CN109317034B - Be arranged in camptotheca acuminata to plant nutrient solution mixing arrangement - Google Patents
Be arranged in camptotheca acuminata to plant nutrient solution mixing arrangement Download PDFInfo
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- CN109317034B CN109317034B CN201811172684.8A CN201811172684A CN109317034B CN 109317034 B CN109317034 B CN 109317034B CN 201811172684 A CN201811172684 A CN 201811172684A CN 109317034 B CN109317034 B CN 109317034B
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- 238000002156 mixing Methods 0.000 title claims abstract description 124
- 235000015097 nutrients Nutrition 0.000 title claims abstract description 29
- 241000759905 Camptotheca acuminata Species 0.000 title claims abstract description 9
- 241000196324 Embryophyta Species 0.000 title description 4
- 239000007788 liquid Substances 0.000 claims abstract description 60
- 238000004062 sedimentation Methods 0.000 claims abstract description 40
- 238000003756 stirring Methods 0.000 claims abstract description 23
- 239000000110 cooling liquid Substances 0.000 claims abstract description 22
- 230000007246 mechanism Effects 0.000 claims abstract description 12
- 238000001816 cooling Methods 0.000 claims abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 39
- 238000007789 sealing Methods 0.000 claims description 19
- 229910000831 Steel Inorganic materials 0.000 claims description 14
- 239000010959 steel Substances 0.000 claims description 14
- 230000005540 biological transmission Effects 0.000 claims description 9
- 230000008602 contraction Effects 0.000 claims description 9
- 230000006835 compression Effects 0.000 claims description 8
- 238000007906 compression Methods 0.000 claims description 8
- 239000003638 chemical reducing agent Substances 0.000 claims description 7
- 239000010802 sludge Substances 0.000 claims description 7
- 238000009434 installation Methods 0.000 claims description 6
- 230000009467 reduction Effects 0.000 claims description 6
- 241000759909 Camptotheca Species 0.000 claims description 5
- 238000009825 accumulation Methods 0.000 claims description 5
- 230000009471 action Effects 0.000 claims description 5
- 239000013049 sediment Substances 0.000 claims description 5
- 230000000149 penetrating effect Effects 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 238000011084 recovery Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 13
- 239000000243 solution Substances 0.000 description 21
- 238000006243 chemical reaction Methods 0.000 description 16
- 239000012752 auxiliary agent Substances 0.000 description 14
- 150000004702 methyl esters Chemical class 0.000 description 14
- 239000000463 material Substances 0.000 description 12
- RYYWUUFWQRZTIU-UHFFFAOYSA-N Thiophosphoric acid Chemical class OP(O)(S)=O RYYWUUFWQRZTIU-UHFFFAOYSA-N 0.000 description 9
- JXHJNEJVUNHLKO-UHFFFAOYSA-N sulprofos Chemical compound CCCSP(=S)(OCC)OC1=CC=C(SC)C=C1 JXHJNEJVUNHLKO-UHFFFAOYSA-N 0.000 description 9
- 239000003431 cross linking reagent Substances 0.000 description 8
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 7
- 125000004177 diethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 7
- 238000007599 discharging Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 229910052725 zinc Inorganic materials 0.000 description 7
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- 238000010438 heat treatment Methods 0.000 description 5
- 230000006872 improvement Effects 0.000 description 5
- 238000000465 moulding Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 229910021642 ultra pure water Inorganic materials 0.000 description 5
- 239000012498 ultrapure water Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
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- 238000002360 preparation method Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000003892 spreading Methods 0.000 description 2
- 230000007480 spreading Effects 0.000 description 2
- NHNMTZZAQRAIOO-UHFFFAOYSA-N OP(O)(=O)OP(=O)(O)O.C1(=CC=CC=C1)C1=C(C(=C(C(=C1O)C1=CC=CC=C1)C1=CC=CC=C1)C(C)(C)C1=CC=C(C=C1)O)C1=CC=CC=C1 Chemical compound OP(O)(=O)OP(=O)(O)O.C1(=CC=CC=C1)C1=C(C(=C(C(=C1O)C1=CC=CC=C1)C1=CC=CC=C1)C(C)(C)C1=CC=C(C=C1)O)C1=CC=CC=C1 NHNMTZZAQRAIOO-UHFFFAOYSA-N 0.000 description 1
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- 238000007667 floating Methods 0.000 description 1
- 235000012041 food component Nutrition 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 125000001972 isopentyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])C([H])([H])* 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 230000008121 plant development Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- RIJDNATVAMLZRB-UHFFFAOYSA-M sodium;oxido-propan-2-yloxy-propan-2-ylsulfanyl-sulfanylidene-$l^{5}-phosphane Chemical compound [Na+].CC(C)OP([O-])(=S)SC(C)C RIJDNATVAMLZRB-UHFFFAOYSA-M 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- WMYJOZQKDZZHAC-UHFFFAOYSA-H trizinc;dioxido-sulfanylidene-sulfido-$l^{5}-phosphane Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S WMYJOZQKDZZHAC-UHFFFAOYSA-H 0.000 description 1
Images
Classifications
-
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
A nutrient solution mixing device used in camptotheca acuminata planting is characterized in that the bottom of a mixing tank is connected with a sedimentation treatment tank through a liquid discharge pipeline, the sedimentation treatment tank is connected with a secondary treatment system, a dredger for preventing the pipeline from being blocked is arranged in the secondary treatment system, the left section of a top rod in the dredger is provided with a thread, and a worm wheel driven by a motor drives the top rod to reciprocate; a liquid feeding pipeline, a separating filter screen funnel and a homogenizing system are arranged in the homogenizing mixing bin body, an opening is formed in the side wall of the separating filter screen funnel, the center of a bottom plate of the separating filter screen funnel is rotatably connected with a funnel rotating shaft through a bearing bottom support, and the funnel rotating shaft is fixedly connected with an upper cross beam; the rotating shaft of the funnel is connected with two funnel stirring blades in the separating filter screen funnel; the liquid inlet end of the liquid feeding pipeline is connected with an external liquid feeding source; the bearing bottom support is provided with a cooling cavity and a cooling liquid supply pipeline; the homogenizing system comprises a pair of homogenizing wave wheel sets sleeved on a pair of homogenizing middle shafts, and the pair of homogenizing middle shafts are driven by a pair of homogenizing driving mechanisms. The device has simple structure and good mixing effect.
Description
Technical Field
The invention belongs to the technical field of forestry planting equipment, and particularly relates to a nutrient solution mixing device for camptotheca acuminate planting.
Background
The nutrient solution cultivation is also called hydroponic cultivation, which is a cultivation technology that uses nutrient solution containing essential elements for plant growth and development to provide nutrition without using natural soil so that the plants normally complete the whole life cycle, greatly expands the agricultural production space, enables the crops to be produced without depending on soil, and has wide development prospect.
Nutrient solution to the nutrient solution cultivation in-process use is according to the required different nutrient elements of plant production, need use nutrient solution mixing arrangement to carry out even mixture with different types of nutrient solution to the quick growth of plant, but current nutrient solution mixing arrangement structure is generally more simple, and the nutrient solution is difficult to carry out even mixture in mixing the storehouse inside, can't satisfy vegetation's demand. In addition, in the process of mixing the nutrient solution, indissolvable small particles are not convenient to separate, so that the quality of the nutrient solution is not high.
Disclosure of Invention
Aiming at the problems in the prior art, the invention provides a nutrient solution mixing device for planting camptotheca acuminate, which is simple in structure, convenient to operate, good in stirring and uniformly mixing effect, favorable for fully mixing nutrient solution, ideal in precipitation effect, convenient for separating insoluble small particles and capable of improving the quality of the nutrient solution.
In order to achieve the purpose, the invention provides a nutrient solution mixing device for camptotheca acuminate planting, which comprises a mixing tank, a plurality of supporting steel frames fixedly connected to the outer side of the lower part of the mixing tank, an upper connecting crank arm, an upper telescopic oil cylinder and a sedimentation treatment tank, wherein the upper connecting crank arm is connected with the upper telescopic oil cylinder;
the supporting steel frame comprises a support, a pair of vertical beams which are parallel and fixedly connected to the support, an L-shaped support arranged on one side of the pair of vertical beams and a support driving motor arranged on one side of the pair of vertical beams; the vertical beams are respectively provided with a longitudinally extending continuous rack and a longitudinally extending sliding rail on the same side; the upper part and the lower part of the vertical section of the L-shaped bracket corresponding to the position of the continuous rack are respectively provided with a bracket gear, and the bracket gear is rotatably connected to the vertical section of the L-shaped bracket through a gear rotating shaft at the center of the bracket gear; a sliding groove is formed in the position, corresponding to the sliding rail, of the vertical section of the L-shaped support, the sliding groove is sleeved outside the sliding rail in a sliding mode, and the end of the support on the horizontal section of the L-shaped support is fixedly connected with the outer side wall of the mixing tank; the support driving motor is fixedly connected to one side of the L-shaped support, which is far away from the support gear, an output shaft of the support driving motor is connected with an input end of a transmission case fixedly connected to one side of the L-shaped support, and an output end of the transmission case is connected with gear shafts of the two support gears;
the upper opening end of the mixing tank is provided with an upper pressure sealing cover for sealing the mixing tank, and the bottom end of the mixing tank is fixedly connected with a liquid discharge pipeline communicated with the inner cavity of the mixing tank; one end of the upper connecting crank arm is fixedly connected with the upper end face of the upper pressure sealing cover, and the other end of the upper connecting crank arm is hinged with a hinge seat fixedly connected to the outer side of the upper end of the mixing tank; one end of the upper telescopic oil cylinder is hinged with the outer side of the hinged end of the upper connecting crank arm, and the other end of the upper telescopic oil cylinder is hinged with the middle part of the tank body of the mixing tank, so that the upper pressure sealing cover is controlled to be closed or opened through telescopic action;
the mixing tank comprises a homogeneous mixing cabin body with a jacket structure, a heat transfer medium is filled in a jacket of the homogeneous mixing cabin body, a heat medium pipeline communicated with the jacket space of the homogeneous mixing cabin body is connected to the outside of the homogeneous mixing cabin body, and the other end of the heat medium pipeline is connected with a heat medium supply source;
the device comprises a homogenizing mixing bin body, a liquid feeding pipeline, a separating screen funnel and a homogenizing system, wherein the liquid feeding pipeline is obliquely arranged in the homogenizing mixing bin body from top to bottom, the separating screen funnel is horizontally placed and can rotate relative to the homogenizing mixing bin body, a plurality of side wall openings are formed in the side wall of the separating screen funnel in a spreading mode, a plurality of small holes are formed in the surface of the bottom plate of the separating screen funnel in a spreading mode, the rotating center of the bottom plate is connected with a funnel rotating shaft through a bearing base fixedly connected with the bottom plate, and the lower end, inside the separating screen funnel, of the funnel rotating shaft is connected with a funnel stirring blade in; the funnel rotating shaft is sleeved with an outer gear ring at the upper end of the outer part of the separating filter screen funnel, and the outer gear ring is fixedly connected with the funnel rotating shaft through a radial connecting beam; a waterproof motor is fixedly connected to the inner side wall of the homogeneous mixing cabin body corresponding to the outer gear ring, a funnel gear is assembled on an output shaft of the waterproof motor, and the funnel gear is meshed with the outer gear ring; the liquid outlet end of the liquid feeding pipeline is positioned above the separating filter screen funnel, and the liquid inlet end of the liquid feeding pipeline penetrates through the side wall of the homogenizing and mixing bin body and then is connected with a liquid feeding source;
a bearing accommodating groove which is sunken downwards is formed in the center of the bearing bottom support, and an annular cavity is formed in the bearing bottom support in a mode of surrounding the bearing accommodating groove; a backstop bearing is fixedly assembled in the bearing accommodating groove, and an inner ring of the backstop bearing is fixedly connected with the funnel rotating shaft; the annular cavity is respectively connected with a cooling liquid inlet pipeline and a cooling liquid outlet pipeline which are communicated with the inner cavity of the annular cavity, and the cooling liquid inlet pipeline and the cooling liquid outlet pipeline are respectively connected with a cooling source and a cooling liquid recovery box after radially penetrating through the separating filter screen funnel and the homogeneous mixing bin body;
the homogenizing system comprises a pair of homogenizing middle shafts which are arranged side by side, a pair of homogenizing middle shafts are respectively sleeved with a pair of corresponding homogenizing impeller sets in a rotatable mode in the middle, each homogenizing impeller set is composed of a plurality of high-speed homogenizing impellers, and high-speed homogenizing impellers in the pair of homogenizing impeller sets are meshed with each other; two opposite ends of the pair of homogenizing middle shafts respectively penetrate out of the homogenizing mixing cabin body in a rotatable mode and then are respectively connected with output parts of homogenizing driving mechanisms fixedly connected to two sides of the outside of the homogenizing mixing cabin body; the other end of the homogenizing middle shaft, which is far away from the driving mechanism, is rotationally connected with the inner side wall of the homogenizing mixing bin body through a closed thrust bearing.
The sedimentation treatment tank comprises a tank body with an opening at the upper end, a screen plate arranged in the tank body, a tank body bracket fixedly supported outside the tank body, a sedimentation treatment tank water inlet pipeline fixedly connected at the upper end of the tank body, a bottom mud discharge pipeline communicated with the bottom of an inner cavity of the tank body and fixedly connected to the bottom end of the tank body, and a sedimentation treatment tank water outlet pipeline communicated with the middle of the inner cavity of the tank body and fixedly connected to one side of the tank body; a clear liquid zone is formed in the middle part in the tank body, and a sludge accumulation zone is formed at the bottom in the tank body; the liquid inlet end of the water inlet pipeline of the sedimentation treatment tank is communicated with the liquid outlet end of the liquid discharge pipeline;
the water outlet end of the water outlet pipeline of the sedimentation treatment tank is connected with a secondary treatment system, and the secondary treatment system comprises a secondary treatment water inlet pipeline which is vertically arranged, a horizontal conveying pipeline which is horizontally arranged and vertically communicated with the water outlet end of the secondary treatment water inlet pipeline, a U-shaped treatment pipeline arranged at the lower part of the water outlet end of the horizontal conveying pipeline, a secondary sedimentation chamber arranged at the lower part of the U-shaped treatment pipeline and a secondary sediment discharge pipeline communicated with the lower end of the secondary sedimentation chamber; the upper end of one vertical section in the U-shaped treatment pipeline is communicated with the water outlet end of the horizontal conveying pipeline, and the upper end of the other vertical section is provided with a secondary treatment drainage pipeline;
the left side of the water inlet end of the horizontal conveying pipeline is also provided with a dredger, the dredger comprises a top head, a top rod and a top rod contraction driving device, the top head is arranged in the inner cavity of the horizontal conveying pipeline, the outer diameter of the top head is smaller than the inner diameter of the horizontal conveying pipeline, the top rod is vertically connected to the center of the left end face of the top head and penetrates through the left end plate of the horizontal conveying pipeline in a sliding and sealing mode, and the top rod contraction driving device is fixedly;
the ejector rod contraction driving device comprises a supporting shell, a sliding cavity, two mounting seats, a worm wheel, a compression roller, a spring cavity and a spring A, wherein the sliding cavity is arranged in the supporting shell and penetrates through the left end and the right end of the supporting shell; the upper mounting seat is longitudinally arranged in the sliding cavity in a sliding mode, the lower mounting seat is fixedly connected in the sliding cavity, the worm wheel is rotatably connected in the lower mounting seat through a rotating shaft A at the rotating center of the worm wheel, and one end of the rotating shaft A rotatably penetrates through the supporting shell and is connected with an output shaft of a speed reduction driving motor fixedly arranged outside the supporting shell; the compression roller is rotatably connected in the mounting seat at the upper part through a rotating shaft B at the rotating center of the compression roller; the worm wheel and the press roller are arranged oppositely, a gap is reserved between the worm wheel and the press roller, the worm wheel and the press roller are sleeved outside the left half section of the ejector rod through the gap, and threads meshed with the worm wheel are arranged outside the left half section of the ejector rod; two ends of the spring A respectively abut against the top of the spring cavity and the upper end face of the mounting seat on the upper side.
Preferably, the homogenizing driving mechanism is formed by connecting a homogenizing driving motor and a speed reducer.
Furthermore, in order to facilitate centralized control, the system also comprises a control box, wherein a speed sensor is arranged on the speed reducer, and the heat medium supply source and the liquid adding source are respectively a heat medium supply pump connected with the heat medium source and a liquid adding pump connected with the liquid source;
the control box is respectively connected with the bracket driving motor, the homogeneous driving motor, the rotating speed sensor, the heat medium supply pump, the liquid feeding pump and the waterproof motor.
Preferably, the number of the supporting steel frames is 3, and the supporting steel frames are uniformly distributed on the outer side of the mixing tank;
the wall thickness of the homogenizing and mixing bin body is 2 mm-50 mm;
the separating filter screen funnel is positioned at the position which is 25 mm-55 mm above the waist part of the homogeneous mixing cabin body;
the included angle between the liquid adding device and the horizontal direction is 10-32 degrees;
the funnel stirring blade consists of a circular ring sleeved outside the funnel rotating shaft and a radial connecting rod for connecting the circular ring and the funnel rotating shaft;
the thickness of the pore canal is 20 mm-30 mm
The secondary sedimentation chamber is a hollow sphere structure with the diameter of 10 cm-15 cm.
Further, in order to facilitate the detection homogeneity degree, still including setting up the homogeneity degree detector in the homogeneous mixing storehouse internal portion, the homogeneity degree detector is connected with the control box.
Furthermore, in order to improve the homogenizing effect, the number of the high-speed homogenizing wave wheels is 10, the adjacent high-speed homogenizing wave wheels are arranged at equal intervals, the interval is between 5mm and 12mm, and the appearance of the high-speed homogenizing wave wheels is in a ratchet shape.
Further, in order to improve the heat dissipation effect, the quantity of fin exhibition pole and hydro-cylinder fin is 6, and the material of hydro-cylinder fin is sheet metal stainless steel.
Further, the bottom of the tank body is in an inverted frustum shape.
Further, the distance between the two bracket gears is 15 cm-25 cm
Further, in order to obtain a high-speed homogeneous wave wheel with good homogeneity improving effect, the high-speed homogeneous wave wheel is made of high polymer materials, and comprises the following components in percentage by mass:
30-65% of methyl ester derivative, 25-60% of thiophosphate derivative, 1-5% of mixed auxiliary agent, 1-5% of cross-linking agent, 15-45% of O-ethyl O- (4-methylthiophenyl) S-propyl phosphorodithioate and 2-15% of (T-4) -bis (diethyl dithiocarbamate-S, S') zinc.
Further, in order to obtain a high-speed homogeneous impeller with good homogeneity improving effect, the preparation method of the high-speed homogeneous impeller comprises the following steps:
step 1: adding 22-32% of ultrapure water with the conductivity of 1.25 muS/cm-3.15 muS/cm into a reaction kettle, starting a stirrer in the reaction kettle at the rotating speed of 125-375 rpm, and starting a heating pump to raise the temperature in the reaction kettle to 75-185 ℃; sequentially adding 30-65% of methyl ester derivatives and 1-5% of mixed auxiliary agents, stirring until the methyl ester derivatives and the mixed auxiliary agents are completely dissolved, adjusting the pH value to 5.5-8.5, adding 25-60% of thiophosphate derivatives, and adjusting the rotation speed of a stirrer to 255-315 rpm at the temperature of 90-395 ℃;
step 2: adding 15-45% of O-ethyl O- (4-methylthiophenyl) S-propyl dithiophosphate and 2-15% of (T-4) -bis (diethyl dithiocarbamate-S, S') zinc, and uniformly mixing;
and 3, step 3: adding 1-5% of cross-linking agent, setting the rotation speed of a stirrer at 75-235 rpm and the temperature at 90-265 ℃, keeping the state for 5-25 hours, discharging, and putting into a molding press to obtain the high-speed homogeneous impeller.
According to the invention, the upper pressure sealing cover is controlled to open and close through the upper telescopic oil cylinder, so that the automation degree of the device can be improved, and the addition of nutritional components is facilitated. Waterproof motor passes through the operation of funnel gear drive funnel pivot, and then drives the rotation of funnel stirring leaf, reach the purpose to the even stirring of material, but also can make the liquid additive that adds and the nutrient solution component that blending tank upper end added carry out even mixture and stir in advance, a pair of homogeneity wheelset is high-speed relative motion by the drive of even actuating mechanism in the homogeneous system, can not only improve stirring effect, can promote the homogeneous mixing between additive and the nutrient solution component moreover. The support steel frame can control the height of the mixing tank relative to the support plane. The arrangement of the sedimentation treatment tank can facilitate the standing sedimentation of the indissolvable substances in the mixed solution, so as to facilitate the separation and discharge of the indissolvable substances. The setting of secondary treatment system can carry out the secondary to the discharged clear solution of sedimentation treatment pond outlet pipe way and deposit, and the setting of U type treatment pipeline can be discharged the precipitate into the secondary sedimentation chamber, and the clear solution is discharged by the one end of the vertical section of U type treatment pipeline, can effectively improve indissolvable material's precipitation effect, reaches the purpose of abundant sediment. The setting of dredge can dredge through the reciprocating motion of ejector pin and top in horizontal conveying line to prevent that horizontal conveying line from taking place the condition of blockking up. The ejector pin contraction driving device drives the worm wheel to rotate through the speed reduction driving motor, so that the ejector pin is driven to reciprocate left and right, the spring A can press the mounting seat elastically downwards, the ejector pin can be pressed by the pressing roller all the time, threads on the ejector pin can be effectively acted on by the worm wheel, and the purpose of stable driving is achieved. The device simple structure, stirring are efficient, and the homogeneity effect is ideal.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic structural view of a support steel frame according to the present invention;
FIG. 3 is a schematic view of the mixing tank of the present invention;
FIG. 4 is a schematic diagram of a separatory strainer funnel of the present invention;
FIG. 5 is a schematic view of the structure of the bearing shoe of the present invention;
FIG. 6 is a schematic diagram of the homogenization system of the present invention;
FIG. 7 is a schematic view showing the structure of a sedimentation treatment tank according to the present invention;
FIG. 8 is a schematic view of the structure of the secondary treatment system of the present invention;
FIG. 9 is a schematic structural view of the ejector pin retracting drive device of the present invention;
FIG. 10 is a graph showing the effect of O-ethyl O- (4-methylthiophenyl) S-propyl dithiophosphate on uniformity improvement rate in accordance with the present invention;
FIG. 11 is a schematic diagram showing the molecular structural features of the methyl ester derivatives according to the present invention;
FIG. 12 is a schematic representation of the molecular structural features of phosphorothioate derivatives of the present invention;
FIG. 13 is a schematic diagram showing the molecular structural characteristics of the oxysilane-based material according to the present invention.
In the figure: 1. the device comprises a supporting steel frame, 1-1 parts, a support driving motor, 1-2 parts, a transmission case, 1-3 parts, support ends, 1-4 parts, sliding rails, 1-5 parts, a continuous rack, 1-6 parts, support gears, 1-7 parts, an L-shaped support, 1-8 parts, a support, 1-9 parts, a vertical beam, 2 parts, a mixing tank, 2-1 parts, a homogeneous mixing bin body, 2-2 parts, a separating filter screen funnel, 2-2-1 parts, side wall openings, 2-2-2 parts, an outer gear ring, 2-2-3 parts, a funnel gear, 2-2-4 parts, a waterproof motor, 2-2-5 parts, a funnel stirring blade, 2-2-6 parts, a bearing base, 2-2-6-1 parts, a bearing accommodating groove, 2-2-6-2 parts, An annular cavity, 2-2-6-3 parts of a retaining bearing, 2-2-6-4 parts of a cooling liquid inlet pipeline, 2-2-6-4 parts of a cooling liquid outlet pipeline, 2-3 parts of a liquid adding pipeline, 2-4 parts of a homogenizing system, 2-4-1 parts of a homogenizing driving motor, 2-4-2 parts of a speed reducer, 2-4-3 parts of a homogenizing middle shaft, 2-4-4 parts of a closed thrust bearing, 2-4-5 parts of a high-speed homogenizing impeller, 2-5 parts of a homogeneity degree detector, 3 parts of an upper pressure sealing cover, 4 parts of an upper connecting crank arm, 5 parts of an upper telescopic oil cylinder, 6 parts of a liquid discharging pipeline, 7 parts of a sedimentation treatment tank, 7-1 parts of a bottom mud discharging pipeline, 7-2 parts of a mesh plate, 7-3 parts of a tank body, 7-5 parts of a tank body, A clear liquid area, 7-6 parts, a sludge accumulation area, 7-7 parts, a sedimentation treatment tank water inlet pipeline, 7-8 parts, a sedimentation treatment tank water outlet pipeline, 7-8-1 parts, a secondary sediment discharge pipeline, 7-8-2 parts, a secondary sedimentation chamber, 7-8-3 parts, a U-shaped treatment pipeline, 7-8-4 parts, a secondary treatment discharge pipeline, 7-8-5 parts, a horizontal conveying pipeline, 7-8-6 parts, a secondary treatment water inlet pipeline, 7-8-7 parts, a top head, 7-8-8 parts, a top rod, 7-8-9 parts, a top rod contraction driving device, 7-8-9-1 parts, a supporting shell, 7-8-9-2 parts, a mounting seat, 7-8-9-3 parts, a worm wheel, 7-8-9-4 parts, 7-8 parts and 7-8 parts, The device comprises a press roll, 7-8-9-5 parts, a sliding cavity, 7-8-9-6 parts, a spring cavity, 7-8-9-7 parts, springs A and 8, a control box, 9 parts, a radial connecting beam, 10 parts and a funnel rotating shaft.
Detailed Description
The present invention is further described below.
As shown in fig. 1 to 9, a nutrient solution mixing device for camptotheca acuminate planting comprises a mixing tank 2, a plurality of supporting steel frames 1 fixedly connected to the outer side of the lower part of the mixing tank 2, an upper connecting crank arm 4, an upper telescopic oil cylinder 5 and a sedimentation treatment tank 7;
the supporting steel frame 1 comprises supports 1-8, a pair of vertical beams 1-9 which are fixedly connected to the supports 1-8 in parallel, L-shaped supports 1-7 arranged on one sides of the pair of vertical beams 1-9 and support driving motors 1-1 arranged on one sides of the pair of vertical beams 1-9; a pair of vertical beams 1-9 are respectively provided with a longitudinally extending continuous rack 1-5 and a longitudinally extending slide rail 1-4 at the same side; the upper part and the lower part of the vertical section of the L-shaped bracket 1-7 corresponding to the position of the continuous rack 1-5 are respectively provided with a bracket gear 1-6, and the bracket gear 1-6 is rotatably connected to the vertical section of the L-shaped bracket 1-7 through a gear rotating shaft at the center of the bracket gear; a sliding groove is formed in the position, corresponding to the sliding rail 1-4, of the vertical section of the L-shaped support 1-7, the sliding groove is sleeved outside the sliding rail 1-4 in a sliding mode, and the support end 1-3 on the horizontal section of the L-shaped support 1-7 is fixedly connected with the outer side wall of the mixing tank 2; the support driving motor 1-1 is fixedly connected to one side of the L-shaped support 1-7, which is far away from the support gear 1-6, an output shaft of the support driving motor is connected with an input end of a transmission case 1-2 fixedly connected to one side of the L-shaped support 1-7, and an output end of the transmission case 1-2 is connected with gear rotating shafts of the two support gears 1-6;
an upper pressure sealing cover 3 for sealing the mixing tank 2 is arranged at the upper opening end of the mixing tank 2, and a liquid discharge pipeline 6 communicated with the inner cavity of the mixing tank 2 is fixedly connected at the bottom end of the mixing tank 2; one end of the upper connecting crank arm 4 is fixedly connected with the upper end face of the upper pressure sealing cover 3, and the other end of the upper connecting crank arm is hinged with a hinge seat fixedly connected to the outer side of the upper end of the mixing tank 2; one end of an upper telescopic oil cylinder 5 is hinged with the outer side of the hinged end of the upper connecting crank arm 4, and the other end of the upper telescopic oil cylinder is hinged with the middle part of the tank body of the mixing tank 2, so that the upper pressure sealing cover 3 is controlled to be closed or opened through telescopic action;
the mixing tank 2 comprises a homogeneous mixing cabin body 2-1 with a jacket structure, a jacket of the homogeneous mixing cabin body 2-1 is filled with a heat transfer medium, a heat medium pipeline communicated with the jacket space of the homogeneous mixing cabin body 2-1 is connected to the outside of the homogeneous mixing cabin body, and the other end of the heat medium pipeline is connected with a heat medium supply source;
a liquid adding pipeline 2-3 which is obliquely arranged, a separating screen funnel 2-2 which is horizontally placed and can rotate relative to the homogenizing mixing cabin body 2-1 and a homogenizing system 2-4 are sequentially arranged in the homogenizing mixing cabin body 2-1 from top to bottom, a plurality of side wall openings 2-2-1 are distributed on the side wall of the separating screen funnel 2-2, a plurality of small holes are distributed on the surface of the bottom plate of the separating screen funnel 2-2, the rotating center of the bottom plate is connected with a funnel rotating shaft 10 through a bearing bottom support 2-2-6 which is fixedly connected with the bottom plate, and the lower end of the funnel rotating shaft 10 in the separating screen funnel 2-2 is connected with a funnel stirring blade 2-2-5 which is in clearance fit with the inner part of the lower end of the homogenizing mixing cabin body 2-1; the funnel rotating shaft 10 is sleeved with an outer gear ring 2-2-2 at the upper end of the outer part of the separating filter screen funnel 2-2, and the outer gear ring 2-2-2 is fixedly connected with the funnel rotating shaft 10 through a radial connecting beam 9; a waterproof motor 2-2-4 is fixedly connected on the inner side wall of the homogeneous mixing cabin body 2-1 corresponding to the outer gear ring 2-2-2, a funnel gear 2-2-3 is assembled on an output shaft of the waterproof motor 2-2-4, and the funnel gear 2-2-3 is meshed with the outer gear ring 2-2-2; the liquid outlet end of the liquid adding pipeline 2-3 is positioned above the separating filter screen funnel 2-2, and the liquid inlet end thereof penetrates through the side wall of the homogeneous mixing cabin body 2-1 and then is connected with a liquid adding source;
a bearing accommodating groove 2-2-6-1 which is sunken downwards is formed in the center of the bearing bottom support 2-2-6, and an annular cavity 2-2-6-2 is formed in the bearing bottom support 2-2-6 in a manner of surrounding the bearing accommodating groove 2-2-6-1; a backstop bearing 2-2-6-3 is fixedly assembled in the bearing accommodating groove, and the inner ring of the backstop bearing 2-2-6-3 is fixedly connected with a funnel rotating shaft 10; the annular cavity 2-2-6-2 is respectively connected with a cooling liquid inlet pipeline 2-2-6-4 and a cooling liquid outlet pipeline 2-2-6-5 which are communicated with the inner cavity of the annular cavity, and the cooling liquid inlet pipeline 2-2-6-4 and the cooling liquid outlet pipeline 2-2-6-5 are respectively connected with a cooling source and a cooling liquid recovery box after radially penetrating through a separating screen funnel 2-2 and a homogenizing mixing cabin body 2-1;
the homogenizing system 2-4 comprises a pair of homogenizing middle shafts 2-4-3 arranged side by side, a pair of homogenizing middle shafts 2-4-3 are respectively sleeved with a pair of corresponding homogenizing impeller sets in the middle in a rotatable manner, each homogenizing impeller set consists of a plurality of high-speed homogenizing impellers 2-4-5, and the high-speed homogenizing impellers 2-4-5 in the pair of homogenizing impeller sets are meshed; the two opposite ends of the pair of homogeneous middle shafts 2-4-3 respectively penetrate out of the homogeneous mixing cabin body 2-1 in a rotatable way and then are respectively connected with the output parts of the homogeneous driving mechanisms fixedly connected with the two outer sides of the homogeneous mixing cabin body 2-1; the other end of the homogenizing middle shaft 2-4-3, which is far away from the driving mechanism, is rotatably connected with the inner side wall of the homogenizing mixing bin body 2-1 through a closed thrust bearing 2-4-4;
the sedimentation treatment tank 7 comprises a tank body 7-3 with an opening at the upper end, a screen plate 7-2 arranged inside the tank body 7-3, a tank body bracket 7-4 fixedly supported outside the tank body 7-3, a sedimentation treatment tank water inlet pipeline 7-7 fixedly connected to the upper end of the tank body 7-3, a bottom mud discharge pipeline 7-1 communicated with the bottom of an inner cavity of the tank body 7-3 and fixedly connected to the bottom end of the tank body 7-3, and a sedimentation treatment tank water outlet pipeline 7-8 communicated with the middle of the inner cavity of the tank body 7-3 and fixedly connected to one side of the tank body 7-3; a clear liquid zone 7-5 is formed in the middle of the inner part of the tank body 7-3, and a sludge accumulation zone 7-6 is formed at the bottom of the tank body 7-3; the liquid inlet end of the water inlet pipeline 7-7 of the sedimentation treatment tank is communicated with the liquid outlet end of the liquid discharge pipeline 6;
the water outlet end of the water outlet pipeline 7-8 of the sedimentation treatment tank is connected with a secondary treatment system, and the secondary treatment system comprises a secondary treatment water inlet pipeline 7-8-6 which is vertically arranged, a horizontal conveying pipeline 7-8-5 which is horizontally arranged and vertically communicated with the water outlet end of the secondary treatment water inlet pipeline 7-8-6, a U-shaped treatment pipeline 7-8-3 arranged at the lower part of the water outlet end of the horizontal conveying pipeline 7-8-5, a secondary sedimentation chamber 7-8-2 arranged at the lower part of the U-shaped treatment pipeline 7-8-3 and a secondary sediment discharge pipeline 7-8-1 communicated with the lower end of the secondary sedimentation chamber 7-8-2; the upper end of one vertical section in the U-shaped processing pipeline 7-8-3 is communicated with the water outlet end of the horizontal conveying pipeline 7-8-5, and the upper end of the other vertical section is provided with a secondary processing drainage pipeline 7-8-4.
The left side of the water inlet end of the horizontal conveying pipeline 7-8-5 is also provided with a dredger, the dredger comprises a top 7-8-7 which is arranged in the inner cavity of the horizontal conveying pipeline 7-8-5 and has an outer diameter smaller than the inner diameter of the horizontal conveying pipeline 7-8-5, a mandril 7-8-8 which is vertically connected to the center of the left end face of the top 7-8-7 and passes through the left end plate of the horizontal conveying pipeline 7-8-5 in a sliding and sealing manner, and a mandril contraction driving device 7-8-9 which is fixedly connected to the left side of the horizontal conveying pipeline 7-8-5; the ejector rod contraction driving device 7-8-9 comprises a supporting shell 7-8-9-1, a sliding cavity 7-8-9-5 which is arranged in the supporting shell 7-8-9-1 and penetrates through the left end and the right end of the supporting shell, two installation bases 7-8-9-2 which are arranged on the upper portion and the lower portion of the sliding cavity 7-8-9-5 in an opposite mode, a worm wheel 7-8-9-3 arranged in the installation base 7-8-9-2 on the lower side, a press roller 7-8-9-4 arranged in the installation base on the upper side, a spring cavity 7-8-9-6 which is arranged in the supporting shell 7-8-9-1 and located on the upper portion of the sliding cavity 7-8-9-5 and a spring A7-8-9-6 arranged in the spring cavity 7-8-9-6 -9-7; the upper mounting seat 7-8-9-2 is longitudinally slidably arranged in the sliding cavity 7-8-9-5, the lower mounting seat 7-8-9-2 is fixedly connected in the sliding cavity 7-8-9-5, the worm wheel is rotatably connected in the lower mounting seat 7-8-9-2 through a rotating shaft A at the rotating center of the worm wheel, and one end of the rotating shaft A rotatably penetrates through the supporting shell 7-8-9-1 and is connected with an output shaft of a speed reduction driving motor fixedly arranged outside the supporting shell 7-8-9-1; the compression roller 7-8-9-4 is rotatably connected in the upper mounting seat 7-8-9-2 through a rotating shaft B of a rotating center of the compression roller; the worm wheel 7-8-9-3 and the press roll 7-8-9-4 are oppositely arranged, a gap is reserved between the worm wheel 7-8-9-3 and the press roll 7-8-9-4, the left half section of the ejector rod 7-8-8 is sleeved with the outside of the left half section of the ejector rod 7-8-8 through the gap, and threads meshed with the worm wheel 7-8-9-3 are arranged on the outside of the left half section of the ejector rod 7-8-; the two ends of the spring A7-8-9-7 respectively abut against the top of the spring cavity 7-8-9-6 and the upper end surface of the mounting seat 7-8-9-2 at the upper side.
The homogenizing driving mechanism is formed by connecting a homogenizing driving motor 2-4-1 and a speed reducer 2-4-2.
The device also comprises a control box 8, wherein a rotating speed sensor is arranged on the speed reducer 2-4-2, and the heat medium supply source and the liquid adding source are respectively a heat medium supply pump connected with the heat medium source and a liquid adding pump connected with the liquid source;
the control box 8 is respectively connected with the bracket driving motor 1-1, the homogeneous driving motor 2-4-1, the rotating speed sensor, the heat medium supply pump, the liquid feeding pump and the waterproof motor 2-2-4.
The number of the supporting steel frames 1 is 3, and the supporting steel frames are uniformly distributed on the outer side of the mixing tank 2;
the wall thickness of the homogeneous mixing cabin body 2-1 is 2 mm-50 mm;
the separating filter screen funnel 2-2 is positioned at the position 25 mm-55 mm above the waist part of the homogeneous mixing cabin body 2-1;
the included angle between the liquid adding device 2-3 and the horizontal direction is 10-32 degrees;
the funnel stirring blade 2-2-5 consists of a circular ring sleeved outside the funnel rotating shaft 10 and a radial connecting rod for connecting the circular ring and the funnel rotating shaft 10;
the thickness of the pore canal 2-2-1-1 is 20 mm-30 mm;
the secondary sedimentation chamber 7-8-2 is a hollow sphere structure with the diameter of 10 cm-15 cm.
The homogenizing degree detector 2-5 is arranged inside the homogenizing mixing cabin body 2-1, and the homogenizing degree detector 2-5 is connected with the control box 8.
The number of the high-speed homogenizing wave wheels 2-4-5 is 10, the adjacent high-speed homogenizing wave wheels 2-4-5 are arranged at equal intervals, the distance is 5 mm-12 mm, and the shape of the high-speed homogenizing wave wheels 2-4-5 is ratchet-shaped.
The bottom of the tank body 7-3 is in an inverted frustum shape.
The distance between the two bracket gears 1-6 is 15 cm-25 cm.
The high-speed homogeneous impeller 2-4-5 is made of high polymer materials and comprises the following components in percentage by mass:
30-65% of methyl ester derivative, 25-60% of thiophosphate derivative, 1-5% of mixed auxiliary agent, 1-5% of cross-linking agent, 15-45% of O-ethyl O- (4-methylthiophenyl) S-propyl phosphorodithioate and 2-15% of (T-4) -bis (diethyl dithiocarbamate-S, S') zinc.
The cross-linking agent is any one of sodium diisopropyl dithiophosphate, isoamyl and isopropyl) zinc dithiophosphate and tetraphenyl (bisphenol-A) diphosphate.
The molecular structure of the methyl ester derivative is characterized as shown in figure 11, wherein R is alkyl with 1-8 carbon atoms.
The molecular structure of the phosphorothioate derivative is characterized as shown in FIG. 12, and the molecular formula is as follows: C10H15O3PS 2; molecular weight: 278.343.
the mixing auxiliary agent is an oxysilane substance, the molecular structural formula of the mixing auxiliary agent is shown in figure 13, and the molecular formula of the molecular structure is as follows: C16H20O2 Si.
The preparation method of the high-speed homogeneous impeller 2-4-5 comprises the following steps:
step 1: adding 22-32% of ultrapure water with the conductivity of 1.25 muS/cm-3.15 muS/cm into a reaction kettle, starting a stirrer in the reaction kettle at the rotating speed of 125-375 rpm, and starting a heating pump to raise the temperature in the reaction kettle to 75-185 ℃; sequentially adding 30-65% of methyl ester derivatives and 1-5% of mixed auxiliary agents, stirring until the methyl ester derivatives and the mixed auxiliary agents are completely dissolved, adjusting the pH value to 5.5-8.5, adding 25-60% of thiophosphate derivatives, and adjusting the rotation speed of a stirrer to 255-315 rpm at the temperature of 90-395 ℃;
step 2: adding 15-45% of O-ethyl O- (4-methylthiophenyl) S-propyl dithiophosphate and 2-15% of (T-4) -bis (diethyl dithiocarbamate-S, S') zinc, and uniformly mixing;
and 3, step 3: adding 1-5% of cross-linking agent, stirring at 75-235 rpm and 90-265 deg.C, holding the state for 5-25 hr, discharging, and molding to obtain the high-speed homogeneous impeller 2-4-5.
The following examples further illustrate the content of the present invention, which is an important component of the present invention as the high-speed homogeneous pulsator 2-4-5, because of its existence, the service life of the whole apparatus is increased, and it plays a key role in the safe and smooth operation of the whole apparatus. To this end, the following examples further demonstrate that the components of the present invention exhibit physical characteristics that are higher than those of other related patents.
Example 1
The high-speed homogeneous impeller 2-4-5 is manufactured according to the following steps, and comprises the following components by mass percent:
step 1: adding 22% of ultrapure water with the conductivity of 1.25 muS/cm into the reaction kettle, starting a stirrer in the reaction kettle at the rotating speed of 125rpm, and starting a heating pump to raise the temperature in the reaction kettle to 75 ℃; sequentially adding 30% of methyl ester derivative and 1% of mixed auxiliary agent, stirring until the methyl ester derivative and the mixed auxiliary agent are completely dissolved, adjusting the pH value to 5.5, adding 25% of thiophosphate derivative, and adjusting the rotation speed of a stirrer to 255rpm at the temperature of 90 ℃;
step 2: adding 15-45% of O-ethyl O- (4-methylthiophenyl) S-propyl dithiophosphate and 2% of (T-4) -bis (diethyl dithiocarbamate-S, S') zinc, and uniformly mixing;
and 3, step 3: adding cross-linking agent 1%, stirring at 75rpm and 90 deg.C, holding the state for 5 hr, discharging, and molding to obtain high-speed homogeneous impeller 2-4-5.
Example 2
The high-speed homogeneous impeller 2-4-5 is manufactured according to the following steps, and comprises the following components by mass percent:
step 1: adding 32% of ultrapure water with the conductivity of 3.15 mu S/cm into the reaction kettle, starting a stirrer in the reaction kettle at the rotating speed of 375rpm, and starting a heating pump to raise the temperature in the reaction kettle to 185 ℃; sequentially adding 65% of methyl ester derivative and 5% of mixed auxiliary agent, stirring until the methyl ester derivative and the mixed auxiliary agent are completely dissolved, adjusting the pH value to 8.5, adding 60% of thiophosphate derivative, and adjusting the rotation speed of a stirrer to 315rpm at 395 ℃;
step 2: adding 45% of O-ethyl O- (4-methylthiophenyl) S-propyl dithiophosphate and 15% of (T-4) -bis (diethyl dithiocarbamate-S, S') zinc, and uniformly mixing;
and 3, step 3: adding cross-linking agent 5%, stirring at 235rpm and 265 deg.C, holding the state for 25 hr, discharging, and molding to obtain high-speed homogeneous impeller 2-4-5.
Example 3
The high-speed homogeneous impeller 2-4-5 is manufactured according to the following steps, and comprises the following components by mass percent:
step 1: adding 29 percent of ultrapure water with the conductivity of 1.315 mu S/cm into a reaction kettle, starting a stirrer in the reaction kettle at the rotating speed of 178rpm, and starting a heating pump to raise the temperature in the reaction kettle to 85 ℃; sequentially adding 39% of methyl ester derivative and 4% of mixed auxiliary agent, stirring until the methyl ester derivative and the mixed auxiliary agent are completely dissolved, adjusting the pH value to 5.8, adding 40% of thiophosphate derivative, and adjusting the rotation speed of a stirrer to 300rpm at the temperature of 90 ℃;
step 2: adding 40% of O-ethyl O- (4-methylthiophenyl) S-propyl dithiophosphate and 10% of (T-4) -bis (diethyl dithiocarbamate-S, S') zinc, and uniformly mixing;
and 3, step 3: adding 3% cross-linking agent, stirring at 90rpm and 91 deg.C, holding the state for 8 hr, discharging, and molding to obtain high-speed homogeneous impeller 2-4-5.
Comparative example
The comparison example is the use condition of a high-speed homogenizing impeller of a certain brand sold in the market in the oil product mixing and sorting process.
The high-speed homogeneous wave wheel 2-4-5 prepared in the embodiment 1-3 and the high-speed homogeneous wave wheel described in the comparative example are used for comparing the use conditions of the oil product mixing process, and the volume resistivity, the oil separation degree, the viscosity reduction rate and the mixing uniformity improvement rate are taken as technical indexes for statistics, and the results are shown in table 1:
table 1 shows the comparison results of various parameters of the high-speed homogenizing impeller described in examples 1 to 3 and the comparative example when used in the oil product mixing process, and it can be seen from table 1 that the volume resistivity, the oil separation degree, the viscosity reduction rate, and the mixing uniformity improvement rate of the high-speed homogenizing impeller 2-4-5 of the present invention are all higher than those of the products produced by the prior art.
Further, as shown in FIG. 9, there is a graph showing the influence of the O-ethyl O- (4-methylthiophenyl) S-propyl dithiophosphate on the uniformity improvement rate. As seen in the figure, the doping amount of the high-speed homogeneous impeller 2-4-5 material is important for improving the product performance, and the doping amount is greatly superior to that of the existing product in the aspect of uniformity improvement rate.
The working method of the device comprises the following steps:
step 1: the material to be processed enters the mixing tank 2 through a guide pipe, the upper pressure sealing cover 3 slowly descends through being connected with the crank arm 4 under the action of the upper telescopic oil cylinder 5 and is fitted with the mixing tank 2 to realize sealing;
step 2: when the support dispatching needs to be adjusted, three support driving motors 1-1 in the three support steel frames 1 are controlled to synchronously operate, and the transmission boxes 1-2 are driven to operate; the transmission case 1-2 simultaneously drives the support gear 1-6 to rotate in the same direction, so that the support gear 1-6 drives the L-shaped support 1-7 to ascend and descend, and the sliding groove arranged at the vertical section of the L-shaped support 1-7 is sleeved outside the sliding rail 1-4 in a sliding manner, so that the L-shaped support 1-7 can be ensured not to be separated from the vertical beam 1-9 in the ascending or descending process; when the bracket gear 1-6 rotates anticlockwise, the L-shaped bracket 1-7 is in a rising state; when the support gear 1-6 rotates clockwise, the L-shaped support 1-7 is in a descending state;
and 3, step 3: in the mixing tank 2, a material to be treated enters the separating screen funnel 2-2 through the liquid adding pipeline 2-3, the liquid adding pipeline 2-3 is obliquely arranged, the entered material acts on the separating screen funnel 2-2, the separating screen funnel 2-2 rotates while performing filtering operation, and the rotating separating screen funnel 2-2 performs filtering, so that the filtering effect is better; the two homogenizing driving mechanisms drive the two pairs of homogenizing impeller groups to move oppositely, and the high-speed homogenizing impellers in the pair of homogenizing impeller groups are meshed, so that the material can achieve a homogenizing effect and further enter the lower part of the homogenizing mixing bin body 2-1; the homogeneity degree detector 2-5 carries out induction reaction on the homogeneity degree of the material entering the lower part of the homogeneous mixing bin body 2-1 and detects the homogeneity degree; when the homogeneity degree does not meet the detection standard, the homogeneity degree detector 2-5 sends an electric signal to the control box 8, and the controller 8 gives an alarm through an alarm connected with the controller.
And 4, step 4: in the separating filter screen funnel 2-2, the waterproof motor 2-2-4 is switched on and then operates to drive the funnel gear 2-2-3 to rotate, and then the funnel gear 2-2-3 drives the funnel rotating shaft 10 to operate to drive the funnel stirring blade 2-2-5 to rotate, so that the materials are uniformly stirred; after being stirred, the materials flow out of the bottom plate and the side wall opening 2-2-1 of the separating filter screen funnel 2-2;
and 5, step 5: in the sedimentation treatment tank 7, the mixed liquid enters a clear liquid zone 7-5 through a sedimentation treatment tank water inlet pipeline 7-7; under the action of the screen plate 7-2, filtering floating objects in the mixed solution; meanwhile, the solid in the mixed solution is settled to a sludge accumulation area 7-6 and discharged from a bottom sludge discharge pipeline 7-1, and the residual clear water flows out from a water outlet pipeline 7-8 of the sedimentation treatment tank;
and 6, step 6: in the bearing bottom support 2-2-6, cooling liquid enters from a cooling liquid inlet pipeline 2-2-6-4 and flows into the annular cavity 2-2-6-2 through a cooling liquid outlet pipeline 2-2-6-4, and then is discharged from the cooling liquid outlet pipeline 2-2-6-4; and cooling the stop bearing 2-2-6-3.
Claims (7)
1. A nutrient solution mixing device used in camptotheca acuminata planting comprises a mixing tank (2) and a plurality of supporting steel frames (1) fixedly connected to the outer side of the lower part of the mixing tank (2), and is characterized by further comprising an upper connecting crank arm (4), an upper telescopic oil cylinder (5) and a sedimentation treatment tank (7);
the supporting steel frame (1) comprises supports (1-8), a pair of vertical beams (1-9) which are fixedly connected to the supports (1-8) in parallel, L-shaped supports (1-7) arranged on one sides of the vertical beams (1-9) and support driving motors (1-1) arranged on one sides of the vertical beams (1-9); a pair of vertical beams (1-9) are respectively provided with a longitudinally extending continuous rack (1-5) and a longitudinally extending slide rail (1-4) at the same side; the upper part and the lower part of the vertical section of the L-shaped bracket (1-7) corresponding to the position of the continuous rack (1-5) are respectively provided with a bracket gear (1-6), and the bracket gear (1-6) is rotatably connected to the vertical section of the L-shaped bracket (1-7) through a gear rotating shaft at the center of the bracket gear; a chute is formed in the position, corresponding to the sliding rail (1-4), of the vertical section of the L-shaped support (1-7), the chute is sleeved outside the sliding rail (1-4) in a sliding mode, and a support end (1-3) on the horizontal section of the L-shaped support (1-7) is fixedly connected with the outer side wall of the mixing tank (2); the support driving motor (1-1) is fixedly connected to one side of the L-shaped support (1-7) departing from the support gears (1-6), an output shaft of the support driving motor is connected with an input end of a transmission case (1-2) fixedly connected to one side of the L-shaped support (1-7), and an output end of the transmission case (1-2) is connected with gear rotating shafts of the two support gears (1-6);
an upper pressure sealing cover (3) for sealing the mixing tank (2) is arranged at the upper opening end of the mixing tank (2), and a liquid discharge pipeline (6) communicated with the inner cavity of the mixing tank (2) is fixedly connected at the bottom end of the mixing tank; one end of the upper connecting crank arm (4) is fixedly connected with the upper end face of the upper pressure sealing cover (3), and the other end of the upper connecting crank arm is hinged with a hinge seat fixedly connected to the outer side of the upper end of the mixing tank (2); one end of the upper telescopic oil cylinder (5) is hinged with the outer side of the hinged end of the upper connecting crank arm (4), and the other end of the upper telescopic oil cylinder is hinged with the middle part of the tank body of the mixing tank (2) so as to control the covering or the opening of the upper pressure sealing cover (3) through telescopic action;
the mixing tank (2) comprises a homogeneous mixing cabin body (2-1) with a jacket structure, a jacket of the homogeneous mixing cabin body (2-1) is filled with heat transfer media, the outside of the homogeneous mixing cabin body (2-1) is connected with a heat medium pipeline communicated with the jacket space of the homogeneous mixing cabin body, and the other end of the heat medium pipeline is connected with a heat medium supply source;
a liquid adding pipeline (2-3) which is obliquely arranged, a separating screen funnel (2-2) which is horizontally placed and can rotate relative to the homogenizing mixing cabin body (2-1) and a homogenizing system (2-4) are sequentially arranged in the homogenizing mixing cabin body (2-1) from top to bottom, a plurality of side wall open pores (2-2-1) are arranged on the side wall of the separating screen funnel (2-2) all over, a plurality of small holes are arranged on the bottom plate of the separating screen funnel (2-2) all over the surface of the separating screen funnel, the rotating center of the bottom plate is connected with a funnel rotating shaft (10) through a bearing bottom support (2-2-6) fixedly connected with the bottom plate, and the lower end of the funnel rotating shaft (10) in the separating screen funnel (2-2) is connected with a funnel stirring blade (2-2-5) in clearance fit with the inner part of the lower end of the homogenizing and mixing bin body (2-1); an outer gear ring (2-2-2) is sleeved at the upper end of the funnel rotating shaft (10) outside the separating filter screen funnel (2-2), and the outer gear ring (2-2-2) is fixedly connected with the funnel rotating shaft (10) through a radial connecting beam (9); a waterproof motor (2-2-4) is fixedly connected to the inner side wall of the homogeneous mixing cabin body (2-1) corresponding to the outer gear ring (2-2-2), a funnel gear (2-2-3) is assembled on an output shaft of the waterproof motor (2-2-4), and the funnel gear (2-2-3) is meshed with the outer gear ring (2-2-2); the liquid outlet end of the liquid adding pipeline (2-3) is positioned above the separating filter screen funnel (2-2), and the liquid inlet end of the liquid adding pipeline penetrates through the side wall of the homogenizing and mixing cabin body (2-1) and then is connected with a liquid adding source;
a bearing accommodating groove (2-2-6-1) which is sunken downwards is formed in the center of the bearing bottom support (2-2-6), and an annular cavity (2-2-6-2) is formed in the bearing bottom support (2-2-6) in a manner of surrounding the bearing accommodating groove (2-2-6-1); a retaining bearing (2-2-6-3) is fixedly assembled in the bearing accommodating groove, and the inner ring of the retaining bearing (2-2-6-3) is fixedly connected with the funnel rotating shaft (10); the annular cavity (2-2-6-2) is respectively connected with a cooling liquid inlet pipeline (2-2-6-4) and a cooling liquid outlet pipeline (2-2-6-5) which are communicated with the inner cavity of the annular cavity, and the cooling liquid inlet pipeline (2-2-6-4) and the cooling liquid outlet pipeline (2-2-6-5) are respectively connected with a cooling source and a cooling liquid recovery box after radially penetrating through the separating screen funnel (2-2) and the homogeneous mixing bin body (2-1);
the homogenizing system (2-4) comprises a pair of homogenizing middle shafts (2-4-3) which are arranged side by side, and a pair of corresponding homogenizing impeller sets are respectively and rotatably sleeved at the middle parts of the pair of homogenizing middle shafts (2-4-3), each homogenizing impeller set consists of a plurality of high-speed homogenizing impellers (2-4-5), and the high-speed homogenizing impellers (2-4-5) in the pair of homogenizing impeller sets are meshed; the two opposite ends of the pair of homogeneous middle shafts (2-4-3) respectively penetrate out of the homogeneous mixing cabin body (2-1) in a rotatable way and then are respectively connected with the output parts of the homogeneous driving mechanisms fixedly connected with the two sides outside the homogeneous mixing cabin body (2-1); the other end of the homogenizing middle shaft (2-4-3) far away from the driving mechanism is rotationally connected with the inner side wall of the homogenizing mixing cabin body (2-1) through a closed thrust bearing (2-4-4);
the sedimentation treatment tank (7) comprises a tank body (7-3) with an opening at the upper end, a screen plate (7-2) arranged inside the tank body (7-3), a tank body bracket (7-4) fixedly supported outside the tank body (7-3), a sedimentation treatment tank water inlet pipeline (7-7) fixedly connected to the upper end of the tank body (7-3), a bottom sludge discharge pipeline (7-1) communicated with the bottom of an inner cavity of the tank body (7-3) and fixedly connected to the bottom end of the tank body (7-3), and a sedimentation treatment tank water outlet pipeline (7-8) communicated with the middle of the inner cavity of the tank body (7-3) and fixedly connected to one side of the tank body (7-3); a clear liquid zone (7-5) is formed in the middle of the inner part of the tank body (7-3), and a sludge accumulation zone (7-6) is formed at the bottom of the inner part of the tank body (7-3); the liquid inlet end of the water inlet pipeline (7-7) of the sedimentation treatment tank is communicated with the liquid outlet end of the liquid discharge pipeline (6);
the water outlet end of the water outlet pipeline (7-8) of the sedimentation treatment tank is connected with a secondary treatment system, and the secondary treatment system comprises a secondary treatment water inlet pipeline (7-8-6) which is vertically arranged, a horizontal conveying pipeline (7-8-5) which is horizontally arranged and vertically communicated with the water outlet end of the secondary treatment water inlet pipeline (7-8-6), a U-shaped treatment pipeline (7-8-3) arranged at the lower part of the water outlet end of the horizontal conveying pipeline (7-8-5), a secondary sedimentation chamber (7-8-2) arranged at the lower part of the U-shaped treatment pipeline (7-8-3) and a secondary sediment discharge pipeline (7-8-1) communicated with the lower end of the secondary sedimentation chamber (7-8-2); the upper end of one vertical section in the U-shaped treatment pipeline (7-8-3) is communicated with the water outlet end of the horizontal conveying pipeline (7-8-5), and the upper end of the other vertical section is provided with a secondary treatment drainage pipeline (7-8-4);
the left side of the water inlet end of the horizontal conveying pipeline (7-8-5) is also provided with a dredger, the dredger comprises a top head (7-8-7) which is arranged in the inner cavity of the horizontal conveying pipeline (7-8-5) and has an outer diameter smaller than the inner diameter of the horizontal conveying pipeline (7-8-5), a top rod (7-8-8) which is vertically connected to the center of the left end face of the top head (7-8-7) and passes through the left end plate of the horizontal conveying pipeline (7-8-5) in a sliding and sealing manner, and a top rod contraction driving device (7-8-9) which is fixedly connected to the left side of the horizontal conveying pipeline (7-8-5);
the ejector rod contraction driving device (7-8-9) comprises a supporting shell (7-8-9-1), a sliding cavity (7-8-9-5) which is arranged in the supporting shell (7-8-9-1) and penetrates through the left end and the right end of the supporting shell, two installation bases (7-8-9-2) which are arranged at the upper part and the lower part of the sliding cavity (7-8-9-5) in a mutually opposite mode, a worm wheel (7-8-9-3) arranged in the installation base (7-8-9-2) at the lower side, a compression roller (7-8-9-4) arranged in the installation base at the upper side, a spring cavity (7-8-9-6) which is arranged in the supporting shell (7-8-9-1) and is positioned at the upper part of the sliding cavity (7-8-9-5), and a spring installed in the spring cavity A spring A (7-8-9-7) in the cavity (7-8-9-6); the upper mounting seat (7-8-9-2) is longitudinally slidably arranged in the sliding cavity (7-8-9-5), the lower mounting seat (7-8-9-2) is fixedly connected in the sliding cavity (7-8-9-5), the worm wheel is rotatably connected in the lower mounting seat (7-8-9-2) through a rotating shaft A at the rotating center of the worm wheel, and one end of the rotating shaft A rotatably penetrates through the supporting shell (7-8-9-1) and is connected with an output shaft of a speed reduction driving motor fixedly arranged outside the supporting shell (7-8-9-1); the compression roller (7-8-9-4) is rotatably connected in the upper mounting seat (7-8-9-2) through a rotating shaft B of a rotating center of the compression roller; the worm wheel (7-8-9-3) and the press roll (7-8-9-4) are arranged oppositely, a gap is reserved between the worm wheel and the press roll and is sleeved outside the left half section of the ejector rod (7-8-8) through the gap, and the outside of the left half section of the ejector rod (7-8-8) is provided with a thread meshed with the worm wheel (7-8-9-3); two ends of the spring A (7-8-9-7) respectively abut against the top of the spring cavity (7-8-9-6) and the upper end surface of the mounting seat (7-8-9-2) at the upper side.
2. The device for mixing nutrient solution for planting camptotheca acuminata according to claim 1, wherein the homogenizing driving mechanism is formed by connecting a homogenizing driving motor (2-4-1) and a speed reducer (2-4-2).
3. The nutrient solution mixing device for planting the camptotheca acuminata according to claim 1 or 2, further comprising a control box (8), wherein a speed sensor is arranged on the speed reducer (2-4-2), and the heat medium supply source and the liquid adding source are respectively a heat medium supply pump connected with the heat medium source and a liquid adding pump connected with the liquid source;
the control box (8) is respectively connected with the bracket driving motor (1-1), the homogeneous driving motor (2-4-1), the rotating speed sensor, the heat medium supply pump, the liquid feeding pump and the waterproof motor (2-2-4).
4. The nutrient solution mixing device for planting camptotheca acuminata according to claim 3, further comprising a homogeneity degree detector (2-5) arranged inside the homogeneity mixing cabin (2-1), wherein the homogeneity degree detector (2-5) is connected with the control box (8).
5. The nutrient solution mixing device for planting camptotheca acuminate according to claim 4, wherein the number of the high speed homogenizing wave wheels (2-4-5) is 10, the high speed homogenizing wave wheels (2-4-5) are arranged at equal intervals, the interval is 5 mm-12 mm, and the high speed homogenizing wave wheels (2-4-5) are ratchet-shaped.
6. The nutrient solution mixing device for planting camptotheca acuminata according to claim 5, wherein the bottom of the tank body (7-3) is in an inverted frustum shape.
7. The mixing device of nutrient solution for planting camptotheca acuminata according to claim 6, wherein the distance between two rack gears (1-6) is 15 cm-25 cm.
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| CN112295489B (en) * | 2020-10-23 | 2022-07-26 | 佛山市顺德区安木森新材料有限公司 | Pre-material mixing process system for dispersing water-based paint |
| CN118045551B (en) * | 2024-04-16 | 2024-06-21 | 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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