CN205773388U - The production system of fluffy Pumex salt - Google Patents
The production system of fluffy Pumex salt Download PDFInfo
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- CN205773388U CN205773388U CN201620485733.3U CN201620485733U CN205773388U CN 205773388 U CN205773388 U CN 205773388U CN 201620485733 U CN201620485733 U CN 201620485733U CN 205773388 U CN205773388 U CN 205773388U
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- halogen
- row
- salt
- pipeline
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Abstract
This utility model relates to salt preparing technical field, specifically discloses the production system of a kind of fluffy Pumex salt.Filtering ponds that the sedimentation tank that described production system including halogen pond connects with describedization halogen pond connects with described sedimentation tank and the halogen storage pool connected with described filtering ponds, described halogen storage pool connects storage halogen tank, described storage halogen tank connects brine transportation device, described brine transportation device connects row's halogen pipeline, and the bottom of described row's halogen pipeline uniformly offers some row's halogen holes along pipe lengths；The lower section being positioned at described row's halogen pipeline is provided with evaporation boiler, and the opening in described row's halogen hole is towards described evaporation boiler.Salt is uniformly entered in evaporation boiler by this utility model by row's halogen hole of row's halogen pipeline, it is to avoid local fills that halogen temperature contrast is big and the problem that affects product particle kenel, it is ensured that product particle is fluffy, band flakes, and has instant feature；Whole production system is reasonable in design, and Productive statistics is little, easy to control, easily realizes industrialization.
Description
Technical field
This utility model relates to salt preparing technical field, particularly relates to the lowest a kind of sodium, fluffy instant
The production system of Pumex salt.
Background technology
At present, the technique of domestic sea salt district production purified salt mainly has salt field saturated brine to enter tank evaporation system
Salt and crude salt dissolve makes saturated bittern evaporation two kinds of methods of salt manufacturing.Partial monopoly provides sea water or
Salt produces the method for Cardia Salt.
Chinese patent (CN101456563A) (applying for artificial Dongying Chunxing Salt-chemical Co., Ltd.) special
Profit provides a kind of sea water and produces the simple process of Cardia Salt, i.e. brewed brine operation, Crystallization Procedure, control
Water warehouse-in operation, by strictly controlling evaporation of seawater, to control wherein sodium, potassium content, after proceed to knot
Brilliant pond intercrystalline, the product salt particle that this kind of method is produced is closely knit, matter hard, and the purity of salt is relatively low, matter
Measure poor.
The evaporization process producing Cardia Salt provided in United States Patent (USP) (US7621968B1) is at rock salt
Residue salt after crystallization adds sea water be evaporated again, to reduce the content of middle sodium chloride of evaporating brine, obtain
Required Cardia Salt product, technique is complex, and product is the most fluffy, it is slower to dissolve.
Utility model content
Technical problem to be solved in the utility model is to provide realization little, the easy industry of a kind of Productive statistics
Change, the production system of the Pumex salt of fluffy instant, the lowest sodium of product.
For solving above-mentioned technical problem, the technical solution of the utility model is:
The production system of fluffy Pumex salt, including change halogen pond and describedization halogen pond for dissolving crude salt
The filtering ponds that connect with described sedimentation tank of sedimentation tank of connection and the storage halogen connected with described filtering ponds
Pond, described halogen storage pool connects storage halogen tank, and described storage halogen tank connects brine transportation device, described halogen
Water conveying device connects row's halogen pipeline, and the bottom of described row's halogen pipeline is uniformly opened along pipe lengths
It is provided with some row's halogen holes；The lower section being positioned at described row's halogen pipeline is provided with evaporation boiler, described row's halogen hole
Opening is towards described evaporation boiler.
As preferably, it is provided with filter pump between described halogen storage pool and described storage halogen tank, passes through filter pump
Salt mechanical filter refined in halogen storage pool is removed floccule further.
As preferably, described brine transportation device includes the delivery pump connected with described storage halogen tank, described
Delivery pump connects has brine pipeline road, described brine pipeline road to be connected with described row's halogen pipeline；Described defeated halogen
Two-step evolution valve it is provided with on pipeline.
As preferably, the row's of being provided above temperature of described evaporation boiler is covered, and is beneficial to evaporation and improves yield, and
Foreign body is avoided to enter in evaporation boiler.
This utility model has the advantages that
(1) defeated halogen mode uses multiple spot vacant pouring halogen method, by row's halogen hole of row's halogen pipeline by salt
Uniformly enter in evaporation boiler, it is to avoid it is big and affect asking of product particle kenel that local fills halogen temperature contrast
Topic, it is ensured that product particle is fluffy, band flakes, and has instant feature.
(2) by changing halogen pond, sedimentation tank, natural filtration pond and mechanical filter, it is possible to ensure to produce
Product pure sparkling and crystal-clear, whole production system is reasonable in design, and Productive statistics is little, controls easy to operate, easily
Realize industrialization.
Accompanying drawing explanation
The following drawings is only intended to, in schematically illustrating this utility model and explaining, not limit this reality
By novel scope.Wherein:
Fig. 1 is the system construction drawing of this utility model embodiment；
Fig. 2 is the partial structurtes schematic diagram of row's halogen pipeline.
In figure: 1-ization halogen pond；2-sedimentation tank；3-filtering ponds；4-halogen storage pool；5-stores up halogen tank；6-is defeated
Send pump；7-arranges halogen pipeline；8-arranges halogen hole；9-evaporation boiler；10-filter pump；11-brine pipeline road；12-
Control valve；13-row's temperature cover.
Detailed description of the invention
Below in conjunction with the accompanying drawings and embodiment, this utility model is expanded on further.In following detailed description
In, only by the way of explanation, describe some one exemplary embodiment of the present utility model.Undoubtedly,
Those of ordinary skill in the art will be consequently realised that, without departing from spirit and scope of the present utility model
In the case of, by various different modes, described embodiment can be modified.Therefore, accompanying drawing
It is inherently the most illustrative with describing rather than is used for limiting scope of the claims.
As depicted in figs. 1 and 2, the production system of fluffy Pumex salt, including the change for dissolving crude salt
The filtering ponds 3 that the sedimentation tank 2 that halogen pond 1 connects with describedization halogen pond 1 connects with described sedimentation tank 2
And the halogen storage pool 4 connected with described filtering ponds 3, described halogen storage pool 4 connects storage halogen tank 5, institute
Stating storage halogen tank 5 connection and have brine transportation device, described brine transportation device connects row's halogen pipeline 7,
The bottom of described row's halogen pipeline 7 uniformly offers some row's halogen holes 8 along pipe lengths；It is positioned at institute
The lower section of the row's of stating halogen pipeline 7 is provided with evaporation boiler 9, and the opening in described row's halogen hole 8 is towards described evaporation
Pot 9.
Wherein, described brine transportation device includes the delivery pump 6 connected with described storage halogen tank 5, described
Delivery pump 6 connects has brine pipeline road 11, described brine pipeline road 11 to be connected with described row's halogen pipeline 7；
It is provided with two-step evolution valve 12 on described brine pipeline road 11.
For removing floccule further, between described halogen storage pool 4 and described storage halogen tank 5, it is provided with filtration
Pump 10, removes floccule by filter pump 10 further by salt mechanical filter refined in halogen storage pool 4.
It addition, the row's of being provided above temperature cover 13 of described evaporation boiler 9, it is beneficial to evaporation and improves yield,
And avoid foreign body to enter in evaporation boiler 9.
Production method is as follows: selected high-quality crude salt, inputization halogen pond 1 dissolvingization halogen, forms saturated halogen
Water；Saturated bittern after sedimentation tank 2 removes silt, impurity to filtering ponds 3；After refined, enter one
To halogen storage pool 4 after step removal molecule silt and floccule；Utilize filter pump 10 by halogen storage pool 4
Refined salt mechanical filter is delivered to store up halogen tank 5 after removing floccule further, refined salt is at storage halogen
In tank 5, precipitation upper strata forms salt clear liquid；Salt clear liquid passes through multiple spot vacant pouring halogen through row's halogen pipeline 7
Method enters evaporation boiler 9, it is to avoid because local, to fill halogen temperature contrast big and affect product particle kenel and product
The problem of quality；Bittern evaporation in evaporation boiler 9, the salt particle of crystallization is fluffy and band flakes,
And there is instant feature；Use fishing device fishing to control drench car, carry out control drench, then drying,
Check, be distributed into bag as sale of finished goods.
The foregoing is only the schematic detailed description of the invention of this utility model, be not limited to this reality
By novel scope.Any those skilled in the art, without departing from design of the present utility model and former
Equivalent variations done on the premise of then and amendment, all should belong to the scope of this utility model protection.
Claims (4)
- The production system of the most fluffy Pumex salt, it is characterised in that: include the change halogen pond for dissolving crude salt, Filtering ponds that the sedimentation tank connected with describedization halogen pond connects with described sedimentation tank and with described filtering ponds The halogen storage pool of connection, described halogen storage pool connects storage halogen tank, and described storage halogen tank connects brine transportation device, Described brine transportation device connects row's halogen pipeline, and the bottom of described row's halogen pipeline is equal along pipe lengths Even offer some row's halogen holes；The lower section being positioned at described row's halogen pipeline is provided with evaporation boiler, described row's halogen hole Opening towards described evaporation boiler.
- The production system of fluffy Pumex salt the most as claimed in claim 1, it is characterised in that: described storage It is provided with filter pump between halogen pond and described storage halogen tank.
- The production system of fluffy Pumex salt the most as claimed in claim 1, it is characterised in that: described halogen Water conveying device includes the delivery pump connected with described storage halogen tank, and described delivery pump connects brine pipeline road, Described brine pipeline road is connected with described row's halogen pipeline；It is provided with two-step evolution valve on described brine pipeline road.
- 4. the production system of the fluffy Pumex salt as described in any one of claims 1 to 3, its feature exists In: the row's of being provided above temperature cover of described evaporation boiler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620485733.3U CN205773388U (en) | 2016-05-25 | 2016-05-25 | The production system of fluffy Pumex salt |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620485733.3U CN205773388U (en) | 2016-05-25 | 2016-05-25 | The production system of fluffy Pumex salt |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205773388U true CN205773388U (en) | 2016-12-07 |
Family
ID=58113101
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620485733.3U Expired - Fee Related CN205773388U (en) | 2016-05-25 | 2016-05-25 | The production system of fluffy Pumex salt |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205773388U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110899263A (en) * | 2019-12-04 | 2020-03-24 | 江苏新源矿业有限责任公司 | Long-distance brine conveying pipeline on-line non-stop conveying cleaning process and cleaning device |
-
2016
- 2016-05-25 CN CN201620485733.3U patent/CN205773388U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110899263A (en) * | 2019-12-04 | 2020-03-24 | 江苏新源矿业有限责任公司 | Long-distance brine conveying pipeline on-line non-stop conveying cleaning process and cleaning device |
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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: 20161207 Termination date: 20200525 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |