CN204550280U - Vitriol works's process water supernatant treatment system - Google Patents
Vitriol works's process water supernatant treatment system Download PDFInfo
- Publication number
- CN204550280U CN204550280U CN201520188428.3U CN201520188428U CN204550280U CN 204550280 U CN204550280 U CN 204550280U CN 201520188428 U CN201520188428 U CN 201520188428U CN 204550280 U CN204550280 U CN 204550280U
- Authority
- CN
- China
- Prior art keywords
- settling pool
- water pump
- settling
- pool
- water
- 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.)
- Expired - Fee Related
Links
Abstract
The utility model relates to a kind of vitriol works process water supernatant treatment system, is supplied to production plant for drawing water from river, described in comprise the first settling pool, the second settling pool, the 3rd settling pool, water pump, frequency transformer, automatic feeder; The inlet channel of described water pump is arranged in river, and described water pump is connected with frequency transformer, to be drawn water speed by Frequency Converter Control water pump; The outlet conduit of described water pump is arranged in the first settling pool; Described first settling pool, the second settling pool, the 3rd settling pool are disposed adjacent, and the first settling pool overflow port is towards the second settling pool, and the second settling pool overflow outlet is towards the 3rd settling pool, and the clear water in the 3rd settling pool is directly utilized by production plant; Described automatic feeder is arranged on by the first settling pool, and automatic feeder discharging goes out to be connected on the first settling pool.The utility model, by frequency conversion control pumping rate, improves water pump matching degree, power cost saving; Production water quality is improved by multi stage precipitation flocculation adsorption.
Description
Technical field
The utility model relates to a kind of process water treatment system, and particularly a kind of vitriol works process water supernatant treatment system, belongs to chemical technology field.
Background technology
Chemical fertilizer industry factory needs to use a large amount of clear water aborning, is usually applicable to drawing from neighbouring surface drainage system directly carrying out production application afterwards according to production requirement.Often happened suddenly in summer storm flood, and surface drainage system turbidity increases about 2000mg/L, increases the pressure load for dirty water of water pump and chemical production equipment, and usually cause production product cannot meet relevant criterion requirement because water source turbidity exceeds standard.
Utility model content
Goal of the invention of the present utility model is: cause production unit pressure load to increase for the increase of prior art industrial land table water system turbidity, affect the problem of product quality, provide a kind of vitriol works process water supernatant treatment system.
To achieve these goals, the technical solution adopted in the utility model is:
A kind of vitriol works process water supernatant treatment system, being supplied to production plant for drawing water from river, comprising the first settling pool, the second settling pool, the 3rd settling pool, water pump, frequency transformer, automatic feeder.
The inlet channel of described water pump is arranged in river, and described water pump is connected with frequency transformer, to be drawn water speed by Frequency Converter Control water pump.
The outlet conduit of described water pump is connected in the first settling pool.Described first settling pool, the second settling pool, the 3rd settling pool are disposed adjacent, and the first settling pool overflow port is towards the second settling pool, and the second settling pool overflow outlet is towards the 3rd settling pool, and the clear water in the 3rd settling pool is directly utilized by production plant.
Described automatic feeder is arranged on by the first settling pool, and automatic feeder discharge port is connected on the first settling pool.
The utility model sets up frequency transformer makes its water withdrawal reach steadily quantitatively, is being provided with multistage settling pool by overflow supernatant, is making the clear water in the 3rd settling pool meet production plant service requirements.Even if in the flood season, also river turbidity can be reduced to 20-70mg/L by original 2000mg/L, meet production requirement.
As preferred version of the present utility model, in described automatic feeder, store flocculation agent, and can quantitatively throw in by self-timing.Described flocculation agent is aluminium chlorohydroxide.Aluminium chlorohydroxide can well adsorption precipitation except the suspended impurity in anhydrating, improve the clarity of river.
in sum, owing to have employed technique scheme, the beneficial effects of the utility model are:
1, by Frequency Converter Control water pump operating rate, the matching degree of pump-out and water of productive use amount in water pump working time is improved, power cost saving.
2, by multi stage precipitation and flocculation adsorption process, effectively improve production water quality, improve product quality, slow down equipment Ordinary Wear and Tear speed.
Accompanying drawing explanation
Fig. 1 is the utility model.
Mark in figure: 1-first settling pool, 2-second settling pool, 3-the 3rd settling pool, 4-water pump, 5-frequency transformer, 6-automatic feeder.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in detail.
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
Vitriol works's process water supernatant treatment system as shown in Figure 1, comprises the first settling pool 1, second settling pool 2, the 3rd settling pool 3, water pump 4, frequency transformer 5, automatic feeder 6.The inlet channel of described water pump 4 is arranged in river, and described water pump 4 is connected with frequency transformer 5, controls water pump 4 and to draw water speed, make it to match with water of productive use amount by frequency transformer 5.The outlet conduit of described water pump 4 is arranged in the first settling pool 1, first settling pool 1, second settling pool 1, the 3rd settling pool 3 are disposed adjacent, water in first settling pool 1 overflows to the second settling pool 2, water in second settling pool 2 overflows to the 3rd settling pool 3, clear water turbidity in 3rd settling pool 3 is reduced to minimum level, meet aquatic products requirement, directly used by production plant.Described automatic feeder 6 is arranged on the first settling pool other 1, and automatic feeder discharge port is connected on the first settling pool.Because frequency transformer installed by water pump, water withdrawal more steadily quantitatively, has effectively saved grid electricity fee cost.Meanwhile, the first settling pool 1, second settling pool 1, the 3rd settling pool 3 cut off body of wall by the choked flow arranged and realize multistage overflow sedimentation blowdown process.Water of productive use turbidity is reduced greatly, improves the product quality such as company's phosphoric acid, sulfuric acid, hydrochloric acid, extend the work-ing life of the equipment such as plate-type heat exchanger, graphite heat exchanger, tail gas washing tower and improve plant efficiency.
Further, in described automatic feeder, store flocculation agent, and can quantitatively throw in by self-timing.Described flocculation agent is aluminium chlorohydroxide.Aluminium chlorohydroxide can well adsorption precipitation except the suspended impurity in anhydrating, improve the clarity of river.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (2)
1. vitriol works's process water supernatant treatment system, is supplied to production plant for drawing water from river, comprises the first settling pool, the second settling pool, the 3rd settling pool, water pump, frequency transformer, automatic feeder;
The inlet channel of described water pump is arranged in river, and described water pump is connected with frequency transformer;
The outlet conduit of described water pump is connected in the first settling pool;
Described first settling pool, the second settling pool, the 3rd settling pool are disposed adjacent, and the first settling pool overflow port is towards the second settling pool, and the second settling pool overflow outlet is towards the 3rd settling pool;
Described automatic feeder is arranged on by the first settling pool, and automatic feeder discharge port is connected on the first settling pool.
2. vitriol works according to claim 1 process water supernatant treatment system, is characterized in that, store flocculation agent in described automatic feeder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520188428.3U CN204550280U (en) | 2015-03-31 | 2015-03-31 | Vitriol works's process water supernatant treatment system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520188428.3U CN204550280U (en) | 2015-03-31 | 2015-03-31 | Vitriol works's process water supernatant treatment system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204550280U true CN204550280U (en) | 2015-08-12 |
Family
ID=53825416
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520188428.3U Expired - Fee Related CN204550280U (en) | 2015-03-31 | 2015-03-31 | Vitriol works's process water supernatant treatment system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN204550280U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106249688A (en) * | 2016-09-19 | 2016-12-21 | 北京德瑞科森环保科技有限公司 | Based on multistage strengthening repair system automatically extraction out controls device and control method |
-
2015
- 2015-03-31 CN CN201520188428.3U patent/CN204550280U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106249688A (en) * | 2016-09-19 | 2016-12-21 | 北京德瑞科森环保科技有限公司 | Based on multistage strengthening repair system automatically extraction out controls device and control method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203281085U (en) | Water treatment sedimentation equipment | |
CN204550280U (en) | Vitriol works's process water supernatant treatment system | |
CN204039217U (en) | Integral life sewage focuses on equipment | |
CN204343376U (en) | A kind of rainwater-collecting recycling equipment | |
CN207608952U (en) | Rainwater-collecting and processing unit | |
CN203144184U (en) | Water purifier | |
CN205347045U (en) | Steel construction sedimentation tank | |
CN205204935U (en) | Construction building site sewage treatment and zero discharge system in sewage | |
CN205275412U (en) | Sewage treatment plant of self -adaptation sewage inflow | |
CN208949003U (en) | A kind of thermal power plant, steam power plant's waste water hierarchical synthesis processing system | |
CN207933077U (en) | A kind of automatic draw-out device of wastewater treatment sludge supernatant | |
CN104998443A (en) | Air lifting system special for drainage and sludge discharge in sewage treatment | |
CN204738982U (en) | Silane crossing cable material is water ring vacuum pump water saving fixtures for production line | |
CN208104088U (en) | The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system | |
CN205031982U (en) | Water circulation system | |
CN204401773U (en) | A kind of blowdown drum for PE tubing | |
CN203790633U (en) | Composite regulation and storage pre-sedimentation tank | |
CN204380333U (en) | A kind of concentration basin overflow water induction system | |
CN204165311U (en) | A kind of cooling water recirculation system | |
CN102990028A (en) | Device for charging overbottom pressure of continuously-cast turbid circulating water to tower | |
CN219415662U (en) | Water circulation recycling device of chemical fiber calciner vacuum system | |
CN202705175U (en) | Sewage heating device of sewage plant | |
CN102029082A (en) | Sloping-plate sedimentation equipment | |
CN203976582U (en) | Suspending type biological bed small-sized domestic sewage processing system | |
CN202298751U (en) | Coke oven waste heat power generation water saving system |
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: 20150812 Termination date: 20160331 |
|
CF01 | Termination of patent right due to non-payment of annual fee |