CN106630280A - Drinking water treatment production line - Google Patents

Drinking water treatment production line Download PDF

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Publication number
CN106630280A
CN106630280A CN201611212175.4A CN201611212175A CN106630280A CN 106630280 A CN106630280 A CN 106630280A CN 201611212175 A CN201611212175 A CN 201611212175A CN 106630280 A CN106630280 A CN 106630280A
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CN
China
Prior art keywords
oil
oil suction
water
cylinder
drinking 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.)
Pending
Application number
CN201611212175.4A
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Chinese (zh)
Inventor
朱立武
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Jiexin Direct Drinking Water Purifying Equipment Co Ltd
Original Assignee
Chongqing Jiexin Direct Drinking Water Purifying Equipment Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chongqing Jiexin Direct Drinking Water Purifying Equipment Co Ltd filed Critical Chongqing Jiexin Direct Drinking Water Purifying Equipment Co Ltd
Priority to CN201611212175.4A priority Critical patent/CN106630280A/en
Publication of CN106630280A publication Critical patent/CN106630280A/en
Pending legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • 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
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • 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
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • 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
    • C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
    • 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
    • C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
    • 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
    • C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
    • 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
    • C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • 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
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281—Installations for water purification using chemical agents
    • 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
    • C02F2101/12—Halogens or halogen-containing compounds
    • 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
    • C02F2301/00—General aspects of water treatment
    • C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/04—Disinfection

Landscapes

  • 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)
  • Water Treatment By Sorption (AREA)

Abstract

The invention belongs to the technical field of water purification, and particularly discloses a drinking water treatment production line. The drinking water treatment production line comprises a settling basin and a purification chamber, wherein the settling basin and the purification chamber are arranged in sequence; the purification chamber is arranged at one side of the settling basin; a water outlet is formed in the bottom of the purification chamber, and is connected with a disinfection bucket; a water inlet channel is arranged between the settling basin and the purification chamber; a water suction pump used for pumping a water source in the settling basin is arranged in the water inlet channel; one end, which is far away from the settling basin, of the water inlet channel is connected with an oil removing barrel; the oil removing barrel is positioned in the purification chamber; the barrel wall of the oil removing barrel is provided with a plurality of water outlets; the inner wall of the oil removing barrel is provided with a filter screen; the diameter of each mesh of the filter screen is smaller than 1mm; an oil suction barrel which is as high as the oil removing barrel is arranged in the oil removing barrel; the oil suction barrel is provided with a motor; the surface of the oil suction barrel is provided with a plurality of oil inlets used for oil suction; the oil suction barrel is provided with a spiral stirring blade; an oil suction pipe is arranged above the oil suction barrel. Compared with the prior art, the drinking water treatment production line is characterized in that purification steps are simplified, and water source purification quality and efficiency can be improved.

Description

Drinking water treatment production line
Technical field
The invention belongs to technical field of water purification.
Background technology
Water is Source of life, and the healthy living of people be unable to do without safety, clean drinking water.But at present the water of China is dirty Dye is extremely serious, causes the drinking water source that China substantially conforms to standard only to account for 30% or so.City with underground water as drinking water source In city, have 77.8% to be polluted by different degrees of, 82% rivers and lakes are contaminated, and 92% city faces the prestige of water pollution The side of body.Rural area water dispersion type water source generally protects difference, there is pollution sources, particularly mountain area around resource of water supply and lacks perfect water Source healthy prevention facility, excrement, rubbish etc. are directly discharged into water source, and water source biologic contamination is more universal.Drinking water pollution accident In 56.6% be because pollution of waterhead causes.
At the same time, the current water resource of China is also very deficient, in order to meet demand of a large amount of populations for the water yield, because This many water factory has to be faced with using the undesirable contaminated water source raw water of more water quality as Drinking Water Water source.Simultaneously with the improvement of people's living standards and the continuous enhancing of healthy and safe consciousness, water quality standard for drinking water is also carried Higher requirement is gone out.
Therefore in order to meet demand of the numerous people to water source, while the water quality of drinking water can be improved, it is accomplished by present Convenient effective drinking water treatment equipment.
The content of the invention
It is an object of the invention to provide drinking water treatment production line, can be carried with convenient effective purifying drinking water The quality of high drinking water.
In order to achieve the above object, base case of the invention provides a kind of drinking water treatment production line, including setting successively The settling tank put, settling tank side is provided with clean room, and clean room bottom is provided with delivery port, and water outlet is connected with disinfecting bucket, institute State and be provided between settling tank and clean room intake tunnel, the suction pump for extracting water source in settling tank is provided with intake tunnel, Intake tunnel is connected with oil removing cylinder away from one end of settling tank, and oil removing cylinder is located inside clean room, is provided with the barrel of oil removing cylinder Some apopores, the inwall of oil removing cylinder is provided with filter screen, and the mesh diameter of filter screen is less than 1mm, is provided with and removes in the oil removing cylinder The contour oil suction cylinder of oily cylinder, oil suction cylinder is provided with motor, and oil suction cylinder surface is provided with some fuel feed holes for oil suction, on oil suction cylinder The stirring vane of spiral is provided with, oil suction cylinder top is provided with fuel sucking pipe.
The principle of this base case is：Pour contaminated water source into settling tank, with the water source in settling tank it is continuous Increase, just artificial addition into settling tank makes the insoluble granule in water source gradually be settled down to the bottom of settling tank, settles Reacted water source, bottom is graininess pollutant, and upper strata is clear water, then proceedes to start suction pump, and suction pump takes out in clear water Enter intake tunnel, and oil removing cylinder is entered along intake tunnel, at the same time start motor and drive oil suction cylinder high-speed rotation.
Stirring vane water also in constantly stirring oil removing cylinder while rotation at a high speed with oil suction cylinder, therefore in oil suction When cylinder high-speed rotation, the water for purifying is needed to be subject to centrifugal action in oil removing cylinder.
Because the water the inside for needing purification is mixed with some oil stains, the viscosity of oil stain is larger, and the mobility of oil stain is much Less than the mobility of oil stain, therefore under the influence of centrifugal force hydrone can be thrown on the inwall of oil removing cylinder, while oil stain point Son directly can be entered in oil suction cylinder near oil suction cylinder from fuel feed hole, because oil stain molecule can not possibly be kept completely separate with hydrone, because This oil stain molecule is entered into can also bring few part hydrone during oil suction cylinder into, while oil stain has water-fast characteristic, Although therefore oil stain can bring part hydrone into into oil suction cylinder, oil stain remains in that the state swum on the water surface, shape Into one layer of oil stain layer.
Fuel sucking pipe is inserted into, oil suction bottom of the tube is just contacted with oil stain layer, then all suction out oil stain, due to filter The mesh diameter of net is less than 1mm, and under static state, water will not be flowed out due to the surface tension of its own from filter screen, only be existed Just water can be thrown away from filter screen in the presence of centrifugal force, therefore the water after oil removing passes through mesh, and from apopore leakage Go out, hydrone slides downwards after spilling from apopore along the outer wall of oil suction cylinder, finally falls into clean room.
Water after deoiling is flowed through from delivery port and carry out in disinfecting bucket last sterilisation step, and the water after sterilization is just The process of whole drinking water treatment is completed, is disposed i.e. capable of direct drinking.
The beneficial effect of this base case is：By setting gradually settling tank, clean room and disinfecting bucket in this programme, letter The step of having changed purification, while realizing the comprehensive decontamination to contaminated water source, can improve the quality and efficiency of water source purifying.
2nd, by arranging clean room in this programme, oil suction cylinder high-speed rotation stirs the water in oil removing cylinder, make to be formed in water from Mental and physical efforts, while the viscosity according to oil stain is larger, and the mobility of oil stain is far smaller than the mobility of oil stain, forms oil stain and enters and inhales Oily cylinder, clean water enters natural separation state as clean room, and the sufficiently effective oil that carried out is separated with water, while removing Water after oil will not occur again making to cause active carbon layer to block due to the viscosity of oil when active carbon layer and zeolite layer State, it is ensured that do not result in secondary pollution, improve the treatment effeciency of drinking water.
Scheme two：Scheme is preferred based on this, and the clean room bottom is sequentially installed with from top to bottom active carbon layer, boiling The zeolite full of powder in activated carbon, zeolite layer is full of in rock layers and ultrafiltration film layer, active carbon layer, is provided with ultrafiltration film layer First milipore filter.
Activated carbon is because with highly developed hole, surface area is big, so water pollutant can be removed, can also remove Some heavy metals, water enters zeolite layer after active carbon layer, and zeolite has that internal surface area is big, many holes feature, while right Ammonia nitrogen element with higher absorption and ion-exchange capacity；Ultrafiltration film layer, the first ultrafiltration are finally entered after zeolite layer Film can be realized to two worms, algae, bacterium, viral and hydrobiological effective removal.
Carry out more comprehensively processing water source after filtration absorption by these three materials, so as to ensure drinking water Safety and Health.
Scheme three：This is preferred for scheme two, and the settling tank is provided with the material trough for throwing in precipitum automatically, thing Hopper bottom is provided with funnel shaped drain spout, and piston rod is combined with drain spout, and piston rod bottom is integrally formed with floating block.
When settling tank water filling, as the water source in settling tank is continuously increased, the water surface is increased and contact with floating block, float Block is subject to buoyancy to promote piston rod to move upwards, the not re-closed drain spout of piston rod, and the material in material trough is just directly from material leakage Mouth spills automatically there is chemical reaction with water source, and large particulate matter is deposited in into the bottom.
Start to feed intake no longer need with the cooperation of buoyancy using floating block and manually add materials so that infall process becomes more It is convenient.
Scheme four：This is preferred for scheme three, and the sterilization bottom of the barrel is provided with drinking water outlet, and drinking water outlet is provided with Second milipore filter.
Scheme five：This is preferred for scheme four, and the fuel sucking pipe is fixedly connected with oil suction cylinder.
Fuel sucking pipe is fixedly connected with oil suction cylinder, and when oil suction cylinder is rotated, fuel sucking pipe can also be with oil suction cylinder synchronization Rotate, the calmness on oil stain surface will not be broken, oil absorbing effect can be improved.
Scheme six：This is preferred for scheme five, and the oil suction cylinder upper surface is provided with the sight for observing pasta in oil suction cylinder Examine device.
Check whether fuel sucking pipe bottom inserts oil stain layer using viewer, can open if fuel sucking pipe inserts oil stain layer Beginning oil suction, if oil stain layer is less than fuel sucking pipe, wait for oil stain assemble to it is enough when carry out oil suction again, improve the accurate of oil suction Property.
Description of the drawings
Fig. 1 is the structural representation of embodiment of the present invention drinking water treatment production line.
Specific embodiment
Below by specific embodiment, the present invention is further detailed explanation：
Reference in Figure of description includes：Settling tank 10, clean room 20, intake tunnel 21, suction pump 22, oil removing cylinder 23rd, apopore 231, filter screen 232, oil suction cylinder 233, stirring vane 234, fuel feed hole 235, fuel sucking pipe 24, viewer 25, activated carbon Layer 26, zeolite layer 27, ultrafiltration film layer 28, delivery port 29, disinfecting bucket 30, valve 31, drinking water outlet 32.
Embodiment
Substantially as shown in Figure 1：Drinking water treatment production line, including settling tank 10, weld on the inwall in the left side of settling tank 10 Material trough is connected to, material trough is provided with funnel shaped drain spout, piston is combined with drain spout built with alum, material trench bottom Bar, piston rod bottom is provided with through hole integrally formed with floating block, the right side wall middle part of settling tank 10.
The right side of settling tank 10 is provided with clean room 20, including clean room 20, and the left side of clean room 20 is provided with opening, peace in opening Equipped with intake tunnel 21, inlet channel includes water inlet end and water side, and water inlet end is connected with the through hole of settling tank 10, and clean room Oil removing cylinder 23, water side insertion oil removing cylinder 23 are installed in 20, and the end face of water side is higher than the bottom surface of oil removing cylinder 23.
The bottom of clean room 20 is sequentially installed with from top to bottom active carbon layer 26, zeolite layer 27 and ultrafiltration film layer 28, activated carbon It is full of in activated carbon, zeolite layer 27 in layer 26 and first milipore filter is installed in the zeolite full of powder, ultrafiltration film layer 28, purifies The bottom of room 20 is provided with delivery port 29.The end face of fuel-displaced cylinder is rounded, and in oil removing cylinder 23 oil suction cylinder 233 is provided with, and oil suction cylinder 233 is pushed up Portion is provided with motor, and oil suction cylinder 233 is located at the circle centre position of fuel-displaced cylinder end face, some fuel feed holes are provided with the barrel of oil suction cylinder 233 235, a diameter of 1cm of fuel feed hole 235, fuel feed hole 235 and the distance of the bottom of oil suction cylinder 233 of the lowermost end of oil suction cylinder 233 are 3cm, integrally formed with the stirring vane 234 of screw type on the barrel of oil suction cylinder 233, integrally formed with oil suction in oil suction cylinder 233 Pipe 24, the bottom of fuel sucking pipe 24 is 8cm with the distance of the bottom of oil suction cylinder 233, and the side of fuel sucking pipe 24 is provided with observation oil suction cylinder 233 The viewer 25 of pasta, is provided with some apopores 231 on the barrel of oil removing cylinder 23, on the inwall of oil removing cylinder 23 filter screen is provided with 232, the mesh diameter of filter screen 232 is 0.5mm.
Disinfecting bucket 30 is installed, the top of disinfecting bucket 30 is provided with valve 31, and the bottom of disinfecting bucket 30 is provided with drink at delivery port 29 With water out 32, the second milipore filter is installed on drinking water outlet 32.
When using, contaminated water source is poured into settling tank 10, as the water source in settling tank 10 is continuously increased, make the water surface Rising is contacted with floating block, and floating block is subject to buoyancy to promote piston rod to move upwards, the not re-closed drain spout of piston rod, in material trough Alum spills automatically from drain spout, and alum reacts into after settling tank 10 with the suspended material in water source, in making water source Insoluble granule is gradually settled down to the bottom of settling tank 10.
There is the water source after sedimentation reaction, bottom is graininess pollutant, and upper strata is clear water, then proceed to start suction pump 22, due to suction pump 22 be located at settling tank 10 right side wall middle part it is just relative with clear water, startup suction pump 22 after, suction pump 22 will be pumped into intake tunnel 21 the clear water in settling tank 10, and enter oil removing cylinder 23 along intake tunnel 21, same with this Shi Qidong motors drive the high-speed rotation of oil suction cylinder 233.
Water endlessly enters oil removing cylinder 23 from intake tunnel 21, stirs while rotation at a high speed with oil suction cylinder 233 Water of the blade 234 also in constantly stirring oil removing cylinder 23 is mixed, therefore when oil suction 233 high-speed rotation of cylinder, oil removing cylinder 23 It is interior to need the water of purification to be subject to centrifugal action, because the water the inside for now needing to purify is mixed with some oil stains, oil stain Viscosity is larger, and the mobility of oil stain is far smaller than the mobility of oil stain, therefore under the influence of centrifugal force hydrone can be got rid of To on the inwall of oil removing cylinder 23, while oil stain molecule can be near oil suction cylinder 233.
Because the surface of oil suction cylinder 233 is provided with some fuel feed holes 235, therefore when oil stain molecule is near oil suction cylinder 233 Directly can enter in oil suction cylinder 233 from fuel feed hole 235, because oil stain molecule can not possibly be kept completely separate with hydrone, therefore oil stain Molecule is entered into can also bring few part hydrone during oil suction cylinder 233 into, while oil stain has water-fast characteristic, therefore Although oil stain can bring part hydrone into into oil suction cylinder 233, oil stain remains in that the state swum on the water surface, is formed One layer of oil stain layer, while integrally formed with fuel sucking pipe 24 in oil suction cylinder 233, therefore fuel sucking pipe 24 can be with oil suction cylinder 233 1 Synchronous axial system is played, checks whether the bottom of 24 fuel sucking pipe of fuel sucking pipe 24 inserts oil stain layer using viewer 25, if fuel sucking pipe 24 is inserted Having entered oil stain layer can then start oil suction, if bottom of the oil stain layer less than fuel sucking pipe 24, wait for oil stain and assemble to enough When carry out oil suction again.
Filter screen 232 is installed, the mesh diameter of filter screen 232 is 0.5mm on the inwall of oil removing cylinder 23, therefore in usual state Under hydrone will not be allowed to pass through, but when oil suction 233 high-speed rotation of cylinder, the hydrone in oil removing cylinder 23 is centrifuged Power effect is thrown on the inwall of oil removing cylinder 23, has certain impulsive force to the inwall of oil removing cylinder 23, also has impact to filter screen 232 Power, now hydrone may pass through mesh, and spill from apopore 231, hydrone from apopore 231 spill after along oil suction The outer wall of cylinder 233 slides downwards, finally falls into clean room 20.
The water for finally falling into clean room 20 is the water after oil removing is complete, due to the bottom of clean room 20 from top to bottom successively Active carbon layer 26, zeolite layer 27 and ultrafiltration film layer 28 be installed, therefore water will successively flow through active carbon layer 26 under upper, activity Charcoal because with highly developed hole, surface area is big, so water pollutant can be removed, can also remove some heavy metals, Water enters zeolite layer 27 after active carbon layer 26, and zeolite has that internal surface area is big, many holes feature, while to ammonia nitrogen element With higher absorption and ion-exchange capacity；Ultrafiltration film layer 28 is finally entered after zeolite layer 27, the first milipore filter can To realize to two worms, algae, bacterium, viral and hydrobiological effective removal, after the purifying step of the above, formation Water is that health is free of contamination, is finally flowed out from delivery port 29.
Valve 31 is opened, disinfecting bucket 30 is connected, the water after settling, deoiling, filter is passed through into disinfecting bucket 30, passed through Substantial amounts of chlorion can be remained in water after sterilization, excessive Chloride residue can produce damage by people's suction in water to human body Evil, thus by the water after sterilization from drinking water outlet 32 discharge when, can the second surpass when water flows through through the second ultrafiltration membrane treatment During filter membrane surface, water, inorganic salts and small-molecule substance is only allowed to pass through the second milipore filter film, therefore the second milipore filter can be effective Chlorion is prevented to flow out together with water source, so as to improve the security of drinking water.
Above-described is only embodiments of the invention, and the general knowledge here such as known concrete structure and characteristic is not made in scheme Excessive description.It should be pointed out that for a person skilled in the art, on the premise of without departing from present configuration, can be with Some deformations and improvement are made, these should also be considered as protection scope of the present invention, these are implemented all without the impact present invention Effect and practical applicability.This application claims protection domain should be defined by the content of its claim, in specification Specific embodiment etc. records the content that can be used for explaining claim.

Claims (6)

1. drinking water treatment production line, including the settling tank for setting gradually, settling tank side is provided with clean room, and clean room opens bottom There is delivery port, water outlet is connected with disinfecting bucket, it is characterised in that be provided with intake tunnel between the settling tank and clean room, The suction pump for extracting water source in settling tank is provided with intake tunnel, intake tunnel is connected with oil removing away from one end of settling tank Cylinder, oil removing cylinder is located inside clean room, and some apopores are provided with the barrel of oil removing cylinder, and the inwall of oil removing cylinder is provided with filter screen, The mesh diameter of filter screen is less than 1mm, and the oil suction cylinder contour with oil removing cylinder is provided with the oil removing cylinder, and oil suction cylinder is provided with motor, Oil suction cylinder surface is provided with some fuel feed holes for oil suction, and oil suction cylinder is provided with the stirring vane of spiral, and oil suction cylinder top is provided with Fuel sucking pipe.
2. drinking water treatment production line according to claim 1, it is characterised in that：The clean room bottom from top to bottom according to Secondary being provided with active carbon layer, zeolite layer and ultrafiltration film layer, active carbon layer is full of the boiling full of powder in activated carbon, zeolite layer Stone, is provided with the first milipore filter in ultrafiltration film layer.
3. drinking water treatment production line according to claim 2, it is characterised in that：The settling tank is provided with for automatic The material trough of precipitum is thrown in, material trench bottom is provided with funnel shaped drain spout, piston rod, piston rod bottom are combined with drain spout Portion is integrally formed with floating block.
4. drinking water treatment production line according to claim 3, it is characterised in that：The sterilization bottom of the barrel is provided with drinking water Outlet, drinking water outlet is provided with the second milipore filter.
5. drinking water treatment production line according to claim 4, it is characterised in that：The fuel sucking pipe is fixed with oil suction cylinder and connected Connect.
6. drinking water treatment production line according to claim 5, it is characterised in that：The oil suction cylinder upper surface be provided with for The viewer of pasta in observation oil suction cylinder.
CN201611212175.4A 2016-12-25 2016-12-25 Drinking water treatment production line Pending CN106630280A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611212175.4A CN106630280A (en) 2016-12-25 2016-12-25 Drinking water treatment production line

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Application Number Priority Date Filing Date Title
CN201611212175.4A CN106630280A (en) 2016-12-25 2016-12-25 Drinking water treatment production line

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Publication Number Publication Date
CN106630280A true CN106630280A (en) 2017-05-10

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CN201611212175.4A Pending CN106630280A (en) 2016-12-25 2016-12-25 Drinking water treatment production line

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107215910A (en) * 2017-06-26 2017-09-29 柳州市融智科技服务有限公司 A kind of wastewater treatment equipment for mill of dying cloth
CN112299601A (en) * 2020-10-14 2021-02-02 杨金蓉 Organic wastewater and sewage treatment equipment and sewage treatment method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE7908036L (en) * 1979-09-28 1981-03-29 Gambro Dialysatoren Separation unit for separating liquids, SPECIAL HELD BLOOD
CN2618449Y (en) * 2003-05-23 2004-06-02 张新元 Automatic sterilizing liquid preparation device
CN102730859A (en) * 2012-07-19 2012-10-17 广东石油化工学院 Novel integrated oil-water separation device
CN205204943U (en) * 2015-08-07 2016-05-04 厦门钜时科技有限公司 Municipal wastewater cyclic utilization's water purifier

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE7908036L (en) * 1979-09-28 1981-03-29 Gambro Dialysatoren Separation unit for separating liquids, SPECIAL HELD BLOOD
CN2618449Y (en) * 2003-05-23 2004-06-02 张新元 Automatic sterilizing liquid preparation device
CN102730859A (en) * 2012-07-19 2012-10-17 广东石油化工学院 Novel integrated oil-water separation device
CN205204943U (en) * 2015-08-07 2016-05-04 厦门钜时科技有限公司 Municipal wastewater cyclic utilization's water purifier

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107215910A (en) * 2017-06-26 2017-09-29 柳州市融智科技服务有限公司 A kind of wastewater treatment equipment for mill of dying cloth
CN112299601A (en) * 2020-10-14 2021-02-02 杨金蓉 Organic wastewater and sewage treatment equipment and sewage treatment method

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Application publication date: 20170510

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