CN109317034A - One kind is for nutrient solution mixing arrangement in camplotheca acuminata plantation - Google Patents
One kind is for nutrient solution mixing arrangement in camplotheca acuminata plantation Download PDFInfo
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- CN109317034A CN109317034A CN201811172684.8A CN201811172684A CN109317034A CN 109317034 A CN109317034 A CN 109317034A CN 201811172684 A CN201811172684 A CN 201811172684A CN 109317034 A CN109317034 A CN 109317034A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/051—Stirrers characterised by their elements, materials or mechanical properties
- B01F27/053—Stirrers characterised by their elements, materials or mechanical properties characterised by their materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/40—Mounting or supporting mixing devices or receptacles; Clamping or holding arrangements therefor
- B01F35/43—Supporting receptacles on frames or stands
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/45—Closures or doors specially adapted for mixing receptacles; Operating mechanisms therefor
- B01F35/453—Closures or doors specially adapted for mixing receptacles; Operating mechanisms therefor by moving them perpendicular to the plane of the opening
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/712—Feed mechanisms for feeding fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
One kind is for nutrient solution mixing arrangement in camplotheca acuminata plantation, it mixes pot bottom and precipitation process pond is connected by drain line, precipitation process pond connects secondary treatment system, the dredge for preventing pipeline blockage is equipped in secondary treatment system, screw thread is provided with for left section of mandril in dredge, and the worm gear being driven by motor drives mandril to move reciprocatingly；Liquid feeding pipeline, liquid separation filter funnel and homogeneous system are equipped with inside homogeneous mixing bunker body, the side wall of liquid separation filter funnel is equipped with aperture, and the center of the bottom plate of liquid separation filter funnel is rotatablely connected funnel shaft by bearing collet, and funnel shaft and upper beam are affixed；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, good mixing effect.
Description
Technical field
The invention belongs to forestry planting equipment technical fields, and in particular to one kind is for nutrient solution mixing dress in camplotheca acuminata plantation
It sets.
Background technique
Nutrient fluid cultivation is also known as hydroponic culture, is a kind of without natural soil, and using required containing plant growth and development
The nutrient solution of element provides nutrition, so that plant is normally completed the cultivation technique of whole life cycle, it greatly extends agricultural
Production space, so that crop can not depend on soil and be produced, development prospect is very extensive.
It is the Different Nutrient Elements according to required for plant production for nutrient solution used in nutrient fluid cultivation process,
It needs uniformly to be mixed different types of nutrient solution using nutrient solution mixing arrangement, in order to the fast-growth of plant,
But generally compared with simple, nutrient solution is difficult to uniformly be mixed inside mixing bunker existing nutrient solution mixing arrangement structure,
It is unable to satisfy the demand of plant growth.In addition, the small particle of indissoluble is not easy to separate in nutrient solution mixed process, cause
Nutrient solution it is of low quality.
Summary of the invention
In view of the above existing problems in the prior art, the present invention provides one kind for nutrient solution mixing dress in camplotheca acuminata plantation
It sets, the apparatus structure is simple, convenient for operation, stir and evenly mix that effect is good, and be conducive to being sufficiently mixed for nutrient solution, meanwhile, it sinks
Shallow lake effect is ideal, is convenient for the short grained separation of indissoluble, can improve the quality of nutrient solution.
To achieve the goals above, the present invention provides a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, including mixing
Tank, the multiple supporting steel frames for being fixedly connected on blending tank lower outside, upper connection crank 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 fixed to be connected
It connects in the side away from support gear of L-type support, and its output shaft and the transmission case that is fixedly connected on L-type support side
Input terminal 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 end for connecting one end and upper pressure sealing cover for cranking arm
Face is fixedly connected, and 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 with it is upper
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, to control top by expanding-contracting action
The lid of pressure seal lid 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, it is provided on the side wall of liquid separation filter funnel throughout ground
Several side-wall holes, the bottom plate of liquid separation filter funnel are outwardly provided with multiple apertures, and the rotation center of bottom plate throughout it
It is connected with funnel shaft by the bearing collet being firmly connected with it, lower end of the funnel shaft inside liquid separation filter funnel connects
It is connected to the funnel stirring blade of one with the cooperation of homogeneous mixing warehouse lower end internal clearance；Funnel shaft is in liquid separation filter funnel
Outer upper ends are set with outer gear ring, are fixedly connected between outer gear ring and funnel shaft by radially connected beam；In homogeneous mixing bunker
It is fixedly connected with waterproof machine on the inner sidewall of body with corresponding to outer gear ring, funnel gear is equipped on the output shaft of waterproof machine,
Funnel gear is engaged with outer gear ring；The outlet end of liquid feeding pipeline is located above liquid separation filter funnel, and it is mixed that liquid feeding end is pierced by homogeneous
It is connect after closing the side wall of warehouse 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
The connection of coolant liquid recycling bins；
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 divided after being rotationally pierced by homogeneous mixing warehouse respectively
It is not 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 drive
The other end of motivation 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 of pond body side with pond body inner cavity middle part
Pond 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
The liquid feeding end of inlet pipeline and the outlet end of drain line are penetrated through and are connected；
In precipitation process pond, the water outlet of outlet pipeline is connected with secondary treatment system, and the secondary treatment system includes perpendicular
Secondary treatment inlet pipeline, the horizontally disposed and water with secondary treatment inlet pipeline water outlet vertically through connection being directly arranged
The U-shaped processing pipeline that horizontal feed pipeline water outlet lower part is arranged in, U-shaped processing pipeline lower part is arranged in flat transfer pipeline
Secondary precipitation room and perforation are connected to the secondary sediment discharge pipe of secondary precipitation room lower end；One in U-shaped processing pipeline is perpendicular
The upper end of straight section is connect with the perforation of horizontal feed pipeline water outlet, and the upper end of another vertical section is provided with secondary treatment row
Water lines；
Dredge is additionally provided on the left of horizontal feed pipeline water inlet end, the dredge includes being arranged in horizontal feed
In pipeline inner cavity and outer diameter is less than the top of horizontal feed pipeline internal diameter, is vertically connected to top left side center and sliding
Sealingly extend through the mandril of horizontal feed pipeline left side plate, the mandril being fixedly connected on the left of horizontal feed pipeline shrinks driving
Device；
It includes supporing shell, the cunning for being arranged in supporing shell and penetrating through its left and right ends that the mandril, which shrinks driving device,
Chamber, the worm gear being arranged in the mounting base of downside, is set opposite each other two mounting bases that sliding chamber upper and lower part is arranged in
The pressure roller in the mounting base of upside is set, is arranged in inside supporing shell and is located at the spring cavity for sliding chamber top and be mounted on bullet
Spring A in spring chamber；The mounting base on top is arranged in longitudinal sliding in sliding chamber, and the mounting base of lower part is fixedly connected on sliding chamber
In, worm gear is rotatably connected in the mounting base of lower part by the shaft A of its rotation center, and one end of shaft A is rotationally worn
Supporing shell and the output axis connection with the deceleration motor being fixedly mounted on outside supporing shell out；Pressure roller is revolved by it
The shaft B for turning center is rotatably connected in the mounting base on top；Worm gear and the opposite setting of pressure roller, and therebetween there are
Gap is simultaneously set in left half section of the outside of mandril by gap, and left half section of the outside of mandril is provided with the spiral shell being meshed with worm gear
Line；The both ends of spring A are against the upper surface at the top of spring cavity and the mounting base of upside respectively.
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
Secondary precipitation room is the hollow-sphere structures of diameter 10cm~15cm.
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.
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 of nutrition composition.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 nutrient solution prescription 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 nutrient solution prescription it
Between uniform mixing.Supporting steel frame can control height of the blending tank relative to supporting plane.The setting in precipitation process pond can be just
Indissoluble substance staticly settles in mixed liquor, in order to isolate indissoluble substance and outlet.Secondary treatment system is set
It sets, secondary precipitation can be carried out to the clear liquid that precipitation process pond outlet pipeline is discharged, the setting of U-shaped processing pipeline can be by sediment
It is discharged into secondary precipitation room, and clear liquid is discharged by one end of U-shaped processing pipeline vertical section, can effectively improve the precipitating of indissoluble substance
Effect achievees the purpose that sufficiently to precipitate.The setting of dredge can pass through the reciprocal fortune of mandril and top in horizontal feed pipeline
It moves to be dredged, to prevent the flat transfer pipeline of water, there is a situation where block.Mandril shrinks driving device and passes through deceleration electricity
Machine drives worm gear to rotate, and then the left and right of mandril is driven to move back and forth, and spring A can push mounting base elasticity, and then make to press
Roller can compress mandril always, to guarantee screw thread that worm gear can be acted on effectively on mandril, achieve the purpose that stabilized driving.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；
The structural schematic diagram of secondary treatment system in Fig. 8 present invention；
Fig. 9 is the structural schematic diagram that mandril shrinks driving device in the present invention；
O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate accounting is to improving uniformity in Figure 10 present invention
The influence graph of relation of rate；
Methyl ester derivative molecular characterization schematic diagram in Figure 11 invention；
Group thiophosphate derivative molecular structure feature schematic diagram in Figure 12 present invention；
Oxysilane substance molecular characterization schematic diagram in Figure 13 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, enclosed thrust axis
Hold, 2-4-5, high speed homogenization impeller, 2-5, homogeneity detector, 3, upper pressure sealing cover, 4, it is upper connection crank arm, 5, on stretch
Contracting 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, 7-6, sludge accumulation area, 7-7, precipitation process pond inlet pipeline, 7-8, precipitation process pond outlet pipeline are 7-8-1, secondary heavy
Slag discharge pipe, 7-8-2, secondary precipitation room, 7-8-3, U-shaped processing pipeline, 7-8-4, secondary treatment discharge line, 7-8-5,
Horizontal feed pipeline, 7-8-6, secondary treatment inlet pipeline, 7-8-7, top, 7-8-8, mandril, 7-8-9, mandril shrink driving
Device, 7-8-9-1, supporing shell, 7-8-9-2, mounting base, 7-8-9-3, worm gear, 7-8-9-4, pressure roller, 7-8-9-5, sliding chamber,
7-8-9-6, spring cavity, 7-8-9-7, spring A, 8, control cabinet, 9, radially connected beam, 10, funnel shaft.
Specific embodiment
The invention will be further described below.
If Fig. 1 to Fig. 9 shows, one kind is for nutrient solution mixing arrangement in camplotheca acuminata plantation, including blending tank 2, is fixedly connected on
Multiple supporting steel frames 1 of 2 lower outside of blending tank, upper connection are cranked arm 4, upper telescopic oil cylinder 5 and precipitation process pond 7；
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
The side away from support gear 1-6 of 1-7, and its output shaft and the transmission case 1-2 that is fixedly connected on the side L-type support 1-7
Input terminal connection, the output end of transmission case 1-2 are 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 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 2-2's
Ground is provided with several side-wall holes 2-2-1 on side wall, the bottom plate of liquid separation filter funnel 2-2 is outwardly arranged throughout it
There are multiple apertures, 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,
Lower end of the funnel shaft 10 inside liquid separation filter funnel 2-2 is connected with one and the homogeneous mixing lower end warehouse 2-1 internal clearance
The funnel stirring blade 2-2-5 of cooperation；Funnel shaft 10 is set with outer gear ring 2-2- in liquid separation filter funnel 2-2 outer upper ends
2, it is fixedly connected between outer gear ring 2-2-2 and funnel shaft 10 by radially connected beam 9；In the inside of homogeneous mixing warehouse 2-1
It is fixedly connected with waterproof machine 2-2-4 with corresponding to outer gear ring 2-2-2 on wall, leakage is equipped on the output shaft of waterproof machine 2-2-4
Bucket tooth wheel 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 the leakage of liquid separation strainer
It struggles against above 2-2, liquid feeding end is 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 only in bearing holding tank
Bearing 2-2-6-3 is moved back, the inner ring of retaining bearing 2-2-6-3 is fixedly connected with funnel shaft 10；Toroidal cavity 2-2-6-2 difference
It is connected 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 feed liquor
Pipeline 2-2-6-4 and coolant liquid outlet tube road 2-2-6-5 is radially across liquid separation filter funnel 2-2, homogeneous mixing warehouse 2-1
It is connect respectively with cooling source and coolant liquid recycling bins afterwards；
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
Corresponding a pair of of homogeneous impeller group it is not set with rotationally, homogeneous impeller group is by multiple high speed homogenization impeller 2-4-5 groups
At being 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 opposite both ends point
Be not pierced by rotationally after homogeneous mixing warehouse 2-1 respectively with the homogeneous that is fixedly connected on homogeneous mixing warehouse 2-1 both sides external
The output section of driving mechanism connects；Homogeneous axis 2-4-3 passes through closed type thrust bearing 2-4-4 far from the other end of driving mechanism
It 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, 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；
In precipitation process pond, the water outlet of outlet pipeline 7-8 is connected with secondary treatment system, the secondary treatment system packet
The secondary treatment inlet pipeline 7-8-6 being vertically arranged is included, is horizontally disposed with and is hung down with the secondary treatment water outlet inlet pipeline 7-8-6
The horizontal feed pipeline 7-8-5 of straight perforation connection, the U-shaped processing pipeline that the horizontal feed water outlet pipeline 7-8-5 lower part is set
7-8-2, the secondary precipitation room 7-8-2 that the U-shaped processing lower part pipeline 7-8-2 is arranged in and perforation are connected to secondary precipitation room 7-8-2
The secondary sediment discharge pipe 7-8-1 of lower end；The upper end of a vertical section in U-shaped processing pipeline 7-8-2 and horizontal conveying pipe
The perforation ground connection of the road water outlet 7-8-5, the upper end of another vertical section is provided with secondary treatment discharge pipe line 7-8-4.
Dredge is additionally provided on the left of horizontal feed pipeline 7-8-5 water inlet end, the dredge includes being arranged in water
In the inner cavity flat transfer pipeline 7-8-5 and outer diameter is less than the top 7-8-7 of horizontal feed pipeline 7-8-5 internal diameter, is vertically connected to
Come directly towards the left side 7-8-7 center and slidably and sealingly across the mandril 7-8-8 of horizontal feed pipeline 7-8-5 left side plate, fixed company
It connects the mandril on the left of horizontal feed pipeline 7-8-5 and shrinks driving device 7-8-9；The mandril shrinks driving device 7-8-9 packet
Include supporing shell 7-8-9-1, the cunning chamber 7-8-9-5 that is arranged in supporing shell 7-8-9-1 and penetrates through its left and right ends, each other
Two mounting base 7-8-9-2 for being oppositely disposed in the upper and lower part sliding chamber 7-8-9-5, the mounting base 7-8- that downside is set
Worm gear 7-8-9-3 in 9-2, the pressure roller 7-8-9-4 being arranged in the mounting base of upside, it is arranged in supporing shell 7-8-9-1
Portion and the spring A7-8-9-7 for being located at the spring cavity 7-8-9-6 on the sliding top chamber 7-8-9-5 and being mounted in spring cavity 7-8-9-6；
The mounting base 7-8-9-2 on top is arranged in longitudinal sliding in sliding chamber 7-8-9-5, and the mounting base 7-8-9-2 of lower part is fixedly connected
In sliding chamber 7-8-9-5, worm gear is rotatably connected in the mounting base 7-8-9-2 of lower part by the shaft A of its rotation center, and
One end of shaft A be rotationally pierced by supporing shell 7-8-9-1 and be fixedly mounted on subtracting outside supporing shell 7-8-9-1
The output axis connection of fast driving motor；Pressure roller 7-8-9-4 is rotatably connected on the installation on top by the shaft B of its rotation center
In seat 7-8-9-2；Worm gear 7-8-9-3 and pressure roller 7-8-9-4 opposite setting, and there are gap and pass through sky therebetween
Gap is set in left half section of the outside mandril 7-8-8, and left half section of the outside mandril 7-8-8 is provided with to be meshed with worm gear 7-8-9-3
Screw thread；The both ends of spring A7-8-9-7 are against the top of spring cavity 7-8-9-6 and the mounting base 7-8-9-2's of upside respectively
Upper surface.
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；
Secondary precipitation room 7-8-2 is the hollow-sphere structures of diameter 10cm~15cm.
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.
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 benzene
Any one in base (bisphenol-A) bisphosphate.
The feature of methyl ester derivative molecular structure is as shown in figure 11, 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 12, molecular formula: C10H15O3PS2；Molecule
Amount: 278.343.
Mixed aid is oxysilane substance, and molecular structural formula is as shown in figure 13, 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%,
Mixed aid is 5%, and to being completely dissolved, adjusting pH value is 8.5 for stirring, and thiophosphate analog derivative 60% is added, will stir
Device 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 4%, to being completely dissolved, adjusting pH value is 5.8 for stirring, and thiophosphate analog derivative 40% is added,
Agitator speed is adjusted to 300rpm, 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-
The homogeneity of the material of 1 lower part makes induction and reacts and detected；When homogeneity does not meet examination criteria, homogeneity inspection
It surveys device 2-5 and issues electric signal to control cabinet 8, 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；
Step 5: in precipitation process pond 7, mixed liquor enters clear liquid area 7-5 by precipitation process pond inlet pipeline 7-7；?
Under the action of web plate 7-2, the floating material in mixed liquor is filtered；Meanwhile the solid content in mixed liquor is settled down to sludge accumulation area
7-6 is simultaneously discharged from bed mud discharge pipe 7-1, and then remaining clear water is flowed out from the outlet pipeline 7-8 of precipitation process pond；
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. one kind is for nutrient solution mixing arrangement in camplotheca acuminata plantation, including blending tank (2) and is fixedly connected on blending tank (2) lower part
Multiple supporting steel frames (1) in outside, which is characterized in that further include upper connection crank arm (4), upper telescopic oil cylinder (5) and precipitation process
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；
It is connected with secondary treatment system in the water outlet of precipitation process pond outlet pipeline (7-8), the secondary treatment system includes
It is the secondary treatment inlet pipeline (7-8-6) that is vertically arranged, horizontally disposed and hang down with the secondary treatment inlet pipeline water outlet (7-8-6)
It is straight to penetrate through the horizontal feed pipeline (7-8-5) connected, the U-shaped processing in the water outlet lower part horizontal feed pipeline (7-8-5) is set
Pipeline (7-8-2), setting are connected to secondary sink in the secondary precipitation room (7-8-2) of U-shaped processing lower part pipeline (7-8-2) and perforation
The secondary sediment discharge pipe (7-8-1) of the lower end shallow lake room (7-8-2)；It is U-shaped to handle the upper of a vertical section in pipeline (7-8-2)
End is connect with the perforation of the horizontal feed pipeline water outlet (7-8-5), and the upper end of another vertical section is provided with secondary treatment draining
Pipeline (7-8-4)；
Dredge is additionally provided on the left of horizontal feed pipeline (7-8-5) water inlet end, the dredge includes being arranged in level
In the inner cavity transfer pipeline (7-8-5) and outer diameter is less than the top (7-8-7) of horizontal feed pipeline (7-8-5) internal diameter, vertically connects
Meet the mandril (7-8- at the left side center top (7-8-7) and slidably and sealingly passing through horizontal feed pipeline (7-8-5) left side plate
8) it, is fixedly connected on the mandril on the left of horizontal feed pipeline (7-8-5) and shrinks driving device (7-8-9)；
The mandril shrinks driving device (7-8-9) and includes supporing shell (7-8-9-1), is arranged at supporing shell (7-8-9-1)
In and penetrate through the cunning chamber (7-8-9-5) of its left and right ends, opposite each other be arranged in the two of sliding upper and lower part chamber (7-8-9-5)
A mounting base (7-8-9-2), the worm gear (7-8-9-3) being arranged in the mounting base (7-8-9-2) of downside, the peace that upside is set
The pressure roller (7-8-9-4) in seat, setting are filled in supporing shell (7-8-9-1) inside and is located at the bullet on sliding top chamber (7-8-9-5)
Spring chamber (7-8-9-6) and the spring A (7-8-9-7) being mounted in spring cavity (7-8-9-6)；The mounting base (7-8-9-2) on top
It is arranged in sliding chamber (7-8-9-5) with longitudinal sliding, the mounting base (7-8-9-2) of lower part is fixedly connected on sliding chamber (7-8-9-5)
In, worm gear is rotatably connected in the mounting base (7-8-9-2) of lower part by the shaft A of its rotation center, and one end of shaft A can
Rotationally it is pierced by supporing shell (7-8-9-1) and the deceleration motor external with supporing shell (7-8-9-1) is fixedly mounted on
Output axis connection；Pressure roller (7-8-9-4) is rotatably connected on the mounting base (7-8-9- on top by the shaft B of its rotation center
2) in；Worm gear (7-8-9-3) and the opposite setting of pressure roller (7-8-9-4), and there are gap and pass through gap therebetween and cover
It is located at left half section of the outside of mandril (7-8-8), left half section of the outside of mandril (7-8-8) is provided with mutually nibbles with worm gear (7-8-9-3)
The screw thread of conjunction；The both ends of spring A (7-8-9-7) are against the top of spring cavity (7-8-9-6) and the mounting base (7-8- of upside respectively
Upper surface 9-2).
2. according to claim 1 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that the homogeneous
Driving mechanism is formed by connecting by homogeneous driving motor (2-4-1) and retarder (2-4-2).
3. according to claim 1 or 2 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that also wrap
It includes control cabinet (8), speed probe is set on retarder (2-4-2), thermal medium source of supply and liquid feeding source are respectively and thermal medium
The thermal medium transfer pump of 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. according to claim 3 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that the support
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；
Secondary precipitation room (7-8-2) is the hollow-sphere structures of diameter 10cm~15cm.
5. according to claim 4 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that further include setting
The homogeneity detector (2-5) internal in homogeneous mixing bunker (2-1) is set, homogeneity detector (2-5) is connect with control cabinet (8).
6. according to claim 5 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that high speed homogenization
Impeller (2-4-5) quantity is 10, is spaced substantially equidistant between adjacent high speed homogenization impeller (2-4-5), and spacing is in 5mm~12mm
Between, high speed homogenization impeller (2-4-5) shape is in ratchet-like.
7. according to claim 6 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that the pond body
The bottom of (7-3) is inverted frustum type.
8. according to claim 7 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that two brackets
The distance between gear (1-6) is 15cm~25cm.
9. according to claim 7 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that the high speed
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. according to claim 7 a kind of for nutrient solution mixing arrangement in camplotheca acuminata plantation, which is characterized in that high speed is
The preparation method of matter 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).
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| CN118045551A (en) * | 2024-04-16 | 2024-05-17 | 四川蜀道建筑科技有限公司 | Polycarboxylate water reducing agent waste material comprehensive utilization apparatus for producing |
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