CN109231386A - A kind of distributed countryside sewage treatment equipment in remote districts - Google Patents
A kind of distributed countryside sewage treatment equipment in remote districts Download PDFInfo
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- CN109231386A CN109231386A CN201811173367.8A CN201811173367A CN109231386A CN 109231386 A CN109231386 A CN 109231386A CN 201811173367 A CN201811173367 A CN 201811173367A CN 109231386 A CN109231386 A CN 109231386A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
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Abstract
A kind of distributed countryside sewage treatment equipment in remote districts, blending tank are supported by multiple supporting steel frames, and bottom connects precipitation process pond by drain line, and slow descending mechanism is provided in precipitation process pond and extends the reaction time；Supporting steel frame realizes the lift adjustment of blending tank by motor driven；Heat transfer medium is full of in the collet of the homogeneous mixing warehouse of blending tank；Aperture is equipped on the side wall of liquid separation filter funnel inside homogeneous mixing bunker body, the center rotating of the bottom plate of liquid separation filter funnel connects funnel shaft, and funnel shaft and upper beam are affixed；Separatory funnel is driven by driving mechanism, and funnel shaft is connected in liquid separation filter funnel there are two funnel stirring blade；The liquid feeding end of liquid feeding pipeline is connect with external liquid feeding source；Bearing collet is equipped with cooling chamber and cooling fluid supply pipeline；Homogeneous system includes a pair of of the homogeneous impeller group being sleeved on a pair of of homogeneous axis, and a pair of of homogeneous axis is driven by a pair of of homogeneous driving mechanism.The apparatus structure is simple, mixing efficiency is high, effect is good.
Description
Technical field
The invention belongs to field of environment protection equipment, and in particular to a kind of distributed countryside sewage treatment equipment in remote districts.
Background technique
In recent years, the distributed rural sewage treatment in remote districts construction, operation, in terms of also much lag behind society
Meeting demand, becomes an important factor for restricting rural is developed.The main purpose of dispersing type rural sewage treatment from far-off regions is by agriculture
Reach reuse water quality requirement after village's sewage treatment, can get utilization after making sewage treatment.
And current ground country sewage brings different degrees of pollution to underground water, lake river etc., leads to water degradation,
It can not normally drink, promote the growth of algae, and aquatic animals and plants are largely dead, upset ecological environment.Therefore, right
It needs urgent handle in rural area bring sewage from far-off regions distributed.Therefore, country sewage is needed urgently
It is handled.There are still some problems in use for the existing agitator tank for rural sewage treatment, structure design
Simply, complicated for operation, stirring efficiency is low, mixing effect is undesirable, it is therefore desirable to design a kind of novel at country sewage
Agitator tank in reason system.
Summary of the invention
In view of the above existing problems in the prior art, the present invention provides a kind of distributed rural sewage treatment dresses in remote districts
It sets, the apparatus structure is simple, is convenient for operation, and stirring efficiency is high, and mixing effect is ideal.
To achieve the goals above, the present invention provides a kind of distributed countryside sewage treatment equipment in remote districts, including mixed
Close tank, multiple supporting steel frames for being fixedly connected on blending tank lower outside, upper connection are cranked arm, upper telescopic oil cylinder and precipitation process
Pond；
The supporting steel frame includes support, parallel a pair of of the vertical beam being fixedly connected on the support, setting in an opposition
The L-type support of beam side and the carriage drive motor that a pair of of vertical beam side is set；A pair of of vertical beam is set respectively in identical side
It is equipped with the continuous rack gear longitudinally extended and the sliding rail longitudinally extended；The vertical section of L-type support is on the position of the continuous rack gear of correspondence
Portion and lower part are each provided with a support gear, and support gear is rotatably connected by the rotary gear shaft at its center in L-type support
Vertical section on；The position that the vertical section of L type bracket corresponds to sliding rail offers sliding slot, and the sliding slot is slidably located in sliding rail
Outside, the bracket end on the horizontal segment of L-type support are fixedly connected with the lateral wall of blending tank；Carriage drive motor is fixedly connected
In the side away from support gear of L-type support, and the input of its output shaft and the transmission case for being fixedly connected on L-type support side
End connection, the output end of transmission case are connect with the rotary gear shaft of two support gears；
The upper open end of blending tank is provided with the upper pressure sealing cover for sealing blending tank, in the bottom end of blending tank
It is fixedly connected with the drain line being connected to its inner cavity；The upper upper surface for connecting one end and upper pressure sealing cover for cranking arm
It is fixedly connected, the other end and the hinged seat being fixedly connected on the outside of blending tank upper end are hinged；One end of upper telescopic oil cylinder and upper company
It connects on the outside of the hinged end cranked arm hingedly, it is hinged in the middle part of the can body of the other end and blending tank, top pressure is controlled to pass through expanding-contracting action
The lid of power sealing cover is closed or is opened；
The blending tank includes jacket structured homogeneous mixing warehouse, is situated between in the collet of homogeneous mixing warehouse full of heat transfer
Matter, homogeneous mixing warehouse are externally connected to the heat medium pipeline being connected to its jacket space, the other end of heat medium pipeline with
The connection of thermal medium source of supply；
It is disposed with the liquid feeding pipeline being obliquely installed, horizontal positioned and can phase from top to bottom inside homogeneous mixing bunker body
To the liquid separation filter funnel and homogeneous system of the rotation of homogeneous mixing warehouse, if being provided on the side wall of liquid separation filter funnel throughout ground
Dry side-wall hole, the bottom plate of liquid separation filter funnel is outwardly provided with multiple apertures throughout it, and the rotation center of bottom plate is logical
It crosses the bearing collet being firmly connected with it and is connected with funnel shaft, lower end of the funnel shaft inside liquid separation filter funnel is connected with
One funnel stirring blade cooperated with homogeneous mixing warehouse lower end internal clearance；Funnel shaft outside the liquid separation filter funnel on
End cap is equipped with outer gear ring, is fixedly connected between outer gear ring and funnel shaft by radially connected beam；In homogeneous mixing warehouse
It is fixedly connected with waterproof machine with corresponding to outer gear ring on side wall, funnel gear, funnel tooth is equipped on the output shaft of waterproof machine
Wheel is engaged with outer gear ring；The outlet end of liquid feeding pipeline is located above liquid separation filter funnel, and liquid feeding end is pierced by homogeneous mixing warehouse
Side wall after connect with liquid feeding source；
The bearing holding tank of bearing collet being provided centrally with to lower recess, the inner loop of bearing collet is around bearing holding tank
Ground is provided with toroidal cavity；Fixing assembling has retaining bearing in bearing holding tank, and the inner ring and funnel shaft of retaining bearing are solid
Fixed connection；Toroidal cavity is connected separately with the coolant liquid inlet pipe being connected to its inner cavity and coolant liquid outlet tube road, coolant liquid
Inlet pipe and coolant liquid outlet tube road after radially across liquid separation filter funnel, homogeneous mixing warehouse respectively with cooling source and cold
But liquid recycling bins connect；
Homogeneous system includes that pair of parellel setting is rotationally set in homogeneous axis, a pair of of homogeneous axis at middle part respectively
There is corresponding a pair of of homogeneous impeller group, homogeneous impeller group is made of multiple high speed homogenization impellers, in a pair of of homogeneous impeller group
It is engaged between high speed homogenization impeller；The opposite both ends of a pair of of homogeneous axis are rotationally pierced by after homogeneous mixing warehouse respectively respectively
It is connect with the output section for the homogeneous driving mechanism for being fixedly connected on homogeneous mixing bunker body both sides external；Homogeneous axis is far from driving machine
The other end of structure is rotatablely connected by closed type thrust bearing with the inner sidewall of homogeneous mixing warehouse.
Precipitation process pond includes the pond body of upper end opening, the web plate being arranged in inside pond body, is fixedly supported on outside pond body
Pond body bracket, be fixedly connected on pond body upper end precipitation process pond inlet pipeline, be connected to pond body intracavity bottom and fixed connect
It is connected to the bed mud discharge pipe of pond body bottom end, is connected to and is fixedly connected on the precipitation process pond of pond body side with pond body inner cavity middle part
Outlet pipeline；Middle part forms clear liquid area in the pond body, and sludge accumulation area is formed on bottom in pond body；The precipitation process pond water inlet
The liquid feeding end of pipeline and the outlet end of drain line are penetrated through and are connected；
The clear liquid area is disposed with dispersion plate unit, the slow gentle drop net of drop plate unit from top to bottom, disperses plate unit
It is made of multiple aerofoil profile dispersion plates arranged side by side, is fixedly connected between adjacent aerofoil profile dispersion plate by connecting rod, delay drop plate list
Member is by multiple rectangular slow drop board groups arranged side by side at adjacent prismatic slow drop is fixedly connected between plate by connecting rod, precipitation process
The water inlet end of pond outlet pipeline is located at the lower part of slow drop net, and clear liquid area is provided with detection mouth, detection mouth on dispersion plate unit top
On be connected with the signal piping with shut-off valve being connected to its inner cavity.
As a preference, the homogeneous driving mechanism is formed by connecting by homogeneous driving motor with retarder.
Further, further include control cabinet in order to facilitate centralized control, speed probe is set on retarder, thermal medium supplies
Ying Yuan and liquid feeding source are respectively the thermal medium transfer pump connecting with thermal medium source and the fluid filling pump connecting with liquid source；
Control cabinet respectively with carriage drive motor, homogeneous driving motor, speed probe, thermal medium transfer pump, fluid filling pump
It is connected with waterproof machine.
As a preference, the supporting steel frame quantity is 3 groups, and it is evenly distributed on the outside of blending tank；
The wall thickness of the homogeneous mixing bunker is 2mm~50mm；
The liquid separation filter funnel is located at the position of homogeneous mixing bunker waist 25mm~55mm on the upper side；
The liquid-adding device and horizontal direction angle are between 10 °~32 °；
Funnel stirring blade is by the radial direction between the annulus being set on the outside of funnel shaft and connection annulus and funnel shaft
Connecting rod composition；
The duct with a thickness of 20mm~30mm.
It further, further include the homogeneity detector being arranged in inside homogeneous mixing bunker for the ease of detecting homogeneous degree,
Homogeneity detector is connect with control cabinet.
Further, in order to improve homogenizing effect, high speed homogenization impeller quantity is 10, between adjacent high speed homogenization impeller etc.
Distance arrangement, and spacing, between 5mm~12mm, high speed homogenization impeller shape is in ratchet-like.
Further, in order to improve heat dissipation effect, the quantity of the fin deployment rod and oil cylinder fin is 6, the oil cylinder wing
The material of piece is thin plate stainless steel material.
Further, the bottom of the pond body is inverted frustum type, is provided in clear liquid is trivial and connect with control cabinet
COD sensor.
Further, the distance between two support gears are 15cm~25cm
Further, the high speed homogenization impeller good in order to the homogenizing effect that gets a promotion, the high speed homogenization impeller is by high score
Sub- material is made, by mass percentage content meter, and constituent is as follows:
Methyl ester derivative 30%~65%, thiophosphate analog derivative 25%~60%, mixed aid be 1%~
5%, crosslinking agent is 1%~5%, O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45%, (T-
4)-bis- (diethyldithiocar bamic acid-S, S') zinc 2%~15%.
Further, the high speed homogenization impeller good in order to the homogenizing effect that gets a promotion, the preparation method of high speed homogenization impeller
It comprises the steps of:
Step 1: the ultrapure water 22%~32% that conductivity is 1.25 μ of μ S/cm~3.15 S/cm is added in a kettle, opens
Blender in dynamic reaction kettle, revolving speed are 125rpm~375rpm, start heat pump, make reactor temperature rise to 75 DEG C~
185℃；Successively methylate ester derivative 30%~65%, mixed aid are 1%~5%, and stirring is adjusted to being completely dissolved
PH value be 5.5~8.5, be added thiophosphate analog derivative 25%~60%, by agitator speed be adjusted to 255rpm~
315rpm, temperature are 90 DEG C~395 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45% is added, (T-4)-is bis-
(diethyldithiocar bamic acid-S, S') zinc 2%~15% is uniformly mixed；
Step 3: it is 1~5% that crosslinking agent, which is added, and agitator speed is 75rpm~235rpm, and temperature is 90 DEG C~265 DEG C,
It keeps this state 5~25 hours, discharges, entering molding press can be prepared by high speed homogenization impeller.
In the present invention, upper pressure sealing cover carries out folding control by upper telescopic oil cylinder, can improve the automatic of the device
Change degree, convenient for the addition for the treatment of sewage.Waterproof machine drives the operating of funnel shaft by funnel gear, and then drives leakage
Struggle against paddle rotation, achievees the purpose that the uniform stirring to material, and can also make on the liquid additive and blending tank that are added
The sewage to be processed that open end is added carries out uniform mixing and pre- stirring, and a pair of of homogeneous impeller group is by uniform in homogeneous system
Driving mechanism driving is done high speed and is moved toward one another, and mixing effect can not only be improved, and can promote additive and treatment sewage it
Between reaction.Supporting steel frame can control height of the blending tank relative to supporting plane.The setting in precipitation process pond can convenient for pair
With staticly settling for the sewage after additive reaction, in order to clear water of isolating that treated and by the bed mud outlet of precipitating.It should
Apparatus structure is simple, stirring efficiency is high, and homogenizing effect is ideal.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention；
Fig. 2 is the structural schematic diagram of supporting steel frame in the present invention；
Fig. 3 is the structural schematic diagram of blending tank in the present invention；
Fig. 4 is the structural schematic diagram of liquid separation filter funnel in the present invention；
Fig. 5 is the structural schematic diagram of middle (center) bearing collet of the present invention；
Fig. 6 is the structural schematic diagram of homogeneous system in the present invention；
Fig. 7 is the structural schematic diagram in precipitation process pond in the present invention；
Fig. 8 is the structural schematic diagram of clear liquid area in the present invention；
Fig. 9 is O- ethyl O- in the present invention (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate accounting to improving uniformity
The influence graph of relation of rate；
Figure 10 is methyl ester derivative molecular characterization schematic diagram in the present invention；
Figure 11 is group thiophosphate derivative molecular structure feature schematic diagram in the present invention；
Figure 12 is oxysilane substance molecular characterization schematic diagram in the present invention.
In figure: 1, supporting steel frame, 1-1, carriage drive motor, 1-2, transmission case, 1-3, bracket end, 1-4, sliding rail, 1-
5, continuous rack gear, 1-6, support gear, 1-7, L-type support, 1-8, support, 1-9, vertical beam, 2, blending tank, 2-1, homogeneous mixing
Storehouse, 2-2, liquid separation filter funnel, 2-2-1, side-wall hole, 2-2-2, outer gear ring, 2-2-3, funnel gear, 2-2-4, anti-water power
Machine, 2-2-5, funnel stirring blade, 2-2-6, bearing collet, 2-2-6-1, bearing holding tank, 2-2-6-2, toroidal cavity, 2-2-
6-3, retaining bearing, 2-2-6-4, coolant liquid inlet pipe, 2-2-6-4, coolant liquid outlet tube road, 2-3, liquid feeding pipeline, 2-4,
Homogeneous system, 2-4-1, homogeneous driving motor, 2-4-2, retarder, 2-4-3, homogeneous axis, 2-4-4, closed type thrust bearing, 2-
4-5, high speed homogenization impeller, 2-5, homogeneity detector, 3, upper pressure sealing cover, 4, it is upper connection crank arm, 5, upper telescopic oil cylinder,
6, drain line, 7, precipitation process pond, 7-1, bed mud discharge pipe, 7-2, web plate, 7-3, pond body, 7-5, clear liquid area, 7-5-1,
COD sensor, 7-5-2, aerofoil profile dispersion plate, 7-5-3, rectangular slow drop plate, 7-5-4, slow drop net, 7-5-5, detection mouth, 7-6, dirt
Mud accumulation area, 7-7, precipitation process pond inlet pipeline, 7-8, precipitation process pond outlet pipeline, 8, control cabinet, 9, radially connected beam,
10, funnel shaft.
Specific embodiment
The invention will be further described below.
As shown in Figures 1 to 8, the distributed countryside sewage treatment equipment in a kind of remote districts, including blending tank 2, fixed company
It connects and cranks arm 4, upper telescopic oil cylinder 5 and precipitation process pond 7 in multiple supporting steel frames 1 of 2 lower outside of blending tank, upper connection；
The supporting steel frame 1 includes support 1-8, parallel a pair of of the vertical beam 1-9 being fixedly connected on support 1-8, sets
Set the side a pair of of vertical beam 1-9 L-type support 1-7 and the carriage drive motor 1-1 of the side a pair of of vertical beam 1-9 is set；It is a pair of
The sliding rail 1-4 that vertical beam 1-9 is respectively arranged with the continuous rack gear 1-5 longitudinally extended and longitudinally extends in identical side；L-type branch
The vertical section of frame 1-7 is each provided with a support gear 1-6, bracket teeth in the position upper and lower part of the continuous rack gear 1-5 of correspondence
Wheel 1-6 is rotatably connected in the vertical section of L-type support 1-7 by the rotary gear shaft at its center；The vertical section of L-type support 1-7
The position of corresponding sliding rail 1-4 offers sliding slot, and the sliding slot is slidably located in the outside of sliding rail 1-4, the level of L-type support 1-7
Bracket end 1-3 in section is fixedly connected with the lateral wall of blending tank 2；Carriage drive motor 1-1 is fixedly connected on L-type support 1-
7 side away from support gear 1-6, and its output shaft and the transmission case 1-2's that is fixedly connected on the side L-type support 1-7 is defeated
Enter end connection, the output end of transmission case 1-2 is connect with the rotary gear shaft of two support gear 1-6；
The upper open end of blending tank 2 is provided with the upper pressure sealing cover 3 for sealing blending tank 2, in blending tank 2
Bottom end is fixedly connected with the drain line 6 being connected to its inner cavity；It is described it is upper connection crank arm 4 one end and upper pressure sealing cover 3
Upper surface be fixedly connected, the other end and the hinged seat being fixedly connected on the outside of 2 upper end of blending tank are hinged；Upper telescopic oil cylinder 5
One end and upper connection crank arm 4 hinged end on the outside of it is hinged, it is hinged in the middle part of the can body of the other end and blending tank 2, by flexible dynamic
The lid for making control upper pressure sealing cover 3 is closed or is opened；
The blending tank 2 includes jacket structured homogeneous mixing warehouse 2-1, is full of in the collet of homogeneous mixing warehouse 2-1
Heat transfer medium, homogeneous mixing warehouse 2-1's is externally connected to the heat medium pipeline being connected to its jacket space, heat medium pipeline
The other end is connect with thermal medium source of supply；
It is disposed with the liquid feeding pipeline 2-3 being obliquely installed from top to bottom inside homogeneous mixing warehouse 2-1, is horizontally arranged
And can relative homogeneous mixing warehouse 2-1 rotation liquid separation filter funnel 2-2 and homogeneous system 2-4, the side of liquid separation filter funnel 2-2
Ground is provided with several side-wall holes 2-2-1 on wall, the bottom plate of liquid separation filter funnel 2-2 is outwardly provided with more throughout it
A aperture, and the rotation center of bottom plate passes through the bearing collet 2-2-6 being firmly connected with it and is connected with funnel shaft 10, funnel turns
Lower end of the axis 10 inside liquid separation filter funnel 2-2 is connected with one and the cooperation of the homogeneous mixing lower end warehouse 2-1 internal clearance
Funnel stirring blade 2-2-5；Funnel shaft 10 is set with outer gear ring 2-2-2, external tooth in liquid separation filter funnel 2-2 outer upper ends
It is fixedly connected between circle 2-2-2 and funnel shaft 10 by radially connected beam 9；It is right on the inner sidewall of homogeneous mixing warehouse 2-1
It is fixedly connected with waterproof machine 2-2-4 with answering outer gear ring 2-2-2, funnel gear is equipped on the output shaft of waterproof machine 2-2-4
2-2-3, funnel gear 2-2-3 are engaged with outer gear ring 2-2-2；The outlet end of liquid feeding pipeline 2-3 is located at liquid separation filter funnel 2-2
Top, liquid feeding end are connect after being pierced by the side wall of homogeneous mixing warehouse 2-1 with liquid feeding source；
The bearing holding tank 2-2-6-1 of bearing collet 2-2-6 being provided centrally with to lower recess, bearing collet 2-2-6's
Inner loop is provided with toroidal cavity 2-2-6-2 around bearing holding tank 2-2-6-1；Fixing assembling has retaining in bearing holding tank
The inner ring of bearing 2-2-6-3, retaining bearing 2-2-6-3 are fixedly connected with funnel shaft 10；Toroidal cavity 2-2-6-2 is separately connected
There are the coolant liquid inlet pipe 2-2-6-4 being connected to its inner cavity and coolant liquid outlet tube road 2-2-6-5, coolant liquid inlet pipe 2-
2-6-4 and coolant liquid outlet tube road 2-2-6-5 after radially across liquid separation filter funnel 2-2, homogeneous mixing warehouse 2-1 respectively with
Cooling source is connected with coolant liquid recycling bins；
Homogeneous system 2-4 includes that pair of parellel is arranged in homogeneous axis 2-4-3, a pair of homogeneous axis 2-4-3 in middle part
It is not set with corresponding a pair of of homogeneous impeller group rotationally, homogeneous impeller group is made of multiple high speed homogenization impeller 2-4-5,
It is engaged between high speed homogenization impeller 2-4-5 in a pair of of homogeneous impeller group；It a pair of of homogeneous axis 2-4-3 opposite both ends respectively can
It is rotationally pierced by after homogeneous mixing warehouse 2-1 and is driven respectively with the homogeneous for being fixedly connected on homogeneous mixing warehouse 2-1 both sides external
The output section of mechanism connects；Homogeneous axis 2-4-3 passes through closed type thrust bearing 2-4-4 and homogeneous far from the other end of driving mechanism
Mix the inner sidewall rotation connection of warehouse 2-1；
Precipitation process pond 7 includes the pond body 7-3 of upper end opening, the web plate 7-2 being arranged in inside pond body 7-3, fixed support
Pond body bracket 7-4 outside pond body 7-3, the precipitation process pond inlet pipeline 7-7 for being fixedly connected on the upper end pond body 7-3 and pond
Body 7-3 intracavity bottom is connected to and is fixedly connected in the middle part of the bed mud discharge pipe 7-1 of the bottom end pond body 7-3 and the inner cavity pond body 7-3
It is connected to and is fixedly connected on the precipitation process pond outlet pipeline 7-8 of the side pond body 7-3；Middle part forms clear liquid in the pond body 7-3
Sludge accumulation area 7-6 is formed on bottom in area 7-5, pond body 7-3；The liquid feeding end of the precipitation process pond inlet pipeline 7-7 and drain
The outlet end of pipeline 6 penetrates through connection；
The clear liquid area 7-5 is disposed with dispersion plate unit, the gentle drop net 7-5-4 of slow drop plate unit from top to bottom, point
The unit that falls apart is made of multiple aerofoil profile dispersion plate 7-5-2 arranged side by side, passes through connecting rod between adjacent aerofoil profile dispersion plate 7-5-2
Be fixedly connected, slow drop plate unit is made of multiple rectangular slow drop plate 7-5-3 arranged side by side, adjacent prismatic is slow drop plate 7-5-3 it
Between be fixedly connected by connecting rod, the water inlet end of precipitation process pond outlet pipeline 7-8 is located at the lower part of slow drop net 7-5-4, clear liquid area
7-5 dispersion plate unit top be provided with detection mouth 7-5-5, be connected on detection mouth 7-5-5 be connected to its inner cavity have section
The only signal piping of valve.
The homogeneous driving mechanism is formed by connecting by homogeneous driving motor 2-4-1 and retarder 2-4-2.
Further include control cabinet 8, speed probe is set on retarder 2-4-2, thermal medium source of supply and liquid feeding source are respectively
The thermal medium transfer pump being connect with thermal medium source and the fluid filling pump being connect with liquid source；
Control cabinet 8 is supplied with carriage drive motor 1-1, homogeneous driving motor 2-4-1, speed probe, thermal medium respectively
Pump, fluid filling pump are connected with waterproof machine 2-2-4.
1 quantity of supporting steel frame is 3 groups, and is evenly distributed on the outside of blending tank 2；
The wall thickness of the homogeneous mixing bunker 2-1 is 2mm~50mm；
The liquid separation filter funnel 2-2 is located at the position of homogeneous mixing bunker 2-1 waist 25mm~55mm on the upper side；
The liquid-adding device 2-3 and horizontal direction angle are between 10 °~32 °；
Funnel stirring blade 2-2-5 by be set in the outside of funnel shaft 10 annulus and connection annulus and funnel shaft 10 it
Between radially directed connecting link composition；
The duct 2-2-1-1 with a thickness of 20mm~30mm.
It further include homogeneity detector 2-5, homogeneity detector 2-5 and the control being arranged in inside homogeneous mixing bunker 2-1
Case 8 connects.
High speed homogenization impeller 2-4-5 quantity is 10, is spaced substantially equidistant between adjacent high speed homogenization impeller 2-4-5, and
Away between 5mm~12mm, high speed homogenization impeller 2-4-5 shape is in ratchet-like.
The bottom of the pond body 7-3 is inverted frustum type, is provided in the area 7-5 of clear liquid area and connect with control cabinet 8
COD sensor 7-5-1.
The distance between two support gear 1-6 are 15cm~25cm.
The high speed homogenization impeller 2-4-5 is made of high molecular material, by mass percentage content meter, and constituent is such as
Under:
Methyl ester derivative 30%~65%, thiophosphate analog derivative 25%~60%, mixed aid be 1%~
5%, crosslinking agent is 1%~5%, O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45%, (T-
4)-bis- (diethyldithiocar bamic acid-S, S') zinc 2%~15%.
The crosslinking agent is (phosphordithiic acid diisopropyl ester sodium, isopentyl and isopropyl) phosphorodithioate zinc salt, four
Any one in phenyl (bisphenol-A) bisphosphate.
The feature of methyl ester derivative molecular structure is as shown in Figure 10, and wherein R is the alkyl that carbon atom number is 1~8.
The feature of group thiophosphate derivative molecular structure is as shown in figure 11, molecular formula: C10H15O3PS2；Molecule
Amount: 278.343.
Mixed aid is oxysilane substance, and molecular structural formula is as shown in figure 12, point of included molecular structure
Minor are as follows: C16H20O2Si.
The preparation method of high speed homogenization impeller 2-4-5 comprises the steps of:
Step 1: the ultrapure water 22%~32% that conductivity is 1.25 μ of μ S/cm~3.15 S/cm is added in a kettle, opens
Blender in dynamic reaction kettle, revolving speed are 125rpm~375rpm, start heat pump, make reactor temperature rise to 75 DEG C~
185℃；Successively methylate ester derivative 30%~65%, mixed aid are 1%~5%, and stirring is adjusted to being completely dissolved
PH value be 5.5~8.5, be added thiophosphate analog derivative 25%~60%, by agitator speed be adjusted to 255rpm~
315rpm, temperature are 90 DEG C~395 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45% is added, (T-4)-is bis-
(diethyldithiocar bamic acid-S, S') zinc 2%~15% is uniformly mixed；
Step 3: it is 1~5% that crosslinking agent, which is added, and agitator speed is 75rpm~235rpm, and temperature is 90 DEG C~265 DEG C,
It keeps this state 5~25 hours, discharges, entering molding press can be prepared by high speed homogenization impeller 2-4-5.
Following embodiment further illustrates the contents of the present invention, and as high speed homogenization impeller 2-4-5, it is weight of the invention
Component is wanted, due to its presence, increases the service life of integral device, it is played for the safety of integral device, even running
Key effect.For this purpose, by it is following be embodiment, further verify the component of the present invention, what is shown is higher than
The physical characteristic of other related patents.
Embodiment 1
High speed homogenization impeller 2-4-5 of the present invention, and content meter by mass percentage are manufactured according to the following steps:
Step 1: the ultrapure water 22% that conductivity is 1.25 μ S/cm being added in a kettle, starts blender in reaction kettle,
Revolving speed is 125rpm, starts heat pump, reactor temperature is made to rise to 75 DEG C；Successively methylate ester derivative 30% mixes
Closing auxiliary agent is 1%, and to being completely dissolved, adjusting pH value is 5.5 for stirring, thiophosphate analog derivative 25% is added, by blender
Revolving speed is adjusted to 255rpm, and temperature is 90 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45% is added, (T-4)-is bis-
(diethyldithiocar bamic acid-S, S') zinc 2% is uniformly mixed；
Step 3: it is 1% that crosslinking agent, which is added, agitator speed 75rpm, and temperature is 90 DEG C, keeps this state 5 hours, out
Material, entering molding press can be prepared by high speed homogenization impeller 2-4-5.
Embodiment 2
High speed homogenization impeller 2-4-5 of the present invention, and content meter by mass percentage are manufactured according to the following steps:
Step 1: the ultrapure water 32% that conductivity is 3.15 μ S/cm being added in a kettle, starts blender in reaction kettle,
Revolving speed is 375rpm, starts heat pump, reactor temperature is made to rise to 185 DEG C；Successively methylate ester derivative 65% mixes
Closing auxiliary agent is 5%, and to being completely dissolved, adjusting pH value is 8.5 for stirring, thiophosphate analog derivative 60% is added, by blender
Revolving speed is adjusted to 315rpm, and temperature is 395 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 45%, (T-4)-bis- (diethyls is added
Base aminodithioformic acid-S, S') zinc 15% be uniformly mixed；
Step 3: it is 5% that crosslinking agent, which is added, agitator speed 235rpm, and temperature is 265 DEG C, keeps this state 25 small
When, discharging, entering molding press can be prepared by high speed homogenization impeller 2-4-5.
Embodiment 3
High speed homogenization impeller 2-4-5 of the present invention, and content meter by mass percentage are manufactured according to the following steps:
Step 1: the ultrapure water 29% that conductivity is 1.315 μ S/cm, stirring in starting reaction kettle are added in a kettle
Device, revolving speed 178rpm start heat pump, reactor temperature are made to rise to 85 DEG C；Successively methylate ester derivative 39%,
Mixed aid is 4%, and to being completely dissolved, adjusting pH value is 5.8 for stirring, and thiophosphate analog derivative 40% is added, will stir
Device revolving speed is adjusted to 300rpm, and temperature is 90 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 40%, (T-4)-bis- (diethyls is added
Base aminodithioformic acid-S, S') zinc 10% be uniformly mixed；
Step 3: it is 3% that crosslinking agent, which is added, agitator speed 90rpm, and temperature is 91 DEG C, keeps this state 8 hours, out
Material, entering molding press can be prepared by high speed homogenization impeller 2-4-5.
Reference examples
Reference examples are that the high speed homogenization impeller of certain commercially available brand is used for the service condition of oil product mixing assorting room.
High speed homogenization impeller described in high speed homogenization impeller 2-4-5 and reference examples that Examples 1 to 3 prepares is used for
The service condition of oil product mixed process compares, and with volume resistivity, oil from spending, reduce sticky rate, mixture homogeneity
Enhancing rate is that technical indicator is counted, and the results are shown in Table 1:
Table 1 is service condition of the high speed homogenization impeller described in Examples 1 to 3 and reference examples for oil product mixed process
The comparing result of parameters, as seen from Table 1, high speed homogenization impeller 2-4-5 of the present invention, volume resistivity, oil from
It spends, reduce sticky rate, mixture homogeneity enhancing rate is above the product that the prior art produces.
In addition, as shown in figure 9, being O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate accounting to the uniformity
Promote the influence relational graph of rate.Find out in figure, as the important component of high speed homogenization impeller 2-4-5 material, incorporation pair
Enhancing product performance, it is vital to play the role of, and mixes its ingredient in terms of improving uniformity rate substantially better than existing production
Product.
The device working method including the following steps:
Step 1: treating material is entered in blending tank 2 by conduit, and upper pressure sealing cover 3 cranks arm 4 by connection, and
Under the action of upper telescopic oil cylinder 5, slow drop is implemented to upper pressure sealing cover 3, and be fitted with blending tank 2, realize sealing；
Step 2: when needing to adjust support scheduling, the three carriage drive motor 1-1 controlled in three supporting steel frames 1 are synchronous
Operating, and drive the operating of transmission case 1-2；Rotation transmission case 1-2 driving arm gear 1-6 in the same direction simultaneously, and then bracket teeth
The rise and fall that 1-6 drives L-type support 1-7 are taken turns, since the sliding slot that the vertical section of L-type support 1-7 is arranged is slidably located in cunning
Outside rail 1-4, so can guarantee that L-type support 1-7 is not separated in rising or dropping process with vertical beam 1-9；Work as support gear
When 1-6 rotates counterclockwise, L-type support 1-7 is in upward status；When support gear 1-6 is rotated clockwise, L-type support 1-7 is in
Decline state；
Step 3: in blending tank 2, treating material enters liquid separation filter funnel 2-2 by liquid feeding pipeline 2-3, due to adding
Liquid pipeline 2-3 is obliquely installed, and the material of entrance acts on liquid separation filter funnel 2-2, carries out the side liquid separation filter funnel 2-2
The rotation of operation side is filtered, is filtered by the liquid separation filter funnel 2-2 rotated, filter effect can be made more preferable；Two homogeneous driving machines
Structure drives two a pair of of homogeneous impeller groups to move toward one another, and engages, can make between the high speed homogenization impeller in a pair of of homogeneous impeller group
Material reaches homogenizing effect, and then enters the lower part homogeneous mixing bunker 2-1；Homogeneity detector 2-5 is to entrance homogeneous mixing bunker 2-1
The homogeneity of the material of lower part makes induction and reacts and detected；When homogeneity does not meet examination criteria, homogeneity detection
Device 2-5 issues electric signal to control cabinet 8, and controller 8 is alarmed by alarm connected to it.
Step 4: in liquid separation filter funnel 2-2, waterproof machine 2-2-4 is operated after powering on, and drives funnel
Gear 2-2-3 rotation, and then the operating of funnel gear 2-2-3 driving funnel shaft 10, drive funnel paddle 2-2-5 rotation,
Reach the uniform stirring to material；Material is after stirring, from the bottom plate and side-wall hole 2-2-1 of liquid separation filter funnel 2-2
Outflow, and precipitated into precipitation process pond 7；
Step 5 after sewage enters, passes sequentially through multiple aerofoil profile dispersion plate 7-5-2, multiple rectangular in the 7-5 of clear liquid area
The slow gentle drop of drop plate 7-5-3 nets 9-5-4, and the slow drop to sewage is realized under the synergy of three；COD sensor 7-5-1
The sewage for entering clear liquid area 7-5 is measured in real time, when the concentration of sewage is more than normal concentration, COD sensor 7-5-1
Warning message is sent to central control cabinet 8 by conducting wire；The degree for the treatment of of sewage is detected by detection mouth 7-5-5；
Step 6: in bearing collet 2-2-6, coolant liquid enters from coolant liquid inlet pipe 2-2-6-4, and passes through cooling
Liquid outlet tube road 2-2-6-4 flows into toroidal cavity 2-2-6-2, then coolant liquid outlet tube road 2-2-6-4 discharge；To retaining bearing
2-2-6-3 cools down.
Claims (10)
1. a kind of distributed countryside sewage treatment equipment in remote districts, including blending tank (2) and it is fixedly connected under blending tank (2)
Multiple supporting steel frames (1) on the outside of portion, which is characterized in that further include upper connection crank arm (4), upper telescopic oil cylinder (5) and place of settling
It manages pond (7)；
The supporting steel frame (1) includes support (1-8), parallel a pair of of the vertical beam (1- being fixedly connected on support (1-8)
9) it is electric that carriage drive of the L-type support (1-7) and setting in the side a pair of of vertical beam (1-9) in the side a pair of of vertical beam (1-9), is set
Machine (1-1)；A pair of of vertical beam (1-9) is respectively arranged with the continuous rack gear (1-5) longitudinally extended and longitudinal extension in identical side
Sliding rail (1-4)；The vertical section of L-type support (1-7) is each provided with one in the position upper and lower part of the continuous rack gear of correspondence (1-5)
A support gear (1-6), support gear (1-6) are rotatably connected by the rotary gear shaft at its center in the perpendicular of L-type support (1-7)
On straight section；The position that the vertical section of L-type support (1-7) corresponds to sliding rail (1-4) offers sliding slot, and the sliding slot is slidably located in cunning
The outside of rail (1-4), the lateral wall of bracket end (1-3) and blending tank (2) on the horizontal segment of L-type support (1-7) is fixed to be connected
It connects；Carriage drive motor (1-1) is fixedly connected on the side away from support gear (1-6) of L-type support (1-7), and it is exported
Axis is connect with the input terminal for the transmission case (1-2) for being fixedly connected on the side L-type support (1-7), the output end of transmission case (1-2) with
The rotary gear shaft connection of two support gears (1-6)；
The upper open end of blending tank (2) is provided with the upper pressure sealing cover (3) for sealing blending tank (2), in blending tank
(2) bottom end is fixedly connected with the drain line (6) being connected to its inner cavity；It is described it is upper connection crank arm (4) one end and top press
The upper surface of power sealing cover (3) is fixedly connected, and the other end and the hinged seat being fixedly connected on the outside of blending tank (2) upper end are hinged；
One end of upper telescopic oil cylinder (5) and upper connection crank arm (4) hinged end on the outside of it is hinged, in the can body of the other end and blending tank (2)
Portion is hinged, to be closed or be opened by the lid of expanding-contracting action control upper pressure sealing cover (3)；
The blending tank (2) includes jacket structured homogeneous mixing warehouse (2-1), is filled in the collet of homogeneous mixing warehouse (2-1)
Full heat transfer medium, homogeneous mixing warehouse (2-1) are externally connected to the heat medium pipeline being connected to its jacket space, thermal medium pipe
The other end on road is connect with thermal medium source of supply；
It is disposed with the liquid feeding pipeline (2-3) being obliquely installed from top to bottom inside homogeneous mixing warehouse (2-1), is horizontally arranged
And can relative homogeneous mixing warehouse (2-1) rotation liquid separation filter funnel (2-2) and homogeneous system (2-4), liquid separation filter funnel
Ground is provided with several side-wall holes (2-2-1) on the side wall of (2-2), the bottom plate of liquid separation filter funnel (2-2) is throughout it
Multiple apertures are outwardly provided with, and the rotation center of bottom plate passes through the bearing collet (2-2-6) being firmly connected with it and is connected with
Funnel shaft (10), funnel shaft (10) are connected with one and homogeneous mixing bunker in the internal lower end of liquid separation filter funnel (2-2)
The funnel stirring blade (2-2-5) of the lower end internal clearance body (2-1) cooperation；Funnel shaft (10) is at liquid separation filter funnel (2-2)
Outer upper ends are set with outer gear ring (2-2-2), pass through radially connected beam (9) between outer gear ring (2-2-2) and funnel shaft (10)
It is fixedly connected；It is fixedly connected with waterproof machine while outer gear ring (2-2-2) is corresponded on the inner sidewall of homogeneous mixing warehouse (2-1)
(2-2-4) is equipped with funnel gear (2-2-3) on the output shaft of waterproof machine (2-2-4), funnel gear (2-2-3) and external tooth
Enclose (2-2-2) engagement；The outlet end of liquid feeding pipeline (2-3) is located above liquid separation filter funnel (2-2), and liquid feeding end is pierced by homogeneous
It is connect after mixing the side wall of warehouse (2-1) with liquid feeding source；
The bearing holding tank (2-2-6-1) of bearing collet (2-2-6) being provided centrally with to lower recess, bearing collet (2-2-6)
Inner loop toroidal cavity (2-2-6-2) is provided with around bearing holding tank (2-2-6-1)；The fixing assembling in bearing holding tank
Have retaining bearing (2-2-6-3), the inner ring of retaining bearing (2-2-6-3) is fixedly connected with funnel shaft (10)；Toroidal cavity (2-
2-6-2) it is connected separately with the coolant liquid inlet pipe (2-2-6-4) being connected to its inner cavity and coolant liquid outlet tube road (2-2-6-
5), coolant liquid inlet pipe (2-2-6-4) and coolant liquid outlet tube road (2-2-6-5) are radially across liquid separation filter funnel (2-
2) it, is connect respectively with cooling source and coolant liquid recycling bins after homogeneous mixing warehouse (2-1)；
Homogeneous system (2-4) includes that pair of parellel is arranged in homogeneous axis (2-4-3), a pair of of homogeneous axis (2-4-3) at middle part
It is rotationally set with corresponding a pair of of homogeneous impeller group respectively, homogeneous impeller group is by multiple high speed homogenization impellers (2-4-5)
It forms, is engaged between the high speed homogenization impeller (2-4-5) in a pair of of homogeneous impeller group；A pair of of homogeneous axis (2-4-3) is opposite
Both ends be rotationally pierced by after homogeneous mixing warehouse (2-1) respectively respectively with to be fixedly connected on homogeneous mixing warehouse (2-1) external
The output section of the homogeneous driving mechanism of two sides connects；Homogeneous axis (2-4-3) is pushed away far from the other end of driving mechanism by enclosed
Power bearing (2-4-4) is rotatablely connected with the inner sidewall of homogeneous mixing warehouse (2-1)；
Precipitation process pond (7) includes the pond body (7-3) of upper end opening, is arranged in the internal web plate (7-2) of pond body (7-3), fixes
The precipitation process pond water inlet pipe for being supported on the external pond body bracket (7-4) of pond body (7-3), being fixedly connected on the upper end pond body (7-3)
Road (7-7), the bed mud discharge pipe (7-1) for being connected to pond body (7-3) intracavity bottom and being fixedly connected on the bottom end pond body (7-3),
With the precipitation process pond outlet pipeline (7-8) for being connected to and being fixedly connected on the side pond body (7-3) in the middle part of the inner cavity pond body (7-3)；Institute
It states middle part in pond body (7-3) and forms clear liquid area (7-5), sludge accumulation area (7-6) is formed on the interior bottom of pond body (7-3)；The precipitating
The liquid feeding end of processing pond inlet pipeline (7-7) and the outlet end of drain line (6) are penetrated through and are connected；
The clear liquid area (7-5) is disposed with dispersion plate unit, slow gentle drop net (7-5-4) of drop plate unit from top to bottom, point
The unit that falls apart is made of multiple aerofoil profile dispersion plates (7-5-2) arranged side by side, is passed through between adjacent aerofoil profile dispersion plate (7-5-2)
Connecting rod is fixedly connected, and slow drop plate unit is made of multiple rectangular slow drop plates (7-5-3) arranged side by side, the slow drop plate of adjacent prismatic
It is fixedly connected between (7-5-3) by connecting rod, the water inlet end of precipitation process pond outlet pipeline (7-8) is located at slow drop net (7-5-4)
Lower part, clear liquid area (7-5) dispersion plate unit top be provided with detection mouth (7-5-5), be connected in detection mouth (7-5-5) with
The signal piping with shut-off valve of its inner cavity connection.
2. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 1, which is characterized in that described equal
Matter driving mechanism is formed by connecting by homogeneous driving motor (2-4-1) and retarder (2-4-2).
3. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 1 or 2, which is characterized in that also
Including control cabinet (8), speed probe is set, thermal medium source of supply and liquid feeding source are respectively to be situated between with heat on retarder (2-4-2)
The thermal medium transfer pump of matter source connection and the fluid filling pump being connect with liquid source；
Control cabinet (8) is supplied with carriage drive motor (1-1), homogeneous driving motor (2-4-1), speed probe, thermal medium respectively
It should pump, the connection of fluid filling pump and waterproof machine (2-2-4).
4. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 3, which is characterized in that the branch
Supportting steelframe (1) quantity is 3 groups, and is evenly distributed on the outside of blending tank (2)；
The wall thickness of the homogeneous mixing bunker (2-1) is 2mm~50mm；
The liquid separation filter funnel (2-2) is located at the position of homogeneous mixing bunker (2-1) waist 25mm~55mm on the upper side；
The liquid-adding device (2-3) and horizontal direction angle are between 10 °~32 °；
Funnel stirring blade (2-2-5) is by the annulus and connection annulus that are set on the outside of funnel shaft (10) and funnel shaft (10)
Between radially directed connecting link composition；
The duct (2-2-1-1) with a thickness of 20mm~30mm.
5. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 4, which is characterized in that further include
The homogeneity detector (2-5) internal in homogeneous mixing bunker (2-1) is set, and homogeneity detector (2-5) and control cabinet (8) are even
It connects.
6. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 5, which is characterized in that high speed is
Matter impeller (2-4-5) quantity is 10, is spaced substantially equidistant between adjacent high speed homogenization impeller (2-4-5), and spacing 5mm~
Between 12mm, high speed homogenization impeller (2-4-5) shape is in ratchet-like.
7. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 6, which is characterized in that the pond
The bottom of body (7-3) is inverted frustum type, is provided with the COD sensor connecting with control cabinet (8) in the area clear liquid area (7-5)
(7-5-1)。
8. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 7, which is characterized in that two branch
The distance between frame gear (1-6) is 15cm~25cm.
9. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 7, which is characterized in that the height
Fast homogeneous impeller (2-4-5) is made of high molecular material, and content meter, constituent are as follows by mass percentage:
Methyl ester derivative 30%~65%, thiophosphate analog derivative 25%~60%, mixed aid are 1%~5%,
Crosslinking agent is 1%~5%, O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45%, and (T-4)-is bis-
(diethyldithiocar bamic acid-S, S') zinc 2%~15%.
10. the distributed countryside sewage treatment equipment in a kind of remote districts according to claim 7, which is characterized in that high speed
The preparation method of homogeneous impeller (2-4-5) comprises the steps of:
Step 1: being added the ultrapure water 22%~32% that conductivity is 1.25 μ of μ S/cm~3.15 S/cm in a kettle, and starting is anti-
Blender in kettle is answered, revolving speed is 125rpm~375rpm, starts heat pump, reactor temperature is made to rise to 75 DEG C~185 DEG C；
Successively methylate ester derivative 30%~65%, mixed aid are 1%~5%, and to being completely dissolved, adjusting pH value is for stirring
5.5~8.5, thiophosphate analog derivative 25%~60% is added, agitator speed is adjusted to 255rpm~315rpm, temperature
It is 90 DEG C~395 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45%, (T-4)-bis- (two is added
Diethyldithiocar bamic acid-S, S') zinc 2%~15% be uniformly mixed；
Step 3: it is 1~5% that crosslinking agent, which is added, and agitator speed is 75rpm~235rpm, and temperature is 90 DEG C~265 DEG C, is kept
This state 5~25 hours, discharging, entering molding press can be prepared by high speed homogenization impeller (2-4-5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811173367.8A CN109231386A (en) | 2018-10-09 | 2018-10-09 | A kind of distributed countryside sewage treatment equipment in remote districts |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811173367.8A CN109231386A (en) | 2018-10-09 | 2018-10-09 | A kind of distributed countryside sewage treatment equipment in remote districts |
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| CN109231386A true CN109231386A (en) | 2019-01-18 |
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ID=65054350
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| Application Number | Title | Priority Date | Filing Date |
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| CN201811173367.8A Withdrawn CN109231386A (en) | 2018-10-09 | 2018-10-09 | A kind of distributed countryside sewage treatment equipment in remote districts |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4008153A (en) * | 1974-04-29 | 1977-02-15 | Agrotechnika, Narodny Podnik | Reactor for purification of water by fluid filtration |
| RU2313384C1 (en) * | 2006-05-24 | 2007-12-27 | Станислав Афанасьевич Герасименко | Method, device and installation for realization of the physical-chemical processes between the moving mediums |
| CN203307613U (en) * | 2013-04-28 | 2013-11-27 | 巢湖市翔宇渔具有限公司 | High-temperature reaction kettle for dyeing fishing net |
| CN108163951A (en) * | 2018-03-02 | 2018-06-15 | 宁波帝杨电子科技有限公司 | A kind of device that sewage disposal is carried out using alum |
| CN207511936U (en) * | 2017-08-16 | 2018-06-19 | 森博嘉禾（天津）科技发展有限公司 | A kind of intelligentized construction industry sand-stone separator reutilization of the sewage equipment |
| CN207734660U (en) * | 2017-11-22 | 2018-08-17 | 陈云 | Bidirectional flow kudzuvine root starch starches sedimentation basin |
| CN108479933A (en) * | 2018-02-28 | 2018-09-04 | 张荷友 | A kind of batch-processed devices of drug rubbish |
-
2018
- 2018-10-09 CN CN201811173367.8A patent/CN109231386A/en not_active Withdrawn
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4008153A (en) * | 1974-04-29 | 1977-02-15 | Agrotechnika, Narodny Podnik | Reactor for purification of water by fluid filtration |
| RU2313384C1 (en) * | 2006-05-24 | 2007-12-27 | Станислав Афанасьевич Герасименко | Method, device and installation for realization of the physical-chemical processes between the moving mediums |
| CN203307613U (en) * | 2013-04-28 | 2013-11-27 | 巢湖市翔宇渔具有限公司 | High-temperature reaction kettle for dyeing fishing net |
| CN207511936U (en) * | 2017-08-16 | 2018-06-19 | 森博嘉禾（天津）科技发展有限公司 | A kind of intelligentized construction industry sand-stone separator reutilization of the sewage equipment |
| CN207734660U (en) * | 2017-11-22 | 2018-08-17 | 陈云 | Bidirectional flow kudzuvine root starch starches sedimentation basin |
| CN108479933A (en) * | 2018-02-28 | 2018-09-04 | 张荷友 | A kind of batch-processed devices of drug rubbish |
| CN108163951A (en) * | 2018-03-02 | 2018-06-15 | 宁波帝杨电子科技有限公司 | A kind of device that sewage disposal is carried out using alum |
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Address after: 221000 Science and Technology Park of Xuzhou University of Engineering, No. 18 South Third Ring Road, Quanshan District, Xuzhou City, Jiangsu Province (Xuzhou 2.5 Industrial Park) Applicant after: Xuzhou Institute of Technology Address before: 221000 University Science Park, Xuzhou Institute of Engineering, No. 18 South Third Ring Road, Quanshan District, Xuzhou City, Jiangsu Province Applicant before: Xuzhou Institute of Technology |
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Application publication date: 20190118 |