CN205133294U - Dish tubular reverse osmosis system - Google Patents
Dish tubular reverse osmosis system Download PDFInfo
- Publication number
- CN205133294U CN205133294U CN201520894455.2U CN201520894455U CN205133294U CN 205133294 U CN205133294 U CN 205133294U CN 201520894455 U CN201520894455 U CN 201520894455U CN 205133294 U CN205133294 U CN 205133294U
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- water
- dtro
- reuse
- reverse osmosis
- mcr
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Abstract
The utility model discloses a dish tubular reverse osmosis system, including wastewater collection pond, MCR materialization treater, DTRO reuse water device, retrieval and utilization pond and thick water tank, the entry of MCR materialization treater is connected in the wastewater collection pond, the exit linkage DTRO reuse water device of MCR materialization treater, dense water exit linkage to the thick water tank of DTRO reuse water device, product water exit linkage to the retrieval and utilization pond of DTRO reuse water device, thick water tank is connected to the retrieval and utilization pond. The utility model discloses area is little, and the mobility can be strong, and reverse osmosis membrane has high clearance to each item pollutant, and it is good to go out water quality of water, and it is very stable to go out water quality of water.
Description
Technical field
The utility model relates to a kind of reverse osmosis system, specifically a kind of disc tube reverse osmosis (dt-ro) system.
Background technology
DT membrane technique and dish tubular membrane technology, being divided into the large class of DTRO (disc tube reverse osmosis (dt-ro)) and DTNF (nanofiltration of dish tubular type) two, is a kind of patent type membrane separation plant.This technology is that pall company is specially for the special membrane product that zero release and percolate process are developed.Its membrane module structure and traditional rolled film, completely different, stoste runner: dish tubular membrane component has the runner design form of patent, adopt open runner, feed liquid enters in pressurized vessel by entrance, the other end of assembly is flow to from the passage between flow guiding disc and shell, at the other end flange, feed liquid enters in flow guiding disc by 8 passages, processed liquid flows through filter membrane fast with the shortest distance, then 180 ° are reversed another face, next flow guiding disc is flow into again from the notch at flow guiding disc center, thus formed by flow guiding disc circumference to circle center on film surface, arrive circumference again, Zai Daoyuan center two " S " shape route, concentrated solution finally flows out from feed end flange.Distance between DT assembly two flow guiding disc is 4mm, the radioactive rays that flow guiding disc surface has certain way to arrange.This special Hydraulic design makes treatment solution flow through under pressure when filter membrane surface meets radioactive rays collision and forms turbulent flow, increase transmission rates and self-cleaning function, thus efficiently avoid film blocking and concentration polarization phenomenon, successfully extend the work-ing life of diaphragm; Also easy during cleaning the incrustation on diaphragm to be cleaned, ensure that dish tubular membrane group is applicable to process high opacity and the high waste water containing sand coefficient, adapt to worse flow condition.Permeate runner: filtration membrane is made up of two concentric annular reverse osmosis membranes, the thread support of film sandwich one deck, makes can rapidly flow toward outlet by the water purification of diaphragm.The outer shroud ultrasonic technology of this shellring shape material welds, inner ring opening, is pure water inlet.Penetrating fluid flows to the permeate passage of center pull rod periphery in the middle of diaphragm along thread support, the O RunddichtringO on flow guiding disc prevents former water from entering permeate passage.The distance of permeate from diaphragm to center is very short, and in assembly filtration membrane all equal.The structure of DT film post uniqueness makes it have above feature, and this is also that membrane separation process is applied to the necessary characteristic of percolate process.
Utility model content
The purpose of this utility model is to provide a kind of disc tube reverse osmosis (dt-ro) system.
For achieving the above object, the utility model provides following technical scheme:
A kind of disc tube reverse osmosis (dt-ro) system, comprise wastewater collection pond, MCR materializing strategy device, DTRO reuse water device, reuse pool and dense water tank, described wastewater collection pond connects the entrance of MCR materializing strategy device, the outlet of described MCR materializing strategy device connects DTRO reuse water device, the dense water out of described DTRO reuse water device is connected to dense water tank, and the product water out of described DTRO reuse water device is connected to reuse pool.
As further program of the utility model: described dense water tank is connected to reuse pool.
Compared with prior art, the beneficial effects of the utility model are: floor space is little, and removable performance is strong, and reverse osmosis membrane all has high clearance to every pollutent, and effluent quality is good, for the less demanding situation of effluent quality, can use nanofiltration membrane; Because the factor affecting membranous system rejection is less, so system effluent quality is very stable, not by biodegradability, with the series-parallel system of adjustment System, adapt to the requirement of water quality and quantity.
Accompanying drawing explanation
Fig. 1 is the structural representation of disc tube reverse osmosis (dt-ro) system.
Embodiment
Be described in more detail below in conjunction with the technical scheme of embodiment to this patent.
Refer to Fig. 1, a kind of disc tube reverse osmosis (dt-ro) system, comprise wastewater collection pond 1, MCR materializing strategy device 2, DTRO reuse water device 3, reuse pool 4 and dense water tank 5, described wastewater collection pond 1 connects the entrance of MCR materializing strategy device 2, the outlet of described MCR materializing strategy device 2 connects DTRO reuse water device 3, the dense water out of described DTRO reuse water device 3 is connected to dense water tank 5, the product water out of described DTRO reuse water device 3 is connected to reuse pool 4, and described dense water tank 5 is connected to reuse pool 4.
Above the better embodiment of this patent is explained in detail, but this patent is not limited to above-mentioned embodiment, in the ken that one skilled in the relevant art possesses, can also makes a variety of changes under the prerequisite not departing from this patent aim.
Claims (2)
1. a disc tube reverse osmosis (dt-ro) system, comprise wastewater collection pond (1), MCR materializing strategy device (2), DTRO reuse water device (3), reuse pool (4) and dense water tank (5), it is characterized in that, described wastewater collection pond (1) connects the entrance of MCR materializing strategy device (2), the outlet of described MCR materializing strategy device (2) connects DTRO reuse water device (3), the dense water out of described DTRO reuse water device (3) is connected to dense water tank (5), the product water out of described DTRO reuse water device (3) is connected to reuse pool (4).
2. disc tube reverse osmosis (dt-ro) system according to claim 1, is characterized in that, described dense water tank (5) is connected to reuse pool (4).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201520894455.2U CN205133294U (en) | 2015-11-10 | 2015-11-10 | Dish tubular reverse osmosis system |
Applications Claiming Priority (1)
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CN201520894455.2U CN205133294U (en) | 2015-11-10 | 2015-11-10 | Dish tubular reverse osmosis system |
Publications (1)
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CN205133294U true CN205133294U (en) | 2016-04-06 |
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CN201520894455.2U Active CN205133294U (en) | 2015-11-10 | 2015-11-10 | Dish tubular reverse osmosis system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114940561A (en) * | 2022-05-20 | 2022-08-26 | 安徽海螺环保集团有限公司 | Oil sludge treatment waste liquid treatment system |
-
2015
- 2015-11-10 CN CN201520894455.2U patent/CN205133294U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114940561A (en) * | 2022-05-20 | 2022-08-26 | 安徽海螺环保集团有限公司 | Oil sludge treatment waste liquid treatment system |
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