, can freely control size, speed and the height of mass transport amount by regulating air-valve;
5, to have fed distance far away for Pneumatic lift, and delivery head is big, in the advantage with band conveyor trestle, has also overcome the former cost of investment and the high defective of maintenance cost, and is more economical, more practical.
Workflow of the present utility model:
After the finished product nitre drying device drying, be delivered to Pneumatic lift through feedway, carry, be promoted to storage nitre storehouse by Pneumatic lift, finished product nitre powder falls to depositing back packing warehouse-in in the storage bin, the gas of Pneumatic lift generation simultaneously carries the thinner finished product nitre dust of part and enters bag dust collector by gas vent, by the filtration of bag dust collector, thin nitre is recycled, and the gas after the filtration enters atmosphere.
The beneficial effects of the utility model:
1, the equipment operation is more stable, and the et out of order probability is low, is conducive to the raising of production efficiency, has reduced the maintenance cost of production facilities;
2, saved the occupation of land space of plant area;
3, not only reclaim the waste of having avoided resource of thin nitre, and protected environment;
4, transport efficiency height, stable in the production, it is more convenient to operate;
5, Modulatory character is strong, can control the operational throughput of finished product nitre in process of production according to actual conditions.
Description of drawings
Fig. 1 is the device schematic flow sheet of the utility model embodiment.
The specific embodiment
Below in conjunction with specific embodiments and the drawings the utility model is further described.
As shown in Figure 1, a kind of glauber salt finished product delivery system comprises the airer that connects successively, feedway, Pneumatic lift, storage nitre storehouse and bag dust collector are as optimal way, as shown in this embodiment, airer is fluid bed, and feedway is conveyor screw.The glauber salt outlet of fluid bed is communicated to conveyor screw, and the glauber salt outlet of conveyor screw is communicated to Pneumatic lift, and the glauber salt outlet of Pneumatic lift is communicated to storage bin, and the storage bin top is provided with gas vent and is communicated to bag dust collector.
Workflow of the present utility model:
Finished product nitre is behind fluidized bed drying, be delivered to Pneumatic lift through conveyor screw, carry, be promoted to storage nitre storehouse by Pneumatic lift, finished product nitre powder falls to depositing back packing warehouse-in in the storage bin, the gas of Pneumatic lift generation simultaneously carries the thinner finished product nitre dust of part and enters bag dust collector by gas vent, by the filtration of bag dust collector, thin nitre is recycled, and the gas after the filtration enters atmosphere.
The above only is preferred embodiment of the present utility model; not in order to limit the utility model; all any modifications of within spirit of the present utility model and principle, doing, be equal to and replace and improvement etc., all should be included within the protection domain of the present utility model.

Claims (4)

1. glauber salt finished product delivery system, it is characterized in that: comprise the airer that connects successively, feedway, Pneumatic lift, storage nitre storehouse and bag dust collector, the glauber salt outlet of described airer is communicated to described feedway, and the glauber salt outlet of described feedway is communicated to described Pneumatic lift, the glauber salt outlet of described Pneumatic lift is communicated to described storage bin, and described storage bin is provided with gas vent and is communicated to described bag dust collector.
2. glauber salt finished product delivery system as claimed in claim 1, it is characterized in that: described airer is fluid bed.
3. glauber salt finished product delivery system as claimed in claim 1, it is characterized in that: described feedway is conveyor screw.
4. glauber salt finished product delivery system as claimed in claim 1, it is characterized in that: described gas vent is located at described storage bin top.
CN 201320068152 2013-02-06 2013-02-06 Conveying system for finished products of anhydrous sodium sulphate Expired - Fee Related CN203143694U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320068152 CN203143694U (en) 2013-02-06 2013-02-06 Conveying system for finished products of anhydrous sodium sulphate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320068152 CN203143694U (en) 2013-02-06 2013-02-06 Conveying system for finished products of anhydrous sodium sulphate

Publications (1)

Publication Number Publication Date
CN203143694U true CN203143694U (en) 2013-08-21

Family

ID=48971238

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201320068152 Expired - Fee Related CN203143694U (en) 2013-02-06 2013-02-06 Conveying system for finished products of anhydrous sodium sulphate

Country Status (1)

Country Link
CN (1) CN203143694U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103086155A (en) * 2013-02-06 2013-05-08 四川省洪雅青衣江元明粉有限公司 Anhydrous sodium sulphate finished product conveying system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103086155A (en) * 2013-02-06 2013-05-08 四川省洪雅青衣江元明粉有限公司 Anhydrous sodium sulphate finished product conveying system

Similar Documents

Publication Publication Date Title
CN101318180B (en) Hydrocarbon black powder removing method and device
CN102756920A (en) Continuous dense-phase positive-pressure pneumatic conveying apparatus and conveying method
CN202575424U (en) Pneumatic conveyor in novel pulverizing system
CN203143694U (en) Conveying system for finished products of anhydrous sodium sulphate
CN107875974B (en) Dry powder rolling granulation system and granulation process
CN202744005U (en) Acetylene sludge closed cycle gas force conveying system
CN202498022U (en) System for screening and recycling blast furnace return ore
CN202703896U (en) Automatic casing machine for bulk bags
CN203998103U (en) Fine powder aggregate air transporting arrangement
CN204713889U (en) Fertilizer conveyer
CN204355805U (en) A kind of environment friendly dedusting hopper
CN202807882U (en) Continuous dense phase positive pressure pneumatic transmission device
CN203842664U (en) Vertical roller mill and grader direct series connection equipment for producing two types of ground calcium carbonate powder
CN103691539B (en) Intelligent double-stage crushing station
CN103086155A (en) Anhydrous sodium sulphate finished product conveying system
CN205661683U (en) Powder coating's crocus package system
CN211470046U (en) Ferrophosphorus production is with vertical mill ejection of compact packaging system
CN201283344Y (en) Black carbon powder removing device
CN210545612U (en) Briquette tailing recycling system and briquette production equipment with same
CN210527861U (en) Pneumatic conveying device for lime
CN203359558U (en) Conveying type automatic feeding device
CN207985989U (en) A kind of PTA powders carrier bar transport system
CN203803604U (en) Intelligent two-stage crushing station
CN203512773U (en) Conveying device for nanometer zinc oxide powder
CN203159480U (en) Sintered lime discharging system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130821

Termination date: 20220206

CF01 Termination of patent right due to non-payment of annual fee