CN203469917U - Concentrated solution diluting device - Google Patents
Concentrated solution diluting device Download PDFInfo
- Publication number
- CN203469917U CN203469917U CN201320506145.XU CN201320506145U CN203469917U CN 203469917 U CN203469917 U CN 203469917U CN 201320506145 U CN201320506145 U CN 201320506145U CN 203469917 U CN203469917 U CN 203469917U
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- China
- Prior art keywords
- concentrated solution
- weak solution
- tank
- solution
- pipe
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Abstract
The utility model relates to a concentrated solution diluting device. The device comprises a water tank, a concentrated solution temporary storage tank, a weak solution batch tank, a weak solution storage tank, a water intake pipe, a concentrated solution charge pipe, a weak solution charge pipe, a discharge pipe and a liquidometer, wherein the water intake pipe is used for connecting the water tank and the weak solution batch tank; the concentrated solution charge pipe is used for connecting the concentrated solution temporary storage tank and the weak solution batch tank; the weak solution charge pipe is used for connecting the weak solution batch tank and the weak solution storage tank; the discharge pipe is connected to the weak solution storage tank; the liquidometer is arranged on the weak solution batch tank and is used for detecting the inner liquid level of the weak solution batch tank; the water intake pipe is provided with a water intake general valve; the concentrated solution charge pipe is sequentially provided with a charge pump and a concentrated solution charge valve along the trend of the liquid level in the concentrated solution charge pipe; the weak solution charge pipe is provided with a weak solution charge valve; the discharge pipe is provided with a discharge valve. The device provided by the utility model is simple in structure, simple and convenient to operate, and can dispose the weak solution concentration accurately.
Description
Technical field
The utility model relates to a kind of for online the solution of high concentration being accurately diluted to the air mix facilities of desired concn.
Background technology
The most structure of existing concentrated solution air mix facilities arranges complexity, the air mix facilities of inconvenient operation, diluent concentration after dilution is often not accurate, and existing concentrated solution air mix facilities Chang Youyi platform measuring pump adds quantitative concentrated solution in pipeline, under detecting, a flowmeter adds quantitative water in same segment pipe, the two adds storage tank again after a blender mixes, the addition that adopts flowmeter or flow pump to control feed liquid can not be controlled the concentration of dilution very accurately, and once flowmeter or flow pump go wrong, to cause the concentration of whole dilution not accurate so, and then waste raw material.On the other hand, if concentrated solution will be diluted to another concentration, need flowmeter and flow pump to reset its parameter, complicated operation is loaded down with trivial details.
Summary of the invention
Technical problem to be solved in the utility model is to overcome the deficiencies in the prior art, and a kind of simple in structure, easy to operate, concentrated solution air mix facilities that can precisely configure weak solution concentration is provided.
For solving the problems of the technologies described above, the utility model adopts following technical scheme:
A kind of concentrated solution air mix facilities, this device comprises water pot, concentrated solution is kept in tank, weak solution batch tank, weak solution storage tank, the water inlet pipe that connects described water pot and described weak solution batch tank, the concentrated solution feed pipe that connects the temporary tank of described concentrated solution and described weak solution batch tank, the weak solution feed pipe that connects described weak solution batch tank and described weak solution storage tank, be connected to the discharge nozzle on described weak solution storage tank, be arranged on described weak solution batch tank the liquid level gauge for detection of liquid level in described weak solution batch tank, described water inlet pipe is provided with into water total valve, trend along feed liquid in described concentrated solution feed pipe on described concentrated solution feed pipe is provided with charge pump and concentrated solution material inlet valve successively, described weak solution feed pipe is provided with weak solution material inlet valve, described discharge nozzle is provided with outlet valve.
Between described water inlet pipe and described concentrated solution feed pipe, be connected with tube connector, the link position of described tube connector and described concentrated solution feed pipe is positioned at the upstream of described charge pump, is provided with tube connector valve on described tube connector.
On described concentrated solution feed pipe and the upstream that is positioned at described link position be provided with stop valve.
Between described water inlet pipe and described weak solution batch tank, be provided with the second water inlet pipe that the first water inlet pipe, caliber are less than described the first water inlet pipe, described the first water inlet pipe is provided with the first inlet valve, and described the second water inlet pipe is provided with the second inlet valve.
Described concentrated solution feed pipe is provided with flow monitoring instrument.
The temporary tank of described concentrated solution is provided with drainage conduit, and described drainage conduit is provided with drain valve.
In described weak solution batch tank, be provided with agitating device.
The capacity of described weak solution batch tank is less than described weak solution storage tank.
Due to the enforcement of above technical scheme, the utility model compared with prior art has following advantages:
The utility model device arranges liquid level gauge for detection of the liquid level in weak solution batch tank on weak solution batch tank, level condition in the observation weak solution batch tank of intuitive and convenient, adopt liquid level gauge to control feed liquid and the water adding in weak solution batch tank, can accurately control addition, make the weak solution concentration after final dilution accurate.
The utility model device simplicity of design, simple, convenient, can precisely configure weak solution concentration, greatly reduce the wasting phenomenon of concentrated solution mother liquor.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Wherein, 1, the temporary tank of concentrated solution; 2, weak solution batch tank; 3, weak solution storage tank; 4, water inlet pipe; 5, water inlet total valve; 6, concentrated solution feed pipe; 7, concentrated solution material inlet valve; 8, charge pump; 9, weak solution feed pipe; 10, weak solution material inlet valve; 11, discharge nozzle; 12, outlet valve; 13, the first water inlet pipe; 14, the second water inlet pipe; 15, the first inlet valve; 16, the second inlet valve; 17, tube connector; 18, tube connector valve; 19, stop valve; 20, drainage conduit; 21, blow-off valve; LT, concentrated solution liquid level gauge; LPT1, water liquid level gauge; LPT2, weak solution liquid level gauge; FS, flow monitoring instrument.
The specific embodiment
Below in conjunction with Figure of description, the utility model is described further:
As shown in Figure 1, a kind of concentrated solution air mix facilities, this device comprises water pot, the temporary tank 1 of concentrated solution, weak solution batch tank 2, weak solution storage tank 3.
Concrete structure and connected mode: between water pot and weak solution batch tank 2, be connected with water inlet pipe 4, water inlet pipe 4 is provided with into water total valve 5; Between the temporary tank 1 of concentrated solution and weak solution batch tank 2, be connected with concentrated solution feed pipe 6, the trend along concentrated solution feed pipe 6 interior feed liquids on concentrated solution feed pipe 6 is provided with charge pump 8 and concentrated solution material inlet valve 7 successively; Between weak solution batch tank 2 and weak solution storage tank 3, be connected with weak solution feed pipe 9, weak solution feed pipe 9 is provided with weak solution material inlet valve 10, is provided with the liquid level gauge for detection of weak solution batch tank 2 interior liquid levels on weak solution batch tank 2; On weak solution storage tank 3, be connected with discharge nozzle 11, discharge nozzle 11 is provided with outlet valve 12.
In the present embodiment, between water inlet pipe 4 and concentrated solution feed pipe 6, be connected with tube connector 17, the link position of tube connector 17 and concentrated solution feed pipe 6 is positioned at the upstream of charge pump 8, is provided with tube connector valve 18 on tube connector 17.On concentrated solution feed pipe 6 and be positioned at tube connector 17 and be provided with stop valve 19 with the upstream of concentrated solution feed pipe 6 link positions.
In the present embodiment, between water inlet pipe 4 and weak solution batch tank 2, be provided with the second water inlet pipe 14, the first water inlet pipes 13 that the first water inlet pipe 13, caliber be less than the first water inlet pipe 13 and be provided with the first inlet valve 15, the second water inlet pipes and be provided with the second inlet valve 16.
In the present embodiment, concentrated solution feed pipe 6 is provided with flow monitoring instrument FS, for monitoring the situation of flowing through of concentrated solution feed pipe 6 interior feed liquids.
In the present embodiment, the temporary tank 1 of concentrated solution is provided with drainage conduit 20, and drainage conduit 20 is provided with blow-off valve 21.In weak solution batch tank 2, be provided with agitating device, the water and the concentrated solution that for stirring, enter weak solution batch tank 2 make its dilution.The capacity of weak solution batch tank 2 is less than weak solution storage tank 3.
As shown in Figure 1, on weak solution batch tank 2, be provided with water liquid level gauge LPT1, concentrated solution liquid level gauge LT, be respectively used to detect the liquid level of weak solution batch tank 2 interior water and the liquid level of concentrated solution.On weak solution storage tank 3, be provided with weak solution liquid level gauge LPT2, for detection of the liquid level of weak solution storage tank 3 interior weak solutions.
The use procedure of the utility model device: concentrated solution liquid level gauge LT is set to concentrated solution liquid level set amount, open all valves and charge pump 8 on concentrated solution feed pipe 6, concentrated solution in the temporary tank 1 of concentrated solution is pumped into weak solution batch tank 2 until concentrated solution liquid level set amount is closed all valves on concentrated solution feed pipe 6.Then water liquid level gauge LPT1 is set to water liquid level set amount, then open all valves on water inlet pipe 4, the first water inlet pipe 13, the second water inlet pipe 14, water in water pot enters in weak solution batch tank 2, when reaching soon water liquid level set amount, close all valves on the first water inlet pipe 13, only stay the second water inlet pipe 14 water inlets until water liquid level set amount is closed all valves on water inlet pipe 4 and the second water inlet pipe 14.When concentrated solution and water all reach set amount separately, open agitating device, concentrated solution and water are evenly mixed and diluted in weak solution batch tank 2.Finally open weak solution material inlet valve 10, the weak solution in weak solution batch tank 2 enter in weak solution storage tank 3, store stand-by.Repeat above-mentioned steps, until weak solution reaches a certain amount of in weak solution storage tank 3, the weak solution in weak solution storage tank 3 is delivered to production line by discharge nozzle 11.
Above the utility model is described in detail; its object is to allow the personage who is familiar with this art can understand content of the present utility model and be implemented; can not limit protection domain of the present utility model with this; all equivalences of doing according to Spirit Essence of the present utility model change or modify, and all should be encompassed in protection domain of the present utility model.
Claims (8)
1. a concentrated solution air mix facilities, it is characterized in that, this device comprises water pot, concentrated solution is kept in tank, weak solution batch tank, weak solution storage tank, the water inlet pipe that connects described water pot and described weak solution batch tank, the concentrated solution feed pipe that connects the temporary tank of described concentrated solution and described weak solution batch tank, the weak solution feed pipe that connects described weak solution batch tank and described weak solution storage tank, be connected to the discharge nozzle on described weak solution storage tank, be arranged on described weak solution batch tank the liquid level gauge for detection of liquid level in described weak solution batch tank, described water inlet pipe is provided with into water total valve, trend along feed liquid in described concentrated solution feed pipe on described concentrated solution feed pipe is provided with charge pump and concentrated solution material inlet valve successively, described weak solution feed pipe is provided with weak solution material inlet valve, described discharge nozzle is provided with outlet valve.
2. concentrated solution air mix facilities according to claim 1, it is characterized in that, between described water inlet pipe and described concentrated solution feed pipe, be connected with tube connector, the link position of described tube connector and described concentrated solution feed pipe is positioned at the upstream of described charge pump, is provided with tube connector valve on described tube connector.
3. concentrated solution air mix facilities according to claim 2, is characterized in that, on described concentrated solution feed pipe and the upstream that is positioned at described link position be provided with stop valve.
4. concentrated solution air mix facilities according to claim 1, it is characterized in that, between described water inlet pipe and described weak solution batch tank, be provided with the second water inlet pipe that the first water inlet pipe, caliber are less than described the first water inlet pipe, described the first water inlet pipe is provided with the first inlet valve, and described the second water inlet pipe is provided with the second inlet valve.
5. concentrated solution air mix facilities according to claim 1, is characterized in that, described concentrated solution feed pipe is provided with flow monitoring instrument.
6. concentrated solution air mix facilities according to claim 1, is characterized in that, the temporary tank of described concentrated solution is provided with drainage conduit, and described drainage conduit is provided with drain valve.
7. concentrated solution air mix facilities according to claim 1, is characterized in that, in described weak solution batch tank, is provided with agitating device.
8. concentrated solution air mix facilities according to claim 1, is characterized in that, the capacity of described weak solution batch tank is less than described weak solution storage tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320506145.XU CN203469917U (en) | 2013-08-19 | 2013-08-19 | Concentrated solution diluting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320506145.XU CN203469917U (en) | 2013-08-19 | 2013-08-19 | Concentrated solution diluting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203469917U true CN203469917U (en) | 2014-03-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320506145.XU Expired - Lifetime CN203469917U (en) | 2013-08-19 | 2013-08-19 | Concentrated solution diluting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203469917U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104481435A (en) * | 2014-12-16 | 2015-04-01 | 四机赛瓦石油钻采设备有限公司 | Batch-type liquid agent adding system and liquid adding method |
| CN110203958A (en) * | 2019-05-31 | 2019-09-06 | 青岛海湾集团有限公司 | Total reduzate is eliminated to the method for appearance effects in a kind of ammonia-soda process calcium chloride process |
| CN111410279A (en) * | 2020-05-21 | 2020-07-14 | 重庆昕晟环保科技有限公司 | Method for supplementing chlorine for secondary water supply and storage equipment |
-
2013
- 2013-08-19 CN CN201320506145.XU patent/CN203469917U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104481435A (en) * | 2014-12-16 | 2015-04-01 | 四机赛瓦石油钻采设备有限公司 | Batch-type liquid agent adding system and liquid adding method |
| CN110203958A (en) * | 2019-05-31 | 2019-09-06 | 青岛海湾集团有限公司 | Total reduzate is eliminated to the method for appearance effects in a kind of ammonia-soda process calcium chloride process |
| CN111410279A (en) * | 2020-05-21 | 2020-07-14 | 重庆昕晟环保科技有限公司 | Method for supplementing chlorine for secondary water supply and storage equipment |
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Granted publication date: 20140312 |
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