CN107235569A - A kind of hydraulic engineering mud wastewater treatment equipment - Google Patents
A kind of hydraulic engineering mud wastewater treatment equipment Download PDFInfo
- Publication number
- CN107235569A CN107235569A CN201710676608.XA CN201710676608A CN107235569A CN 107235569 A CN107235569 A CN 107235569A CN 201710676608 A CN201710676608 A CN 201710676608A CN 107235569 A CN107235569 A CN 107235569A
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- Prior art keywords
- filter
- activated carbon
- separation chamber
- precipitation separation
- amorphous particle
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 123
- 239000002245 particle Substances 0.000 claims abstract description 73
- 238000000926 separation method Methods 0.000 claims abstract description 63
- 238000001556 precipitation Methods 0.000 claims abstract description 59
- 238000001914 filtration Methods 0.000 claims abstract description 18
- 239000002351 wastewater Substances 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 39
- 229910000881 Cu alloy Inorganic materials 0.000 claims description 25
- 239000008187 granular material Substances 0.000 claims description 22
- 229910001220 stainless steel Inorganic materials 0.000 claims description 14
- 239000010802 sludge Substances 0.000 claims description 13
- 238000011282 treatment Methods 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 10
- 239000010935 stainless steel Substances 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 6
- 229920002472 Starch Polymers 0.000 claims description 5
- WHWDWIHXSPCOKZ-UHFFFAOYSA-N hexahydrofarnesyl acetone Natural products CC(C)CCCC(C)CCCC(C)CCCC(C)=O WHWDWIHXSPCOKZ-UHFFFAOYSA-N 0.000 claims description 5
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 claims description 5
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 claims description 5
- 235000019698 starch Nutrition 0.000 claims description 5
- 239000008107 starch Substances 0.000 claims description 5
- 239000003610 charcoal Substances 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims 3
- 229910000831 Steel Inorganic materials 0.000 claims 1
- 229910052742 iron Inorganic materials 0.000 claims 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims 1
- 239000010959 steel Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 5
- 239000002131 composite material Substances 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000020535 bottled fortified water Nutrition 0.000 description 1
- 238000007596 consolidation process Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- RSMUVYRMZCOLBH-UHFFFAOYSA-N metsulfuron methyl Chemical compound COC(=O)C1=CC=CC=C1S(=O)(=O)NC(=O)NC1=NC(C)=NC(OC)=N1 RSMUVYRMZCOLBH-UHFFFAOYSA-N 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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
- C02F1/283—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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- 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
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)
- Filtration Of Liquid (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention relates to a kind of hydraulic engineering mud wastewater treatment equipment, including filter chamber, precipitation separation chamber, activated carbon filter and amorphous particle filter.By being configured and specifically improving to all parts so that mud waste water filtering effect is further lifted.
Description
Technical field
The invention belongs to hydraulic engineering field of waste water treatment, and in particular to a kind of hydraulic engineering mud wastewater treatment equipment.
Background technology
During the construction of hydro project of sludge treatment, many times all mud and water can integrally be extracted（Sometimes it is
Processing mud can also add water in addition）Handled, the water after separation mud much can be all again introduced into as recycle-water
Into sludge treatment system, but it is due to much can all have substantial amounts of heavy metal, and separate the water after mud in mud
In can still have many mud residual, if directly produced using these merely through the water after primary treatment, can send out
It is raw to block (operating) water nozzle and generation situations such as corroding water tube component, and such case can cause device integrally to give birth to if occurring
Production is terminated, and these parts for maintenance costs damaged all are usually very big（The not exclusively cost of these parts in itself,
Also include cost of labor and the dismounting and change with its component）.
The content of the invention
A kind of hydraulic engineering mud wastewater treatment equipment of proposition of the present invention.
Realized by following technological means：
A kind of hydraulic engineering mud wastewater treatment equipment, including filter chamber, precipitation separation chamber, activated carbon filter and amorphous particle
Filter.
Angularly disposed in the filter chamber to have mud filter, the mud filter is inclined by the way of right low left high
Tiltedly so that filter chamber's left hand inlet port is arranged at the downside of mud filter, and filter chamber's right-side outlet is arranged at mud filter
Upside；Filter chamber's left hand inlet port is provided with inlet channel, the inlet channel and is provided with booster water pump, in the mistake
Filter chamber right-side outlet is connected with waste water dispatch tube；Filter chamber lower end is provided with silt collecting box.
It is divided into mistress, middle room and interior room inside the precipitation separation chamber, the entrance of the precipitation separation chamber is arranged on described
The top centre of separation chamber is precipitated, and is connected with the waste water dispatch tube, during side is provided with the vertex of a cone upward under the inlet
Empty cone, the vertex of a cone of cone is located at the underface of entrance, and cone side wall upper part is slanting baffle, and bottom is to be provided with filter opening
Outer filter plate, slanting baffle, outer filter plate with precipitation separation chamber shell constitute mistress；The position connected with outer filter plate from slanting baffle to
Under extend to the precipitation separation chamber exit of precipitation separation chamber bottom centre and be provided with interior filter membranous layer, outer filter plate and interior filter membranous layer
And the region between precipitation separation chamber's bottom wall forms middle room；The region of interior filter membranous layer and slanting baffle Inner Constitution forms interior room,
It is provided with agitating shaft straight down at interior ceiling end, the stirring vane of the agitating shaft is propeller blade, passes through agitating shaft
Stirring so that water in interior room is to precipitation separation chamber's output flow；The slanting baffle is stainless steel plate, and the outer filter plate is porous
Stainless steel plate on the multiple filtration film layer laid, the interior filter membranous layer is the multiple filtration film layer that stainless steel wire is laid on the net；
The outside of the precipitation separation chamber of outer filter plate lower terminal end is provided with refuse collecting case, for collecting what is tumbled from outer filter plate top
Debris.
The entrance of the amorphous particle filter is connected with precipitation separation chamber outlet, is internally provided with the amorphous of multilayer
Particle, the outlet of amorphous particle filter is arranged on the two ends on the downside of amorphous particle filter.
The entrance of the activated carbon filter is connected with the outlet of the amorphous particle filter, is internally provided with multilayer
Activated carbon filter, the outlet of activated carbon filter is arranged on the center on the downside of activated carbon filter, with filtering water outlet phase
Even.
Preferably, the entrance of the silt collecting box is disposed thereon the right-hand member in portion.
Preferably, the refuse collecting case precipitates the outer of separation chamber for the setting of ring-type in outer filter plate lower terminal end
Portion.
Preferably, the amorphous particle is Fe-based amorphous particle.
Preferably, the amorphous particle filter is internally provided with the amorphous particle of multilayer, specially copper alloy plate is pressed from both sides
The amorphous particle held, and multilayer copper alloy plate is snakelike setting so that the serpentine-like mode of filter water is contacted with amorphous particle.
Preferably, the activated carbon filter of the multilayer is the activated carbon granule that porous copper alloy plate is clamped, every two layers
Activated carbon granule, and aperture of the particle diameter more than porous copper alloy plate of activated carbon granule are clamped between porous copper alloy plate.
Preferably, the material of the amorphous particle is Fe68Ni11Sm0.3Tb0.9C3B6La3P5（Atomic ratio）.
Preferably, the activated carbon granule is composite activated carbon grain, specific weight is：Activated carbon：15~20
Part, starch：11 ~ 13 parts, Sodium Polyacrylate：1 ~ 1.8 part, phytone：1 ~ 2 part.
Preferably, the mud filter angle of inclination（With horizontal plane angle）For 20 ~ 29.
Effect of the invention is that：
1, because waste water is to handle the waste water after mud, therefore it wherein can still contain certain mud, and mud is with higher
Viscosity, by using the oblique filter of the reverse filter type of lower solid upper liquid so that residual sludge is directly fallen, and by
In the factor of gravity, the water on top can also downwards be flowed back by filter, again rush the mud residue adhered on filter
Brush off, prevent adherence to and filter is blocked on filter.The purpose of supercharging is reached by setting water pump, filtering effect is enhanced
Rate.
2, by designing the precipitation separation chamber of abnormity, center of top enters water, surrounding is separated water into by conical top
Mistress in, because mistress has oblique slanting baffle, due to the factor of gravity, therefore floccule in water and water all can be along
Slanting baffle and outer filter plate are moved down, and integrally in static state in mistress, solid-state floccule is easy to downward precipitation.And in bottom,
By outer filter plate, solid-state debris is filtered, solid-state debris and sediment continue to move down by oblique outer filter plate,
So as to reach in refuse collecting case, water is entered in middle room by outer filter plate, is entered by the filtering film layer between middle room and interior room
The further filter operation of row is entered in interior room.And due in interior room be provided with rotate propeller blade and bottom be water outlet
Mouthful so that interior room formation negative pressure, and the power that then such negative pressure meeting fortified water flows to interior room again from mistress to middle room, from
And in the case where keeping mistress static relative increase hydraulic pressure, enhance purification efficiency.
3, due in the waste water after sludge treatment except solid matter, heavy metal also containing many ionic conditions and other
Ion, by setting amorphous particle filter to handle these ions, then by activated carbon to various residuals and
Consolidation ion is adsorbed, so that harmful substance has obtained removal as much as possible in waste water.By to amorphous particle mistake
The entrance and exit position of filter plate and activated carbon filter is specifically set so that processing water is in amorphous particle and in activity
The contact with many areas as far as possible for a long time as far as possible is reached in charcoal, so as in the case where not increasing device volume, enhance
Filter effect.Specifically improved by the material to activated carbon granule and amorphous particle so that it more conforms to sludge treatment
The specific water quality of waste water.
Brief description of the drawings
Fig. 1 is the structural representation of hydraulic engineering mud wastewater treatment equipment.
Wherein：1- filter chambers, 11- inlet channels, 12- booster water pumps, 13- mud filters, 14- silt collecting boxes, 15-
Filter membranous layer in waste water dispatch tube, 21- slanting baffles, the outer filter plates of 22-, 23- agitating shafts, 24-, 25- refuse collecting casees, 26- precipitations point
From room outlet, 3- amorphous particle filters, 31- amorphous particle filter delivery ports, 4- activated carbon filters, 5- filter waters go out
Mouthful.
Embodiment
Embodiment 1
A kind of hydraulic engineering mud wastewater treatment equipment, including filter chamber, precipitation separation chamber, activated carbon filter and amorphous particle
Filter.
Angularly disposed in the filter chamber to have mud filter, the mud filter is inclined by the way of right low left high
Tiltedly so that filter chamber's left hand inlet port is arranged at the downside of mud filter, and filter chamber's right-side outlet is arranged at mud filter
Upside；Filter chamber's left hand inlet port is provided with inlet channel, the inlet channel and is provided with booster water pump, in the mistake
Filter chamber right-side outlet is connected with waste water dispatch tube；Filter chamber lower end is provided with silt collecting box.
It is divided into mistress, middle room and interior room inside the precipitation separation chamber, the entrance of the precipitation separation chamber is arranged on described
The top centre of separation chamber is precipitated, and is connected with the waste water dispatch tube, during side is provided with the vertex of a cone upward under the inlet
Empty cone, the vertex of a cone of cone is located at the underface of entrance, and cone side wall upper part is slanting baffle, and bottom is to be provided with filter opening
Outer filter plate, slanting baffle, outer filter plate with precipitation separation chamber shell constitute mistress；The position connected with outer filter plate from slanting baffle to
Under extend to the precipitation separation chamber exit of precipitation separation chamber bottom centre and be provided with interior filter membranous layer, outer filter plate and interior filter membranous layer
And the region between precipitation separation chamber's bottom wall forms middle room；The region of interior filter membranous layer and slanting baffle Inner Constitution forms interior room,
It is provided with agitating shaft straight down at interior ceiling end, the stirring vane of the agitating shaft is propeller blade, passes through agitating shaft
Stirring so that water in interior room is to precipitation separation chamber's output flow；The slanting baffle is stainless steel plate, and the outer filter plate is porous
Stainless steel plate on the multiple filtration film layer laid, the interior filter membranous layer is the multiple filtration film layer that stainless steel wire is laid on the net；
The outside of the precipitation separation chamber of outer filter plate lower terminal end is provided with refuse collecting case, for collecting what is tumbled from outer filter plate top
Debris.
The entrance of the amorphous particle filter is connected with precipitation separation chamber outlet, is internally provided with the amorphous of multilayer
Particle, the outlet of amorphous particle filter is arranged on the two ends on the downside of amorphous particle filter.
The entrance of the activated carbon filter is connected with the outlet of the amorphous particle filter, is internally provided with multilayer
Activated carbon filter, the outlet of activated carbon filter is arranged on the center on the downside of activated carbon filter, with filtering water outlet phase
Even.
The entrance of the silt collecting box is disposed thereon the right-hand member in portion.
The refuse collecting case is outside of the setting in the precipitation separation chamber of outer filter plate lower terminal end of ring-type.
The amorphous particle is Fe-based amorphous particle.
The amorphous particle filter is internally provided with the amorphous of the amorphous particle of multilayer, specially copper alloy plate clamping
Grain, and multilayer copper alloy plate is snakelike setting so that the serpentine-like mode of filter water is contacted with amorphous particle.
The activated carbon filter of the multilayer is the activated carbon granule that porous copper alloy plate is clamped, every two layers of porous copper alloy
Activated carbon granule, and aperture of the particle diameter more than porous copper alloy plate of activated carbon granule are clamped between plate.
The material of the amorphous particle is Fe68Ni11Sm0.3Tb0.9C3B6La3P5（Atomic ratio）.
The activated carbon granule is composite activated carbon grain, and specific weight is：Activated carbon：16 parts, starch：12
Part, Sodium Polyacrylate：1.2 parts, phytone：1.3 part.
The mud filter angle of inclination（With horizontal plane angle）For 23.
Embodiment 2
A kind of hydraulic engineering mud wastewater treatment equipment, including filter chamber, precipitation separation chamber, activated carbon filter and amorphous particle
Filter.
Angularly disposed in the filter chamber to have mud filter, the mud filter is inclined by the way of right low left high
Tiltedly so that filter chamber's left hand inlet port is arranged at the downside of mud filter, and filter chamber's right-side outlet is arranged at mud filter
Upside；Filter chamber's left hand inlet port is provided with inlet channel, the inlet channel and is provided with booster water pump, in the mistake
Filter chamber right-side outlet is connected with waste water dispatch tube；Filter chamber lower end is provided with silt collecting box.
It is divided into mistress, middle room and interior room inside the precipitation separation chamber, the entrance of the precipitation separation chamber is arranged on described
The top centre of separation chamber is precipitated, and is connected with the waste water dispatch tube, during side is provided with the vertex of a cone upward under the inlet
Empty cone, the vertex of a cone of cone is located at the underface of entrance, and cone side wall upper part is slanting baffle, and bottom is to be provided with filter opening
Outer filter plate, slanting baffle, outer filter plate with precipitation separation chamber shell constitute mistress；The position connected with outer filter plate from slanting baffle to
Under extend to the precipitation separation chamber exit of precipitation separation chamber bottom centre and be provided with interior filter membranous layer, outer filter plate and interior filter membranous layer
And the region between precipitation separation chamber's bottom wall forms middle room；The region of interior filter membranous layer and slanting baffle Inner Constitution forms interior room,
It is provided with agitating shaft straight down at interior ceiling end, the stirring vane of the agitating shaft is propeller blade, passes through agitating shaft
Stirring so that water in interior room is to precipitation separation chamber's output flow；The slanting baffle is stainless steel plate, and the outer filter plate is porous
Stainless steel plate on the multiple filtration film layer laid, the interior filter membranous layer is the multiple filtration film layer that stainless steel wire is laid on the net；
The outside of the precipitation separation chamber of outer filter plate lower terminal end is provided with refuse collecting case, for collecting what is tumbled from outer filter plate top
Debris.
The entrance of the amorphous particle filter is connected with precipitation separation chamber outlet, is internally provided with the amorphous of multilayer
Particle, the outlet of amorphous particle filter is arranged on the two ends on the downside of amorphous particle filter.
The entrance of the activated carbon filter is connected with the outlet of the amorphous particle filter, is internally provided with multilayer
Activated carbon filter, the outlet of activated carbon filter is arranged on the center on the downside of activated carbon filter, with filtering water outlet phase
Even.
The entrance of the silt collecting box is disposed thereon the right-hand member in portion.
The refuse collecting case is outside of the setting in the precipitation separation chamber of outer filter plate lower terminal end of ring-type.
The amorphous particle is Fe-based amorphous particle.
The amorphous particle filter is internally provided with the amorphous of the amorphous particle of multilayer, specially copper alloy plate clamping
Grain, and multilayer copper alloy plate is snakelike setting so that the serpentine-like mode of filter water is contacted with amorphous particle.
The activated carbon filter of the multilayer is the activated carbon granule that porous copper alloy plate is clamped, every two layers of porous copper alloy
Activated carbon granule, and aperture of the particle diameter more than porous copper alloy plate of activated carbon granule are clamped between plate.
The material of the amorphous particle is Fe68Ni11Sm0.3Tb0.9C3B6La3P5（Atomic ratio）.
The activated carbon granule is composite activated carbon grain, and specific weight is：Activated carbon：18 parts, starch：12.5
Part, Sodium Polyacrylate：1.6 parts, phytone：1.8 part.
The mud filter angle of inclination（With horizontal plane angle）For 26.
Embodiment 3
A kind of hydraulic engineering mud wastewater treatment equipment, including filter chamber, precipitation separation chamber, activated carbon filter and amorphous particle
Filter.
Angularly disposed in the filter chamber to have mud filter, the mud filter is inclined by the way of right low left high
Tiltedly so that filter chamber's left hand inlet port is arranged at the downside of mud filter, and filter chamber's right-side outlet is arranged at mud filter
Upside；Filter chamber's left hand inlet port is provided with inlet channel, the inlet channel and is provided with booster water pump, in the mistake
Filter chamber right-side outlet is connected with waste water dispatch tube；Filter chamber lower end is provided with silt collecting box.
It is divided into mistress, middle room and interior room inside the precipitation separation chamber, the entrance of the precipitation separation chamber is arranged on described
The top centre of separation chamber is precipitated, and is connected with the waste water dispatch tube, during side is provided with the vertex of a cone upward under the inlet
Empty cone, the vertex of a cone of cone is located at the underface of entrance, and cone side wall upper part is slanting baffle, and bottom is to be provided with filter opening
Outer filter plate, slanting baffle, outer filter plate with precipitation separation chamber shell constitute mistress；The position connected with outer filter plate from slanting baffle to
Under extend to the precipitation separation chamber exit of precipitation separation chamber bottom centre and be provided with interior filter membranous layer, outer filter plate and interior filter membranous layer
And the region between precipitation separation chamber's bottom wall forms middle room；The region of interior filter membranous layer and slanting baffle Inner Constitution forms interior room,
It is provided with agitating shaft straight down at interior ceiling end, the stirring vane of the agitating shaft is propeller blade, passes through agitating shaft
Stirring so that water in interior room is to precipitation separation chamber's output flow；The slanting baffle is stainless steel plate, and the outer filter plate is porous
Stainless steel plate on the multiple filtration film layer laid, the interior filter membranous layer is the multiple filtration film layer that stainless steel wire is laid on the net；
The outside of the precipitation separation chamber of outer filter plate lower terminal end is provided with refuse collecting case, for collecting what is tumbled from outer filter plate top
Debris.
The entrance of the amorphous particle filter is connected with precipitation separation chamber outlet, is internally provided with the amorphous of multilayer
Particle, the outlet of amorphous particle filter is arranged on the two ends on the downside of amorphous particle filter.
The entrance of the activated carbon filter is connected with the outlet of the amorphous particle filter, is internally provided with multilayer
Activated carbon filter, the outlet of activated carbon filter is arranged on the center on the downside of activated carbon filter, with filtering water outlet phase
Even.
The entrance of the silt collecting box is disposed thereon the right-hand member in portion.
The refuse collecting case is outside of the setting in the precipitation separation chamber of outer filter plate lower terminal end of ring-type.
The amorphous particle is Fe-based amorphous particle.
The amorphous particle filter is internally provided with the amorphous of the amorphous particle of multilayer, specially copper alloy plate clamping
Grain, and multilayer copper alloy plate is snakelike setting so that the serpentine-like mode of filter water is contacted with amorphous particle.
The activated carbon filter of the multilayer is the activated carbon granule that porous copper alloy plate is clamped, every two layers of porous copper alloy
Activated carbon granule, and aperture of the particle diameter more than porous copper alloy plate of activated carbon granule are clamped between plate.
The material of the amorphous particle is Fe68Ni11Sm0.3Tb0.9C3B6La3P5（Atomic ratio）.
The activated carbon granule is composite activated carbon grain, and specific weight is：Activated carbon：19 parts, starch：11.5
Part, Sodium Polyacrylate：1.5 parts, phytone：1.5 part.
The mud filter angle of inclination（With horizontal plane angle）For 25.
Claims (9)
1. a kind of hydraulic engineering mud wastewater treatment equipment, it is characterised in that including filter chamber, precipitation separation chamber, activated carbon mistake
Filter plate and amorphous particle filter；
Angularly disposed in the filter chamber to have mud filter, the mud filter is tilted by the way of right low left high, made
The downside that filter chamber's left hand inlet port is arranged at mud filter is obtained, and filter chamber's right-side outlet is arranged at the upper of mud filter
Side；Filter chamber's left hand inlet port is provided with inlet channel, the inlet channel and is provided with booster water pump, in the filter chamber
Right-side outlet is connected with waste water dispatch tube；Filter chamber lower end is provided with silt collecting box；
It is divided into mistress, middle room and interior room inside the precipitation separation chamber, the entrance of the precipitation separation chamber is arranged on the precipitation
The top centre of separation chamber, and be connected with the waste water dispatch tube, side is provided with the hollow circle of the vertex of a cone upward under the inlet
Cone, the vertex of a cone of cone is located at the underface of entrance, and cone side wall upper part is slanting baffle, and bottom is be provided with filter opening outer
Filter plate, slanting baffle, outer filter plate and the shell of precipitation separation chamber constitute mistress；The position connected with outer filter plate from slanting baffle is to downward
The precipitation separation chamber exit for reaching precipitation separation chamber bottom centre is provided with interior filter membranous layer, outer filter plate and interior filter membranous layer and
Region between precipitation separation chamber's bottom wall forms middle room；The region of interior filter membranous layer and slanting baffle Inner Constitution forms interior room, inside
Ceiling end is provided with agitating shaft straight down, and the stirring vane of the agitating shaft is propeller blade, by the stirring of agitating shaft,
So that water in interior room is to precipitation separation chamber's output flow；The slanting baffle be stainless steel plate, the outer filter plate for it is porous not
The multiple filtration film layer laid on rust steel plate, the interior filter membranous layer is the multiple filtration film layer that stainless steel wire is laid on the net；Outside
The outside of the precipitation separation chamber of filter plate lower terminal end is provided with refuse collecting case, for collect from outer filter plate top tumble it is miscellaneous
Thing；
The entrance of the amorphous particle filter is connected with precipitation separation chamber outlet, is internally provided with the amorphous of multilayer
Grain, the outlet of amorphous particle filter is arranged on the two ends on the downside of amorphous particle filter；
The entrance of the activated carbon filter is connected with the outlet of the amorphous particle filter, is internally provided with the work of multilayer
Property charcoal filter, the outlet of activated carbon filter is arranged on the center on the downside of activated carbon filter, is connected with filtering water outlet.
2. hydraulic engineering according to claim 1 sludge treatment device, it is characterised in that the silt collecting box enters
Mouth is disposed thereon the right-hand member in portion.
3. hydraulic engineering according to claim 1 sludge treatment device, it is characterised in that the refuse collecting case is ring
Outside of the setting of shape in the precipitation separation chamber of outer filter plate lower terminal end.
4. hydraulic engineering according to claim 1 sludge treatment device, it is characterised in that the amorphous particle is iron-based
Amorphous particle.
5. hydraulic engineering according to claim 1 sludge treatment device, it is characterised in that the amorphous particle filter
The amorphous particle of the amorphous particle of multilayer, specially copper alloy plate clamping is internally provided with, and multilayer copper alloy plate sets to be snakelike
Put so that the serpentine-like mode of filter water is contacted with amorphous particle.
6. hydraulic engineering according to claim 1 sludge treatment device, it is characterised in that the activated carbon mistake of the multilayer
Filter plate is to be clamped with activated carbon granule between the activated carbon granule that porous copper alloy plate is clamped, every two layers of porous copper alloy plate,
And the particle diameter of activated carbon granule is more than the aperture of porous copper alloy plate.
7. hydraulic engineering according to claim 1 sludge treatment device, it is characterised in that the material of the amorphous particle
For Fe68Ni11Sm0.3Tb0.9C3B6La3P5（Atomic ratio）.
8. hydraulic engineering according to claim 1 sludge treatment device, it is characterised in that the activated carbon granule is multiple
Activated carbon granule is closed, specific weight is：Activated carbon：15 ~ 20 parts, starch：11 ~ 13 parts, Sodium Polyacrylate：1 ~ 1.8 part,
Phytone：1 ~ 2 part.
9. hydraulic engineering according to claim 1 sludge treatment device, it is characterised in that the mud filter is tilted
Angle（With horizontal plane angle）For 20 ~ 29.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710676608.XA CN107235569B (en) | 2017-08-09 | 2017-08-09 | Hydraulic engineering silt effluent treatment plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
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| CN107697960A (en) * | 2017-10-24 | 2018-02-16 | 重庆广恒食品开发有限公司 | A kind of anti-clogging soybean wastewater processing equipment |
| CN107824601A (en) * | 2017-11-21 | 2018-03-23 | 申忠领 | A kind of method for processing kitchen waste |
| CN107935347A (en) * | 2017-11-14 | 2018-04-20 | 陈建祥 | A kind of hydraulic engineering mud separator |
| CN108031258A (en) * | 2017-12-28 | 2018-05-15 | 赵登强 | A kind of small-sized flue gas processing unit |
| CN108046465A (en) * | 2017-12-05 | 2018-05-18 | 陈建祥 | A kind of desulfurization process for treating industrial waste water |
| CN108324973A (en) * | 2018-04-27 | 2018-07-27 | 王文娟 | Medical apparatus sterilizing sterilizing methods |
| CN108675471A (en) * | 2018-05-21 | 2018-10-19 | 台州鼎拓工业设计有限公司 | A kind of hydraulic engineering filter device |
| CN109569046A (en) * | 2018-12-10 | 2019-04-05 | 北京北矿亿博科技有限责任公司 | A kind of automatic filtering system of ammonium nitrate solution |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107697960A (en) * | 2017-10-24 | 2018-02-16 | 重庆广恒食品开发有限公司 | A kind of anti-clogging soybean wastewater processing equipment |
| CN107697960B (en) * | 2017-10-24 | 2020-05-05 | 重庆广恒食品开发有限公司 | Prevent blockking up bean products processing waste water treatment equipment |
| CN107935347A (en) * | 2017-11-14 | 2018-04-20 | 陈建祥 | A kind of hydraulic engineering mud separator |
| CN107824601A (en) * | 2017-11-21 | 2018-03-23 | 申忠领 | A kind of method for processing kitchen waste |
| CN108046465A (en) * | 2017-12-05 | 2018-05-18 | 陈建祥 | A kind of desulfurization process for treating industrial waste water |
| CN108046465B (en) * | 2017-12-05 | 2020-05-08 | 中瑞工程设计院有限公司 | Desulfurization industrial wastewater treatment method |
| CN108031258A (en) * | 2017-12-28 | 2018-05-15 | 赵登强 | A kind of small-sized flue gas processing unit |
| CN108324973A (en) * | 2018-04-27 | 2018-07-27 | 王文娟 | Medical apparatus sterilizing sterilizing methods |
| CN108324973B (en) * | 2018-04-27 | 2020-10-16 | 闫爱丽 | Medical instrument disinfection and sterilization method |
| CN108675471A (en) * | 2018-05-21 | 2018-10-19 | 台州鼎拓工业设计有限公司 | A kind of hydraulic engineering filter device |
| CN108675471B (en) * | 2018-05-21 | 2020-07-31 | 温州冲亚电子科技有限公司 | Hydraulic engineering filter equipment |
| CN109569046A (en) * | 2018-12-10 | 2019-04-05 | 北京北矿亿博科技有限责任公司 | A kind of automatic filtering system of ammonium nitrate solution |
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