CN107899278A - Integrated fine salt particle reclamation device - Google Patents
Integrated fine salt particle reclamation device Download PDFInfo
- Publication number
- CN107899278A CN107899278A CN201711356351.6A CN201711356351A CN107899278A CN 107899278 A CN107899278 A CN 107899278A CN 201711356351 A CN201711356351 A CN 201711356351A CN 107899278 A CN107899278 A CN 107899278A
- Authority
- CN
- China
- Prior art keywords
- feed inlet
- saline mixture
- sieve
- conical filter
- filter tank
- 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.)
- Pending
Links
- 150000003839 salts Chemical class 0.000 title claims abstract description 82
- 239000002245 particle Substances 0.000 title claims abstract description 33
- 239000000203 mixture Substances 0.000 claims abstract description 60
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 56
- 239000011780 sodium chloride Substances 0.000 claims abstract description 56
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 230000008021 deposition Effects 0.000 claims abstract description 20
- 239000004677 Nylon Substances 0.000 claims description 30
- 229920001778 nylon Polymers 0.000 claims description 30
- 239000012267 brine Substances 0.000 claims description 4
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 3
- 230000010354 integration Effects 0.000 claims 4
- 238000000034 method Methods 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 241001131796 Botaurus stellaris Species 0.000 description 5
- 230000008901 benefit Effects 0.000 description 5
- 238000009825 accumulation Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 230000007547 defect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000006855 networking Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/03—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
- B01D36/045—Combination of filters with centrifugal separation devices
Abstract
The invention belongs to receive salt engineering device technique field, and in particular to integrated fine salt particle reclamation device.Including conical filter tank, sieve, water outlet, saline mixture feed inlet, not separated deposition saline mixture feed inlet, valve and feed opening；Sieve is set inside the conical filter tank, the water outlet is arranged on conical filter tank, water outlet is located at sieve top, the saline mixture feed inlet is arranged on conical filter tank, the not separated deposition saline mixture feed inlet is connected to saline mixture feed inlet, saline mixture feed inlet is located at sieve lower part, and conical filter pot bottom sets feed opening, and feed opening position sets valve.The fine salt particle that the present invention can not be collected the prior art recycles, and avoids unnecessary waste；And the salt face color that this portion collection arrives is whiter, and particle is thinner, and quality is more preferable.
Description
Technical field
The invention belongs to receive salt engineering device technique field, and in particular to integrated fine salt particle reclamation device.
Background technology
By Tuo Tai in pipeline to beach using salt pump, water pump by crude salt in the receipts salt method used more in salt manufacturing the field
Stockpiling, recycles bucket wheel machine, belt conveyor to be attached on salt trolley, and water content is about 15% in crude salt, hauled weight increase, consumption
Can increase.Changing for technical solution has been carried out for the patent " reciprocating dewaterer " of this defect patent application CN105890326
Into it filters in crude salt 15% water using reciprocating screen, reduces the loss of landing salt to a certain extent, but still has
The fine salt particle in the similar salt face of a part still can not filter, and eventually pass through reciprocating screen and be discharged into salt pond again, existing to take off salt system
This part salt face is discharged and can not collected all the time by system together with brine, and the salt face do not collected accounts for salt total amount 5% or so, greatly
2.5 ten thousand tons or so of salt face is about discharged every year, causes very big waste.Breaking will be passed through, utilize salt pump by taking off salt in the prior art
The processes such as conveying, produce a large amount of salt faces in salt.It fine salt particle can equally be produced can not recycle and cause to waste.
The content of the invention
In view of the defects of prior art, the present invention provides a kind of integrated fine salt particle reclamation device, its it is recyclable can not
The salt face of collection, easy to carry out the processing and packing of new varieties salt again to salt face, caused benefit will be huger.
In order to achieve the above object, technical solution provided by the present invention is integrated fine salt particle reclamation device, it is wrapped
Include conical filter tank, sieve, water outlet, saline mixture feed inlet, not separated deposition saline mixture feed inlet, valve
And feed opening；Sieve is set inside the conical filter tank, and the water outlet is arranged on conical filter tank, and water outlet is positioned at sieve
Online portion, the saline mixture feed inlet are arranged on conical filter tank, it is described it is not separated deposition saline mixture into
Material mouth is connected to saline mixture feed inlet, and saline mixture feed inlet is located at sieve lower part, under conical filter pot bottom is set
Material mouth, feed opening position set valve.
The saline mixture feed inlet is connected to the drip pan of the reciprocal lower part of screen of reciprocating dewaterer, not separated heavy
Salification aqueous mixtures feed inlet is connected to reciprocating dewaterer and enters salt hopper bottom.
Based on above-mentioned technical proposal, the present invention by the dewatered bittern filtered out of reciprocating dewaterer not only to carrying out
Processing, directly can also directly filter filtered bittern.
Further, net formula nylon tape feeding end is arranged on below feed opening, and net formula nylon tape is by oblique below feed opening
Upper extension, the discharge end of net formula nylon tape, which is set, scrapes salt plate, and centrifuge is set below the discharge end.
Based on above-mentioned technical proposal, after the circulating filtration in conical filter tank, net formula nylon tape is dropped down onto, obliquely
Natural secondary filter is carried out on the net formula nylon tape of extension, until discharge end is scraped to centrifuge, carries out phase III mistake
Filter, last output finished product, the advantages of this arrangement are as follows, carry out secondary filter using net formula nylon tape and alleviate the work of centrifuge
Make task, can be cost-effective.
Further, centrifuge is set below the feed opening, and the centrifuge sets with retracting device and is integrated.
Based on above-mentioned technical proposal, after the circulating filtration in conical filter tank, centrifuge, the efficient mistake of memory are dropped down onto
Filter, can save process time.
Further, net formula nylon tape feeding end is arranged on below feed opening, and the discharge end of net formula nylon tape, which is set, scrapes salt
Plate, driving device, driving device connection driven roller are set in rack, and the net formula nylon tape is arranged in the driven roller, institute
State and vacuum chamber is set below net formula nylon tape, vacuum chamber connection vacuum extractor, vacuum chamber connection gas and water separator, the gas
Water separation device connects catch basin.
Based on above-mentioned technical proposal, after the circulating filtration in conical filter tank, drop down onto net formula nylon tape, on it into
Row vacuum belt filters, and good filter effect can both be reached by so setting, and can also save filtration time.
The course of work of the present invention：Valve is closed, by the saline mixture containing collection salt face in need by salt
Aqueous mixtures feed inlet and not separated deposition saline mixture feed inlet introducing device, saline mixture are gradually filled with taper
Filtering tank, the brine liquid level in conical filter tank gradually rise up to sieve, carry out the mistake of fine salt particle by sieve from the bottom to top
Filter, fine salt particle stay in sieve lower part, and water enters the water outlet on sieve top by sieve, and the fine salt particle of sieve lower part is continuous
Accumulation, due to gravity effect a part accumulation fine salt particle fall to feed opening, open valve at this time, be deposited on bottom
The pulpous state fine salt particle containing a small amount of water from feed opening flow out, further filtered into centrifuge or net formula nylon bring one into
Step, from after valve opening, saline mixture is entered by saline mixture feed inlet constantly to be filtered upwards under sieve, while part
Filtered water will be attached to the Yan Mianchong of sieve lower surface since gravity downwards recoils sieve from sieve
Under, the blocking of sieve is avoided, saline mixture constantly circulates in conical filter tank, carries out filtering recoil, completes first
Stage filters.
Beneficial effects of the present invention：The fine salt particle that the present invention can not be collected the prior art recycles,
Avoid unnecessary waste；And the salt face color that this portion collection arrives is whiter, and particle is thinner, and quality is more preferable.
Brief description of the drawings
Fig. 1 is the structure diagram of the present invention；
Fig. 2 is the structure diagram of the embodiment of the present invention 2；
Fig. 3 is the structure diagram of embodiment 3；
In figure：1st, conical filter tank, 2, sieve, 3, water outlet, 4, saline mixture feed inlet, 5, valve, 6, feed opening, 7,
Centrifuge, 8, net formula nylon tape, 9, feeding end, 10, discharge end, 11, scrape salt plate, 12, not separated deposition saline mixture
Feed inlet, 13, reciprocating dewaterer, 14, reciprocating screen, 15, drip pan, 16, enter salt hopper, 18, frame driving device, 19, driving
Device, 20, connection driven roller, 21, vacuum chamber, 22, vacuum extractor, 23, gas and water separator, 24, catch basin.
Embodiment
To become apparent from the object, technical solutions and advantages of the present invention, with reference to Figure of description and instantiation
It is illustrated.
Embodiment 1
Integrated fine salt particle reclamation device, it include conical filter tank 1, sieve 2, water outlet 3, saline mixture feed inlet 4,
Valve 5, feed opening 6 and not separated deposition saline mixture feed inlet 12；The inside of conical filter tank 1 sets sieve 2,
The water outlet 3 is arranged on conical filter tank 1, and water outlet 3 is located at 2 top of sieve, and the saline mixture feed inlet 4 is set
On conical filter tank 1, the not separated deposition saline mixture feed inlet 12 is connected to saline mixture feed inlet 4,
Saline mixture feed inlet 4 is located at 2 lower part of sieve, and 1 bottom of conical filter tank sets feed opening 6, and 6 position of feed opening sets valve
5, the saline mixture feed inlet 4 is connected to reciprocating dewaterer 13（The patent of patent application CN105890326 is " reciprocating
Dewaterer "）The drip pan 15 of 14 lower part of reciprocating screen, not separated deposition saline mixture feed inlet 12 are connected to reciprocating de-
Water dispenser enters 16 bottom of salt hopper.The centrifuge 7 is arranged on the lower section of feed opening 6.
The course of work：Valve 5 is closed, and salt machine first separation water outlet is taken off and reciprocating dewaterer enters salt hopper 16 by reciprocating
The not separated deposition saline mixture of bottom is directly accessed device saline mixture feed inlet 4, in 1 inner salt of conical filter tank
Aqueous mixtures liquid level gradually rises discharges by sieve 2, bittern by sieve 2 via water outlet 3, and fine salt particle cannot pass through sieve
Net 2 is constantly accumulated in conical filter tank 1, after being accumulated to certain volume, opens valve 5, fine salt particle enters through valve to be centrifuged
Machine 7, carries out the separation of fine salt particle and water.
Embodiment 2
Integrated fine salt particle reclamation device, it include conical filter tank 1, sieve 2, water outlet 3, saline mixture feed inlet 4,
Valve 5, feed opening 6 and not separated deposition saline mixture feed inlet 12；The inside of conical filter tank 1 sets sieve 2,
The water outlet 3 is arranged on conical filter tank 1, and water outlet 3 is located at 2 top of sieve, and the saline mixture feed inlet 4 is set
On conical filter tank 1, the not separated deposition saline mixture feed inlet 12 is connected to saline mixture feed inlet 4,
Saline mixture feed inlet 4 is located at 2 lower part of sieve, and 1 bottom of conical filter tank sets feed opening 6, and 6 position of feed opening sets valve
5, the saline mixture feed inlet 4 is connected to reciprocating dewaterer 13（The patent of patent application CN105890326 is " reciprocating
Dewaterer "）The drip pan 15 of 14 lower part of reciprocating screen, not separated deposition saline mixture feed inlet 12 are connected to reciprocating de-
Water dispenser enters 16 bottom of salt hopper.
8 feeding end 9 of net formula nylon tape is arranged on the lower section of feed opening 6, and net formula nylon tape 8 is oblique by the lower section of feed opening 6
Upper extension, the discharge end 10 of net formula nylon tape 8, which is set, scrapes salt plate 11, and the lower section of discharge end 10 sets centrifuge 7.
The course of work：Valve 5 is closed, by it is reciprocating take off salt machine first separation water outlet and it is not separated deposition brine mix
Compound is directly accessed the saline mixture feed inlet 4 of fine salt particle, and saline mixture liquid level gradually rises in conical filter tank 1
By sieve, bittern is discharged by sieve 2 via water outlet, and it is continuous in conical filter tank 1 that fine salt particle cannot pass through sieve 2
Accumulation, after being accumulated to certain volume, open valve 5, fine salt particle through valve 5 into networking formula nylon tape 8, in net formula nylon tape 8
Upper secondary separation bittern, then be delivered to discharge end 10 by net formula nylon tape 8, discharge end 10 scrape salt plate 11 and will pass through secondary filter
Fine salt particle scrape, into centrifuge 7, carry out the separation of fine salt particle and water.
Embodiment 3
Integrated fine salt particle reclamation device, it include conical filter tank 1, sieve 2, water outlet 3, saline mixture feed inlet 4,
Valve 5, feed opening 6 and not separated deposition saline mixture feed inlet 12；The inside of conical filter tank 1 sets sieve 2,
The water outlet 3 is arranged on conical filter tank 1, and water outlet 3 is located at 2 top of sieve, and the saline mixture feed inlet 4 is set
On conical filter tank 1, the not separated deposition saline mixture feed inlet 12 is connected to saline mixture feed inlet 4,
Saline mixture feed inlet 4 is located at 2 lower part of sieve, and 1 bottom of conical filter tank sets feed opening 6, and 6 position of feed opening sets valve
5, the saline mixture feed inlet 4 is connected to reciprocating dewaterer 13（The patent of patent application CN105890326 is " reciprocating
Dewaterer "）The drip pan 15 of 14 lower part of reciprocating screen, not separated deposition saline mixture feed inlet 12 are connected to reciprocating de-
Water dispenser enters 16 bottom of salt hopper.The feeding end 9 of net formula nylon tape 8 is arranged on the lower section of feed opening 6, the discharge end 10 of net formula nylon tape 8
Salt plate 11 is scraped in setting, and driving device 19 is set in rack 18, and driving device 19 connects driven roller 20, and the net formula nylon tape 8 is set
To put in the driven roller 20, the lower section of net formula nylon tape 8 sets vacuum chamber 21, and vacuum chamber 21 connects vacuum extractor 22,
Vacuum chamber 22 connects gas and water separator 23, and the gas and water separator 23 connects catch basin 24.
Annual to take off 500,000 tons of salt amount, salt per ton is calculated by 5% salt face of recycling, can increase by 2.5 ten thousand tons of yield, by 200 yuan per ton
Calculate, 5,000,000 yuan of benefit can be increased.Such as carry out the processing and packing of new varieties salt again to salt face, caused benefit will be huger
Greatly.
The above described is only a preferred embodiment of the present invention, not make limitation in any form to the present invention, this
Field technology personnel make a little simple modification, equivalent variations or modification using the technology contents of the disclosure above, all fall within this hair
In bright protection domain.
Claims (5)
1. integrated fine salt particle reclamation device, it is characterised in that：Including conical filter tank, sieve, water outlet, saline mixture
Feed inlet, not separated deposition saline mixture feed inlet, valve and feed opening；Sieve is set inside the conical filter tank
Net, the water outlet are arranged on conical filter tank, and water outlet is located at sieve top, and the saline mixture feed inlet is arranged on
On conical filter tank, the not separated deposition saline mixture feed inlet is connected to saline mixture feed inlet, and brine mixes
Compound feed inlet is located at sieve lower part, and conical filter pot bottom sets feed opening, and feed opening position sets valve.
2. integration fine salt particle reclamation device according to claim 1, it is characterised in that：The saline mixture charging
Mouth is connected to the drip pan of the reciprocal lower part of screen of reciprocating dewaterer, and not separated deposition saline mixture feed inlet is connected to past
Compound dewaterer enters salt hopper bottom.
3. integration fine salt particle reclamation device according to claim 1, it is characterised in that：Net formula nylon tape feeding end is set
To put below feed opening, for net formula nylon tape by extending obliquely below feed opening, the discharge end of net formula nylon tape, which is set, scrapes salt plate,
Centrifuge is set below the discharge end.
4. integration fine salt particle reclamation device according to claim 1, it is characterised in that：Set below the feed opening
Centrifuge.
5. integration fine salt particle reclamation device according to claim 1, it is characterised in that：Net formula nylon tape feeding end is set
Put below feed opening, the discharge end of net formula nylon tape, which is set, scrapes salt plate, and driving device is set in rack, and driving device connection is driven
Dynamic roller, the net formula nylon tape are arranged in the driven roller, and vacuum chamber, vacuum chamber connection are set below the net formula nylon tape
Vacuum extractor, vacuum chamber connection gas and water separator, the gas and water separator connect catch basin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711356351.6A CN107899278A (en) | 2017-12-16 | 2017-12-16 | Integrated fine salt particle reclamation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711356351.6A CN107899278A (en) | 2017-12-16 | 2017-12-16 | Integrated fine salt particle reclamation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107899278A true CN107899278A (en) | 2018-04-13 |
Family
ID=61870079
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711356351.6A Pending CN107899278A (en) | 2017-12-16 | 2017-12-16 | Integrated fine salt particle reclamation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107899278A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113750646A (en) * | 2021-10-15 | 2021-12-07 | 大连盐化集团有限公司 | Movable combined brine separation system |
| CN113769477A (en) * | 2021-10-15 | 2021-12-10 | 大连盐化集团有限公司 | Combined brine separation system |
| CN113750646B (en) * | 2021-10-15 | 2024-05-10 | 大连盐化集团有限公司 | Mobile combined brine separation system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202173844U (en) * | 2011-08-01 | 2012-03-28 | 北京中环嘉诚环境工程有限公司 | Reaction, sedimentation and filtration integrated device |
| CN202590500U (en) * | 2012-01-09 | 2012-12-12 | 宝山钢铁股份有限公司 | Silicon mud removing device in strip steel surface cleaning agent |
| CN205269231U (en) * | 2015-12-14 | 2016-06-01 | 河南晋开化工投资控股集团有限责任公司 | Coal is pulp water filtration system for gasification |
| CN206700929U (en) * | 2017-03-04 | 2017-12-05 | 天津市滨海新区兴宏达石油设备有限公司 | A kind of oil field extracted water settling tank water dispensing apparatus |
| CN208003533U (en) * | 2017-12-16 | 2018-10-26 | 大连盐化集团有限公司 | A kind of integration fine salt particle reclamation device |
-
2017
- 2017-12-16 CN CN201711356351.6A patent/CN107899278A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202173844U (en) * | 2011-08-01 | 2012-03-28 | 北京中环嘉诚环境工程有限公司 | Reaction, sedimentation and filtration integrated device |
| CN202590500U (en) * | 2012-01-09 | 2012-12-12 | 宝山钢铁股份有限公司 | Silicon mud removing device in strip steel surface cleaning agent |
| CN205269231U (en) * | 2015-12-14 | 2016-06-01 | 河南晋开化工投资控股集团有限责任公司 | Coal is pulp water filtration system for gasification |
| CN206700929U (en) * | 2017-03-04 | 2017-12-05 | 天津市滨海新区兴宏达石油设备有限公司 | A kind of oil field extracted water settling tank water dispensing apparatus |
| CN208003533U (en) * | 2017-12-16 | 2018-10-26 | 大连盐化集团有限公司 | A kind of integration fine salt particle reclamation device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113750646A (en) * | 2021-10-15 | 2021-12-07 | 大连盐化集团有限公司 | Movable combined brine separation system |
| CN113769477A (en) * | 2021-10-15 | 2021-12-10 | 大连盐化集团有限公司 | Combined brine separation system |
| CN113750646B (en) * | 2021-10-15 | 2024-05-10 | 大连盐化集团有限公司 | Mobile combined brine separation system |
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|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180413 |