CN113149267A - Multifunctional water treatment system of combined fluidized bed - Google Patents
Multifunctional water treatment system of combined fluidized bed Download PDFInfo
- Publication number
- CN113149267A CN113149267A CN202110311175.4A CN202110311175A CN113149267A CN 113149267 A CN113149267 A CN 113149267A CN 202110311175 A CN202110311175 A CN 202110311175A CN 113149267 A CN113149267 A CN 113149267A
- Authority
- CN
- China
- Prior art keywords
- fluidized bed
- main body
- body device
- water
- water inlet
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 169
- 238000005469 granulation Methods 0.000 claims abstract description 81
- 230000003179 granulation Effects 0.000 claims abstract description 81
- 239000000701 coagulant Substances 0.000 claims abstract description 51
- 239000000126 substance Substances 0.000 claims abstract description 49
- 238000002425 crystallisation Methods 0.000 claims abstract description 47
- 230000008025 crystallization Effects 0.000 claims abstract description 47
- 239000007788 liquid Substances 0.000 claims abstract description 37
- 238000000926 separation method Methods 0.000 claims abstract description 36
- 239000013078 crystal Substances 0.000 claims abstract description 32
- 239000002245 particle Substances 0.000 claims abstract description 18
- 230000003068 static effect Effects 0.000 claims abstract description 17
- 239000003814 drug Substances 0.000 claims abstract description 16
- 238000007599 discharging Methods 0.000 claims abstract description 11
- 239000004576 sand Substances 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 8
- 239000002253 acid Substances 0.000 claims description 17
- 239000004570 mortar (masonry) Substances 0.000 claims description 16
- 239000008187 granular material Substances 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000010802 sludge Substances 0.000 claims description 5
- 230000010485 coping Effects 0.000 abstract description 2
- 230000002195 synergetic effect Effects 0.000 abstract description 2
- 239000011575 calcium Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910001425 magnesium ion Inorganic materials 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229910001424 calcium ion Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000002535 acidifier Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
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
-
- 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F2001/007—Processes including a sedimentation step
-
- 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
- C02F2001/5218—Crystallization
-
- 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
- C02F2101/14—Fluorine or fluorine-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
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/001—Upstream control, i.e. monitoring for predictive control
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/03—Pressure
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/05—Conductivity or salinity
- C02F2209/055—Hardness
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/11—Turbidity
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
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)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention provides a combined fluidized bed multifunctional water treatment system.A first water outlet pipe of a chemical crystallization circulating granulation fluidized bed main body device is communicated with a second water inlet pipe of a solid-liquid separation circulating granulation fluidized bed main body device through a first static mixer; the main body device of the chemical crystallization circulating granulation fluidized bed is connected with a seed crystal feeding unit, a medicament feeding unit and a particle discharging unit; a coagulant adding unit is arranged on the first water outlet pipe; the second water inlet pipe is connected with a micro-sand adding unit; the main body device of the solid-liquid separation circulating granulation fluidized bed is connected with a coagulant aid adding unit and a mud-water separation unit; a second static mixer is arranged on the second water outlet pipe, and a pH adjusting unit is arranged on the second water outlet pipe between the main body device of the solid-liquid separation circulating granulation fluidized bed and the second static mixer. The organic combination of the crystallization granulation fluidized bed and the circulating granulation fluidized bed can well perform synergistic treatment on the turbidity and the hardness, and provides an efficient coping and solving method.
Description
Technical Field
The invention belongs to the field of water treatment, relates to a granulation fluidized bed, and particularly relates to a multifunctional water treatment system of a combined fluidized bed.
Background
With the development of industry and the increase of population, water as a life source is seriously polluted, and in order to realize the sustainable development of human society, the problem of water pollution is solved firstly, and the composite pollution in water is increasingly serious. Ca is present in water2+、Mg2+、Fe2+、Mn2+、As3+And F-When the plasma exists in excess in water, the plasma can harm human health and reduce the efficiency of production equipment. In general, water plants need to ensure the water outlet effect through combined processes of medicament softening, aeration, filtration, electrodialysis and the like, so that the problems of large occupied area, complex process, difficult operation and management, increased treatment cost and the like are caused. When the turbidity in water changes greatly and the turbidity is higher or lower, the stability and the effect of the water treatment process can be influenced, the existing water quality purification device can treat single high-turbidity water, various technologies are developed at home and abroad, and the device is applied to actual engineering.
Disclosure of Invention
Aiming at the defects in the prior art, the invention aims to provide a combined fluidized bed multifunctional water treatment system, which solves the technical problem that the water treatment device in the prior art is not ideal in complex water quality treatment effect.
In order to solve the technical problems, the invention adopts the following technical scheme:
a combined fluidized bed multifunctional water treatment system comprises a chemical crystallization circulating granulation fluidized bed main body device and a solid-liquid separation circulating granulation fluidized bed main body device; a first water inlet pipe and a first water outlet pipe are arranged on the main body device of the chemical crystallization circulating granulation fluidized bed; a second water inlet pipe and a second water outlet pipe are arranged on the main body device of the solid-liquid separation circulating granulation fluidized bed;
the electromagnetic variable-frequency raw water pump and the first main water inlet valve are sequentially arranged on the first water inlet pipe along the water inlet direction; the first water outlet pipe is communicated with the second water inlet pipe through a first static mixer; the electromagnetic flow meter and the second main water inlet valve are sequentially arranged on the second water inlet pipe along the water inlet direction;
the upper part of the main body device of the chemical crystallization circulating granulation fluidized bed is connected with a crystal seed adding unit, the lower part of the main body device of the chemical crystallization circulating granulation fluidized bed is connected with a medicament adding unit, and the lower part of the main body device of the chemical crystallization circulating granulation fluidized bed is also connected with a particle discharging unit;
a coagulant adding unit is arranged on the first water outlet pipe;
a micro-sand feeding unit is connected on a second water inlet pipe between the electromagnetic flowmeter and a second main water inlet valve;
the lower part of the main body device of the solid-liquid separation circulating granulation fluidized bed is connected with a coagulant aid adding unit, and the bottom of the main body device of the solid-liquid separation circulating granulation fluidized bed is provided with a mud-water separation unit;
and a second water outlet pipe is provided with a second static mixer, and a pH adjusting unit is arranged on the second water outlet pipe between the main body device of the solid-liquid separation circulating granulation fluidized bed and the second static mixer.
The invention also has the following technical characteristics:
the seed crystal feeding unit comprises a seed crystal conveying tank water inlet pump, a seed crystal conveying tank, a particle pump and a seed crystal feeding valve which are sequentially connected, and the seed crystal feeding valve is communicated with the chemical crystallization circulating granulation fluidized bed main body device.
The medicament feeding unit comprises a medicament storage tank, a variable-frequency medicament feeding pump and a medicament feeding control valve which are sequentially connected, and the medicament feeding control valve is communicated with the chemical crystallization circulating granulation fluidized bed main body device.
The particle discharge unit comprises a particle discharge valve and a particle collection storage box which are sequentially connected to the main body device of the chemical crystallization circulating granulation fluidized bed along the particle discharge direction.
The coagulant adding unit comprises a coagulant solution tank, a coagulant control valve and a coagulant adding pump which are sequentially arranged on the first water outlet pipe along the water outlet direction.
The micro-sand adding unit comprises a mortar box, a mortar control valve and a mortar adding pump which are sequentially connected, and the mortar adding pump is communicated with the second water inlet pipe.
The coagulant aid adding unit comprises a coagulant aid solution tank, a coagulant aid control valve and a coagulant aid adding pump which are sequentially connected, and the coagulant aid adding pump is communicated with the main body device of the solid-liquid separation circulating granulation fluidized bed.
The mud-water separation unit comprises a mud-water separator arranged at the bottom of the main body device of the solid-liquid separation circulating granulation fluidized bed, the mud-water separator is connected with one end of a mud discharge pipeline, a mud discharge control valve and a mud discharge pump are sequentially arranged on the mud discharge pipeline, and the other end of the mud discharge pipeline is connected with a sludge dewatering workshop.
The pH adjusting unit comprises an acid liquid storage tank, an acid liquid variable-frequency feeding pump and an acid liquid feeding control valve which are sequentially connected, and the acid liquid feeding control valve is communicated with the second water outlet pipe.
The first water inlet pipe is also provided with a water inlet flowmeter and a water inlet pressure gauge; and a second water outlet pipe in front of the pH adjusting unit is provided with a first pH real-time online detector, and a second water outlet pipe behind the second static mixer is provided with a second pH real-time online detector and an online turbidity detector.
Compared with the prior art, the invention has the following technical effects:
high suspended matters in water can influence the crystallization and granulation process of calcium and magnesium ions, and high concentration of the calcium and magnesium ions can cause high turbidity of effluent. The organic combination of the crystallization granulation fluidized bed and the circulating granulation fluidized bed can well perform synergistic treatment on the turbidity and the hardness, and provides an efficient coping and solving method aiming at the complexity of water quality.
The system of the invention adjusts the position of the fluidized bed according to the quality of the inlet water, can mainly solve the problems of high/low turbidity, high calcium hardness, high magnesium hardness, high algae, high organic matter, high fluorine, high metal ion and other water quality, and has wide application range.
The system of the invention (III) can completely realize automatic control, has simple operation and management, compact connection of all functional units, high plane utilization rate, small occupied area and strong economic practicability.
(IV) the front and back sequence of the main body device of the chemical crystallization circulating granulation fluidized bed and the main body device of the solid-liquid separation circulating granulation fluidized bed can be adjusted according to the water quality condition. The water inlet turbidity is low, the hardness is high, and the chemical crystallization circulating granulation fluidized bed main body device is in front; the inlet water has high turbidity and low hardness, and the chemical crystallization circulating granulation fluidized bed is arranged behind the main body.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the combined fluidized bed multifunctional water treatment system of the invention.
The meaning of the individual reference symbols in the figures is: 1-a chemical crystallization circulating granulation fluidized bed main body device, 2-a solid-liquid separation circulating granulation fluidized bed main body device, 3 a first water inlet pipe, 4-a first water outlet pipe, 5-a second water inlet pipe, 6-a second water outlet pipe, 7-an electromagnetic frequency conversion raw water pump, 8-a first total water inlet valve, 9-a first static mixer, 10-an electromagnetic flow meter, a second total water inlet valve, 12-a crystal seed adding unit, 13-a medicament adding unit, 14-a particle discharging unit, 15-a coagulant adding unit, 16-a micro-sand adding unit, 17-a coagulant aid adding unit, 18-a mud-water separating unit, 19-a second static mixer, 20-a pH adjusting unit, 21-a water inlet flow meter, 22-a water inlet pressure gauge and 23-a first pH real-time online detector, 24-a second pH real-time online detector and 25-an online turbidity detector;
1201-seed crystal conveying tank water inlet pump, 1202-seed crystal conveying tank, 1203-particle pump and 1204-seed crystal feeding valve;
1301-a medicament storage tank, 1302-a variable-frequency medicament feeding pump and 1303-a medicament feeding control valve;
1401-particle discharge valve, 1402-particle collection storage tank;
1501-coagulant solution pool, 1502-coagulant control valve, 1503-coagulant adding pump;
1601-mortar box, 1602-mortar control valve, 1603-mortar adding pump;
1701-coagulant aid solution pool, 1702-coagulant aid control valve, 1703-coagulant aid feeding pump;
1801-mud-water separator, 1802-mud discharge pipeline, 1803-mud discharge control valve, 1804-mud discharge pump, 1805-sludge dewatering workshop;
2001-acid liquor storage tank, 2002-acid liquor variable frequency adding pump, 2003-acid liquor adding control valve.
The present invention will be explained in further detail with reference to examples.
Detailed Description
It is to be understood that all components and devices of the present invention, unless otherwise specified, are constructed using components known in the art. For example, a chemical crystallization circulating granulation fluid bed main body device 1 and a solid-liquid separation circulating granulation fluid bed main body device 2.
As a preferable mode of the invention, the chemical crystallization circulating granulation fluidized bed main body device 1 adopts a chemical crystallization circulating granulation fluidized bed main body in the Chinese utility model patent with the patent number of ZL 201820576426.5, the grant publication number of CN 208327613U and the patent name of 'chemical crystallization circulating granulation fluidized bed water treatment system and carbon dioxide adjusting device'.
As a preferable mode of the invention, the chemical crystallization circulating granulation fluidized bed main body device 1 adopts a chemical crystallization circulating granulation fluidized bed water treatment device disclosed in Chinese invention patent with patent number ZL 201510864696.7, grant publication number CN 105502692B and patent name 'a chemical crystallization circulating granulation fluidized bed water treatment device'.
As a preferable mode of the present invention, the main body device 2 of the solid-liquid separation circulating granulation fluidized bed in the present invention is a main body device of a fluidized bed in the chinese utility model patent having patent No. ZL201820584535.1, No. CN208265834U, and a patent name of "a circulating granulation fluidized bed apparatus for low-temperature low-turbidity, high-turbidity or high-algae water treatment".
The invention introduces the Chinese utility model patent with patent number ZL 201820576426.5, grant publication number CN 208327613U, and patent name "chemical crystallization circulating granulation fluidized bed water treatment system and carbon dioxide adjusting device" to further explain the concrete technical scheme and technical principle of the invention.
The invention further explains the specific technical scheme and the technical principle of the invention by citing all the contents described in Chinese invention patent with patent number ZL 201510864696.7, grant publication number CN 105502692B and patent name 'a chemical crystallization circulating granulation fluidized bed water treatment device'.
The invention introduces the Chinese utility model patent with patent number ZL201820584535.1, grant publication number CN208265834U and patent name "a circulating granulation fluidized bed equipment for low-temperature low-turbidity, high-turbidity or high-algae water treatment", and the whole content of the invention further explains the specific technical scheme and technical principle of the invention.
The following embodiments of the present invention are provided, and it should be noted that the present invention is not limited to the following embodiments, and all equivalent changes based on the technical solutions of the present invention are within the protection scope of the present invention.
Example (b):
the embodiment provides a combined fluidized bed multifunctional water treatment system, as shown in fig. 1, comprising a chemical crystallization circulating granulation fluidized bed main body device 1 and a solid-liquid separation circulating granulation fluidized bed main body device 2; a first water inlet pipe 3 and a first water outlet pipe 4 are arranged on the chemical crystallization circulating granulation fluidized bed main body device 1; a second water inlet pipe 5 and a second water outlet pipe 6 are arranged on the main body device 2 of the solid-liquid separation circulating granulation fluidized bed;
an electromagnetic variable-frequency raw water pump 7 and a first main water inlet valve 8 are sequentially arranged on the first water inlet pipe 3 along the water inlet direction; the first water outlet pipe 4 is communicated with the second water inlet pipe 5 through a first static mixer 9; an electromagnetic flowmeter 10 and a second main water inlet valve 11 are sequentially arranged on the second water inlet pipe 5 along the water inlet direction;
the upper part of the main body device 1 of the chemical crystallization circulating granulation fluidized bed is connected with a crystal seed adding unit 12, the lower part of the main body device 1 of the chemical crystallization circulating granulation fluidized bed is connected with a medicament adding unit 13, and the lower part of the main body device 1 of the chemical crystallization circulating granulation fluidized bed is also connected with a particle discharging unit 14;
a coagulant adding unit 15 is arranged on the first water outlet pipe 4;
a micro-sand adding unit 16 is connected on the second water inlet pipe 5 between the electromagnetic flow meter 10 and the second main water inlet valve 11;
the lower part of the main body device 2 of the solid-liquid separation circulating granulation fluidized bed is connected with a coagulant aid adding unit 17, and the bottom of the main body device 2 of the solid-liquid separation circulating granulation fluidized bed is provided with a mud-water separation unit 18;
a second static mixer 19 is arranged on the second water outlet pipe 6, and a pH adjusting unit 20 is arranged on the second water outlet pipe 6 between the solid-liquid separation circulating granulation fluidized bed main body device 2 and the second static mixer 19.
As a preferable scheme of this embodiment, the seed crystal feeding unit 12 includes a seed crystal conveying tank water inlet pump 1201, a seed crystal conveying tank 1202, a particle pump 1203 and a seed crystal feeding valve 1204, which are connected in sequence, where the seed crystal feeding valve 1204 is communicated with the chemical crystallization circulating granulation fluidized bed main body device 1. The seed crystal adding unit 6 realizes the adding control by controlling the quality of the added seed crystal.
As a preferable scheme of this embodiment, the chemical adding unit 13 includes a chemical storage tank 1301, a variable frequency chemical adding pump 1302 and a chemical adding control valve 1303, which are connected in sequence, and the chemical adding control valve 1303 is communicated with the chemical crystallization circulating granulation fluidized bed main body device 1. The agent adding unit 13 is used for adding NaOH, Ca (OH)2Or Na2CO3。
As a preferable mode of this embodiment, the granule discharging unit 14 includes a granule discharging valve 1401 and a granule collecting storage tank 1402 which are connected to the chemical crystallization circulating granulation fluid bed main body apparatus 1 in this order in the granule discharging direction.
As a preferable scheme of this embodiment, the coagulant adding unit 15 includes a coagulant solution tank 1501, a coagulant control valve 1502, and a coagulant adding pump 1503, which are sequentially disposed on the first water outlet pipe 4 along the water outlet direction. The coagulant used in the coagulant adding unit 15 can be the conventional coagulant in the field.
As a preferable scheme of this embodiment, the fine sand adding unit 16 includes a mortar box 1601, a mortar control valve 1602 and a mortar adding pump 1603 connected in sequence, and the mortar adding pump 1603 is communicated with the second water inlet pipe 5. The fine sand used in the fine sand adding unit 16 may be conventional fine sand in the art.
As a preferable scheme of the embodiment, the coagulant aid adding unit 17 comprises a coagulant aid solution tank 1701, a coagulant aid control valve 1702 and a coagulant aid adding pump 1703 which are connected in sequence, wherein the coagulant aid adding pump 1703 is communicated with the main body device 2 of the solid-liquid separation circulating granulation fluidized bed. The coagulant aid used in the coagulant aid adding unit 17 can be conventional coagulant aids in the field.
As a preferable mode of this embodiment, the mud-water separation unit 18 includes a mud-water separator 1801 disposed at the bottom of the main body 2 of the solid-liquid separation circulating granulation fluid bed, the mud-water separator 1801 is connected to one end of a mud discharge pipe 1802, the mud discharge pipe 1802 is sequentially provided with a mud discharge control valve 1803 and a mud discharge pump 1804, and the other end of the mud discharge pipe 1802 is connected to a mud dewatering plant 1805.
As a preferable scheme of this embodiment, the pH adjusting unit 20 includes an acid liquid storage tank 2001, an acid liquid variable frequency adding pump 2002, and an acid liquid adding control valve 2003, which are connected in sequence, where the acid liquid adding control valve 2003 is communicated with the second water outlet pipe 6. The acidifying agent used in the pH adjustment unit 20 is HCl or H2SO4。
As a preferable scheme of this embodiment, the first water inlet pipe 12 is further provided with a water inlet flow meter 21 and a water inlet pressure gauge 22; a first real-time online pH detector 23 is arranged on the second water outlet pipe 6 in front of the pH adjusting unit 20, and a second real-time online pH detector 24 and an online turbidity detector 25 are arranged on the second water outlet pipe 6 behind the second static mixer 19. Furthermore, the system of the embodiment can be matched with a corresponding automatic control module according to actual needs to realize automatic control.
The working process of the invention is as follows:
when the system is used, the seed crystal feeding unit 12 fills seed crystals at the bottom of the main body device 1 of the chemical crystallization circulating granulation fluidized bed, and high-hardness raw water enters the bottom of the main body device 1 of the chemical crystallization circulating granulation fluidized bed through the electromagnetic frequency conversion raw water pump 7 to enable the seed crystals to be in a fluidized state; the variable-frequency medicament feeding pump 1302 feeds the softening medicament into the chemical crystallization circulating granulation fluidized bed main body device 1, the target component is precipitated and crystallized on the seed crystal, the particles grow and become heavy and gradually sink to the bottom of the chemical crystallization circulating granulation fluidized bed main body device 3, a certain number of large-particle crystals are discharged through the particle discharge valve 1401 regularly, and a certain number of seed crystals are fed through the seed crystal conveying tank 1202, and the cycle is repeated.
The effluent treated by the main body device 1 of the chemical crystallization circulating granulation fluidized bed enters a main body device 2 of the solid-liquid separation circulating granulation fluidized bed, corresponding materials are added into a first water outlet pipe 4 through a coagulant adding pump 1503 and a second water inlet pipe 5 through a mortar adding pump 1603 and a coagulant aid adding pump 1703, the amount of acid liquor is controlled through a second pH real-time online detector 24, the pH of the effluent is adjusted through an acid liquor variable-frequency adding pump 2002, and the sludge produced by treatment through a mud-water separator 1801 is discharged to a sludge dewatering workshop 1805.
The system has the advantages of clear integral structure, compact connection of all functional units, high plane utilization rate and convenient operation, can simultaneously remove turbidity and hardness in water, and can synchronously and efficiently remove various ions in the water.
According to the scheme, the water treatment system of the invention perfects single equipment in the prior art, makes up for the defects of equipment application, provides a new combination mode of the joint operation of two fluidized beds, and can be flexibly replaced according to water quality.
Claims (10)
1. A combined fluidized bed multifunctional water treatment system comprises a chemical crystallization circulating granulation fluidized bed main body device (1) and a solid-liquid separation circulating granulation fluidized bed main body device (2); a first water inlet pipe (3) and a first water outlet pipe (4) are arranged on the chemical crystallization circulating granulation fluidized bed main body device (1); a second water inlet pipe (5) and a second water outlet pipe (6) are arranged on the main body device (2) of the solid-liquid separation circulating granulation fluidized bed;
the method is characterized in that:
an electromagnetic variable-frequency raw water pump (7) and a first main water inlet valve (8) are sequentially arranged on the first water inlet pipe (3) along the water inlet direction; the first water outlet pipe (4) is communicated with the second water inlet pipe (5) through a first static mixer (9); an electromagnetic flowmeter (10) and a second main water inlet valve (11) are sequentially arranged on the second water inlet pipe (5) along the water inlet direction;
the upper part of the chemical crystallization circulating granulation fluidized bed main body device (1) is connected with a seed crystal feeding unit (12), the lower part of the chemical crystallization circulating granulation fluidized bed main body device (1) is connected with a medicament feeding unit (13), and the lower part of the chemical crystallization circulating granulation fluidized bed main body device (1) is also connected with a particle discharging unit (14);
a coagulant adding unit (15) is arranged on the first water outlet pipe (4);
a micro-sand adding unit (16) is connected on the second water inlet pipe (5) between the electromagnetic flowmeter (10) and the second main water inlet valve (11);
the lower part of the main body device (2) of the solid-liquid separation circulating granulation fluidized bed is connected with a coagulant aid adding unit (17), and the bottom of the main body device (2) of the solid-liquid separation circulating granulation fluidized bed is provided with a mud-water separation unit (18);
a second static mixer (19) is arranged on the second water outlet pipe (6), and a pH adjusting unit (20) is arranged on the second water outlet pipe (6) between the solid-liquid separation circulating granulation fluidized bed main body device (2) and the second static mixer (19).
2. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the seed crystal feeding unit (12) comprises a seed crystal delivery tank water inlet pump (1201), a seed crystal delivery tank (1202), a particle pump (1203) and a seed crystal feeding valve (1204) which are connected in sequence, and the seed crystal feeding valve (1204) is communicated with the chemical crystallization circulating granulation fluidized bed main body device (1).
3. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the agent adding unit (13) comprises an agent storage tank (1301), a variable frequency agent adding pump (1302) and an agent adding control valve (1303) which are connected in sequence, and the agent adding control valve (1303) is communicated with the chemical crystallization circulating granulation fluidized bed main body device (1).
4. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the granule discharging unit (14) comprises a granule discharging valve (1401) and a granule collecting storage tank (1402) which are connected to the chemical crystallization circulating granulation fluidized bed main body device (1) in sequence along the granule discharging direction.
5. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the coagulant adding unit (15) comprises a coagulant solution tank (1501), a coagulant control valve (1502) and a coagulant adding pump (1503) which are sequentially arranged on the first water outlet pipe (4) along the water outlet direction.
6. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the micro-sand adding unit (16) comprises a mortar box (1601), a mortar control valve (1602) and a mortar adding pump (1603) which are connected in sequence, and the mortar adding pump (1603) is communicated with the second water inlet pipe (5).
7. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the coagulant aid adding unit (17) comprises a coagulant aid solution tank (1701), a coagulant aid control valve (1702) and a coagulant aid adding pump (1703) which are connected in sequence, and the coagulant aid adding pump (1703) is communicated with the main body device (2) of the solid-liquid separation circulating granulation fluidized bed.
8. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the mud-water separation unit (18) comprises a mud-water separator (1801) arranged at the bottom of the solid-liquid separation circulating granulation fluidized bed main body device (2), the mud-water separator (1801) is connected with one end of a mud discharge pipeline (1802), a mud discharge control valve (1803) and a mud discharge pump (1804) are sequentially arranged on the mud discharge pipeline (1802), and the other end of the mud discharge pipeline (1802) is connected with the sludge dewatering plant (1805).
9. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the pH adjusting unit (20) comprises an acid storage tank (2001), an acid variable frequency adding pump (2002) and an acid adding control valve (2003) which are connected in sequence, and the acid adding control valve (2003) is communicated with the second water outlet pipe (6).
10. The combined fluidized bed multifunctional water treatment system as claimed in claim 1, wherein the first water inlet pipe (12) is further provided with a water inlet flow meter (21) and a water inlet pressure gauge (22); a first pH real-time online detector (23) is arranged on a second water outlet pipe (6) in front of the pH adjusting unit (20), and a second pH real-time online detector (24) and an online turbidity detector (25) are arranged on the second water outlet pipe (6) behind the second static mixer (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110311175.4A CN113149267A (en) | 2021-03-24 | 2021-03-24 | Multifunctional water treatment system of combined fluidized bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110311175.4A CN113149267A (en) | 2021-03-24 | 2021-03-24 | Multifunctional water treatment system of combined fluidized bed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN113149267A true CN113149267A (en) | 2021-07-23 |
Family
ID=76888406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110311175.4A Pending CN113149267A (en) | 2021-03-24 | 2021-03-24 | Multifunctional water treatment system of combined fluidized bed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN113149267A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105502692A (en) * | 2015-11-30 | 2016-04-20 | 西安建筑科技大学 | Fluidized bed water treatment device realizing chemical crystallization circulating granulation |
| CN208265834U (en) * | 2018-04-23 | 2018-12-21 | 西安唯源环保科技有限公司 | A kind of low-temperature and low turbidity, high turbid or algae blooms water processing the granulating fluidized bed equipment of circulation |
| CN208327613U (en) * | 2018-04-20 | 2019-01-04 | 西安建筑科技大学 | Chemicrystallization recycles granulating fluidized bed water treatment system and carbon dioxide regulating device |
| CN214936611U (en) * | 2021-03-24 | 2021-11-30 | 西安建筑科技大学 | Multifunctional water treatment system of combined fluidized bed |
-
2021
- 2021-03-24 CN CN202110311175.4A patent/CN113149267A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105502692A (en) * | 2015-11-30 | 2016-04-20 | 西安建筑科技大学 | Fluidized bed water treatment device realizing chemical crystallization circulating granulation |
| CN208327613U (en) * | 2018-04-20 | 2019-01-04 | 西安建筑科技大学 | Chemicrystallization recycles granulating fluidized bed water treatment system and carbon dioxide regulating device |
| CN208265834U (en) * | 2018-04-23 | 2018-12-21 | 西安唯源环保科技有限公司 | A kind of low-temperature and low turbidity, high turbid or algae blooms water processing the granulating fluidized bed equipment of circulation |
| CN214936611U (en) * | 2021-03-24 | 2021-11-30 | 西安建筑科技大学 | Multifunctional water treatment system of combined fluidized bed |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN111153531A (en) | Liquid crystal display panel production plant fluorine-containing wastewater treatment device and process | |
| CN214936611U (en) | Multifunctional water treatment system of combined fluidized bed | |
| CN205442869U (en) | It produces brackish water desalination system of water recovery rate to improve bitter | |
| CN101955301B (en) | Method and equipment for treating micropollution raw water based on biological bamboo charcoal contact oxidation method | |
| CN112479396A (en) | Deep treatment softening system and process for drainage water | |
| CN113003757A (en) | Integrated rural water supply treatment device and method | |
| CN113149267A (en) | Multifunctional water treatment system of combined fluidized bed | |
| CN207943967U (en) | Electrolytic manganese ammonia nitrogen waste water processing system | |
| CN106007040A (en) | Heavy metal wastewater treatment system and method | |
| CN102642952A (en) | Pressure type integrated water purifier | |
| CN204490648U (en) | The complexes of a kind of electrolytic manganese ammonia nitrogen waste water process | |
| CN210736403U (en) | Heavy metal wastewater treatment system | |
| CN206089273U (en) | Multi -stage filtration formula sewage treatment device | |
| CN215559437U (en) | Wastewater treatment system | |
| CN213771731U (en) | A online phosphorus removal device for sewage treatment | |
| CN215592773U (en) | Integrated rural water supply treatment device | |
| CN211871651U (en) | Liquid crystal display panel manufacturing plant fluorine-containing wastewater treatment device | |
| CN210140512U (en) | Environment-friendly RO reverse osmosis effluent treatment plant of cycle recycle | |
| CN103641259B (en) | Desulfurization wastewater treatment device | |
| CN112125471A (en) | Online phosphorus removal device and method for sewage treatment | |
| CN206799338U (en) | A kind of complete water-purifying apparatus of container-type | |
| TWI534094B (en) | Treatment method by using fluidized-bed crystallization technology to remove phosphate from phosphate-containing wastewater | |
| JPH11147088A (en) | Dephosphorization of waste water | |
| CN215161887U (en) | Landfill leachate treatment system | |
| CN210736402U (en) | Integrated treatment system for heavy metal wastewater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |