CN204193854U - A kind of continuous high-efficient Nacl dissolver - Google Patents
A kind of continuous high-efficient Nacl dissolver Download PDFInfo
- Publication number
- CN204193854U CN204193854U CN201420594251.2U CN201420594251U CN204193854U CN 204193854 U CN204193854 U CN 204193854U CN 201420594251 U CN201420594251 U CN 201420594251U CN 204193854 U CN204193854 U CN 204193854U
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- dissolvers
- salt
- pipeline
- blending tank
- pipe
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Abstract
The utility model relates to a kind of continuous high-efficient Nacl dissolver, comprise salt feed bin and blending tank, salt bin blanking mouth connects blending tank, also comprise star-like blanking device, screw crusher, salt solution ratio adjusting valve, brine pump, first pipeline dissolvers and second pipe dissolvers, salt bin blanking mouth connects screw crusher import by pipeline, and the pipeline between salt feed bin and screw crusher is provided with star-like blanking device, screw crusher outlet connects the charging aperture of blending tank, the charging aperture of blending tank also connects water inlet pipe simultaneously, water inlet pipe is provided with salt solution ratio adjusting valve, the discharging opening of blending tank is sequentially connected in series the first pipeline dissolvers and second pipe dissolvers, and the connecting pipe between blending tank and the first pipeline dissolvers is provided with brine pump, the discharge nozzle of pipeline dissolvers leads to alkaline workshop, the utility model product is cost-saving, minimizing is taken up an area, salt solution without interruption, and salt and water eurythmy, be applicable to each large-scale alkali factory.
Description
Technical field
The utility model belongs to field of chemical equipment, relates to a kind of dissolver, specifically a kind of continuous high-efficient Nacl dissolver.
Background technology
Current alkali factory all dissolves so that rough salt amount is added in groove tank the method carrying out stirring, the method this small-sized alkali factory still can, and for large-scale alkali factory, due to huge by the salt water yield, this then needs to prepare a large amount of large-scale dissolved salt grooves or tank, and not only occupation of land is many, cost is high, and salt impurity can amass in bottom land, cause the interior easily salt scale coagulation of groove, thus cause salt dissolving tank to need often cleaning, affect and produce and add the amount of labour to workman; Meanwhile, salt solution ratio cannot carry out strict control, directly impacts the output of alkali and product quality.
Chinese patent CN2580302 discloses " large-sized boiler automatic stirring salt dissolving device " and the patent provides a kind of large-sized boiler automatic stirring salt dissolution equipment, although this equipment can accomplish automatic stirring and quick dissolved salt, but salt dissolution rate does not reach 100% all the time, and the dissolved salt time is longer, often a large amount of water wastes.
Chinese patent CN101703899A discloses " mixing dissolver ", mixing dissolver comprises mixing section, mixing section rear end is connected with lysing segment, and this apparatus structure is reasonable, completes more than two strands media and first carry out premixed in an equipment, then dissolve, favorable working performance, simple to operate, pressure is little, safeguard easily, the feature such as not easily scab; But this mixing dissolver meltage is restricted, and medium amount is large, also can scab; And automatically can not regulate the ratio of medium, be not suitable for a large amount of medium continuity and dissolve.
Utility model content
Technical problem to be solved in the utility model is, overcome the shortcoming of prior art, a kind of continuous high-efficient Nacl dissolver be provided, the utility model product is cost-saving, reduce take up an area, salt solution without interruption, and salt and water eurythmy, be applicable to each large-scale alkali factory.
In order to solve above technical problem, the utility model provides a kind of continuous high-efficient Nacl dissolver, comprise salt feed bin and blending tank, salt bin blanking mouth connects blending tank, also comprise star-like blanking device, screw crusher, salt solution ratio adjusting valve, brine pump, first pipeline dissolvers and second pipe dissolvers, salt bin blanking mouth connects screw crusher import by pipeline, and the pipeline between salt feed bin and screw crusher is provided with star-like blanking device, screw crusher outlet connects the charging aperture of blending tank, the charging aperture of blending tank also connects water inlet pipe simultaneously, water inlet pipe is provided with salt solution ratio adjusting valve, the discharging opening of blending tank is sequentially connected in series the first pipeline dissolvers and second pipe dissolvers, and the connecting pipe between blending tank and the first pipeline dissolvers is provided with brine pump, the discharge nozzle of pipeline dissolvers leads to alkaline workshop.
The technical scheme that the utility model limits further is:
Aforementioned star-like blanking device and salt solution ratio adjusting valve are controlled by pneumatic interlocking, adopt pneumatic flowrate control valve; First pipeline dissolvers and second pipe dissolvers comprise blade, interior pipe, outer tube and transmissometer respectively, outer tube is cylindrical seal barrel structure and vertically arranges, interior pipe vertically extend into outer tube, on the outer wall that blade is welded on interior pipe and within centered by pipe to surrounding scattering device, be provided with transmissometer in outer tube; Blade is the laminated structure of graphite carbon plate, resin blade, glass fibre, carbon fiber or aluminum alloy; Salt solution ratio adjusting valve both sides on water inlet pipe are respectively equipped with a water adjusting valve.
The beneficial effects of the utility model are:
The utility model utilizes star-like blanking device to control salt amount, the ratio of salt and water is interlocked by control valve simultaneously, and when star-like blanking device flow is excessive, the flow signal teletransmission of increasing is to pneumatic control valve, and pneumatic control valve increases open degree, increases the flow of water; When star-like blanking device flow is too small, the flow signal teletransmission of minimizing is to pneumatic control valve, and pneumatic control valve reduces open degree, reduces the flow of water; Thus regulate the amount of salt and water in proportion, accurate control, flexible modulation salt and the object of the ratio of water can be reached, promote to dissolve fully, guarantee product quality;
The utility model not only utilizes screw crusher by broken for caking salt to dissolve, and to change dissolving tank be that pipeline carries out salt dissolving, in pipeline dissolvers, establish blade outside pipe simultaneously, accelerate the dissolving of salt, and look into salt dissolving situation by transmissometer sight, salt solution ratio can be adjusted in time; Salt slurry by managing in pipeline dissolvers, then enters outer tube, enters next pipeline dissolvers, has carried out more efficiently dissolving to salt; And the salt water yield that the duct length of dissolvers can need according to the dissolution velocity of salt and alkaline is determined, convenient with repacking, not only cost-saving, and substantially increase production efficiency.
The utility model device in use, is different from traditional salt dissolving tank, and impurity is the long-pending end not easily, and not easily salt scale coagulation in groove, does not need normal cleaning, save the amount of labour of workman; And the large large-scale alkali factory of salt dosage also can avoid arranging huge salt dissolving tank, can realize completely its when not increasing new equipment steady control salt solution than and salt solution without interruption, make production more safe and reliable; The utility model device not only there will not be because salt dissolving tank prodelta clay what too much affects salt solution supply, causes stopping production, and supplies salt solution for continous-stable and provide guarantee.
Accompanying drawing explanation
Fig. 1 is the connection diagram of continuous high-efficient Nacl dissolver of the present utility model;
Wherein, 1-salt feed bin, the star-like blanking device of 2-, 3-screw crusher, 4-salt solution ratio adjusting valve, 5-blending tank, 6-brine pump, 7-blade, pipe in 8-, 9-outer tube, 10-transmissometer, 11-first pipeline dissolvers, 12-second pipe dissolvers.
Detailed description of the invention
Below by way of specific embodiment, detailed description of the invention of the present utility model is described in further detail.
The PE type product that said spiral disintegrating machine selects Huading, Weifang heavy industry machinery Science and Technology Ltd. to produce;
The YJD-6A type product that aforementioned Star-like unloader selects company of Gong Cheng vibratory equipment Co., Ltd of Xinxiang City to produce;
The ZJHS type pneumatic control valve that aforementioned pneumatic flowrate control valve selects Shanghai Ye Dong valve Co., Ltd to produce;
The ZD-100G type product that aforementioned transmissometer selects Dalian Dong Lian instrument and meter Co., Ltd to produce.
embodiment 1
The present embodiment provides a kind of continuous high-efficient Nacl dissolver, structure as shown in Figure 1, comprise salt feed bin 1 and blending tank 5, salt feed bin 1 feed opening connects blending tank 5, also comprise star-like blanking device 2, screw crusher 3, salt solution ratio adjusting valve 4, brine pump 6, first pipeline dissolvers 11 and second pipe dissolvers 12, salt feed bin 1 feed opening connects screw crusher 3 import by pipeline, and the pipeline between salt feed bin 1 and screw crusher 3 is provided with star-like blanking device 2, screw crusher 3 exports the charging aperture connecting blending tank 5, the charging aperture of blending tank 5 also connects water inlet pipe simultaneously, water inlet pipe is provided with salt solution ratio adjusting valve 4, the discharging opening of blending tank 5 is sequentially connected in series the first pipeline dissolvers 11 and second pipe dissolvers 12, and the connecting pipe between blending tank 5 and the first pipeline dissolvers 11 is provided with brine pump 6, the discharge nozzle of pipeline dissolvers leads to alkaline workshop.
Aforementioned star-like blanking device 2 is controlled by pneumatic interlocking with salt solution ratio adjusting valve 4, adopts pneumatic flowrate control valve; First pipeline dissolvers 11 and second pipe dissolvers 12 comprise blade 7, interior pipe 8, outer tube 9 and transmissometer 10 respectively, outer tube 9 is cylindrical seal barrel structure and vertically arranges, it is inner that interior pipe 8 vertically extend into outer tube 9, on the outer wall that blade 7 is welded on interior pipe 8 and within centered by pipe 8 to surrounding scattering device, be provided with transmissometer 10 in outer tube 9; Blade 7 is the laminated structure of glass fibre; Salt solution ratio adjusting valve 4 both sides on water inlet pipe are respectively equipped with a water adjusting valve.
This product in use, star-like blanking device 2 is first utilized to control salt amount, the ratio of salt and water is interlocked by control valve simultaneously, follow-uply can accurately to control, the ratio of flexible modulation salt and water, then utilize screw crusher 3 by broken for caking salt to dissolve, next changing dissolving tank is that pipeline carries out salt dissolving, in pipeline dissolvers, establish blade 7 outside pipe simultaneously, accelerate the dissolving of salt, and look into salt dissolving situation by transmissometer 10 sight, salt solution ratio can be adjusted in time; Salt slurry, by pipe 8 in pipeline dissolvers, then enters outer tube 9, after enter next pipeline dissolvers, more efficiently dissolving has been carried out to salt; And the salt water yield that the duct length of dissolvers can need according to the dissolution velocity of salt and alkaline is determined, convenient with repacking, not only cost-saving, and substantially increase production efficiency.
Concrete operation method: first, check whole equipment sealing, guarantee equipment and junction thereof do not have leakage scenarios, close all valves; In salt feed bin 1, add appropriate salt material, open star-like blanking device 2 and screw crusher 3, preliminary pulverizing is carried out to salt material and then enters blending tank 5, open the water adjusting valve on salt solution ratio adjusting valve 4 and both sides thereof simultaneously, discharge water and enter in blending tank 5; Then, open brine pump 6, saline mixture is pushed ahead, saline mixture to be sent in the first pipeline dissolvers 11 in pipe; When aforementioned saline mixture flows into outer tube from interior pipe, stir through blade, dissolve further, then enter second pipe dissolvers 12 through pipeline, carry out more efficiently dissolving, observe dissolving situation by transmissometer simultaneously and adjust salt solution ratio in time by salt solution ratio adjusting valve; Finally, the salt solution that the discharge nozzle of second pipe dissolvers 12 flows out is transported to alkaline workshop.
Above embodiment is only and technological thought of the present utility model is described; protection domain of the present utility model can not be limited with this; every technological thought according to the utility model proposes, any change that technical scheme basis is done, all falls within the utility model protection domain.
Claims (5)
1. a continuous high-efficient Nacl dissolver, comprise salt feed bin (1) and blending tank (5), described salt feed bin (1) feed opening connects described blending tank (5), it is characterized in that, also comprise star-like blanking device (2), screw crusher (3), salt solution ratio adjusting valve (4), brine pump (6), first pipeline dissolvers (11) and second pipe dissolvers (12), described salt feed bin (1) feed opening connects described screw crusher (3) import by pipeline, and the pipeline between described salt feed bin (1) and described screw crusher (3) is provided with star-like blanking device (2), described screw crusher (3) outlet connects the charging aperture of described blending tank (5), the charging aperture of described blending tank (5) also connects water inlet pipe simultaneously, described water inlet pipe is provided with salt solution ratio adjusting valve (4), the discharging opening of described blending tank (5) is sequentially connected in series the first pipeline dissolvers (11) and second pipe dissolvers (12), and the connecting pipe between described blending tank (5) and described first pipeline dissolvers (11) is provided with brine pump (6), the discharge nozzle of described pipeline dissolvers leads to alkaline workshop.
2. continuous high-efficient Nacl dissolver according to claim 1, is characterized in that, described star-like blanking device (2) and described salt solution ratio adjusting valve (4) are controlled by pneumatic interlocking, adopts pneumatic flowrate control valve.
3. continuous high-efficient Nacl dissolver according to claim 1, it is characterized in that, described first pipeline dissolvers (11) and second pipe dissolvers (12) comprise blade (7) respectively, interior pipe (8), outer tube (9) and transmissometer (10), described outer tube (9) is the also vertically setting of cylindrical seal barrel structure, it is inner that described interior pipe (8) vertically extend into described outer tube (9), on the outer wall that described blade (7) is welded on described interior pipe (8) and within centered by pipe (8) to surrounding scattering device, transmissometer (10) is provided with in described outer tube (9).
4. continuous high-efficient Nacl dissolver according to claim 3, is characterized in that, described blade (7) is graphite carbon plate, the laminated structure of resin blade, glass fibre, carbon fiber or aluminum alloy.
5. continuous high-efficient Nacl dissolver according to claim 1, is characterized in that, salt solution ratio adjusting valve (4) both sides on described water inlet pipe are respectively equipped with a water adjusting valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420594251.2U CN204193854U (en) | 2014-10-14 | 2014-10-14 | A kind of continuous high-efficient Nacl dissolver |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420594251.2U CN204193854U (en) | 2014-10-14 | 2014-10-14 | A kind of continuous high-efficient Nacl dissolver |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204193854U true CN204193854U (en) | 2015-03-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420594251.2U Withdrawn - After Issue CN204193854U (en) | 2014-10-14 | 2014-10-14 | A kind of continuous high-efficient Nacl dissolver |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204193854U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104307418A (en) * | 2014-10-14 | 2015-01-28 | 江苏金象赛瑞化工科技有限公司 | Continuous high-efficiency industrial salt dissolving device and operating method thereof |
| CN106190129A (en) * | 2016-08-31 | 2016-12-07 | 江阴市化学试剂厂有限公司 | Ferric chloride ITO etching liquid compounding system |
| CN106244147A (en) * | 2016-08-31 | 2016-12-21 | 江阴市化学试剂厂有限公司 | ITO etching liquid compounding system |
-
2014
- 2014-10-14 CN CN201420594251.2U patent/CN204193854U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104307418A (en) * | 2014-10-14 | 2015-01-28 | 江苏金象赛瑞化工科技有限公司 | Continuous high-efficiency industrial salt dissolving device and operating method thereof |
| CN106190129A (en) * | 2016-08-31 | 2016-12-07 | 江阴市化学试剂厂有限公司 | Ferric chloride ITO etching liquid compounding system |
| CN106244147A (en) * | 2016-08-31 | 2016-12-21 | 江阴市化学试剂厂有限公司 | ITO etching liquid compounding system |
| CN106244147B (en) * | 2016-08-31 | 2018-05-11 | 江阴市化学试剂厂有限公司 | ITO etching liquid compounding systems |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150311 Effective date of abandoning: 20160427 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |