CN203736982U - Interconnecting pipeline device of settling tanks and press filters - Google Patents

Interconnecting pipeline device of settling tanks and press filters Download PDF

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Publication number
CN203736982U
CN203736982U CN201420136935.8U CN201420136935U CN203736982U CN 203736982 U CN203736982 U CN 203736982U CN 201420136935 U CN201420136935 U CN 201420136935U CN 203736982 U CN203736982 U CN 203736982U
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CN
China
Prior art keywords
filter press
sedimentation basin
sedimentation
booster pump
interconnected
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
Application number
CN201420136935.8U
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Chinese (zh)
Inventor
管超
彭春生
王旺
钟国海
林沛
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Ganzhou Zhonglian Environment Protection Science Development Co Ltd
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Ganzhou Zhonglian Environment Protection Science Development Co Ltd
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Priority to CN201420136935.8U priority Critical patent/CN203736982U/en
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Publication of CN203736982U publication Critical patent/CN203736982U/en
Anticipated expiration legal-status Critical
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Abstract

The utility model belongs to the technical field of chemical electroplating wastewater treatment and relates to an interconnecting pipeline device of settling tanks and press filters.The utility model aims at providing an interconnecting pipeline device of settling tanks and press filters. The press filters are low in equipment utilization rate and maintenance cost.The interconnecting pipeline device of the settling tanks and the press filters comprises a settling tank system, a settling tank postposition interconnecting pipeline, a booster pump system, a press filter preposition interconnecting pipeline and a press filter system, wherein the settling tank system is connected with the booster pump system via the settling tank postposition interconnecting pipeline, and the booster pump system is connected with the press filter system via the press filter preposition interconnecting pipeline.A blocking rate of subsequent equipment is effectively reduced; the service life of the subsequent equipment is prolonged; a utilization rate and service efficiency of press filter equipment are increased and improved; the working reliability of the system is improved; the maintenance cost of the system is lowered; and equipment input is also reduced for a newly-built electroplating wastewater treatment facility.

Description

The interconnected piping installation of a kind of sedimentation basin and filter press
Technical field
The utility model belongs to chemical industry electroplating waste water treatment technology field, is specifically related to the interconnected piping installation of a kind of sedimentation basin and filter press.
Background technology
Fig. 1 and Fig. 2 are the structural representation of the connecting line of existing two kinds of sedimentation basins and filter press, as depicted in figs. 1 and 2, in current electroplating wastewater processing, generally there is polytype waste water, after each electroplating wastewater Separation of Solid and Liquid, it is the pressing process of a pair of same form to the compacting of solid phase, in this kind of technological work process, there will be following situation: the solid phase of a certain waste water is on the high side, a compacting cannot all be handled well, this situation causes reclaiming in time the supernatant of sedimentation basin, has incured loss through delay the operation of postorder equipment.If the clean solid phase of not compacting, in the time that one-level equipment is carried supernatant backward, can contain a large amount of solid phases in supernatant, just easy occluding device, causes shorten the service life of equipment, and operating efficiency reduces.Meanwhile, the solid phase of some waste water is on the low side, usually within 1-2 month, just can carry out compaction treatment, thereby make filter press for a long time in dormant state, easily causes the aging of machine parts, and the utilization rate of machinery equipment is low, and maintenance cost is high.
Utility model content
(1) technical problem that will solve
The utility model is in order to overcome the shortcoming that in sedimentation basin solid phase compaction treatment, filter press utilization rate of equipment and installations is low, maintenance cost is high, and the technical problems to be solved in the utility model is to provide sedimentation basin that a kind of filter press utilization rate of equipment and installations, maintenance cost are low and the interconnected piping installation of filter press.
(2) technical scheme
In order to solve the problems of the technologies described above, the utility model provides the interconnected piping installation of a kind of like this sedimentation basin and filter press, include sedimentation tank system, the rearmounted interconnected pipeline of sedimentation basin, booster pump system, the preposition interconnected pipeline of filter press and filter press system, described sedimentation tank system is connected by the rearmounted interconnected pipeline of sedimentation basin with described booster pump system, described booster pump system is connected by the preposition interconnected pipeline of filter press with described filter press system, the rearmounted interconnected pipeline of described sedimentation basin is connected with each sedimentation basin in described sedimentation tank system by valve, the preposition interconnected pipeline of described filter press is connected with each filter press in described filter press system by valve.
Preferably, booster pump system includes 2 booster pumps in parallel.
Preferably, described sedimentation tank system includes phosphorized electrocoating sedimentation basin, zinc-containing precipitated pond, comprehensive wastewater sedimentation basin, burnt copper sedimentation basin and sour copper sedimentation basin, and described filter press system includes 5 rubber plate type pressure filters.
Preferably, described sedimentation tank system includes cyanide precipitates pond, contains chromium sedimentation basin, explodes hook sedimentation basin, strip sedimentation basin, nickeliferous sedimentation basin, and described filter press system includes 5 rubber plate type pressure filters.
Operation principle: in the time that certain sedimentation basin in sedimentation tank system need to use filter press to suppress, open the valve of the corresponding sedimentation basin being connected with the rearmounted interconnected pipeline of sedimentation basin, open again the valve being connected with the booster pump that will use in booster pump system, open again the valve of the filter press that will use being connected with the preposition interconnected pipeline of filter press, filter press is communicated with the sedimentation basin that will suppress, then suppresses; After a filter press compacting, by controlling corresponding valve, make another filter press work, remaining body refuse in sedimentation basin is continued to compacting, adopt one by one multiple filter presses once by whole the body refuse in sedimentation basin compactings thereby can realize; By the alternation of each filter press in booster pump and filter press system in parallel in booster pump system, can effectively improve the utilization rate of equipment and the reliability of work; Due to the often operation of each equipment, also reduce its maintenance cost.
2 booster pumps in parallel, in the time of work, are generally normal operations, and another is for subsequent use, after a period of time, and duty alternate with each other, one is for subsequent use, and another normally moves, to improve the service life of equipment.
(3) beneficial effect
Effectively reduce the plugging rate of postorder equipment, extended the service life of postorder equipment; Improve utilization rate and the service efficiency of filter press equipment, improved the reliability of system works, reduced its maintenance cost; For wanting newly-built electroplating wastewater processing facility, also reduce its equipment investment.
Brief description of the drawings
Fig. 1 is the structural representation of the connecting line of existing a kind of sedimentation basin and filter press.
Fig. 2 is the structural representation of the connecting line of existing another sedimentation basin and filter press.
Fig. 3 is structural representation of the present utility model.
Fig. 4 is the utility model embodiment 1structural representation.
Fig. 5 is the utility model embodiment 2structural representation.
Being labeled as in accompanying drawing: 1-sedimentation tank system, the rearmounted interconnected pipeline of 2-sedimentation basin, 3-booster pump system, the preposition interconnected pipeline of 4-filter press, 5-filter press system, valve I-211, valve II-214, valve III-221, valve IV-222, valve V-31, valve VI-32, valve VII-41, valve VIII-42, valve IX-43, valve X-44, valve XI-45.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further described.
embodiment 1
The interconnected piping installation of a kind of sedimentation basin and filter press, as shown in Figure 3, include sedimentation tank system 1, the rearmounted interconnected pipeline 2 of sedimentation basin, booster pump system 3, the preposition interconnected pipeline 4 of filter press and filter press system 5, described sedimentation tank system 1 is connected by the rearmounted interconnected pipeline 2 of sedimentation basin with described booster pump system 3, described booster pump system 3 is connected by the preposition interconnected pipeline 4 of filter press with described filter press system 5, the rearmounted interconnected pipeline 2 of described sedimentation basin is connected with each sedimentation basin in described sedimentation tank system 1 by valve, the preposition interconnected pipeline 4 of described filter press is connected with each filter press in described filter press system 5 by valve.Booster pump system 3 includes 2 booster pumps in parallel.
Operation principle: in the time that certain sedimentation basin in sedimentation tank system 1 need to use filter press to suppress, open the valve of the corresponding sedimentation basin being connected with the rearmounted interconnected pipeline 2 of sedimentation basin, open again the valve being connected with the booster pump that will use in booster pump system 3, open again the valve of the filter press that will use being connected with the preposition interconnected pipeline 4 of filter press, filter press is communicated with the sedimentation basin that will suppress, then suppresses; By the alternation of each filter press in booster pump and filter press system 5 in parallel in booster pump system 3, can effectively improve the utilization rate of equipment and the reliability of work; Due to the often operation of each equipment, also reduce its maintenance cost.
embodiment 2
The interconnected piping installation of a kind of sedimentation basin and filter press, as shown in Figure 4, include sedimentation tank system 1, the rearmounted interconnected pipeline 2 of sedimentation basin, booster pump system 3, the preposition interconnected pipeline 4 of filter press and filter press system 5, described sedimentation tank system 1 is connected by the rearmounted interconnected pipeline 2 of sedimentation basin with described booster pump system 3, described booster pump system 3 is connected by the preposition interconnected pipeline 4 of filter press with described filter press system 5, the rearmounted interconnected pipeline 2 of described sedimentation basin is connected with each sedimentation basin in described sedimentation tank system 1 by valve, the preposition interconnected pipeline 4 of described filter press is connected with each filter press in described filter press system 5 by valve.Booster pump system 3 includes 2 booster pumps in parallel.
Described sedimentation tank system 1 includes No. 1 sedimentation basin of phosphorized electrocoating, No. 2 sedimentation basins of phosphorized electrocoating, contains No. 1 sedimentation basin of zinc, contains No. 2 sedimentation basins of zinc, No. 1 sedimentation basin of comprehensive wastewater, No. 2 sedimentation basins of comprehensive wastewater, No. 1 sedimentation basin of burnt copper, No. 2 sedimentation basins of burnt copper, No. 1 sedimentation basin of sour copper, No. 2 sedimentation basins of sour copper, No. 3 sedimentation basins of sour copper and No. 4 sedimentation basins of sour copper, and described filter press system 5 includes 5 rubber plate type pressure filters.
Operation principle: when No. 1 sedimentation basin of the phosphorized electrocoating being connected with valve I 211 in sedimentation tank system 1 be connected with valve II 214 containing No. 2 sedimentation basins of zinc need to use filter press to suppress time, open valve I 211, valve II 214, valve III 221, valve IV 222, open again the valve V 31 being connected with the booster pump that will use in booster pump system 3, open again the valve VII 41 of the filter press that will use being connected with the preposition interconnected pipeline 4 of filter press, filter press is communicated with the sedimentation basin that will suppress, then suppresses, in the time that the working time is longer, close the booster pump and the valve V 31 that in booster pump system 3, are connected with valve V 31, open valve VI 32, and the booster pump that is connected with valve VI of startup, two booster pump alternations, after the filter press compacting being connected with valve VII 41, shut off valve VII 41 and coupled filter press, open valve VIII 42 and coupled filter press carries out compacting work, after the filter press compacting being connected with valve VIII 42, shut off valve VIII 42 and coupled filter press, open valve IX 43 and coupled filter press carries out compacting work, after the filter press compacting being connected with valve IX 43, shut off valve IX 43 and coupled filter press, open valve X 44 and coupled filter press carries out compacting work, after the filter press compacting being connected with valve X 44, shut off valve X 44 and coupled filter press, open valve XI 45 and coupled filter press carries out compacting work, remaining body refuse in sedimentation basin is continued to compacting, adopt one by one multiple filter presses once by whole the body refuse in sedimentation basin compactings thereby can realize.The operation principle of other each sedimentation basin similarly, does not repeat them here.
embodiment 3
The interconnected piping installation of a kind of sedimentation basin and filter press, as shown in Figure 4, include sedimentation tank system 1, the rearmounted interconnected pipeline 2 of sedimentation basin, booster pump system 3, the preposition interconnected pipeline 4 of filter press and filter press system 5, described sedimentation tank system 1 is connected by the rearmounted interconnected pipeline 2 of sedimentation basin with described booster pump system 3, described booster pump system 3 is connected by the preposition interconnected pipeline 4 of filter press with described filter press system 5, the rearmounted interconnected pipeline 2 of described sedimentation basin is connected with each sedimentation basin in described sedimentation tank system 1 by valve, the preposition interconnected pipeline 4 of described filter press is connected with each filter press in described filter press system 5 by valve.Booster pump system 3 includes 2 booster pumps in parallel.
Described sedimentation tank system 1 includes No. 1 sedimentation basin of phosphorized electrocoating, No. 2 sedimentation basins of phosphorized electrocoating, contains No. 1 sedimentation basin of zinc, contains No. 2 sedimentation basins of zinc, No. 1 sedimentation basin of comprehensive wastewater, No. 2 sedimentation basins of comprehensive wastewater, No. 1 sedimentation basin of burnt copper, No. 2 sedimentation basins of burnt copper, No. 1 sedimentation basin of sour copper, No. 2 sedimentation basins of sour copper, No. 3 sedimentation basins of sour copper and No. 4 sedimentation basins of sour copper, and described filter press system 5 includes 5 rubber plate type pressure filters.
Operation principle: in the time that certain sedimentation basin in sedimentation tank system 1 need to use filter press to suppress, open the valve of the corresponding sedimentation basin being connected with the rearmounted interconnected pipeline 2 of sedimentation basin, open again the valve being connected with the booster pump that will use in booster pump system 3, open again the valve of the filter press that will use being connected with the preposition interconnected pipeline 4 of filter press, filter press is communicated with the sedimentation basin that will suppress, then suppresses; By the alternation of each filter press in booster pump and filter press system 5 in parallel in booster pump system 3, can effectively improve the utilization rate of equipment and the reliability of work; Due to the often operation of each equipment, also reduce its maintenance cost.
embodiment 4
The interconnected piping installation of a kind of sedimentation basin and filter press, as shown in Figure 5, include sedimentation tank system 1, the rearmounted interconnected pipeline 2 of sedimentation basin, booster pump system 3, the preposition interconnected pipeline 4 of filter press and filter press system 5, described sedimentation tank system 1 is connected by the rearmounted interconnected pipeline 2 of sedimentation basin with described booster pump system 3, described booster pump system 3 is connected by the preposition interconnected pipeline 4 of filter press with described filter press system 5, the rearmounted interconnected pipeline 2 of described sedimentation basin is connected with each sedimentation basin in described sedimentation tank system 1 by valve, the preposition interconnected pipeline 4 of described filter press is connected with each filter press in described filter press system 5 by valve.Booster pump system 3 includes 2 booster pumps in parallel.
Described sedimentation tank system 1 includes containing No. 1 sedimentation basin of cyanogen, containing No. 2 sedimentation basins of cyanogen, containing No. 3 sedimentation basins of cyanogen, containing No. 1 sedimentation basin of chromium, containing No. 2 sedimentation basins of chromium, containing No. 3 sedimentation basins of chromium, fried No. 1 sedimentation basin of hook, fried No. 2 sedimentation basins of hook, No. 1 sedimentation basin of strip, No. 2 sedimentation basins of strip, nickeliferous No. 1 sedimentation basin, nickeliferous No. 2 sedimentation basins, and described filter press system 5 includes 5 rubber plate type pressure filters.
Operation principle: in the time that certain sedimentation basin in sedimentation tank system 1 need to use filter press to suppress, open the valve of the corresponding sedimentation basin being connected with the rearmounted interconnected pipeline 2 of sedimentation basin, open again the valve being connected with the booster pump that will use in booster pump system 3, open again the valve of the filter press that will use being connected with the preposition interconnected pipeline 4 of filter press, filter press is communicated with the sedimentation basin that will suppress, then suppresses; By the alternation of each filter press in booster pump and filter press system 5 in parallel in booster pump system 3, can effectively improve the utilization rate of equipment and the reliability of work; Due to the often operation of each equipment, also reduce its maintenance cost.
The above embodiment has only expressed preferred embodiment of the present utility model, and it describes comparatively concrete and detailed, but can not therefore be interpreted as the restriction to the utility model the scope of the claims.It should be pointed out that for the person of ordinary skill of the art, without departing from the inventive concept of the premise, can also make some distortion, improvement and substitute, these all belong to protection domain of the present utility model.Therefore, the protection domain of the utility model patent should be as the criterion with claims.

Claims (4)

1. the interconnected piping installation of a sedimentation basin and filter press, it is characterized in that, include sedimentation tank system (1), the rearmounted interconnected pipeline of sedimentation basin (2), booster pump system (3), the preposition interconnected pipeline of filter press (4) and filter press system (5), described sedimentation tank system (1) is connected by the rearmounted interconnected pipeline of sedimentation basin (2) with described booster pump system (3), described booster pump system (3) is connected by the preposition interconnected pipeline of filter press (4) with described filter press system (5), the rearmounted interconnected pipeline of described sedimentation basin (2) is connected with each sedimentation basin in described sedimentation tank system (1) by valve, the preposition interconnected pipeline of described filter press (4) is connected with each filter press in described filter press system (5) by valve.
2. the interconnected piping installation of a kind of sedimentation basin according to claim 1 and filter press, is characterized in that, booster pump system (3) includes 2 booster pumps in parallel.
3. the interconnected piping installation of a kind of sedimentation basin according to claim 1 and filter press, it is characterized in that, described sedimentation tank system (1) includes phosphorized electrocoating sedimentation basin, zinc-containing precipitated pond, comprehensive wastewater sedimentation basin, burnt copper sedimentation basin and sour copper sedimentation basin, and described filter press system (5) includes 5 rubber plate type pressure filters.
4. the interconnected piping installation of a kind of sedimentation basin according to claim 1 and filter press, it is characterized in that, described sedimentation tank system (1) includes cyanide precipitates pond, contains chromium sedimentation basin, explodes hook sedimentation basin, strip sedimentation basin, nickeliferous sedimentation basin, and described filter press system (5) includes 5 rubber plate type pressure filters.
CN201420136935.8U 2014-03-25 2014-03-25 Interconnecting pipeline device of settling tanks and press filters Expired - Fee Related CN203736982U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420136935.8U CN203736982U (en) 2014-03-25 2014-03-25 Interconnecting pipeline device of settling tanks and press filters

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420136935.8U CN203736982U (en) 2014-03-25 2014-03-25 Interconnecting pipeline device of settling tanks and press filters

Publications (1)

Publication Number Publication Date
CN203736982U true CN203736982U (en) 2014-07-30

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420136935.8U Expired - Fee Related CN203736982U (en) 2014-03-25 2014-03-25 Interconnecting pipeline device of settling tanks and press filters

Country Status (1)

Country Link
CN (1) CN203736982U (en)

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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: 20140730

Termination date: 20200325

CF01 Termination of patent right due to non-payment of annual fee