CN113501588A - Full automatic equipment of sewage treatment dual system integral type - Google Patents
Full automatic equipment of sewage treatment dual system integral type Download PDFInfo
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- CN113501588A CN113501588A CN202110865726.1A CN202110865726A CN113501588A CN 113501588 A CN113501588 A CN 113501588A CN 202110865726 A CN202110865726 A CN 202110865726A CN 113501588 A CN113501588 A CN 113501588A
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- 239000010865 sewage Substances 0.000 title claims abstract description 34
- 230000009977 dual effect Effects 0.000 title claims description 4
- 238000009292 forward osmosis Methods 0.000 claims abstract description 28
- 238000009826 distribution Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 125
- 239000012528 membrane Substances 0.000 claims description 91
- 239000008186 active pharmaceutical agent Substances 0.000 claims description 68
- 239000002351 wastewater Substances 0.000 claims description 54
- 102100030373 HSPB1-associated protein 1 Human genes 0.000 claims description 48
- 101000843045 Homo sapiens HSPB1-associated protein 1 Proteins 0.000 claims description 48
- 238000004140 cleaning Methods 0.000 claims description 34
- 239000007788 liquid Substances 0.000 claims description 27
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000012467 final product Substances 0.000 claims description 6
- 238000012423 maintenance Methods 0.000 abstract description 7
- 238000009434 installation Methods 0.000 abstract description 2
- 238000012876 topography Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 15
- 150000003839 salts Chemical class 0.000 description 9
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/445—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by forward osmosis
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a sewage treatment double-system integrated full-automatic device, which comprises: the container is internally provided with a double-door power distribution cabinet and a double-system equipment rack; the forward osmosis system is arranged on the double-system equipment rack and is connected with the double-door power distribution cabinet, and the forward osmosis system can perform forward osmosis treatment on sewage; the high-salt concentration system is arranged on the double-system equipment rack, is connected with the double-door power distribution cabinet and can be used for carrying out high-salt concentration treatment on the sewage; and the equipment pipeline is arranged in the container and connected among the double-door power distribution cabinet, the forward osmosis system and the high-salt concentration system. The invention has the advantages of strong maneuverability, strong adaptability, small occupied space area, full automation, convenient incremental expansion, simple and convenient manual maintenance, maintenance and replacement of parts, installation and movement according to the environment topography, direct large-scale treatment and the like.
Description
Technical Field
The invention relates to the technical field of sewage treatment devices, in particular to a double-system integrated full-automatic sewage treatment device.
Background
At present, the treatment product for treating high-difficulty high-salinity sewage is single, the requirement on the treatment capacity of high-pollution water treatment equipment is high, and the conventional simple process and equipment can only be used for treating low-concentration water, but the standard of zero emission cannot be effectively achieved. However, when high-difficulty and high-pollution wastewater treatment is faced, equipment for treating high-concentration industrial wastewater by using traditional sewage has the problems that the technical design cannot be achieved, the equipment is easy to block and the equipment is easy to shut down and overhaul. Therefore, improving the utilization rate of water and reducing environmental pollution become a big problem of industrial water treatment, and the water recycling of industrial sewage, domestic sewage, coal chemical industry, desulfurization wastewater, sea brine desalination, municipal waste penetrating fluid and the like also face to solve the problems, so that the sewage circulating water treatment technology and development equipment in various fields are worthy of exploration and research.
Disclosure of Invention
Therefore, in order to solve the above technical problems, it is necessary to provide a dual-system integrated full-automatic sewage treatment device which has the advantages of high sewage treatment speed, wide application range and good reliability.
The utility model provides a full automatic equipment of sewage treatment dual system integral type, it includes:
the container is internally provided with a double-door power distribution cabinet and a double-system equipment rack;
the forward osmosis system is arranged on the double-system equipment rack and is connected with the double-door power distribution cabinet, and the forward osmosis system can perform forward osmosis treatment on sewage;
the high-salt concentration system is arranged on the double-system equipment rack and is connected with the double-door power distribution cabinet, and the high-salt concentration system can perform high-salt concentration treatment on the sewage;
the equipment pipeline is arranged in the container and connected among the double-door power distribution cabinet, the forward osmosis system and the high-salt concentration system.
In one embodiment, the forward osmosis system comprises: the system comprises a wastewater tank, a wastewater feed pump, a wastewater filter, a first-stage membrane shell, a first-stage wastewater circulating pump, a second-stage membrane shell, a second-stage wastewater circulating pump, a concentrated water tank, a concentrated drawing liquid water tank, a DS drawing liquid feed pump, a cartridge filter, a first-stage DS drawing liquid circulating pump, a second-stage DS drawing liquid circulating pump, a DS cleaning water tank and a PASS1 water tank;
the waste water tank is connected with the inlet of the waste water filter through a waste water feed pump;
a first outlet of the wastewater filter is connected with the first-section membrane shell through a wastewater circulating pump, a second outlet of the wastewater filter is connected with the second-section membrane shell through a second-section wastewater circulating pump, and a third outlet of the wastewater filter is connected with the concentrated water tank; the first section of membrane shell and the second section of membrane shell are connected with the concentrated water tank;
the concentrated draw solution water tank is connected with a security filter through a DS draw solution feed pump, the security filter is connected with a first-section DS draw solution circulating pump, the first-section DS draw solution circulating pump pumps the concentrated draw solution water into the first-section membrane shell for drawing, and the second-section DS draw solution circulating pump pumps the concentrated draw solution water into the second-section membrane shell for drawing;
part of the circulating draw solution water produced in the first-stage membrane shell and the second-stage membrane shell flows into the DS cleaning water tank, and the other part of the circulating draw solution water flows into a PASS1 water tank.
In one embodiment, the high salt concentration system comprises: a final product water tank, a final product external feed pump, a PASS1 booster pump, a PASS1 filter, a PASS1 high-pressure pump, a PASS1 high-salt concentration membrane housing, a PASS2 water tank, a PASS2 booster pump, a PASS2 filter, a PASS2 high-pressure pump, a PASS2 high-salt concentration membrane housing, a PASS3 water tank, a PASS3 vertical high-pressure pump, a PASS3 membrane housing, a DS cleaning booster pump, a DS cleaning filter, a DS high-pressure pump and a DS cleaning high-salt concentration membrane housing;
the PASS1 water tank is connected with a PASS1 filter through a PASS1 booster pump;
the PASS1 filter is sequentially connected with a PASS1 high-pressure pump, a PASS1 high-salt concentration membrane shell, a PASS2 water tank, a PASS2 booster pump, a PASS2 filter, a PASS2 high-pressure pump, a PASS2 high-salt concentration membrane shell, a PASS3 water tank, a PASS3 vertical high-pressure pump and a PASS3 membrane shell; the PASS3 membrane shell is connected with a final production delivery pump through a final production water tank;
the PASS1 water tank is connected with a PASS2 high-salt concentration membrane shell, the PASS2 water tank is connected with a PASS3 membrane shell and a DS cleaning high-salt concentration membrane shell, the PASS2 high-salt concentration membrane shell is connected with a DS cleaning water tank, the DS cleaning water tank is connected with the DS cleaning high-salt concentration membrane shell, and the DS cleaning booster pump is further connected with the wastewater tank.
The sewage treatment double-system integrated full-automatic equipment has the beneficial effects that:
1) the high-salt concentration system has the advantages of being high in mobility, designed by combining a forward osmosis system and a high-salt concentration system into a whole, high in adaptability, small in occupied space area, full-automatic, convenient in incremental capacity expansion, simple and convenient in manual overhaul, maintenance and replacement of parts, capable of being installed and moved according to the environment terrain, and capable of being directly processed in a large scale.
2) Reduced complex operation when traditional single container formula equipment treatment sewage operation and maintenance, its application scope is wide, effectively improves sewage treatment speed efficiency, the good reliability.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to these drawings without creative efforts.
FIG. 1 is a frame diagram of a sewage treatment dual-system integrated fully-automatic apparatus of the present invention;
FIG. 2 is a schematic structural diagram of the integrated fully-automatic sewage treatment system of the present invention.
Detailed Description
To facilitate an understanding of the invention, the invention will now be described more fully with reference to the accompanying drawings. Preferred embodiments of the present invention are shown in the drawings. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
It will be understood that when an element is referred to as being "secured to" another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present. The terms "vertical," "horizontal," "left," "right," and the like as used herein are for illustrative purposes only and do not represent the only embodiments.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
Referring to fig. 1-2, an embodiment of the present invention provides a dual-system integrated full-automatic sewage treatment apparatus, which includes:
the container 35 is internally provided with a double-door power distribution cabinet 36 and a double-system equipment rack 37;
the forward osmosis system 38 is installed on the dual-system equipment rack 37, the forward osmosis system 38 is connected with the dual-door power distribution cabinet 36, and the forward osmosis system 38 can perform forward osmosis treatment on sewage;
the high-salt concentration system 39 is installed on the double-system equipment rack 37, the high-salt concentration system 39 is connected with the double-door power distribution cabinet 36, and the high-salt concentration system 39 can perform high-salt concentration treatment on the sewage;
and the equipment pipeline 40 is arranged in the container 35, and the equipment pipeline 40 is connected among the double-door power distribution cabinet 36, the forward osmosis system 38 and the high-salt concentration system 39.
In the invention, the forward osmosis system 38 and the high-salt concentration system 39 are integrally designed, so that manual overhaul, maintenance and control of the operation of the double systems are facilitated, and a control valve, an adjusting valve, a manual control valve and the like can be respectively installed in each pipeline of the double systems. The instrument control cabinet and the power distribution cabinet of the double-system are both designed with the advantage characteristic of double doors, the unique power distribution cabinet completely meets the requirements of double-system power supply and PLC control system electric circuit installation, and the single power distribution design of the traditional single-container type sewage treatment equipment can be saved in space and simplified.
In one embodiment of the present invention, the forward osmosis system 38 comprises: the system comprises a wastewater tank 1, a wastewater feed pump 2, a wastewater filter 3, a first-section membrane shell 4, a first-section wastewater circulating pump 5, a second-section membrane shell 7, a second-section wastewater circulating pump 8, a concentrated water tank 10, a concentrated drawing liquid water tank 11, a DS drawing liquid feed pump 12, a security filter 13, a first-section DS drawing liquid circulating pump 15, a second-section DS drawing liquid circulating pump 14, a DS cleaning water tank 17 and a PASS1 water tank 18;
the waste water tank 1 is connected with the inlet of a waste water filter 3 through a waste water feed pump 2;
a first outlet of the wastewater filter 3 is connected with a first-section membrane shell 4 through a wastewater circulating pump 5, a second outlet of the wastewater filter 3 is connected with a second-section membrane shell 7 through a second-section wastewater circulating pump 8, and a third outlet of the wastewater filter 3 is connected with the concentrated water tank 10; and the first section membrane shell 4 and the second section membrane shell 7 are connected with the concentrated water tank 10;
the concentrated drawing liquid water tank 11 is connected with a security filter 13 through a DS drawing liquid feed pump 12, the security filter 13 is connected with a first-section DS drawing liquid circulating pump 15, the first-section DS drawing liquid circulating pump 15 pumps concentrated drawing liquid water into the first-section membrane shell 4 for drawing, and the second-section DS drawing liquid circulating pump 14 pumps the concentrated drawing liquid water into the second-section membrane shell 7 for drawing;
the water portion of the circulating draw solution produced in the first stage membrane shell 4 and the second stage membrane shell 7 flows into the DS wash tank 17, and the other portion thereof flows into the PASS1 tank 18.
The forward osmosis system 38 of the present invention operates as follows:
waste water in the outward conveying pipeline enters a waste water tank 1, then, a waste water feed pump 2 conveys the waste water to a waste water filter 3 for filtering, the filtered waste water is conveyed to a section of membrane shell 4 through a section of waste water circulating pump 5 for permeation, after circulating for a certain time, water in the waste water tank 1 and a section of partial permeated water are sequentially pumped into a second-section membrane shell 7 for concentration circulation, at the moment, the first-section membrane shell 4 and the second-section membrane shell 7 are continuously circulated, part of water in a waste water main pipeline enters a concentrated water tank 10, and the other part of water returns to the waste water tank 1.
At the moment, the wastewater passes through the continuous concentration cycle of the forward osmosis system 38, the liquid-drawing water in the first-stage membrane shell 4 and the second-stage membrane shell 7 is produced, the concentrated liquid-drawing water tank 11 is connected with the DS liquid-drawing water feed pump 12 to be started, the DS liquid-drawing water is fed to the security filter 13 to be filtered, the concentrated liquid-drawing water enters the first-stage membrane shell 4 through the pipeline, and therefore, the concentrated liquid-drawing water enters the first-stage DS liquid-drawing circulating pump 15 to be drawn into the first-stage membrane shell 4, the concentrated liquid-drawing water enters the second-stage DS liquid-drawing circulating pump 14 to run after the circulation of drawing, the concentrated liquid-drawing water is drawn into the second-stage membrane shell 7 to be drawn through the continuous circulation of the first-stage, and the liquid-drawing liquid is produced. At this time, the concentrated draw solution in the main pipe of the concentrated draw solution tank 11 and a part of the circulating draw solution water produced in the two-stage membrane shell 7 enter the PASS1 water tank 18 of the high salt concentration system, and enter the DS wash water tank 17 of the high salt concentration system.
In one embodiment of the present invention, the high salt concentration system 39 comprises: a final product water tank 6, a final product external feed pump 9, a PASS1 booster pump 19, a PASS1 filter 20, a PASS1 high pressure pump 21, a PASS1 high salt concentration membrane housing 22, a PASS2 water tank 23, a PASS2 booster pump 24, a PASS2 filter 25, a PASS2 high pressure pump 26, a PASS2 high salt concentration membrane housing 27, a PASS3 water tank 28, a PASS3 vertical high pressure pump 29, a PASS3 membrane housing 30, a DS wash booster pump 31, a DS wash filter 32, a DS high pressure pump 33, and a DS wash high salt concentration membrane housing 34;
the PASS1 water tank 18 is connected with a PASS1 filter 20 through a PASS1 booster pump 19;
the PASS1 filter 20 is sequentially connected with a PASS1 high-pressure pump 21, a PASS1 high-salt concentration membrane shell 22, a PASS2 water tank 23, a PASS2 booster pump 24, a PASS2 filter 25, a PASS2 high-pressure pump 26, a PASS2 high-salt concentration membrane shell 27, a PASS3 water tank 28, a PASS3 vertical high-pressure pump 29 and a PASS3 membrane shell 30; the PASS3 membrane shell 30 is connected with a final production external pump 9 through a final production water tank 6;
wherein, the PASS1 water tank 18 is connected with a PASS2 high-salt concentration membrane shell 27, the PASS2 water tank 23 is connected with a PASS3 membrane shell 30 and a DS cleaning high-salt concentration membrane shell 34, the PASS2 high-salt concentration membrane shell 27 is connected with the DS cleaning water tank 17, the DS cleaning water tank 17 is connected with the DS cleaning high-salt concentration membrane shell 34, and the DS cleaning booster pump 31 is also connected with the wastewater tank 1.
The high salt concentration system 39 of the present invention operates as follows:
concentrated water in a PASS1 water tank 18 is pumped into a PASS1 filter 20 through a PASS1 booster pump 19, at the moment, a PASS1 high-pressure pump 21 is started, the concentrated water is conveyed into a PASS1 high-salt concentration membrane shell 22 for concentration, the concentrated water enters a concentrated draw solution water tank 11, and produced water enters a PASS2 water tank 23.
The PASS2 booster pump 24 operates to deliver the concentrated water to the PASS2 filter 25, at the moment, the PASS2 high-pressure pump 26 is started to deliver the concentrated water to the PASS2 high-salt concentration membrane shell 27 for concentration, and the concentrated water of the PASS2 high-salt concentration membrane shell 27 enters the PASS1 water tank 18. The produced water of the PASS2 high-salt concentration membrane shell 27 sequentially enters a PASS3 water tank 28, and a part of the produced water electric three-way valve of the PASS2 high-salt concentration membrane shell 27 enters a DS cleaning water tank 17.
The water produced by the PASS1 high-salt concentration membrane shell 22 enters a water tank 28 of a PASS3 of a high-salt concentration system, at the moment, a PASS3 vertical high-pressure pump 29 runs to directly convey the concentrated water into a PASS3 high-salt concentration membrane shell 30 for concentration, and after concentration, the concentrated water of the PASS3 high-salt concentration membrane shell 30 enters a water tank 23 of a PASS 2. The produced water of the PASS3 high-salt concentration membrane shell 30 is conveyed to a final produced water tank 6 of the forward osmosis system, and at the moment, a final produced water delivery pump 9 is started to operate and discharge the final produced water.
The water production pipeline of the PASS1 high-salt concentration membrane shell 22 is connected with a part of produced water at the electric three-way valve and enters the DS cleaning water tank 17. At this time, the DS cleaning booster pump 31 operates to feed the cleaning section concentrated water into the DS cleaning filter 32, at this time, the DS high-pressure pump 33 is started to deliver the concentrated water into the DS cleaning high-salt concentration membrane shell 34 for concentration, and after concentration, the concentrated water in the DS cleaning high-salt concentration membrane shell 34 enters back into the DS cleaning water tank 17. The produced water in the DS wash tank 17 is then fed into the high salt concentration system PASS2 water tank 23. Through the circulating operation of the integral sewage treatment equipment structure of the forward osmosis system 38 and the high-salt concentration system 39, the produced clear water is concentrated and drawn, and the water can be recycled.
In summary, the invention has the advantages that:
1) the high-salt concentration system has the advantages of being high in mobility, designed by combining a forward osmosis system and a high-salt concentration system into a whole, high in adaptability, small in occupied space area, full-automatic, convenient in incremental capacity expansion, simple and convenient in manual overhaul, maintenance and replacement of parts, capable of being installed and moved according to the environment terrain, and capable of being directly processed in a large scale.
2) Reduced complex operation when traditional single container formula equipment treatment sewage operation and maintenance, its application scope is wide, effectively improves sewage treatment speed efficiency, the good reliability.
The technical features of the embodiments described above may be arbitrarily combined, and for the sake of brevity, all possible combinations of the technical features in the embodiments described above are not described, but should be considered as being within the scope of the present specification as long as there is no contradiction between the combinations of the technical features.
The above-described examples merely represent several embodiments of the present application and are not to be construed as limiting the scope of the claims. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the concept of the present application, which falls within the scope of protection of the present application. Therefore, the protection scope of the present patent shall be subject to the appended claims.
Claims (3)
1. The utility model provides a full automatic equipment of sewage treatment dual system integral type which characterized in that includes:
the container (35), there are double-door switch boards (36) and double system equipment framework (37) in the said container (35);
the forward osmosis system (38) is installed on the double-system equipment rack (37), the forward osmosis system (38) is connected with the double-door power distribution cabinet (36), and the forward osmosis system (38) can perform forward osmosis treatment on sewage;
the high-salt concentration system (39) is installed on the double-system equipment rack (37), the high-salt concentration system (39) is connected with the double-door power distribution cabinet (36), and the high-salt concentration system (39) can perform high-salt concentration treatment on the sewage;
the equipment pipeline (40) is arranged in the container (35), and the equipment pipeline (40) is connected among the double-door power distribution cabinet (36), the forward osmosis system (38) and the high-salt concentration system (39).
2. The sewage treatment dual-system integrated fully automatic apparatus according to claim 1, wherein the forward osmosis system (38) comprises: the system comprises a waste water tank (1), a waste water feed pump (2), a waste water filter (3), a first-section membrane shell (4), a first-section waste water circulating pump (5), a second-section membrane shell (7), a second-section waste water circulating pump (8), a concentrated water tank (10), a concentrated drawing liquid water tank (11), a DS drawing liquid feed pump (12), a cartridge filter (13), a first-section DS drawing liquid circulating pump (15), a second-section DS drawing liquid circulating pump (14), a DS cleaning water tank (17) and a PASS1 water tank (18);
the waste water tank (1) is connected with an inlet of a waste water filter (3) through a waste water feed pump (2);
a first outlet of the wastewater filter (3) is connected with a first section of membrane shell (4) through a wastewater circulating pump (5), a second outlet of the wastewater filter (3) is connected with a second section of membrane shell (7) through a second section of wastewater circulating pump (8), and a third outlet of the wastewater filter (3) is connected with the concentrated water tank (10); the first section of membrane shell (4) and the second section of membrane shell (7) are connected with the concentrated water tank (10);
the concentrated drawing liquid water tank (11) is connected with a security filter (13) through a DS drawing liquid feed pump (12), the security filter (13) is connected with a first-section DS drawing liquid circulating pump (15), the first-section DS drawing liquid circulating pump (15) pumps the concentrated drawing liquid water into the first-section membrane shell (4) for drawing, and the second-section DS drawing liquid circulating pump (14) pumps the concentrated drawing liquid water into the second-section membrane shell (7) for drawing;
the part of the circulating draw solution water produced in the first section membrane shell (4) and the second section membrane shell (7) flows into the DS cleaning water tank (17), and the other part of the circulating draw solution water flows into a PASS1 water tank (18).
3. The sewage treatment dual-system integrated fully automatic apparatus according to claim 2, wherein the high-salt concentration system (39) comprises: a final product water tank (6), a final product external feeding pump (9), a PASS1 booster pump (19), a PASS1 filter (20), a PASS1 high-pressure pump (21), a PASS1 high-salt concentration membrane shell (22), a PASS2 water tank (23), a PASS2 booster pump (24), a PASS2 filter (25), a PASS2 high-pressure pump (26), a PASS2 high-salt concentration membrane shell (27), a PASS3 water tank (28), a PASS3 vertical high-pressure pump (29), a PASS3 membrane shell (30), a DS cleaning booster pump (31), a DS cleaning filter (32), a DS high-pressure pump (33) and a DS cleaning high-salt concentration membrane shell (34);
the PASS1 water tank (18) is connected with a PASS1 filter (20) through a PASS1 booster pump (19);
the PASS1 filter (20) is sequentially connected with a PASS1 high-pressure pump (21), a PASS1 high-salt concentration membrane shell (22), a PASS2 water tank (23), a PASS2 booster pump (24), a PASS2 filter (25), a PASS2 high-pressure pump (26), a PASS2 high-salt concentration membrane shell (27), a PASS3 water tank (28), a PASS3 vertical high-pressure pump (29) and a PASS3 membrane shell (30); the PASS3 membrane shell (30) is connected with a final production delivery pump (9) through a final production water tank (6);
wherein the PASS1 water tank (18) is connected with a PASS2 high-salt concentration membrane shell (27), the PASS2 water tank (23) is connected with the PASS3 membrane shell (30) and a DS cleaning high-salt concentration membrane shell (34), the PASS2 high-salt concentration membrane shell (27) is connected with the DS cleaning water tank (17), the DS cleaning water tank (17) is connected with the DS cleaning high-salt concentration membrane shell (34), and the DS cleaning booster pump (31) is also connected with the wastewater tank (1).
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| Application Number | Priority Date | Filing Date | Title |
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| CN202110865726.1A CN113501588A (en) | 2021-07-29 | 2021-07-29 | Full automatic equipment of sewage treatment dual system integral type |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202110865726.1A CN113501588A (en) | 2021-07-29 | 2021-07-29 | Full automatic equipment of sewage treatment dual system integral type |
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| CN113501588A true CN113501588A (en) | 2021-10-15 |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009039599A (en) * | 2007-08-06 | 2009-02-26 | Kurita Water Ind Ltd | Water treatment system |
| CN208500435U (en) * | 2018-06-07 | 2019-02-15 | 上海缘脉环境科技有限公司 | A kind of concentration with high salt and penetration equipment |
| CN109734152A (en) * | 2019-03-05 | 2019-05-10 | 上海缘脉环境科技有限公司 | A kind of HBCR concentration membrane treatment process with high salt |
| CN111646596A (en) * | 2020-06-15 | 2020-09-11 | 上海缘脉环境科技有限公司 | Container type movable forward osmosis treatment equipment and forward osmosis treatment method thereof |
| CN211677195U (en) * | 2020-01-13 | 2020-10-16 | 上海缘脉环境科技有限公司 | Membrane concentration and zero discharge system for chemical industry |
-
2021
- 2021-07-29 CN CN202110865726.1A patent/CN113501588A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009039599A (en) * | 2007-08-06 | 2009-02-26 | Kurita Water Ind Ltd | Water treatment system |
| CN208500435U (en) * | 2018-06-07 | 2019-02-15 | 上海缘脉环境科技有限公司 | A kind of concentration with high salt and penetration equipment |
| CN109734152A (en) * | 2019-03-05 | 2019-05-10 | 上海缘脉环境科技有限公司 | A kind of HBCR concentration membrane treatment process with high salt |
| CN211677195U (en) * | 2020-01-13 | 2020-10-16 | 上海缘脉环境科技有限公司 | Membrane concentration and zero discharge system for chemical industry |
| CN111646596A (en) * | 2020-06-15 | 2020-09-11 | 上海缘脉环境科技有限公司 | Container type movable forward osmosis treatment equipment and forward osmosis treatment method thereof |
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Application publication date: 20211015 |