CN108301489B - Pipeline system and control method thereof - Google Patents
Pipeline system and control method thereof Download PDFInfo
- Publication number
- CN108301489B CN108301489B CN201810135430.2A CN201810135430A CN108301489B CN 108301489 B CN108301489 B CN 108301489B CN 201810135430 A CN201810135430 A CN 201810135430A CN 108301489 B CN108301489 B CN 108301489B
- Authority
- CN
- China
- Prior art keywords
- water
- valve
- water pipe
- tank
- pipe
- 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.)
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Links
- 238000000034 method Methods 0.000 title claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 239
- 239000003513 alkali Substances 0.000 claims abstract description 32
- 239000002002 slurry Substances 0.000 claims abstract description 28
- 238000011084 recovery Methods 0.000 claims abstract description 25
- 238000004140 cleaning Methods 0.000 claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 claims abstract description 14
- 239000002893 slag Substances 0.000 claims abstract description 8
- 230000001502 supplementing effect Effects 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims description 3
- 238000004064 recycling Methods 0.000 abstract description 3
- 239000013589 supplement Substances 0.000 abstract 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03F—SEWERS; CESSPOOLS
- E03F3/00—Sewer pipe-line systems
- E03F3/02—Arrangement of sewer pipe-lines or pipe-line systems
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
-
- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03F—SEWERS; CESSPOOLS
- E03F9/00—Arrangements or fixed installations methods or devices for cleaning or clearing sewer pipes, e.g. by flushing
- E03F9/007—Devices providing a flushing surge
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/005—Valves
Abstract
The invention discloses a pipeline system, which is characterized in that: the water tank comprises a water tank I, a water tank II, a water diversion tank, a water pump, a valve and a water pipe, wherein an alkali liquor recovery treatment unit is arranged in the water tank I, a water inlet and a slag discharge port are arranged on the outer side of the water tank I, the water inlet and the slag discharge port are respectively connected with the water pipe I and the water pipe II, the alkali liquor recovery treatment unit is connected with the top FV03 valve of the water diversion tank through a water pipe III, the water pipe III is provided with a branch water pipe IV, the water pipe IV is connected with a water outlet, the right side of the water diversion tank is provided with a FV04 valve, the left side of the water diversion tank is provided with a FV08 valve, the FV04 valve is connected with the water tank II through a water pipe V, the FV08 valve is connected with the water pump through a water pipe V, and the water pump is connected with the water pipe IV through a water pipe V; the control method of the pipeline system comprises water production, cleaning, water supplementing and exhaust. The slurry recycling treatment is realized, the produced water is recycled, and the system can automatically clean, supplement water and exhaust, so that the environment is protected, the resources are saved, and the cost is reduced.
Description
Technical Field
The invention relates to a pipeline system, in particular to a system for producing water, cleaning, supplementing water and exhausting in a pipeline.
Background
The slurry produced by the printing and dyeing mill contains a large amount of heavy metals and alkali, the direct discharge can pollute the environment, in order to recycle alkali-containing liquid in the slurry, an alkali liquor recycling device is designed for the slurry, and the device comprises various devices, such as a water pump, a water diversion tank, various valves, pipelines and the like.
Disclosure of Invention
The invention aims to provide a pipeline system, which can recycle alkali liquor in slurry, protect the environment, recycle produced water in the slurry by controlling a valve in a pipeline, and can automatically clean the pipeline and an internal device, supply water and timely exhaust the interior of the system.
In order to achieve the above purpose, the invention adopts the following technical scheme: the utility model provides a pipe-line system, includes water tank one, water tank two, diversion jar, water pump, valve and water pipe, water tank one inside is provided with alkali lye recovery processing unit, water tank one outside is provided with water inlet, slag tap, connect water pipe one, water pipe two in water inlet, the slag tap respectively, alkali lye recovery processing unit pass through water pipe three with diversion jar top FV03 valve links to each other, water pipe three is provided with branch water pipe four, water pipe four connects the delivery port, diversion jar both sides are provided with FV04 valve, FV08 valve, FV04 valve through water pipe five with water tank two links to each other, FV08 valve through water pipe six with the water pump links to each other, the water pump is through water pipe seven with water pipe four links to each other.
In the technical scheme, the number of the water pumps is two.
In the technical scheme, the junction of the fourth water pipe and the seventh water pipe is a node, and FV05 valves and FV02 valves are respectively arranged in front of and behind the node.
In the technical scheme, the joint is connected with the FV05 valve through the water pipe eight and the water tank II, and the FV06 valve is arranged on the water pipe eight.
In the technical scheme, the FV01 valve is arranged on the second water pipe, the branch water pipe is arranged on the third water pipe, and the FV07 valve is installed.
In order to achieve the above purpose, the invention adopts the following technical scheme: a control method of a pipeline system comprises water production, cleaning, water supplementing and exhaust.
In the above technical scheme, the water production control step comprises: opening FV03 valve, FV08 valve and FV05 valve, the flow direction of slurry and produced water is: the slurry enters the first water tank from the first water pipe, the alkali liquor recovery processing unit is used for processing the slurry, the processed slurry extracts alkali liquor, the slurry is concentrated and stored in the first water tank, after the slurry is concentrated to the upper limit of processing, the slurry is discharged from the second water pipe from the FV01 valve, produced water enters the third water pipe from the upper part of the alkali liquor recovery processing unit, enters the diversion tank from the top of the diversion tank through the FV03 valve, flows to the water pump from the side edge of the diversion tank through the FV08 valve, and finally flows to the seventh water pipe, the FV05 valve and the fourth water pipe discharging equipment through the seventh water pipe.
In the above technical scheme, the cleaning control steps are as follows: opening FV02 valve FV04 valve FV08 valve, water flow direction in cleaning process is: the water flow is provided from the second water tank, enters the diversion tank through the FV04 valve through the water pipe five, flows out of the FV08 valve and enters the water pump, and finally enters the alkali liquor recovery processing unit through the fourth water pipe, the FV02 valve and the third water pipe, so that the inside of the alkali liquor recovery processing unit is cleaned.
In the above technical scheme, the water replenishing control step comprises: and opening the FV03 valve, the FV08 valve, the FV05 valve and the FV06 valve, wherein the water flow direction is increased in the water production process, and the water flows back to the second water tank from the fourth pipeline through the eighth pipeline.
In the above technical solution, the exhaust gas control step includes: the FV02 valve, the FV04 valve, the FV05 valve, the FV03 valve, the FV08 valve, and the FV07 valve are opened, and their water flow direction increases during cleaning to be discharged from the FV07 valve.
Due to the application of the technical scheme, compared with the prior art, the invention has the following advantages:
1. the invention has the advantages of simple connection relation between each part and the device and low production cost.
2. An alkali liquor recovery treatment unit is arranged in the first water tank, the slurry is treated by the alkali liquor recovery treatment unit, the obtained alkali liquor is recovered and utilized, the environment is protected, the obtained produced water is stored in the second water tank, the cyclic utilization is realized, and the resources are saved.
3. By controlling the FV03 valve, the FV04 valve and the FV08 valve on the water diversion tank, different processes of water production, cleaning, water supplementing, air exhaust and the like are realized, and the method is simple, convenient and easy to operate.
4. Two water pumps are arranged to provide power for water circulation.
Drawings
FIG. 1 is a schematic view of the water production of the present invention;
FIG. 2 is a schematic view of the cleaning of the present invention;
FIG. 3 is a schematic illustration of the water replenishment of the present invention;
fig. 4 is an exhaust schematic diagram of the present invention.
1, a first water tank; 2. a second water tank; 3. an alkali liquor recovery treatment unit; 4. a first water pipe; 5. a second water pipe; 6. a third water pipe; 7. a water pipe IV; 8. a fifth water pipe; 9. a water pipe six; 10. a water pipe seven; 11. a water pipe eight; 12. a water diversion tank; 13. and (3) a water pump.
Detailed Description
The invention is further described below with reference to the accompanying drawings and examples:
embodiment one: referring to fig. 1-4, a pipeline system comprises a first water tank 1, a second water tank 2, a diversion tank 12, a water pump 13, a valve and a water pipe, wherein an alkali liquor recovery processing unit 3 is arranged in the first water tank 1, a water inlet and a slag discharge port are arranged on the outer side of the first water tank 1, the first water pipe 4 and the second water pipe 5 are respectively connected in the water inlet and the slag discharge port, the alkali liquor recovery processing unit 3 is connected with the top FV03 valve of the diversion tank 12 through a third water pipe 6, the third water pipe 6 is provided with a branch water pipe four 7, the fourth water pipe 7 is connected with a water outlet, the right side of the diversion tank 12 is provided with a FV04 valve, the left side of the diversion tank 12 is provided with a FV08 valve, the FV04 valve is connected with the second water tank 2 through a fifth water pipe 8, the FV08 valve is connected with the water pump 13 through a sixth water pipe 9, and the water pump 13 is connected with the fourth water pipe 7 through a seventh water pipe 10. The connection relation of each part and the device is simple, the production cost is low, the alkali liquor recovery processing unit is arranged in the first water tank 1, the slurry is processed by the alkali liquor recovery processing unit, the obtained alkali liquor is recycled, the environment is protected, the obtained produced water is stored in the second water tank 2, the recycling is realized, and the resources are saved.
As shown in fig. 1, the number of the water pumps 13 is two, and the water circulation is powered.
As shown in fig. 1, the junction of the fourth water pipe 7 and the seventh water pipe 10 is a node, and FV05 valves and FV02 valves are respectively arranged in front of and behind the node.
As shown in fig. 1, the joint is connected with the FV05 valve via a water pipe eight 11 to the second water tank 2, and the FV06 valve is disposed on the water pipe eight 11.
As shown in fig. 1, the second water pipe 5 is provided with a FV01 valve, the third water pipe 6 is provided with a branch water pipe, and the FV07 valve is installed.
A control method of pipeline system includes water production, cleaning, water supplementing and air exhausting.
As shown in fig. 1, the water production control step comprises: opening FV03 valve, FV08 valve and FV05 valve, the flow direction of slurry and produced water is: the slurry enters the first water tank 1 from the first water pipe 4, the alkali liquor recovery processing unit is used for processing the slurry, alkali liquor is extracted from the processed slurry, the slurry is concentrated and stored in the first water tank 1, after the slurry is concentrated to the upper processing limit, the slurry is discharged from the second water pipe 5 by the FV01 valve, produced water enters the third water pipe 6 from the upper part of the alkali liquor recovery processing unit, enters the diversion tank 12 from the top of the diversion tank 12 through the FV03 valve, flows to the water pump 13 from the side edge of the diversion tank 12 through the FV08 valve, and finally flows to the seventh water pipe 10, the FV05 valve and the fourth water pipe 7 discharging equipment.
As shown in fig. 2, the cleaning control step includes: opening FV02 valve FV04 valve FV08 valve, water flow direction in cleaning process is: the water flow is provided from the water tank II 2, enters the diversion tank 12 from the water pipe V8 through the FV04 valve, flows out from the FV08 valve and enters the water pump 13, and finally enters the alkali liquor recovery processing unit from the water pipe V7, the FV02 valve and the water pipe V6 to clean the inside of the alkali liquor recovery processing unit.
As shown in fig. 3, the water replenishment control step is as follows: and opening the FV03 valve, the FV08 valve, the FV05 valve and the FV06 valve, wherein the water flow direction is increased in the water production process, and the water flows back to the water tank two 2 from the pipeline four through the pipeline eight.
As shown in fig. 4, the exhaust gas control step is: the FV02 valve, the FV04 valve, the FV05 valve, the FV03 valve, the FV08 valve, and the FV07 valve are opened, and their water flow direction increases during cleaning to be discharged from the FV07 valve.
The above embodiments are provided to illustrate the technical concept and features of the present invention and are intended to enable those skilled in the art to understand the content of the present invention and implement the same, and are not intended to limit the scope of the present invention. All equivalent changes or modifications made in accordance with the spirit of the present invention should be construed to be included in the scope of the present invention.
Claims (2)
1. A piping system, characterized in that: the water tank comprises a water tank I, a water tank II, a water diversion tank, a water pump, a valve and a water pipe, wherein an alkali liquor recovery treatment unit is arranged in the water tank I, a water inlet and a slag discharge port are formed in the outer side of the water tank I, the water inlet and the slag discharge port are respectively connected with the water pipe I and the water pipe II, the alkali liquor recovery treatment unit is connected with the FV03 valve at the top of the water diversion tank through a water pipe III, the water pipe III is provided with a branch water pipe IV, the water pipe IV is connected with a water outlet, the right side of the water diversion tank is provided with a FV04 valve, the left side of the water diversion tank is provided with a FV08 valve, the FV04 valve is connected with the water tank II through a water pipe V, the FV08 valve is connected with the water pump through a water pipe V, and the water pump is connected with the water pipe IV through a water pipe V;
the junction of the fourth water pipe and the seventh water pipe is a node, and an FV02 valve is arranged behind the node;
the junction of the fourth water pipe and the seventh water pipe is a node, and an FV05 valve is arranged in front of the node;
the second water pipe is provided with a FV01 valve;
the joint is connected with the FV05 valve through a water pipe eight which is provided with an FV06 valve;
a branch water pipe is arranged on the third water pipe, and an FV07 valve is arranged;
the control method of the pipeline system comprises water production, cleaning, water supplementing and exhaust;
the water production control step comprises the following steps: opening the FV03 valve, the FV08 valve and the FV05 valve, and the flow directions of the slurry and the produced water are as follows: the slurry enters the first water tank from the first water pipe, the alkali liquor recovery processing unit is used for processing the slurry, the processed slurry is extracted into alkali liquor, the slurry is concentrated and stored in the first water tank, after the concentration is up to the upper treatment limit, the slurry is discharged from the second water pipe by the FV01 valve, produced water enters the third water pipe from the upper part of the alkali liquor recovery processing unit, enters the diversion tank from the top of the diversion tank through the FV03 valve, flows to the water pump from the FV08 valve at the side edge of the diversion tank, and finally flows to the seventh water pipe, the FV05 valve and the fourth water pipe discharging equipment;
the cleaning control steps are as follows: opening FV02 valve FV04 valve FV08 valve, water flow direction in cleaning process is: the water flow is provided from the second water tank, enters the diversion tank through the FV04 valve from the water pipe five, flows out from the FV08 valve into the water pump, and finally enters the lye recovery processing unit through the fourth water pipe, the FV02 valve and the third water pipe, so that the interior of the lye recovery processing unit is cleaned;
the water supplementing control step comprises the following steps: opening the FV03 valve, the FV08 valve, the FV05 valve and the FV06 valve, wherein the water flow direction is increased in the water production process and flows back into the water tank II from the water pipe IV through the water pipe eight;
the exhaust control step is as follows: the FV02 valve, the FV04 valve, the FV05 valve, the FV03 valve, the FV08 valve, and the FV07 valve are opened, and the direction of water flow increases during cleaning to be discharged from the FV07 valve.
2. A pipe system according to claim 1, characterized in that: the number of the water pumps is two.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810135430.2A CN108301489B (en) | 2018-02-09 | 2018-02-09 | Pipeline system and control method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810135430.2A CN108301489B (en) | 2018-02-09 | 2018-02-09 | Pipeline system and control method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108301489A CN108301489A (en) | 2018-07-20 |
| CN108301489B true CN108301489B (en) | 2024-03-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810135430.2A Active CN108301489B (en) | 2018-02-09 | 2018-02-09 | Pipeline system and control method thereof |
Country Status (1)
| Country | Link |
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| CN (1) | CN108301489B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113976571A (en) * | 2021-09-07 | 2022-01-28 | 浙江泰嘉光电科技有限公司 | Novel full-automatic general TFT-LCD cleaning equipment pipeline system |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002210461A (en) * | 2001-01-17 | 2002-07-30 | Toshiba Corp | Waste water treatment system |
| CN1715199A (en) * | 2005-07-21 | 2006-01-04 | 井庆有 | Alkali recovering process and apparatus for waste water containing alkali |
| CN101224930A (en) * | 2008-01-31 | 2008-07-23 | 厦门大学 | Zero-discharge reuse treating method for spandex dyeing waste water |
| CN101224927A (en) * | 2008-01-24 | 2008-07-23 | 常州老三集团有限公司 | Dyeing waste water advanced treatment system and method |
| CN101333055A (en) * | 2008-07-29 | 2008-12-31 | 龚先木 | Complete plant for treating and recovering printing light polluted waste liquid |
| CN101549875A (en) * | 2008-10-29 | 2009-10-07 | 浙江东洋环境工程有限公司 | Process for purifying and recovering mercerized waste alkali and system thereof |
| CN102689945A (en) * | 2011-03-24 | 2012-09-26 | 吕维学 | Device for treating alkaliferous waste water through nanofiltration |
| CN104649521A (en) * | 2015-03-03 | 2015-05-27 | 石泰山 | Printing and dyeing wastewater treatment process for intensifying internal circulation of sludge water |
| CN208009591U (en) * | 2018-02-09 | 2018-10-26 | 刘诗军 | A kind of pipe-line system |
-
2018
- 2018-02-09 CN CN201810135430.2A patent/CN108301489B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002210461A (en) * | 2001-01-17 | 2002-07-30 | Toshiba Corp | Waste water treatment system |
| CN1715199A (en) * | 2005-07-21 | 2006-01-04 | 井庆有 | Alkali recovering process and apparatus for waste water containing alkali |
| CN101224927A (en) * | 2008-01-24 | 2008-07-23 | 常州老三集团有限公司 | Dyeing waste water advanced treatment system and method |
| CN101224930A (en) * | 2008-01-31 | 2008-07-23 | 厦门大学 | Zero-discharge reuse treating method for spandex dyeing waste water |
| CN101333055A (en) * | 2008-07-29 | 2008-12-31 | 龚先木 | Complete plant for treating and recovering printing light polluted waste liquid |
| CN101549875A (en) * | 2008-10-29 | 2009-10-07 | 浙江东洋环境工程有限公司 | Process for purifying and recovering mercerized waste alkali and system thereof |
| CN102689945A (en) * | 2011-03-24 | 2012-09-26 | 吕维学 | Device for treating alkaliferous waste water through nanofiltration |
| CN104649521A (en) * | 2015-03-03 | 2015-05-27 | 石泰山 | Printing and dyeing wastewater treatment process for intensifying internal circulation of sludge water |
| CN208009591U (en) * | 2018-02-09 | 2018-10-26 | 刘诗军 | A kind of pipe-line system |
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| Publication number | Publication date |
|---|---|
| CN108301489A (en) | 2018-07-20 |
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Effective date of registration: 20220524 Address after: 215210 29-101, international building, Shunhu West Road, Shengze Town, Wujiang District, Suzhou City, Jiangsu Province Applicant after: Suzhou Jiechang Environmental Protection Technology Co.,Ltd. Address before: 215000 408, 4th floor, Shangling building, No. 1729, Zhongshan South Road, Taihu new town, Wujiang District, Suzhou City, Jiangsu Province Applicant before: Liu Shijun |
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