CN108816128A - One kind injecting mixing arrangement for surface water runoff purifying plant cultivation block medicament - Google Patents

Abstract

Disclosure of the invention is a kind of to inject mixing arrangement for surface water runoff purifying plant cultivation block medicament.Medicament inlet positioned at one end, medicament inlet right side are equipped with diluent and enter pipe, and diluent enters pipe one end and is connected to external diluent bottle, and it is open that diluent, which enters the pipe other end, and is inserted into inside diffusion horn mouth；The stable net is located on the right side of agitation ball, and stablizing net is holey, vertical display；Medicament enters from medicament inlet, and the diluent for entering pipe ejection with diluent meets, and under the action of decentralized network, diffusion horn mouth, diluent is further dispersed and is mixed with medicament；Diffusant enters pipe by diffusant and sprays from diffusant jet pipe, and buffer subsystem implements buffering to the diffusant of ejection, and in the case where stirring ball agitaion, diffusant, diluent, medicament are sufficiently mixed, and mixture is discharged from agent outlet.The device intelligence degree is high, and stability is high, small to workpiece impact force, guarantees that workpiece is not damaged, high yield rate.

Description

One kind injecting mixing arrangement for surface water runoff purifying plant cultivation block medicament

Technical field

The invention belongs to plant cultivation equipment manufacturing fields, and in particular to one kind is cultivated for surface water runoff purifying plant Block medicament injects mixing arrangement.

Background technique

Agent mixer is mixed for two or more different agents, and confection is then reused, But existing most agent mixer only has two medicaments input port, it, will two kinds of medicament investments when various medicaments mix Afterwards, then other two kinds of medicaments are put into, needs repeatedly to put into, leads to operating personnel's heavy workload, mixing efficiency is low, repeatedly puts into It is poor to will lead to mixed effect, existing agent mixer is unable to control medical fluid and flows to speed in confection, will cause mixing Not exclusively, mixed effect is poor, and for existing agent mixer in confection, incorporation time is short, causes mixed effect poor, mixing Not exclusively.

Summary of the invention

In order to solve the above technical problem, the present invention provides one kind for surface water runoff purifying plant cultivation block medicament note Enter mixing arrangement, including：Shock-absorbing foot pad 1, fixed frame 2, pushing mechanism 3, work piece holder 4, support platform 5, control system 6, Rolling cutter 7；The fixed frame 2 is stainless steel rectangular structure, and thickness is between 3cm~4cm；The number of shock-absorbing foot pad 1 Amount is four, is respectively and fixedly installed to 2 bottom four corners of fixed frame；The support platform 5 is rectangle galvanized sheet, support platform 5 It is fixedly mounted on 2 top of fixed frame；The pushing mechanism 3 is arranged in 5 side of support platform；The work piece holder 4 is arranged in 5 other side of support platform；The control system 6 is fixedly mounted on fixed frame 2；The rolling cutter 7 is located at pushing mechanism 3 Left side, the two connection.

Further, the pushing mechanism 3 includes：Slideway fixed block 3-1, slideway 3-2, sliding block 3-3, speed regulating motor 3-4, Fuel tank 3-5, hydraulic cylinder 3-6 push disk 3-7, slide motor 3-8, push disk brake apparatus 3-9；Wherein, the slideway 3-2 is logical Slideway fixed block 3-1 is crossed to be fixedly connected with support platform 5；The cross section the slideway 3-2 is in " Ω " shape, and slideway 3-2 quantity is 2 It is a；The sliding block 3-3 and slideway 3-2 is slidably connected, and the end sliding block 3-3 is provided with slide motor 3-8, slide motor 3-8 driving Sliding block 3-3 is slided on slideway 3-2；The speed regulating motor 3-4 is variable-frequency motor, and speed regulating motor 3-4 pedestal and sliding block 3-3 are welded It is fixed；Described one end speed regulating motor transmission shaft 3-10 is connect with speed regulating motor 3-4, and the other end passes through fuel tank 3-5, pushes disk braking Device 3-9, hydraulic cylinder 3-6 are fixedly connected with disk 3-7 is pushed, and speed regulating motor 3-4, which drives, pushes disk 3-7 rotation；The fuel tank 3-5 It is connected to the one end hydraulic cylinder 3-6 conduit；The hydraulic cylinder 3-6 other end pushes disk 3-7 to connect with detachable；The promotion disk system Dynamic device 3-9, which is located at, pushes disk 3-7 and hydraulic cylinder 3-6 between the two；The speed regulating motor 3-4, hydraulic cylinder 3-6, disk 3-7 is pushed Central axis in the same horizontal line, pushes disk 3-7 to connect with rolling cutter 7, pushes disk 3-7 that rolling cutter 7 is driven to rotate；Institute State speed regulating motor 3-4, hydraulic cylinder 3-6 passes through conducting wire respectively and the control of control system 6 connects；The slide motor 3-8 is by leading Line and the control of control system 6 connect.

Further, the rolling cutter 7 includes：Driven wheel 7-1, transformer 7-2, cutting edge 7-3, back-up roller bearing 7- 4, heating tube 7-5, cutting edge spray head 7-6, water inlet pipe 7-7, intake port 7-8, transmission shaft 7-9；Driven wheel 7- positioned at one end 1, it is connect with external cutter motor, meanwhile, driven wheel 7-1 is fixedly connected with transmission shaft 7-9；It is set on the inside of driven wheel 7-1 There is back-up roller bearing 7-4, the back-up roller bearing 7-4 quantity is 2, is located at the both ends of transmission shaft 7-9；The transmission shaft 7-9 hollow structure, inside are equipped with transformer 7-2, heating tube 7-5, water inlet pipe 7-7；Water inlet pipe 7-7 is parallel to transmission shaft 7-9, into The quantity of water pipe 7-7 is 3, and water inlet pipe 7-7 is connected to water inlet port 7-8, and water inlet port 7-8 is connected to external pump；Water inlet The periphery pipe 7-7 is equipped with heating tube 7-5, heating tube 7-5 helical structure, and the one end heating tube 7-5 is connected by conducting wire and transformer 7-2 Logical, the other end of transformer 7-2 is electrically connected by conducting wire with external city, and heating tube 7-5 implements to heat to water inlet pipe 7-7, transformation Device 7-2 implements to adjust to heating temperature；Cutting edge 7-3 is equipped with outside transmission shaft 7-9, cutting edge 7-3 quantity is 4, and 4 are cut Blade 7-3 is angularly, mode substantially symmetrical about its central axis is fixed on transmission shaft 7-9；Cutting edge spray head 7- is equipped in the root cutting edge 7-3 6, cutting edge spray head 7-6 open at one end designs and is directed toward cutting edge 7-3 knife face, the cutting edge spray head 7-6 other end and water inlet pipe 7-7 Connection；Driven wheel 7-1 drives cutting edge 7-3 rotation by transmission shaft 7-9, and cutting edge 7-3 implements equidistant cutting to material；Together When, cutting edge spray head 7-6 implements to clean to cutting edge 7-3 knife face.

Further, slideway 3-2 is equipped with cooling device, and cooling device includes：By coolant liquid entrance 3-2-1, heat-exchange tube 3-2-2, heat-exchanging chamber 3-2-3, partition 3-2-4, buffered room 3-2-5, refrigerant inlet 3-2-6 export 3-2- by coolant liquid 7, medicament mixing device 3-2-8, refrigerant exit 3-2-9；Positioned at side by coolant liquid entrance 3-2-1 and heat-exchanging chamber 3-2-3 Connection, and the lower part heat-exchanging chamber 3-2-3, low level are located at by coolant liquid entrance 3-2-1；It is described to be located at by coolant liquid outlet 3-2-7 The top heat-exchanging chamber 3-2-3, a high position, and be connected to by coolant liquid outlet 3-2-7 with heat-exchanging chamber 3-2-3；The heat-exchange tube 3- 2-2 is located in the middle part of heat-exchanging chamber 3-2-3, heat-exchange tube 3-2-2 hollow structure, and the quantity of heat-exchange tube 3-2-2 is 20, more The vertical equidistant arrangement of heat-exchange tube 3-2-2；The both ends heat-exchange tube 3-2-2 are respectively equipped with buffered room 3-2-5, heat-exchange tube 3- The both ends 2-2 are connected to the buffered room 3-2-5 for being located at its upper and lower ends respectively；The heat-exchanging chamber 3-2-3 passes through partition 3- The 2-4 and buffered room 3-2-5 of upper and lower ends separates；Superposed buffered room 3-2-5, top enter equipped with refrigerant Mouthful 3-2-6, the buffered room 3-2-5 on top are connected to refrigerant inlet 3-2-6, positioned at the buffered room 3-2-5 of lower part its Bottom is equipped with refrigerant exit 3-2-9, and the buffered room 3-2-5 of lower part is connected to the refrigerant exit 3-2-9 of bottom；The medicament Mixing arrangement 3-2-8 is connected to heat-exchanging chamber 3-2-3；Refrigerant enters buffered room 3-2-5 from refrigerant inlet 3-2-6, in turn It enters inside heat-exchange tube 3-2-2, is flowed by heat absorption caused by heat-exchange tube 3-2-2, and from refrigerant exit 3-2-9 Out；Heat-exchanging chamber 3-2-3 is entered from by coolant liquid entrance 3-2-1 by coolant liquid, transfers heat to heat-exchange tube 3-2-2, and From by coolant liquid outlet 3-2-7 outflow；Meanwhile external agent is controllably added to heat exchange by medicament mixing device 3-2-8 Inside the 3-2-3 of room, reacted with by coolant liquid.

Further, the medicament mixing device 3-2-8 is L-type pipe structure, both ends perforation, medicament mixing device 3-2-8 Including：Medicament inlet 3-2-8-1, diffusant jet pipe 3-2-8-2, diffusant enter pipe 3-2-8-3, buffer subsystem 3-2-8-4, stir ball 3-2-8-5 stablizes net 3-2-8-6, spreads horn mouth 3-2-8-7, decentralized network 3-2-8-8, and diluent enters pipe 3-2-8-9, medicine Agent exports 3-2-8-10；Diluent, which is equipped with, on the right side of medicament inlet 3-2-8-1 positioned at one end, medicament inlet 3-2-8-1 enters pipe 3-2-8-9, diluent enter the one end pipe 3-2-8-9 and are connected to external diluent bottle, and diluent enters the pipe 3-2-8-9 other end To be open, and it is inserted into inside diffusion horn mouth 3-2-8-7；Decentralized network 3-2-8- is equipped in the middle part of diffusion horn mouth 3-2-8-7 8, it is holey, vertical display；Diffusion horn mouth 3-2-8-7 is flared structure, and large diameter end is spread towards right side The diameter of horn mouth 3-2-8-7 large diameter end and small-caliber end ratio is 3:1；The diffusant jet pipe 3-2-8-2 is located at diffusion loudspeaker It is hollow ring pipe structure on the right side of mouth 3-2-8-7, the ring pipe right lateral surface of diffusant jet pipe 3-2-8-2 is equipped with a large amount of Through-hole, diffusant one end jet pipe 3-2-8-2 enter pipe 3-2-8-3 with diffusant and are connected to；The buffer subsystem 3-2-8-4 is located at diffusant Enter on the right side of pipe 3-2-8-3, buffer subsystem 3-2-8-4 is holey, vertical display；The agitation ball 3-2-8-5 is located at buffer subsystem On the right side of 3-2-8-4, agitation ball 3-2-8-5 is macromolecule thin-walled hollow structure, and agitation ball 3-2-8-5 material density is less than the close of water Degree, agitation ball 3-2-8-5 quantity are 50~100, and the single ball 3-2-8-5 mass that stirs is less than 10 grams, multiple agitation ball 3- 2-8-5 is limited at buffer subsystem 3-2-8-4 and stablizes between net 3-2-8-6, and the agitation ball 3-2-8-5 is scattered distribution, is stirred Dynamic ball 3-2-8-5 mutual gap is greater than 5cm；The stable net 3-2-8-6 is located on the right side of agitation ball 3-2-8-5, stablizes Net 3-2-8-6 is holey, vertical display；Medicament enters from medicament inlet 3-2-8-1, enters pipe 3-2-8-9 with diluent The diluent of ejection meets, and under the action of decentralized network 3-2-8-8, diffusion horn mouth 3-2-8-7, diluent is further dispersed And it is mixed with medicament；Diffusant enters pipe 3-2-8-3 by diffusant and sprays from diffusant jet pipe 3-2-8-2, buffer subsystem 3-2-8-4 Buffering is implemented to the diffusant of ejection, and is entered together with medicament, diluent and is located at buffer subsystem 3-2-8-4 and stablizes net 3-2-8- Agitation ball 3-2-8-5 action space between 6, in the case where stirring ball 3-2-8-5 agitaion, diffusant, diluent, medicament are abundant Mixing, mixture are discharged from agent outlet 3-2-8-10.

Further, the promotion disk brake apparatus 3-9 includes：Brake cooling system 3-9-1, traction mechanism 3-9-2, system Dynamic hauling rope 3-9-3, brake caliper 3-9-4, radiator fan 3-9-5, friction plate 3-9-6；Speed regulating motor on central axes Transmission shaft 3-10 is surrounded by friction plate 3-9-6, and friction plate 3-9-6 quantity is 4, and 4 friction plate 3-9-6 will adjust the speed electricity Machine transmission shaft 3-10 is wrapped up wherein, and the periphery of friction plate 3-9-6 is equipped with brake caliper 3-9-4, brake caliper 3-9-4 is cyclic annular, It is divided into pintongs, friction plate 3-9-6 is fixed on the inside of brake caliper 3-9-4；Radiator fan 3- is equipped on the left of brake caliper 3-9-4 9-5, radiator fan 3-9-5 are brake caliper 3-9-4 cooling；The periphery brake caliper 3-9-4 is equipped with braking hauling rope 3-9-3, system Dynamic hauling rope 3-9-3 is around brake caliper 3-9-4 surrounding, and the two is hinged；Brake the other end and dragger of hauling rope 3-9-3 Structure 3-9-2 connection；It is equipped with brake cooling system 3-9-1 on the top brake caliper 3-9-4, the two is connected by conduit；Dragger Structure 3-9-2 rotation, tightening braking hauling rope 3-9-3, and then 4 friction plate 3-9-6 are tightly attached to by tune by brake caliper 3-9-4 On speed motor transmission shaft 3-10, speed regulating motor transmission shaft 3-10 is made to stop operating；At the same time, friction plate 3-9-6 is because of friction production Raw heat is taken away by the brake cooling system 3-9-1 connecting with brake caliper 3-9-4.

Further, the work piece holder 4 includes：Rotating electric machine 4-1, service chamber 4-2, workpiece handgrip 4-3, gear wheel 4- 4, central gear 4-5, handgrip gear 4-6, lap count 4-7；Wherein, the gear wheel 4-4 is arranged in service chamber 4-2 Portion, gear wheel 4-4 are interior tooth type hollow structure, and interior teeth are located in gear wheel 4-4 internal circumference, are equipped in gear wheel 4-4 Central gear 4-5 and handgrip gear 4-6, central gear 4-5, handgrip gear 4-6 are outer toothing；Described central gear 4-5 At the central axes gear wheel 4-4, it is surrounded by handgrip gear 4-6 in central gear 4-5, gear wheel 4-4, central gear 4-5, is grabbed Hand gear 4-6 three engages connection；The handgrip gear 4-6 quantity is three, is circumferentially symmetrically divided around central gear 4-5 Cloth；The rotating electric machine 4-1 is fixedly mounted on the side service chamber 4-2, and rotating electric machine 4-1 and central gear 4-5 are drivingly connected；Institute It states workpiece handgrip 4-3 and is arranged in the other side service chamber 4-2, workpiece one end handgrip 4-3 is fixedly connected with handgrip gear 4-6；It is described Lap count 4-7 is fixedly connected on rotating electric machine 4-1 turntable；The rotating electric machine 4-1, lap count 4-7 lead to respectively It crosses conducting wire and the control of control system 6 connects；Rotating electric machine 4-1 drives central gear 4-5 rotation, and then drives three, periphery handgrip Gear 4-6 does revolution motion along gear wheel 4-4 interior tooth, while three handgrip gear 4-6 are also done rotation movement, handgrip gear 4- 6 drive workpiece revolution and rotation by workpiece handgrip 4-3.

Further, the workpiece handgrip 4-3 includes：Arm 4-3-1, workpiece slot 4-3-2, banjo traction splint 4-3-3, work Part clamping degree inductor 4-3-4；Wherein, the workpiece slot 4-3-2 is arranged in the top arm 4-3-1, and workpiece slot 4-3-2 is circle Groove, diameter are 8cm~12cm；The banjo traction splint 4-3-3 quantity is three, and circumference is equally distributed on workpiece slot Around 4-3-2, the end banjo traction splint 4-3-3 is equipped with antiskid protection pad and workpiece clamp tightness inductor 4-3-4；Finger traction Folder 4-3-3 driving motor, workpiece clamp tightness inductor 4-3-4 pass through conducting wire respectively and the control of control system 6 connects.The control Timer is provided in system 6, the timer is connect with speed regulating motor 3-4 actuating coil polygon control survey.

Further, the decentralized network 3-2-8-8 is formed by high molecular material pressing mold, the composition of decentralized network 3-2-8-8 at Divide and manufacturing process is as follows：

One, decentralized network 3-2-8-8 constituent：

Purify 339.2~564.8 parts of lake water according to parts by weight, N- methyl-1,1,2,2,3,3,4,4,5,5,5- ten one fluoro- 131.5~173.6 parts of 1- pentane sulfonamide, 134.2~243.1 parts of methylbenzene of 1- (methoxy) -4-, 4- (methyl mercapto) fourth 130.4~147.4 parts of aldehyde, 133.1~190.3 parts of rutile, bis- [2- (2- the acrylic)] phenol of 4,4'- (1- methyl ethylidene) With 136.9~197.5 parts of polymer of (chloromethyl) ethylene oxide, 138.7~193.3 parts of silver nano-particle, polymerization oxidation 1,1,2,3,3,3,131.1~173.6 parts of-hexafluoro -1- propylene, the polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate 133.6~173.5 parts, 133.9~156.6 parts of zinc salt of alkali formula aphthenic acids, methyl ethyl ketoxime sealing end [2,4,6- tri- oxygen triazine -1, 3,5 (2H, 4H, 6H)-three bases] three 122.5~158.8 parts of (cyclohexyl) isocyanates, 121.2~164.8 parts of 7- methyl octanal, 130.8~175.4 parts of ester of (2E)-formic acid -2- hexen-1-ol, 140.3~184.3 parts of the polymer of polyurethane, mass concentration is 163.4~217.8 parts of the rosolic acid cetyl ester of 130mg/L~397mg/L；

Two, the manufacturing process of decentralized network 3-2-8-8, comprises the steps of：

Step 1：In stirring vertical tower reactor, it is added and purifies lake water and N- methyl-1,1,2,2,3,3,4,4,5,5,5- ten The blender in vertical tower reactor is stirred in one fluoro -1- pentane sulfonamide, starting, and setting speed is 132rpm~178rpm, The steam oil heater in vertical tower reactor is stirred in starting, and temperature is made to rise to 147.2 DEG C~148.8 DEG C, and 1- (methoxy is added Ylmethyl) -4- methylbenzene stirs evenly, and carries out reaction 124.5~135.6 minutes, and 4- (methyl mercapto) butyraldehyde is added, is passed through flow For 123.5m³/ min~164.4m³The helium of/min 124.5~135.6 minutes；It is added in stirring vertical tower reactor later Rutile is again started up the steam oil heater stirred in vertical tower reactor, temperature is made to rise to 164.2 DEG C~197.1 DEG C, 4,4'- (1- methyl ethylidene) bis- [2- (2- acrylic)] phenol and (chloromethyl) ring is added in heat preservation 124.4~135.4 minutes The polymer of oxidative ethane, the pH value that solution in vertical tower reactor is stirred in adjustment is 4.1~8.3, keeps the temperature 124.1~364.1 points Clock；

Step 2：Separately take silver nano-particle, by silver nano-particle power be 6.64KW~12.08KW under ultrasonication 0.130 After~1.197 hours；Silver nano-particle is added to another to stir in vertical tower reactor, addition mass concentration is 134mg/ The 1 of the polymerization oxidation of L~364mg/L, 1,2,3,3,3,-hexafluoro -1- propylene disperses silver nano-particle, and starting stirring is stood tower anti- The steam oil heater in device is answered, makes solution temperature between 45 DEG C~89 DEG C, stirring in vertical tower reactor is stirred in starting Machine is mixed, and with 4 × 10²Rpm~8 × 10²The speed of rpm stirs, and adjusts pH value between 4.5~8.8, and insulated and stirred 130~ 197 minutes；Stop reaction later and stand 6.64 × 10~12.08 × 10 minutes, removes impurity；Formaldehyde and two is added in suspension The polymer of cyano diamides and ethylenediamine sulfate adjusts pH value between 1.5~2.8, forms sediment and is washed with purification lake water It is de-, by centrifuge in revolving speed 4.192 × 10³Rpm~9.643 × 10³Solid content is obtained under rpm, 2.407 × 10²DEG C~ 3.642×10²It is dry at a temperature of DEG C, 0.192 × 10 is crossed after grinding³~1.643 × 10³Mesh, it is spare；

Step 3：Silver nano-particle after separately taking alkali formula aphthenic acids zinc salt and step 2 to handle, uses the small angle of glancing incidence after mixing Gamma-rays diffusing reflection irradiation is spent, the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 121.2MeV~149.8MeV, agent Amount is 169.2kGy~209.8kGy, irradiation time is 133.2~158.8 minutes, obtains the alkali formula zinc naphthenate of character change Salt and silver nano-particle mixture；Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stirring and stand tower reaction In device, the steam oil heater in vertical tower reactor is stirred in starting, and 132.8 DEG C~178.4 DEG C of set temperature, starting is stirred Blender in vertical tower reactor, revolving speed are 124rpm~519rpm, and pH is adjusted between 4.3~8.3, dehydration 133.3~ 147.3 minute, spare；

Step 4：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that step 3 is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazine -1,3,5 (2H, 4H, 6H) of 2,4,6-] three that the methyl ethyl ketoxime that degree is 134mg/L~364mg/L blocks In (cyclohexyl) isocyanates, cocurrent add to step 1 stirring stand tower reactor in, flow acceleration be 269mL/min~ 997mL/min；Vertical tower reactor blender is stirred in starting, and setting speed is 138rpm~178rpm；Stirring 4~8 minutes；Again 7- methyl octanal is added, starting stirs the steam oil heater in vertical tower reactor, is warming up to 168.4 DEG C~205.8 DEG C, PH is adjusted between 4.4~8.8, and being passed through helium ventilatory capacity is 123.118m³/ min~164.273m³/ min, heat preservation are stood 158.2~188.8 minutes；It is again started up the vertical tower reactor blender of stirring, revolving speed is 133rpm~178rpm, is added (2E)-formic acid -2- hexen-1-ol ester, and pH is adjusted between 4.4~8.8, heat preservation stands 157.5~197.6 minutes；

Step 5：The blender in vertical tower reactor is stirred in starting, and setting speed is 130rpm~197rpm, and starting stirring is vertical Steam oil heater in tower reactor sets and stirs temperature in vertical tower reactor as 1.287 × 10²DEG C~2.32 ×10²DEG C, the polymer of polyurethane is added, reacts 124.2~135.1 minutes；Rosolic acid cetyl ester, starting are added later Stir the steam oil heater in vertical tower reactor, set stirring stand temperature in tower reactor as 208.4 DEG C~ 264.4 DEG C, pH is adjusted between 4.1~8.1, and pressure is 1.3MPa~1.31MPa, and the reaction time is 0.4~0.9 hour；It After be depressurized to normal pressure, be cooled to 124.2 DEG C~135.1 DEG C and discharge into molding press to get to decentralized network 3-2-8-8；The silver is received The partial size of rice particle is 138 μm~148 μm.

Further, a kind of working method for surface water runoff purifying plant cultivation block medicament injection mixing arrangement, This method includes following steps：

Step 1：Object to be cut is encased in the workpiece slot 4-3-2 on workpiece handgrip 4-3 by treatment process, control system 6 Banjo traction splint 4-3-3 work is controlled, process object is clamped；Workpiece clamp tightness inductor 4-3-4 real-time monitoring process object Clamping degree, when workpiece clamp tightness inductor 4-3-4 detects that process object clamping degree reaches default value M, Workpiece clamping Feedback signal is sent to control system 6 by degree inductor 4-3-4, and control system 6 controls banjo traction splint 4-3-3 and stops working；

Step 2：At the same time, control system 6 starts the slide motor 3-8 of the end sliding block 3-3, under slide motor 3-8 drive, Sliding block 3-3 does sliding motion along slideway 3-2, pushes disk 3-7 to lean on to the workpiece for being fixed on the end workpiece handgrip 4-3 to drive Closely；When pushing disk 3-7 apart from workpiece 3cm~5cm, control system 6 stops slide motor 3-8 work, while controlling hydraulic cylinder 3-6 work；Under hydraulic cylinder 3-6 driving, push disk 3-7 slowly close to workpiece, until pushing disk 3-7 front end blade and processing Object end face is in contact；

Step 3：Control system 6 starts the rotating electric machine 4- in speed regulating motor 3-4 and work piece holder 4 in pushing mechanism 3 simultaneously 1；Under speed regulating motor 3-4 driving, disk 3-7 is pushed to do circular motion clockwise；Under rotating electric machine 4-1 motor driven, workpiece Handgrip 4-3 does counterclockwise circular motion by handgrip gear 4-6；

Step 4：In rotating electric machine 4-1 rotary course, lap count 4-7 real-time monitoring rotating electric machine 4-1 rotating cycle；When When lap count 4-7 detects that rotating electric machine 4-1 rotating cycle reaches default value R, lap count 4-7 is by feedback letter It number is sent to control system 6, control system 6 controls rotating electric machine 4-1 and stops working；

Step 5：In the speed regulating motor 3-4 course of work, when the timer in control system 6 works to speed regulating motor 3-4 Between carry out timing；When timer, which adds up timing time, reaches default value T, control system 6 stops speed regulating motor 3-4；

Step 6：Control system 6 controls banjo traction splint 4-3-3 and unclamps, and the workpiece handled well enters subsequent processing.

It is of the present invention a kind of for surface water runoff purifying plant cultivation block medicament injection mixing arrangement, the device intelligence Degree height can be changed, time intelligence is controllable, and product quality is substantially improved, and stability is high, and the speed of service is fast, impacts to other equipment Power is small, and work efficiency is high.

Detailed description of the invention

Fig. 1 is that heretofore described one kind is shown for surface water runoff purifying plant cultivation block medicament injection mixing arrangement It is intended to.

Fig. 2 is heretofore described 3 structural schematic diagram of pushing mechanism.

Fig. 3 is heretofore described 7 structural schematic diagram of rolling cutter.

Fig. 4 is in the present invention for the cooling device structural schematic diagram of slideway 3-2 setting.

Fig. 5 is heretofore described medicament mixing device 3-2-8 structural schematic diagram.

Fig. 6 is heretofore described promotion disk brake apparatus 3-9 structural schematic diagram.

Fig. 7 is heretofore described 4 structural schematic diagram of work piece holder.

Fig. 8 is heretofore described workpiece handgrip 4-3 structural schematic diagram.

Fig. 9 is heretofore described decentralized network 3-2-8-8 material wear-resistant rate with using time variation diagram.

Specific embodiment

With reference to the accompanying drawings and examples to provided by the invention a kind of for surface water runoff purifying plant cultivation block medicine Agent injection mixing arrangement is further described.

As shown in Figure 1, being that heretofore described one kind is mixed for the cultivation block medicament injection of surface water runoff purifying plant Close schematic device.As seen from the figure, the fixed frame 2 is stainless steel rectangular structure, and thickness is between 3cm~4cm；Institute Stating 1 quantity of shock-absorbing foot pad is four, is respectively and fixedly installed to 2 bottom four corners of fixed frame；The support platform 5 is that rectangle is zinc-plated Plate, support platform 5 are fixedly mounted on 2 top of fixed frame；The pushing mechanism 3 is arranged in 5 side of support platform；The workpiece Fixture 4 is arranged in 5 other side of support platform；The control system 6 is fixedly mounted on fixed frame 2；The rolling cutter 7 In 3 left side of pushing mechanism, the two connection.

As shown in Fig. 2, being heretofore described 3 structural schematic diagram of pushing mechanism.As seen from the figure, the slideway 3-2 It is fixedly connected by slideway fixed block 3-1 with support platform 5；The cross section the slideway 3-2 is in " Ω " shape, slideway 3-2 quantity It is 2；The sliding block 3-3 and slideway 3-2 is slidably connected, and the end sliding block 3-3 is provided with slide motor 3-8, and slide motor 3-8 drives Movable slider 3-3 is slided on slideway 3-2；The speed regulating motor 3-4 is variable-frequency motor, and speed regulating motor 3-4 pedestal and sliding block 3-3 are welded Connect fixation；Described one end speed regulating motor transmission shaft 3-10 is connect with speed regulating motor 3-4, and the other end passes through fuel tank 3-5, pushes disk system Dynamic device 3-9, hydraulic cylinder 3-6 are fixedly connected with disk 3-7 is pushed, and speed regulating motor 3-4, which drives, pushes disk 3-7 rotation；The fuel tank 3-5 is connected to the one end hydraulic cylinder 3-6 conduit；The hydraulic cylinder 3-6 other end pushes disk 3-7 to connect with detachable；The promotion Disk brake apparatus 3-9, which is located at, pushes disk 3-7 and hydraulic cylinder 3-6 between the two；The speed regulating motor 3-4, it hydraulic cylinder 3-6, pushes Disk 3-7 central axis in the same horizontal line, pushes disk 3-7 to connect with rolling cutter 7, pushes disk 3-7 that rolling cutter 7 is driven to revolve Turn；The speed regulating motor 3-4, hydraulic cylinder 3-6 pass through conducting wire respectively and the control of control system 6 connects；The slide motor 3-8 is logical It crosses conducting wire and the control of control system 6 connects.

As shown in figure 3, being heretofore described 7 structural schematic diagram of rolling cutter.As seen from the figure, positioned at the driven of one end 7-1 is taken turns, is connect with external cutter motor, meanwhile, driven wheel 7-1 is fixedly connected with transmission shaft 7-9；In driven wheel 7-1 Side is equipped with back-up roller bearing 7-4, and the back-up roller bearing 7-4 quantity is 2, is located at the both ends of transmission shaft 7-9；The biography Moving axis 7-9 hollow structure, inside are equipped with transformer 7-2, heating tube 7-5, water inlet pipe 7-7；Water inlet pipe 7-7 is parallel to transmission shaft 7- The quantity of 9, water inlet pipe 7-7 are 3, and water inlet pipe 7-7 is connected to water inlet port 7-8, and water inlet port 7-8 is connected to external pump； The periphery water inlet pipe 7-7 is equipped with heating tube 7-5, heating tube 7-5 helical structure, and the one end heating tube 7-5 passes through conducting wire and transformer 7-2 The other end of connection, transformer 7-2 is electrically connected by conducting wire with external city, and heating tube 7-5 implements to heat to water inlet pipe 7-7, becomes Depressor 7-2 implements to adjust to heating temperature；Cutting edge 7-3 is equipped with outside transmission shaft 7-9, cutting edge 7-3 quantity is 4,4 Cutting edge 7-3 is angularly, mode substantially symmetrical about its central axis is fixed on transmission shaft 7-9；Cutting edge spray head is equipped in the root cutting edge 7-3 7-6, cutting edge spray head 7-6 open at one end design and are directed toward cutting edge 7-3 knife face, the cutting edge spray head 7-6 other end and water inlet pipe 7-7 connection；Driven wheel 7-1 drives cutting edge 7-3 rotation by transmission shaft 7-9, and cutting edge 7-3 implements equidistant cutting to material； Meanwhile cutting edge spray head 7-6 implements to clean to cutting edge 7-3 knife face.

As shown in figure 4, being in the present invention for the cooling device structural schematic diagram of slideway 3-2 setting.As seen from the figure, it is located at Side is connected to by coolant liquid entrance 3-2-1 with heat-exchanging chamber 3-2-3, and is located at heat-exchanging chamber 3- by coolant liquid entrance 3-2-1 The lower part 2-3, low level；It is described that the top heat-exchanging chamber 3-2-3, a high position are located at by coolant liquid outlet 3-2-7, and 3- is exported by coolant liquid 2-7 is connected to heat-exchanging chamber 3-2-3；The heat-exchange tube 3-2-2 is located in the middle part of heat-exchanging chamber 3-2-3, in heat-exchange tube 3-2-2 Hollow structure, the quantity of heat-exchange tube 3-2-2 are 20, the more vertical equidistant arrangements of heat-exchange tube 3-2-2；Heat-exchange tube 3-2-2 Both ends are respectively equipped with buffered room 3-2-5, the both ends heat-exchange tube 3-2-2 respectively with the buffered room that is located at its upper and lower ends 3-2-5 connection；The heat-exchanging chamber 3-2-3 is separated by partition 3-2-4 and the buffered room 3-2-5 of upper and lower ends；It is located at The buffered room 3-2-5 on top, top are equipped with refrigerant inlet 3-2-6, the buffered room 3-2-5 and refrigerant inlet on top 3-2-6 connection, buffered room its bottom 3-2-5 positioned at lower part are equipped with refrigerant exit 3-2-9, the buffered room 3- of lower part 2-5 is connected to the refrigerant exit 3-2-9 of bottom；The medicament mixing device 3-2-8 is connected to heat-exchanging chamber 3-2-3；Refrigerant from Refrigerant inlet 3-2-6 enters buffered room 3-2-5, and then enters inside heat-exchange tube 3-2-2, by heat-exchange tube 3-2-2 Generated heat absorption, and flowed out from refrigerant exit 3-2-9；Heat exchange is entered from by coolant liquid entrance 3-2-1 by coolant liquid Room 3-2-3 transfers heat to heat-exchange tube 3-2-2, and from by coolant liquid outlet 3-2-7 outflow；Meanwhile external agent passes through Medicament mixing device 3-2-8 is controllably added to inside heat-exchanging chamber 3-2-3, is reacted with by coolant liquid.

As shown in figure 5, being heretofore described medicament mixing device 3-2-8 structural schematic diagram.As seen from the figure, it is located at Diluent is equipped on the right side of the medicament inlet 3-2-8-1 of one end, medicament inlet 3-2-8-1 and enters pipe 3-2-8-9, and diluent enters pipe The one end 3-2-8-9 is connected to external diluent bottle, and it is open that diluent, which enters the pipe 3-2-8-9 other end, and is inserted into diffusion Inside horn mouth 3-2-8-7；It is equipped with decentralized network 3-2-8-8 in the middle part of diffusion horn mouth 3-2-8-7, is holey, vertical It puts；Diffusion horn mouth 3-2-8-7 is flared structure, and large diameter end spreads horn mouth 3-2-8-7 heavy caliber towards right side The diameter ratio of end and small-caliber end is 3:1；The diffusant jet pipe 3-2-8-2 is located on the right side of diffusion horn mouth 3-2-8-7, is The ring pipe right lateral surface of hollow ring pipe structure, diffusant jet pipe 3-2-8-2 is equipped with a large amount of through-holes, diffusant jet pipe 3-2-8- 2 one end enter pipe 3-2-8-3 with diffusant and are connected to；The buffer subsystem 3-2-8-4 is located at diffusant and enters on the right side of pipe 3-2-8-3, buffering Net 3-2-8-4 is holey, vertical display；The agitation ball 3-2-8-5 is located on the right side of buffer subsystem 3-2-8-4, stirs ball 3- 2-8-5 is macromolecule thin-walled hollow structure, and agitation ball 3-2-8-5 material density is less than the density of water, stirs ball 3-2-8-5 quantity It is 50~100, for the single ball 3-2-8-5 mass that stirs less than 10 grams, multiple agitation ball 3-2-8-5 are limited at buffer subsystem 3- 2-8-4 and stablize net 3-2-8-6 between, the agitation ball 3-2-8-5 be scattered distribution, agitation ball 3-2-8-5 between each other Gap is greater than 5cm；The stable net 3-2-8-6, which is located at, to be stirred on the right side of ball 3-2-8-5, is stablized net 3-2-8-6 and is holey, erects Directly put；Medicament enters from medicament inlet 3-2-8-1, and the diluent for entering pipe 3-2-8-9 ejection with diluent meets, and is dispersing Under the action of netting 3-2-8-8, diffusion horn mouth 3-2-8-7, diluent is further dispersed and is mixed with medicament；Diffusant passes through Diffusant enters pipe 3-2-8-3 and sprays from diffusant jet pipe 3-2-8-2, and buffer subsystem 3-2-8-4 implements buffering to the diffusant of ejection, And enters the agitation ball 3-2-8-5 for being located at buffer subsystem 3-2-8-4 and stablizing between net 3-2-8-6 together with medicament, diluent and make With space, in the case where stirring ball 3-2-8-5 agitaion, diffusant, diluent, medicament are sufficiently mixed, and mixture is from agent outlet 3-2-8-10 discharge.

As shown in fig. 6, being heretofore described promotion disk brake apparatus 3-9 structural schematic diagram.As seen from the figure, it is located at Speed regulating motor transmission shaft 3-10 on central axes is surrounded by friction plate 3-9-6, and friction plate 3-9-6 quantity is 4, and 4 are rubbed Pad 3-9-6 wraps up speed regulating motor transmission shaft 3-10 wherein, and the periphery of friction plate 3-9-6 is equipped with brake caliper 3-9-4, system Dynamic chuck 3-9-4 is cyclic annular, is divided into pintongs, and friction plate 3-9-6 is fixed on the inside of brake caliper 3-9-4；Brake caliper 3-9-4 is left Side is equipped with radiator fan 3-9-5, and radiator fan 3-9-5 is brake caliper 3-9-4 cooling；The periphery brake caliper 3-9-4 is equipped with system Dynamic hauling rope 3-9-3, braking hauling rope 3-9-3 is around brake caliper 3-9-4 surrounding, and the two is hinged；Brake hauling rope 3-9-3 The other end connect with traction mechanism 3-9-2；It is equipped with brake cooling system 3-9-1 on the top brake caliper 3-9-4, the two passes through Conduit connection；Traction mechanism 3-9-2 rotation, tightening braking hauling rope 3-9-3, and then 4 are rubbed by brake caliper 3-9-4 Piece 3-9-6 is tightly attached on speed regulating motor transmission shaft 3-10, and speed regulating motor transmission shaft 3-10 is made to stop operating；At the same time, it rubs The heat that piece 3-9-6 is generated by friction, is taken away by the brake cooling system 3-9-1 connecting with brake caliper 3-9-4.

As shown in fig. 7, being heretofore described 4 structural schematic diagram of work piece holder.As seen from the figure, wherein described big Gear 4-4 is arranged in inside service chamber 4-2, and gear wheel 4-4 is interior tooth type hollow structure, and interior teeth are located in gear wheel 4-4 On portion's circumference, central gear 4-5 is equipped in gear wheel 4-4 and handgrip gear 4-6, central gear 4-5, handgrip gear 4-6 are outer Toothing；The central gear 4-5 is located at the central axes gear wheel 4-4, is surrounded by handgrip gear 4-6 in central gear 4-5, Gear wheel 4-4, central gear 4-5, handgrip gear 4-6 three engage connection；The handgrip gear 4-6 quantity is three, is surrounded Central gear 4-5 is circumferentially symmetrical；The rotating electric machine 4-1 is fixedly mounted on the side service chamber 4-2, rotating electric machine 4-1 It is drivingly connected with central gear 4-5；The workpiece handgrip 4-3 is arranged in the other side service chamber 4-2, workpiece one end handgrip 4-3 with Handgrip gear 4-6 is fixedly connected；The lap count 4-7 is fixedly connected on rotating electric machine 4-1 turntable；The rotating electric machine 4-1, lap count 4-7 pass through conducting wire respectively and the control of control system 6 connects；Rotating electric machine 4-1 drives central gear 4-5 rotation Turn, and then three, periphery handgrip gear 4-6 is driven to be revolution motion, while three handgrip gear 4-6 along gear wheel 4-4 interior tooth Also it does rotation movement, handgrip gear 4-6 drives workpiece revolution and rotation by workpiece handgrip 4-3.

As shown in figure 8, being heretofore described workpiece handgrip 4-3 structural schematic diagram.As seen from the figure, the workpiece slot 4-3-2 is arranged in the top arm 4-3-1, and workpiece slot 4-3-2 is circular groove, and diameter is 8cm~12cm；The finger Haulage clip 4-3-3 quantity is three, and circumference is equally distributed on around workpiece slot 4-3-2, and the end banjo traction splint 4-3-3 is equipped with Antiskid protection pad and workpiece clamp tightness inductor 4-3-4；Banjo traction splint 4-3-3 driving motor, workpiece clamp tightness inductor 4- 3-4 passes through conducting wire respectively and the control of control system 6 connects.Timer, the timer and tune are provided in the control system 6 The connection of speed motor 3-4 actuating coil polygon control survey.

Following embodiment further illustrates the contents of the present invention, and as decentralized network 3-2-8-8, it is important set of the invention Part increases the service life of integral device due to its presence, it plays pass for the safety of integral device, even running Key effect.For this purpose, by it is following be embodiment, further verify decentralized network 3-2-8-8 of the present invention, the height shown In the physical characteristic of other related patents.

Embodiment 1

Decentralized network 3-2-8-8 of the present invention is prepared according to the following steps, and according to parts by weight：

Step 1：In stirring vertical tower reactor, it is added and purifies 339.2 parts of lake water and N- methyl-1,1,2,2,3,3,4,4,5, 5,5- ten one 131.5 parts of sulfonamide of fluoro -1- pentane, the blender in vertical tower reactor is stirred in starting, and setting speed is 132rpm, starting stir the steam oil heater in vertical tower reactor, temperature are made to rise to 147.2 DEG C, and 1- (methoxyl group is added Methyl) 134.2 parts of -4- methylbenzene stir evenly, carry out reaction 124.5 minutes, be added 130.4 parts of butyraldehyde of 4- (methyl mercapto), lead to Inbound traffics are 123.5m³The helium of/min 124.5 minutes；133.1 parts of rutile are added in stirring vertical tower reactor later, It is again started up the steam oil heater stirred in vertical tower reactor, temperature is made to rise to 164.2 DEG C, 124.4 minutes is kept the temperature, adds Enter 136.9 parts of polymer of bis- [2- (2- the acrylic)] phenol of 4,4'- (1- methyl ethylidene) and (chloromethyl) ethylene oxide, adjusts The whole pH value for stirring solution in vertical tower reactor is 4.1, keeps the temperature 124.1 minutes；

Step 2：138.7 parts of silver nano-particle separately are taken, ultrasonication 0.130 is small in the case where power is 6.64KW by silver nano-particle Shi Hou；Silver nano-particle is added to another to stir in vertical tower reactor, the polymeric oxygen that mass concentration is 134mg/L is added The steaming in vertical tower reactor is stirred in 1,1,2,3,3,3 changed, 131.1 parts of dispersion silver nano-particles of-hexafluoro -1- propylene, starting Vapour formula oil heater makes solution temperature at 45 DEG C, and the blender in vertical tower reactor is stirred in starting, and with 4 × 10²Rpm's Speed stirring adjusts pH value 4.5, insulated and stirred 130 minutes；Stop reaction later and stand 6.64 × 10 minutes, removes impurity； Suspension is added 133.6 parts of polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate, adjustment pH value is formed 1.5 Sediment purification lake water elution, by centrifuge in revolving speed 4.192 × 10³Solid content is obtained under rpm, 2.407 × 10²℃ At a temperature of it is dry, 0.192 × 10 is crossed after grinding³Mesh, it is spare；

Step 3：Silver nano-particle after separately taking alkali formula aphthenic acids zinc salt 133.9 and step 2 to handle, uses glancing incidence after mixing Low-angle gamma-rays diffusing reflection irradiation, the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 121.2MeV, dosage is 169.2kGy, irradiation time are 133.2 minutes, obtain the alkali formula aphthenic acids zinc salt and silver nano-particle mixture of character change； Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stir to stand in tower reactor, starting stirring is stood tower anti- The steam oil heater in device is answered, 132.8 DEG C of set temperature, the blender in vertical tower reactor is stirred in starting, and revolving speed is 124rpm, pH are adjusted to 4.3, are dehydrated 133.3 minutes, spare；

Step 4：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that step 3 is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazine -1,3,5 (2H, 4H, 6H) of 2,4,6-] three (cyclohexyl) that the methyl ethyl ketoxime that degree is 134mg/L blocks are different In 122.5 parts of cyanate, the stirring that cocurrent adds to step 1 is stood in tower reactor, flow acceleration 269mL/min；Starting is stirred Mix vertical tower reactor blender, setting speed 138rpm；Stirring 4 minutes；121.2 parts of 7- methyl octanal are added, starting The steam oil heater in vertical tower reactor is stirred, is warming up to 168.4 DEG C, pH is adjusted to 4.4, is passed through helium ventilatory capacity and is 123.118m³/ min, heat preservation stand 158.2 minutes；It is again started up and stirs vertical tower reactor blender, revolving speed 133rpm, 130.8 parts of ester of (2E)-formic acid -2- hexen-1-ol are added, and pH is made to be adjusted to 4.4, heat preservation stands 157.5 minutes；

Step 5：The blender in vertical tower reactor, setting speed 130rpm are stirred in starting, and tower reaction is stood in starting stirring Steam oil heater in device sets and stirs temperature in vertical tower reactor as 1.287 × 10²DEG C, polyurethane is added It 140.3 parts of polymer, reacts 124.2 minutes；The rosolic acid cetyl ester 163.4 that mass concentration is 130mg/L is added later Part, the steam oil heater in vertical tower reactor is stirred in starting, set stirring and founds temperature in tower reactor as 208.4 DEG C, pH is adjusted to 4.1, and pressure 1.3MPa, the reaction time is 0.4 hour；It is depressurized to normal pressure later, is cooled to 124.2 DEG C and goes out Expect into molding press to get to decentralized network 3-2-8-8；

The partial size of the silver nano-particle is 138 μm.

Embodiment 2

Decentralized network 3-2-8-8 of the present invention is prepared according to the following steps, and according to parts by weight：

Step 1：In stirring vertical tower reactor, it is added and purifies 564.8 parts of lake water and N- methyl-1,1,2,2,3,3,4,4,5, 5,5- ten one 173.6 parts of sulfonamide of fluoro -1- pentane, the blender in vertical tower reactor is stirred in starting, and setting speed is 178rpm, starting stir the steam oil heater in vertical tower reactor, temperature are made to rise to 148.8 DEG C, and 1- (methoxyl group is added Methyl) 243.1 parts of -4- methylbenzene stir evenly, carry out reaction 135.6 minutes, be added 147.4 parts of butyraldehyde of 4- (methyl mercapto), lead to Inbound traffics are 164.4m³The helium of/min 135.6 minutes；190.3 parts of rutile are added in stirring vertical tower reactor later, It is again started up the steam oil heater stirred in vertical tower reactor, temperature is made to rise to 197.1 DEG C, 135.4 minutes is kept the temperature, adds Enter 197.5 parts of polymer of bis- [2- (2- the acrylic)] phenol of 4,4'- (1- methyl ethylidene) and (chloromethyl) ethylene oxide, adjusts The whole pH value for stirring solution in vertical tower reactor is 8.3, keeps the temperature 364.1 minutes；

Step 2：Separately take 193.3 parts of silver nano-particle, by silver nano-particle power be 12.08KW under ultrasonication 1.197 After hour；Silver nano-particle is added to another to stir in vertical tower reactor, the polymerization that mass concentration is 364mg/L is added The 1,1,2,3,3,3 of oxidation, 173.6 parts of dispersion silver nano-particles of-hexafluoro -1- propylene, starting are stirred in vertical tower reactor Steam oil heater makes solution temperature between 89 DEG C, and the blender in vertical tower reactor is stirred in starting, and with 8 × 10²The speed of rpm stirs, and adjusts pH value 8.8, insulated and stirred 197 minutes；Stop reaction later and stand 12.08 × 10 minutes, Remove impurity；Suspension is added 173.5 parts of polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate, adjustment pH value exists 2.8, sediment purification lake water elution is formed, solid content is obtained at 9.643 × 103rpm of revolving speed by centrifuge, 3.642×10²It is dry at a temperature of DEG C, 1.643 × 103 meshes are crossed after grinding, it is spare；

Step 3：Separately take silver nano-particle after 156.6 parts of alkali formula aphthenic acids zinc salt and step 2 processing, after mixing using plunder into Low-angle gamma-rays diffusing reflection irradiation is penetrated, the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 149.8MeV, dosage is 209.8kGy, irradiation time are 158.8 minutes, obtain the alkali formula aphthenic acids zinc salt and silver nano-particle mixture of character change； Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stir to stand in tower reactor, starting stirring is stood tower anti- The steam oil heater in device is answered, 178.4 DEG C of set temperature, the blender in vertical tower reactor is stirred in starting, and revolving speed is 519rpm, pH are adjusted to 8.3, are dehydrated 147.3 minutes, spare；

Step 4：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that step 3 is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazine -1,3,5 (2H, 4H, 6H) of 2,4,6-] three (cyclohexyl) that the methyl ethyl ketoxime that degree is 364mg/L blocks are different In 158.8 parts of cyanate, the stirring that cocurrent adds to step 1 is stood in tower reactor, flow acceleration 997mL/min；Starting is stirred Mix vertical tower reactor blender, setting speed 178rpm；Stirring 8 minutes；164.8 parts of 7- methyl octanal are added, starting The steam oil heater in vertical tower reactor is stirred, is warming up to 205.8 DEG C, pH is adjusted to 8.8, is passed through helium ventilatory capacity and is 164.273m3/min heat preservation stands 188.8 minutes；It is again started up and stirs vertical tower reactor blender, revolving speed 178rpm, 175.4 parts of ester of (2E)-formic acid -2- hexen-1-ol are added, and pH is made to be adjusted to 8.8, heat preservation stands 197.6 minutes；

Step 5：The blender in vertical tower reactor, setting speed 197rpm are stirred in starting, and tower reaction is stood in starting stirring Steam oil heater in device sets and stirs temperature in vertical tower reactor as 2.32 × 10²DEG C, the poly- of polyurethane is added 184.3 parts of object are closed, is reacted 135.1 minutes；217.8 parts of rosolic acid cetyl ester that mass concentration is 397mg/L are added later, The steam oil heater in vertical tower reactor is stirred in starting, set stirring and founds temperature in tower reactor as 264.4 DEG C, PH is adjusted to 8.1, and pressure 1.31MPa, the reaction time is 0.9 hour；It is depressurized to normal pressure later, is cooled to 135.1 DEG C of dischargings Enter molding press to get decentralized network 3-2-8-8 is arrived；

The partial size of the silver nano-particle is 148 μm.

Embodiment 3

Decentralized network 3-2-8-8 of the present invention is prepared according to the following steps, and according to parts by weight：

Step 1：In stirring vertical tower reactor, it is added and purifies 339.9 parts of lake water and N- methyl-1,1,2,2,3,3,4,4,5, 5,5- ten one 131.9 parts of sulfonamide of fluoro -1- pentane, the blender in vertical tower reactor is stirred in starting, and setting speed is 132rpm, starting stir the steam oil heater in vertical tower reactor, temperature are made to rise to 147.9 DEG C, and 1- (methoxyl group is added Methyl) 134.9 parts of -4- methylbenzene stir evenly, carry out reaction 124.9 minutes, be added 130.9 parts of butyraldehyde of 4- (methyl mercapto), lead to Inbound traffics are helium 124.9 minutes of 123.9m3/min；133.9 parts of rutile are added in stirring vertical tower reactor later, It is again started up the steam oil heater stirred in vertical tower reactor, temperature is made to rise to 164.9 DEG C, 124.9 minutes is kept the temperature, adds Enter 136.9 parts of polymer of bis- [2- (2- the acrylic)] phenol of 4,4'- (1- methyl ethylidene) and (chloromethyl) ethylene oxide, adjusts The whole pH value for stirring solution in vertical tower reactor is 4.9, keeps the temperature 124.9 minutes；

Step 2：Separately take 138.9 parts of silver nano-particle, by silver nano-particle power be 6.649KW under ultrasonication 0.1309 After hour；Silver nano-particle is added to another to stir in vertical tower reactor, it is the poly- of 134.9mg/L that mass concentration, which is added, The 1,1,2,3,3,3 of oxidation, 131.9 parts of dispersion silver nano-particles of-hexafluoro -1- propylene are closed, starting is stirred in vertical tower reactor Steam oil heater, make solution temperature at 45.9 DEG C, the blender in vertical tower reactor is stirred in starting, and with 4.9 × 10²The speed of rpm stirs, and adjusts pH value 4.9, insulated and stirred 130.9 minutes；Stop reaction later and stands 6.64 × 10 points Clock removes impurity；Suspension is added 133.9 parts of polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate, adjusts pH Value forms sediment purification lake water elution, obtains solid content at 4.192 × 103rpm of revolving speed by centrifuge 1.9, 2.407×10²It is dry at a temperature of DEG C, 0.192 × 103 mesh is crossed after grinding, it is spare；

Step 3：Silver nano-particle after separately taking alkali formula aphthenic acids zinc salt 133.9 and step 2 to handle, uses glancing incidence after mixing Low-angle gamma-rays diffusing reflection irradiation, the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 121.9MeV, dosage is 169.9kGy, irradiation time are 133.9 minutes, obtain the alkali formula aphthenic acids zinc salt and silver nano-particle mixture of character change； Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stir to stand in tower reactor, starting stirring is stood tower anti- The steam oil heater in device is answered, 132.9 DEG C of set temperature, the blender in vertical tower reactor is stirred in starting, and revolving speed is 124rpm, pH are adjusted to 4.9, are dehydrated 133.9 minutes, spare；

Step 4：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that step 3 is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazine -1,3,5 (2H, 4H, 6H) of 2,4,6-] three (cyclohexyl) that the methyl ethyl ketoxime that degree is 134.9mg/L blocks In 122.9 parts of isocyanates, the stirring that cocurrent adds to step 1 is stood in tower reactor, flow acceleration 269.9mL/min；It opens It is dynamic to stir vertical tower reactor blender, setting speed 138rpm；Stirring 4.9 minutes；Add 7- methyl octanal 121.9 Part, the steam oil heater in vertical tower reactor is stirred in starting, is warming up to 168.9 DEG C, pH is adjusted to 4.9, is passed through helium Ventilatory capacity is 123.9m3/min, and heat preservation stands 158.9 minutes；It is again started up the vertical tower reactor blender of stirring, revolving speed is 133rpm is added 130.9 parts of ester of (2E)-formic acid -2- hexen-1-ol, and pH is made to be adjusted to 4.9, and heat preservation stands 157.9 points Clock；

Step 5：The blender in vertical tower reactor, setting speed 130rpm are stirred in starting, and tower reaction is stood in starting stirring Steam oil heater in device sets and stirs temperature in vertical tower reactor as 1.287 × 10²DEG C, polyurethane is added It 140.9 parts of polymer, reacts 124.9 minutes；The rosolic acid cetyl ester 163.4 that mass concentration is 130mg/L is added later Part, the steam oil heater in vertical tower reactor is stirred in starting, set stirring and founds temperature in tower reactor as 208.9 DEG C, pH is adjusted to 4.9, and pressure 1.3MPa, the reaction time is 0.41 hour；It is depressurized to normal pressure later, is cooled to 124.9 DEG C and goes out Expect into molding press to get to decentralized network 3-2-8-8；

The partial size of the silver nano-particle is 138 μm.

Reference examples

Reference examples are tested for the property test using the decentralized network of certain commercially available brand.

Embodiment 4

Examples 1 to 3 and reference examples decentralized network obtained are tested for the property test, mechanical strength is mentioned after test The parameters such as the rate of liter, compression strength enhancing rate, anti-yield strength enhancing rate, wear rate enhancing rate are analyzed.Data analysis such as table 1 It is shown.

As seen from Table 1, decentralized network 3-2-8-8 of the present invention, mechanical strength enhancing rate, compression strength enhancing rate, Anti- yield strength enhancing rate, wear rate enhancing rate are above the product of prior art production.

In addition, as shown in figure 9, decentralized network 3-2-8-8 of the present invention is carried out with reference examples, with using the time Change test data statistics.Find out in figure, Examples 1 to 3 is substantially raw better than the prior art in test data technical indicator The product of production.

Claims (10)

1. one kind injects mixing arrangement for surface water runoff purifying plant cultivation block medicament, including：Shock-absorbing foot pad（1）, fixed Frame（2）, pushing mechanism（3）, work piece holder（4）, support platform（5）, control system（6）, rolling cutter（7）；Its feature exists In the fixed frame（2）For stainless steel rectangular structure, thickness is between 3cm~4cm；The shock-absorbing foot pad（1）Quantity is Four, it is respectively and fixedly installed to fixed frame（2）Bottom four corners；The support platform（5）For rectangle galvanized sheet, support platform （5）It is fixedly mounted on fixed frame（2）Top；The pushing mechanism（3）It is arranged in support platform（5）Side；The workpiece clamp Tool（4）It is arranged in support platform（5）The other side；The control system（6）It is fixedly mounted on fixed frame（2）On；

The rolling cutter（7）Positioned at pushing mechanism（3）Left side, the two connection；

The pushing mechanism（3）Equipped with slideway（3-2）；

The slideway（3-2）Equipped with medicament mixing device（3-2-8）；

The medicament mixing device（3-2-8）It is penetrated through for L-type pipe structure, both ends, medicament mixing device（3-2-8）Including：Medicament Import（3-2-8-1）, diffusant jet pipe（3-2-8-2）, diffusant enters pipe（3-2-8-3）, buffer subsystem（3-2-8-4）, stir ball （3-2-8-5）, stablize net（3-2-8-6）, spread horn mouth（3-2-8-7）, decentralized network（3-2-8-8）, diluent enters pipe（3- 2-8-9）, agent outlet（3-2-8-10）；

Medicament inlet positioned at one end（3-2-8-1）, medicament inlet（3-2-8-1）Right side is equipped with diluent and enters pipe（3-2-8- 9）, diluent enters pipe（3-2-8-9）One end is connected to external diluent bottle, and diluent enters pipe（3-2-8-9）The other end To be open, and it is inserted into diffusion horn mouth（3-2-8-7）It is internal；In diffusion horn mouth（3-2-8-7）Middle part is equipped with decentralized network（3- 2-8-8）, it is holey, vertical display；Spread horn mouth（3-2-8-7）For flared structure, the large diameter end direction right side Horn mouth is spread in side（3-2-8-7）The diameter of large diameter end and small-caliber end ratio is 3:1；The diffusant jet pipe（3-2-8-2） Positioned at diffusion horn mouth（3-2-8-7）Right side is hollow ring pipe structure, diffusant jet pipe（3-2-8-2）Ring pipe it is right Side surface is equipped with a large amount of through-holes, diffusant jet pipe（3-2-8-2）One end and diffusant enter pipe（3-2-8-3）Connection；The buffering Net（3-2-8-4）Enter pipe positioned at diffusant（3-2-8-3）Right side, buffer subsystem（3-2-8-4）For holey, vertical display；Institute State agitation ball（3-2-8-5）Positioned at buffer subsystem（3-2-8-4）Right side stirs ball（3-2-8-5）For macromolecule thin-walled hollow structure, Stir ball（3-2-8-5）Material density is less than the density of water, stirs ball（3-2-8-5）Quantity is 50~100, single to stir Ball（3-2-8-5）Quality is less than 10 grams, multiple agitation balls（3-2-8-5）It is limited at buffer subsystem（3-2-8-4）With stablize net（3- 2-8-6）Between, the agitation ball（3-2-8-5）For scattered distribution, ball is stirred（3-2-8-5）Mutual gap is greater than 5cm；The stable net（3-2-8-6）Positioned at agitation ball（3-2-8-5）Net is stablized on right side（3-2-8-6）For holey, vertically It puts；

Medicament is from medicament inlet（3-2-8-1）Into entering pipe with diluent（3-2-8-9）The diluent of ejection meets, and is dividing Dissipate net（3-2-8-8）, diffusion horn mouth（3-2-8-7）Under the action of, diluent is further dispersed and is mixed with medicament；

Diffusant enters pipe by diffusant（3-2-8-3）From diffusant jet pipe（3-2-8-2）It sprays, buffer subsystem（3-2-8-4）It is right The diffusant of ejection implements buffering, and enters together with medicament, diluent and be located at buffer subsystem（3-2-8-4）With stablize net（3-2- 8-6）Between agitation ball（3-2-8-5）Action space, in agitation ball（3-2-8-5）Under agitaion, diffusant, diluent, Medicament is sufficiently mixed, and mixture is from agent outlet（3-2-8-10）Discharge.

2. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 1 injects mixing arrangement, It is characterized in that, the pushing mechanism（3）Including：Slideway fixed block（3-1）, slideway（3-2）, sliding block（3-3）, speed regulating motor（3- 4）, fuel tank（3-5）, hydraulic cylinder（3-6）, push disk（3-7）, slide motor（3-8）, push disk brake apparatus（3-9）, speed regulation electricity Machine transmission shaft（3-10）；

Wherein, the slideway（3-2）Pass through slideway fixed block（3-1）With support platform（5）It is fixedly connected；The slideway（3-2） Cross section is in " Ω " shape, slideway（3-2）Quantity is 2；The sliding block（3-3）With slideway（3-2）It is slidably connected, sliding block（3- 3）End is provided with slide motor（3-8）, slide motor（3-8）Drive sliding block（3-3）In slideway（3-2）Upper sliding；The tune Speed motor（3-4）For variable-frequency motor, speed regulating motor（3-4）Pedestal and sliding block（3-3）It is welded and fixed；The speed regulating motor transmission shaft （3-10）One end and speed regulating motor（3-4）Connection, the other end pass through fuel tank（3-5）, push disk brake apparatus（3-9）, hydraulic cylinder （3-6）With promotion disk（3-7）It is fixedly connected, speed regulating motor（3-4）It drives and pushes disk（3-7）Rotation；The fuel tank（3-5）With liquid Cylinder pressure（3-6）The connection of one end conduit；The hydraulic cylinder（3-6）The other end and detachable promotion disk（3-7）Connection；The promotion disk Brake apparatus（3-9）Positioned at promotion disk（3-7）With hydraulic cylinder（3-6）Between the two；The speed regulating motor（3-4）, hydraulic cylinder（3- 6）, push disk（3-7）Central axis in the same horizontal line, pushes disk（3-7）With rolling cutter（7）Connection pushes disk（3-7） Drive rolling cutter（7）Rotation；

The speed regulating motor（3-4）, hydraulic cylinder（3-6）Pass through conducting wire and control system respectively（6）Control connection；

The slide motor（3-8）Pass through conducting wire and control system（6）Control connection.

3. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 2 injects mixing arrangement, It is characterized in that, the rolling cutter（7）Including：Driven wheel（7-1）, transformer（7-2）, cutting edge（7-3）, back-up roller bearing （7-4）, heating tube（7-5）, cutting edge spray head（7-6）, water inlet pipe（7-7）, intake port（7-8）, transmission shaft（7-9）；It is located at The driven wheel of one end（7-1）, it is connect with external cutter motor, meanwhile, driven wheel（7-1）With transmission shaft（7-9）It is fixed to connect It connects；In driven wheel（7-1）Side is equipped with back-up roller bearing（7-4）, the back-up roller bearing（7-4）Quantity is 2, is located at Transmission shaft（7-9）Both ends；The transmission shaft（7-9）Hollow structure, inside are equipped with transformer（7-2）, heating tube（7-5）, into Water pipe（7-7）；Water inlet pipe（7-7）It is parallel to transmission shaft（7-9）, water inlet pipe（7-7）Quantity be 3, water inlet pipe（7-7）With into Water end (W.E.) mouth（7-8）Connection, intake port（7-8）It is connected to external pump；Water inlet pipe（7-7）Periphery is equipped with heating tube（7-5）, add Heat pipe（7-5）Helical structure, heating tube（7-5）One end passes through conducting wire and transformer（7-2）Connection, transformer（7-2）It is another End is electrically connected by conducting wire with external city, heating tube（7-5）To water inlet pipe（7-7）Implement heating, transformer（7-2）To heating temperature Degree is implemented to adjust；In transmission shaft（7-9）Outside is equipped with cutting edge（7-3）, cutting edge（7-3）Quantity is 4,4 cutting edges（7- 3）Angularly, mode substantially symmetrical about its central axis is fixed on transmission shaft（7-9）On；In cutting edge（7-3）Root is equipped with cutting edge spray head（7- 6）, cutting edge spray head（7-6）Open at one end designs and is directed toward cutting edge（7-3）Knife face, cutting edge spray head（7-6）The other end with into Water pipe（7-7）Connection；

Driven wheel（7-1）Pass through transmission shaft（7-9）Drive cutting edge（7-3）Rotation, cutting edge（7-3）Material implementation is equidistantly cut It cuts；Meanwhile cutting edge spray head（7-6）To cutting edge（7-3）Knife face implements cleaning.

4. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 3 injects mixing arrangement, It is characterized in that, slideway（3-2）Equipped with cooling device, cooling device includes：By coolant liquid entrance（3-2-1）, heat-exchange tube（3-2- 2）, heat-exchanging chamber（3-2-3）, partition（3-2-4）, buffered room（3-2-5）, refrigerant inlet（3-2-6）, exported by coolant liquid （3-2-7）, medicament mixing device（3-2-8）, refrigerant exit（3-2-9）；

Positioned at side by coolant liquid entrance（3-2-1）With heat-exchanging chamber（3-2-3）Connection, and by coolant liquid entrance（3-2-1） Positioned at heat-exchanging chamber（3-2-3）Lower part, low level；It is described to be exported by coolant liquid（3-2-7）Positioned at heat-exchanging chamber（3-2-3）Top, A high position, and exported by coolant liquid（3-2-7）With heat-exchanging chamber（3-2-3）Connection；The heat-exchange tube（3-2-2）Positioned at heat exchange Room（3-2-3）Middle part, heat-exchange tube（3-2-2）Hollow structure, heat-exchange tube（3-2-2）Quantity be 20, more heat exchanges Pipe（3-2-2）Vertical equidistant arrangement；Heat-exchange tube（3-2-2）Both ends are respectively equipped with buffered room（3-2-5）, heat-exchange tube （3-2-2）Both ends respectively with the buffered room that is located at its upper and lower ends（3-2-5）Connection；The heat-exchanging chamber（3-2-3）It is logical Cross partition（3-2-4）With the buffered room of upper and lower ends（3-2-5）Separate；Superposed buffered room（3-2-5）, Top is equipped with refrigerant inlet（3-2-6）, the buffered room on top（3-2-5）With refrigerant inlet（3-2-6）Connection is located at lower part Buffered room（3-2-5）Its bottom is equipped with refrigerant exit（3-2-9）, the buffered room of lower part（3-2-5）With bottom Refrigerant exit（3-2-9）Connection；The medicament mixing device（3-2-8）With heat-exchanging chamber（3-2-3）Connection.

5. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 4 injects mixing arrangement, It is characterized in that, the promotion disk brake apparatus（3-9）Including：Brake cooling system（3-9-1）, traction mechanism（3-9-2）, braking Hauling rope（3-9-3）, brake caliper（3-9-4）, radiator fan（3-9-5）, friction plate（3-9-6）；Tune on central axes Speed motor transmission shaft（3-10）, it is surrounded by friction plate（3-9-6）, friction plate（3-9-6）Quantity is 4,4 friction plates （3-9-6）By speed regulating motor transmission shaft（3-10）It wraps up wherein, friction plate（3-9-6）Periphery be equipped with brake caliper（3-9- 4）, brake caliper（3-9-4）Ring-type is divided into pintongs, friction plate（3-9-6）It is fixed on brake caliper（3-9-4）Inside；Braking Chuck（3-9-4）Left side is equipped with radiator fan（3-9-5）, radiator fan（3-9-5）For brake caliper（3-9-4）Cooling；Braking Chuck（3-9-4）Periphery is equipped with braking hauling rope（3-9-3）, brake hauling rope（3-9-3）Around brake caliper（3-9-4）Four Week, and the two is hinged；Brake hauling rope（3-9-3）The other end and traction mechanism（3-9-2）Connection；In brake caliper（3-9- 4）Top is equipped with brake cooling system（3-9-1）, the two pass through conduit connect；

Traction mechanism（3-9-2）By braking hauling rope（3-9-3）By brake caliper（3-9-4）Tightening, promotes friction plate（3-9- 6）To speed regulating motor transmission shaft（3-10）Generation friction brake force is closely encircled, the heat that friction generates passes through radiator fan （3-9-5）, brake cooling system（3-9-1）Heat is taken away.

6. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 5 injects mixing arrangement, It is characterized in that, the work piece holder（4）Including：Rotating electric machine（4-1）, service chamber（4-2）, workpiece handgrip（4-3）, gear wheel （4-4）, central gear（4-5）, handgrip gear（4-6）, lap count（4-7）；Wherein, the gear wheel（4-4）It is arranged in Service chamber（4-2）Inside, gear wheel（4-4）For interior tooth type hollow structure, interior teeth are located at gear wheel（4-4）Internal circumference On, gear wheel（4-4）It is interior to be equipped with central gear（4-5）With handgrip gear（4-6）, central gear（4-5）, handgrip gear（4-6） For outer toothing；The central gear（4-5）Positioned at gear wheel（4-4）At central axes, in central gear（4-5）It is surrounded by and grabs Hand gear（4-6）, gear wheel（4-4）, central gear（4-5）, handgrip gear（4-6）Three engages connection；The handgrip gear （4-6）Quantity is three, surrounds central gear（4-5）It is circumferentially symmetrical；The rotating electric machine（4-1）It is fixedly mounted on inspection Repair case（4-2）Side, rotating electric machine（4-1）With central gear（4-5）It is drivingly connected；The workpiece handgrip（4-3）It is arranged in inspection Repair case（4-2）The other side, workpiece handgrip（4-3）One end and handgrip gear（4-6）It is fixedly connected；The lap count（4-7） It is fixedly connected on rotating electric machine（4-1）On turntable；

The rotating electric machine（4-1）, lap count（4-7）Pass through conducting wire and control system respectively（6）Control connection；

Rotating electric machine（4-1）Drive central gear（4-5）Rotation, and then drive three, periphery handgrip gear（4-6）Along canine tooth Wheel（4-4）Interior tooth does revolution motion, while three handgrip gears（4-6）Also it does rotation movement, handgrip gear（4-6）Pass through workpiece Handgrip（4-3）Drive workpiece revolution and rotation.

7. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 6 injects mixing arrangement, It is characterized in that, the workpiece handgrip（4-3）Including：Arm（4-3-1）, workpiece slot（4-3-2）, banjo traction splint（4-3-3）, work Part clamping degree inductor（4-3-4）；Wherein, the workpiece slot（4-3-2）It is arranged in arm（4-3-1）Top, workpiece slot（4-3- 2）For circular groove, diameter is 8cm~12cm；The banjo traction splint（4-3-3）Quantity is three, and circumference equidistantly divides Cloth is in workpiece slot（4-3-2）Around, banjo traction splint（4-3-3）End is equipped with antiskid protection pad and workpiece clamp tightness inductor （4-3-4）；

Banjo traction splint（4-3-3）Driving motor, workpiece clamp tightness inductor（4-3-4）Pass through conducting wire and control system respectively （6）Control connection.

8. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 7 injects mixing arrangement, It is characterized in that, the control system（6）Inside it is provided with timer, the timer and speed regulating motor（3-4）Actuating coil conducting wire Control connection.

9. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 8 injects mixing arrangement, It is characterized in that, the decentralized network（3-2-8-8）It is formed by high molecular material pressing mold, decentralized network（3-2-8-8）Constituent such as Under：

Purify 339.2~564.8 parts of lake water according to parts by weight, N- methyl-1,1,2,2,3,3,4,4,5,5,5- ten one fluoro- 131.5~173.6 parts of 1- pentane sulfonamide, 134.2~243.1 parts of methylbenzene of 1- (methoxy) -4-, 4- (methyl mercapto) fourth 130.4~147.4 parts of aldehyde, 133.1~190.3 parts of rutile, bis- [2- (2- the acrylic)] phenol of 4,4'- (1- methyl ethylidene) With 136.9~197.5 parts of polymer of (chloromethyl) ethylene oxide, 138.7~193.3 parts of silver nano-particle, polymerization oxidation 1,1,2,3,3,3,131.1~173.6 parts of-hexafluoro -1- propylene, the polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate 133.6~173.5 parts, 133.9~156.6 parts of zinc salt of alkali formula aphthenic acids, methyl ethyl ketoxime sealing end [2,4,6- tri- oxygen triazine -1, 3,5 (2H, 4H, 6H)-three bases] three 122.5~158.8 parts of (cyclohexyl) isocyanates, 121.2~164.8 parts of 7- methyl octanal, 130.8~175.4 parts of ester of (2E)-formic acid -2- hexen-1-ol, 140.3~184.3 parts of the polymer of polyurethane, mass concentration is 163.4~217.8 parts of the rosolic acid cetyl ester of 130mg/L~397mg/L.

10. a kind of surface water runoff purifying plant cultivation block medicament that is used for according to claim 9 injects mixing arrangement, It is characterized in that, decentralized network（3-2-8-8）Manufacturing process, comprise the steps of：

Step 1：In stirring vertical tower reactor, it is added and purifies lake water and N- methyl-1,1,2,2,3,3,4,4,5,5,5- ten The blender in vertical tower reactor is stirred in one fluoro -1- pentane sulfonamide, starting, and setting speed is 132rpm~178rpm, The steam oil heater in vertical tower reactor is stirred in starting, and temperature is made to rise to 147.2 DEG C~148.8 DEG C, and 1- (methoxy is added Ylmethyl) -4- methylbenzene stirs evenly, and carries out reaction 124.5~135.6 minutes, and 4- (methyl mercapto) butyraldehyde is added, is passed through flow For 123. 5 m³The m of/min~164. 4³The helium of/min 124.5~135.6 minutes；Later in stirring vertical tower reactor Rutile is added, is again started up the steam oil heater stirred in vertical tower reactor, make temperature rise to 164. 2 DEG C~ 197. 1 DEG C, keep the temperature 124. 4~135. 4 minutes, be added 4,4'- (1- methyl ethylidene) bis- [2- (2- acrylic)] phenol with The polymer of (chloromethyl) ethylene oxide, the pH value that solution in vertical tower reactor is stirred in adjustment is 4. 1~8. 3, heat preservation 124. 1~364. 1 minutes；

Step 2：Separately take silver nano-particle, by silver nano-particle power be 6.64KW~12.08KW under ultrasonication 0.130 After~1.197 hours；Silver nano-particle is added to another to stir in vertical tower reactor, it is 134 that mass concentration, which is added, The 1 of the polymerization oxidation of the mg/L of mg/L~364,1,2,3,3,3,-hexafluoro -1- propylene disperses silver nano-particle, and vertical tower is stirred in starting Steam oil heater in formula reactor makes solution temperature between 45 DEG C~89 DEG C, and vertical tower reactor is stirred in starting In blender, and with 4 × 10²Rpm~8 × 10²The speed of rpm stirs, and adjusts pH value between 4.5~8.8, insulated and stirred 130~197 minutes；Stop reaction later and stand 6.64 × 10~12.08 × 10 minutes, removes impurity；First is added in suspension The polymer of aldehyde and dicyanodiamide and ethylenediamine sulfate adjusts pH value between 1.5~2.8, forms sediment purification Lake water elution, by centrifuge in revolving speed 4.192 × 10³Rpm~9.643 × 10³Solid content is obtained under rpm, 2.407 × 10² DEG C~3.642 × 10²It is dry at a temperature of DEG C, 0.192 × 10 is crossed after grinding³~1.643 × 10³Mesh, it is spare；

Step 3：Silver nano-particle after separately taking alkali formula aphthenic acids zinc salt and step 2 to handle, uses the small angle of glancing incidence after mixing Gamma-rays diffusing reflection irradiation is spent, the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 121.2MeV~149.8MeV, agent Amount is 169.2kGy~209.8kGy, irradiation time is 133.2~158.8 minutes, obtains the alkali formula zinc naphthenate of character change Salt and silver nano-particle mixture；Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stirring and stand tower reaction In device, the steam oil heater in vertical tower reactor is stirred in starting, and 132.8 DEG C~178.4 DEG C of set temperature, starting is stirred Blender in vertical tower reactor, revolving speed are 124rpm~519rpm, and pH is adjusted between 4.3~8.3, dehydration 133.3~ 147.3 minute, spare；

Step 4：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that step 3 is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazine -1,3,5 (2H, 4H, 6H) of 2,4,6-] three that the methyl ethyl ketoxime that degree is the mg/L of 134 mg/L~364 blocks In (cyclohexyl) isocyanates, cocurrent add to step 1 stirring stand tower reactor in, flow acceleration be 269mL/min~ 997mL/min；Vertical tower reactor blender is stirred in starting, and setting speed is 138rpm~178rpm；Stirring 4~8 minutes；Again 7- methyl octanal is added, starting stirs the steam oil heater in vertical tower reactor, is warming up to 168.4 DEG C~205.8 DEG C, PH is adjusted between 4.4~8.8, and being passed through helium ventilatory capacity is 123.118m³/ min~164.273m³/ min, heat preservation stand 158. 2~188. 8 minutes；It is again started up the vertical tower reactor blender of stirring, revolving speed is 133rpm~178rpm, and (2E)-first is added Acid -2- hexen-1-ol ester, and pH is adjusted between 4.4~8.8, heat preservation stands 157. 5~197. 6 minutes；

Step 5：The blender in vertical tower reactor is stirred in starting, and setting speed is 130rpm~197rpm, and starting stirring is vertical Steam oil heater in tower reactor sets and stirs temperature in vertical tower reactor as 1.287 × 10²DEG C~2.32 ×10²DEG C, the polymer of polyurethane is added, reacts 124.2~135.1 minutes；Rosolic acid cetyl ester, starting are added later Stir the steam oil heater in vertical tower reactor, set stirring stand temperature in tower reactor as 208. 4 DEG C~ 264. 4 DEG C, pH is adjusted between 4. 1~8. 1, and pressure is 1.3MPa~1.31MPa, and the reaction time is 0.4~0.9 hour； It is depressurized to normal pressure later, is cooled to 124.2 DEG C~135.1 DEG C and discharges into molding press to get to decentralized network（3-2-8-8）；

The partial size of the silver nano-particle is 138 μm~148 μm；

The working method for surface water runoff purifying plant cultivation block medicament injection mixing arrangement, this method includes following Several steps：

Step 1：Object to be cut is encased in workpiece handgrip by treatment process（4-3）On workpiece slot（4-3-2）In, control system System（6）Control banjo traction splint（4-3-3）Work clamps process object；Workpiece clamp tightness inductor（4-3-4）Real-time monitoring Clamping degree is dealt with objects, when workpiece clamp tightness inductor（4-3-4）Detect that process object clamping degree reaches default value M When, workpiece clamp tightness inductor（4-3-4）Feedback signal is sent to control system（6）, control system（6）Control finger traction Folder（4-3-3）It stops working；

Step 2：At the same time, control system（6）Start sliding block（3-3）The slide motor of end（3-8）, in slide motor（3- 8）Under drive, sliding block（3-3）Along slideway（3-2）Sliding motion is done, to drive promotion disk（3-7）To being fixed on workpiece handgrip （4-3）The workpiece of end is close；Pushing disk（3-7）When apart from workpiece 3cm~5cm, control system（6）Stop slide motor （3-8）Work, while controlling hydraulic cylinder（3-6）Work；In hydraulic cylinder（3-6）Under driving, disk is pushed（3-7）Slowly leaned on to workpiece Closely, until pushing disk（3-7）Front end blade is in contact with process object end face；

Step 3：Control system（6）Start pushing mechanism simultaneously（3）In speed regulating motor（3-4）And work piece holder（4）In rotation Rotating motor（4-1）；In speed regulating motor（3-4）Under driving, disk is pushed（3-7）Do circular motion clockwise；In rotating electric machine（4-1） Under motor driven, workpiece handgrip（4-3）Pass through handgrip gear（4-6）Do counterclockwise circular motion；

Step 4：In rotating electric machine（4-1）In rotary course, lap count（4-7）Real-time monitoring rotating electric machine（4-1）Rotation Enclose number；Work as lap count（4-7）Detect rotating electric machine（4-1）When rotating cycle reaches default value R, lap count （4-7）Feedback signal is sent to control system（6）, control system（6）Control rotating electric machine（4-1）It stops working；

Step 5：In speed regulating motor（3-4）In the course of work, it is located at control system（6）In timer to speed regulating motor（3-4） Working time carries out timing；When timer, which adds up timing time, reaches default value T, control system（6）Stop speed regulation electricity Machine（3-4）；

Step 6：Control system（6）Control banjo traction splint（4-3-3）It unclamps, the workpiece handled well enters subsequent processing.