CN113603185A - Water sterilization apparatus overflows of UVC LED light source - Google Patents

Water sterilization apparatus overflows of UVC LED light source Download PDF

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Publication number
CN113603185A
CN113603185A CN202110880745.1A CN202110880745A CN113603185A CN 113603185 A CN113603185 A CN 113603185A CN 202110880745 A CN202110880745 A CN 202110880745A CN 113603185 A CN113603185 A CN 113603185A
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water
led lamp
lamp panel
stirring
light source
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王佳
桂建生
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Wuxi Haocheng Photoelectric Technology Co ltd
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Wuxi Haocheng Photoelectric Technology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • C02F1/32Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • C02F1/325Irradiation devices or lamp constructions
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/38Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols
    • C08G65/40Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols from phenols (I) and other compounds (II), e.g. OH-Ar-OH + X-Ar-X, where X is halogen atom, i.e. leaving group
    • C08G65/4012Other compound (II) containing a ketone group, e.g. X-Ar-C(=O)-Ar-X for polyetherketones
    • C08G65/4056(I) or (II) containing sulfur
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D171/00Coating compositions based on polyethers obtained by reactions forming an ether link in the main chain; Coating compositions based on derivatives of such polymers
    • C09D171/08Polyethers derived from hydroxy compounds or from their metallic derivatives
    • C09D171/10Polyethers derived from hydroxy compounds or from their metallic derivatives from phenols
    • C09D171/12Polyphenylene oxides
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/08Anti-corrosive paints
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/60Additives non-macromolecular
    • C09D7/61Additives non-macromolecular inorganic
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/32Details relating to UV-irradiation devices
    • C02F2201/322Lamp arrangement
    • C02F2201/3222Units using UV-light emitting diodes [LED]
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/32Details relating to UV-irradiation devices
    • C02F2201/322Lamp arrangement
    • C02F2201/3223Single elongated lamp located on the central axis of a turbular reactor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/38Boron-containing compounds
    • C08K2003/382Boron-containing compounds and nitrogen
    • C08K2003/385Binary compounds of nitrogen with boron
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/011Nanostructured additives

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
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  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Toxicology (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Physical Water Treatments (AREA)

Abstract

The invention discloses an overflowing water sterilizing device with a UVCLED light source, and relates to the technical field of drinking water sterilization.A drinking water is introduced into an inner cavity of a slow flow bottom cylinder from a water inlet pipe, an ultraviolet LED lamp panel works to release ultraviolet rays, the ultraviolet rays pass through a transparent waterproof shell to enter the drinking water to sterilize and disinfect the drinking water, and the drinking water is finally discharged from a water outlet pipe; when the ultraviolet LED lamp panel works, the heat released by the ultraviolet LED lamp panel is transferred to the plugging nut through the LED lamp panel base and finally transferred to water; this sterilizing equipment utilizes dark ultraviolet UVCLED technique to disinfect with overflowing water, and bactericidal effect is good, and the heat transfer to the aquatic with ultraviolet LED lamp plate release in the sterilization process in addition realizes the quick heat dissipation of ultraviolet LED lamp plate, can protect the shutoff nut through rust-resistant heat dissipation coating can not rusted by the water corrosion, prolongs the life of LED submodule piece, avoids the scale to influence quality of water simultaneously.

Description

Water sterilization apparatus overflows of UVC LED light source
Technical Field
The invention relates to the technical field of drinking water sterilization, in particular to an overflowing water sterilization device with a UVC LED light source.
Background
Along with the continuous progress and development of society, people pay more and more attention to their health, higher standards and requirements are provided for diet and drinking water health closely related to daily life, from the perspective of healthy drinking water, the national health department has a very clear drinking water health standard GB5749-2006, strict health indexes are provided for the quality of drinking water, modern water purification devices applying high and new technologies such as reverse osmosis are accelerating to step into thousands of households, and the drinking water health problem of people is improved, while in the process of purifying the water quality by applying various filtering means, a problem is often overlooked, namely the problem of secondary pollution of purified water, and the quality of the purified water is changed due to the influence of a storage environment or a transportation pipeline in the process of storing or transporting the purified water, so that the potential threat to the health of the drinking water is formed;
at present, for the secondary pollution of purified water, the most common problem is that bacterial colonies exceed the standard, in the drinking water standard GB5749-2006 of Ministry of health, the total number of the bacterial colonies in drinking water is definitely specified to be not more than 100cfu/mL, and the total number of the bacterial colonies of the purified water subjected to secondary pollution is usually far higher than the value, so that the health of users drinking water is damaged, therefore, measures are necessary to be taken, and the bacterial colonies in the purified water are sterilized and controlled to protect the water quality;
the existing relatively mature bacterial colony sterilizing technology in the market comprises ozone and ultraviolet sterilizing technology, wherein the ozone sterilizing technology inactivates bacterial viruses by utilizing the strong oxidizing property of ozone, but because the ozone has certain irritation to human respiratory mucosa, the concentration and dosage need to be accurately controlled in the using process, the mode is more applied to large-scale water plants or centralized water making at present and is rarely applied to consumer-grade application occasions, the other sterilizing technology is the ultraviolet sterilizing technology, and because the ultraviolet has the characteristics of broad-spectrum sterilization, no color, no odor and no by-product, the method is an ideal choice for consumer-grade sterilizing products;
at present, ultraviolet mercury lamps are more in the market, most ultraviolet sterilizing devices for flowing purified water adopt ultraviolet light sources, and ultraviolet rays are generated by a technology of discharging under high pressure of mercury vapor, because materials contain mercury, the environment is greatly damaged in use and subsequent waste treatment occasions, currently, along with the formal effective water-good convention in 2020 in China, the market urgently needs the upgrading and updating of the ultraviolet sterilizing technology for the trend of gradually going to the comprehensive prohibition of products containing mercury;
the novel generation light source adopting the deep ultraviolet UVC LED technology provides a chance for the regeneration of the ultraviolet sterilization technology, the ultraviolet LED has important application potential in the ultraviolet sterilization occasion due to the characteristics of small volume, no lead and no mercury in materials, environmental friendliness and the like, but the high-power ultraviolet LED has lower luminous efficiency (ultraviolet power/total power) due to the current technical limit of the ultraviolet LED, the high-power ultraviolet LED faces serious LED heating problem in the application process, the service life and the use effect of the product are reduced, a complex heat dissipation system needs to be considered in the application, and the cost of the sterilization system is invisibly increased;
in view of the above technical drawbacks, a solution is proposed.
Disclosure of Invention
In order to overcome the technical problems, the invention aims to provide an overflowing water sterilizing device of a UVC LED light source, which comprises: introducing drinking water into an inner cavity of the slow flow bottom cylinder from the water inlet pipe, starting the ultraviolet LED lamp panel, enabling the ultraviolet LED lamp panel to work to release ultraviolet rays, enabling the ultraviolet rays to penetrate through the transparent waterproof shell to enter the drinking water, sterilizing the drinking water, and finally discharging the drinking water from the water outlet pipe; ultraviolet ray LED lamp plate during operation release heat transmits to the shutoff nut through LED lamp plate base, later transmits to aquatic through the shutoff nut, has solved current high-power ultraviolet LED and has faced serious LED problem of generating heat in the application, has reduced the life-span and the result of use of product, has increased the problem of sterilization system cost.
The purpose of the invention can be realized by the following technical scheme:
an overflowing water sterilizing device of a UVC LED light source comprises a slow flow cavity and an LED sub-module, wherein the LED sub-module is installed on the slow flow cavity;
the slow flow cavity comprises a slow flow bottom cylinder, an upper cover, a water inlet pipe, a water outlet pipe, mounting holes, an O-shaped sealing ring, mounting grooves and a connecting port, the upper cover is arranged at the top of the slow flow bottom cylinder, a plurality of mounting holes are formed in the edge position of the upper cover, the upper cover is connected to the top of the slow flow bottom cylinder through the mounting holes through bolts, the O-shaped sealing ring is mounted at the joint of the slow flow bottom cylinder and the upper cover, the water inlet pipe and the water outlet pipe are symmetrically mounted at the top of the upper cover, the LED sub-modules are mounted on the upper cover in a penetrating mode, and the bottom ends of the LED sub-modules are located in the inner cavity of the slow flow bottom cylinder;
the LED submodule comprises a transparent waterproof shell, a mounting plate, a plugging nut, an LED lamp plate base, an ultraviolet LED lamp plate, a fixing groove, a threaded hole, a threaded column and a sealing groove, wherein a sealing ring is installed at the top and the bottom of the transparent waterproof shell, the transparent waterproof shell is sleeved outside the LED lamp plate base and the ultraviolet LED lamp plate, the ultraviolet LED lamp plate is installed on the LED lamp plate base, the mounting plate is installed at the top of the LED lamp plate base, the bottom of the LED lamp plate base is provided with the plugging nut, the plugging nut comprises a metal base body and an antirust heat dissipation coating coated on the metal base body, and the antirust heat dissipation coating is formed by the solidification of antirust heat dissipation coating.
As a further scheme of the invention: the mounting groove has been seted up to top one side of upper cover, the connector has been seted up to the intermediate position of mounting groove, the mounting panel passes through the bolt and installs in the mounting groove, transparent waterproof cover runs through the connector.
As a further scheme of the invention: the LED lamp panel base is characterized in that a sealing groove is formed in the top of the plugging nut, a threaded column is installed in the center of the sealing groove, a threaded hole is formed in the bottom of the LED lamp panel base, the threaded column is connected to the inner cavity of the threaded hole in a threaded mode, a fixing groove is formed in the side face of the LED lamp panel base, and the ultraviolet LED lamp panel is connected to the fixing groove through bolts.
As a further scheme of the invention: the preparation method of the antirust heat dissipation coating comprises the following steps:
a1: weighing 100 parts of temperature-resistant emulsion 150 parts, 50-70 parts of polytetrafluoroethylene emulsion, 50-100 parts of deionized water, 10-50 parts of heat-conducting filler, 0.2-1.5 parts of defoaming agent, 1-5 parts of flatting agent and 1-10 parts of curing agent according to parts by weight for later use;
a2: mixing the temperature-resistant emulsion, the polytetrafluoroethylene emulsion, deionized water and the heat-conducting filler, and then carrying out ultrasonic dispersion for 5-8min under the condition that the ultrasonic frequency is 45-65kHz to obtain dispersion liquid;
a3: and adding the defoaming agent, the flatting agent and the curing agent into the dispersion liquid, and shearing for 20-30min under the condition that the stirring speed is 800-1000r/min to obtain the antirust heat dissipation coating.
As a further scheme of the invention: the heat-conducting filler is one of graphene, a carbon nano tube and boron nitride, the defoaming agent is an organic silicon defoaming agent, the leveling agent is N-methylpyrrolidone, and the curing agent is a polyamide curing agent.
As a further scheme of the invention: the preparation method of the temperature-resistant emulsion comprises the following steps:
a11: adding anisole and acetic anhydride into a three-neck flask provided with a stirrer, adding anhydrous aluminum chloride while stirring under the conditions of ice water bath and stirring speed of 1000-2000r/min, continuing stirring until no hydrogen chloride is released after the addition is finished, cooling a reaction product to room temperature, introducing the reaction product into ice water, adding concentrated hydrochloric acid, stirring, standing for layering, extracting an aqueous phase with diethyl ether for 2-3 times, combining an organic phase with an extraction liquid, washing with distilled water and a sodium hydroxide solution for 2-3 times in sequence, drying with anhydrous magnesium sulfate, distilling under reduced pressure, collecting a fraction at 140 ℃ of 137-DEG, cooling and crystallizing to obtain an intermediate 1;
the reaction principle is as follows:
Figure BDA0003192179960000051
a12: adding the intermediate 1 and absolute ethyl alcohol into a three-neck flask provided with a stirrer, a reflux condenser tube and a constant-pressure dropping funnel, dropwise adding silicon tetrachloride while stirring under the condition that the stirring speed is 1000-2000r/min, controlling the dropwise adding speed to be 1 drop/s, continuously stirring and reacting for 10-20h after the dropwise adding is finished, adding deionized water 3-5 times at intervals of 5-10min each time, continuously stirring for 20-30min after the adding is finished, then adding a sodium hydroxide solution until the mixture turns from deep red to gray, carrying out vacuum filtration on reaction products, washing a filter cake for 2-3 times by using distilled water, then placing the filter cake into a vacuum drying box, drying the filter cake to constant weight under the condition of the temperature of 50-70 ℃, then carrying out reflux reaction for 30-50min by using an ethanol solution, then cooling the reaction products to room temperature, carrying out vacuum filtration and drying to obtain an intermediate 2;
the reaction principle is as follows:
Figure BDA0003192179960000052
a13: adding the intermediate 2 and dichloromethane into a three-neck flask provided with a stirrer, a gas-guide tube and a constant-pressure dropping funnel, stirring at the stirring rate of 300-500r/min until the intermediate 2 is completely dissolved, introducing nitrogen for protection, then adding a boron tribromide solution dropwise under the stirring rate of 1000-2000r/min while stirring, controlling the dropwise adding rate to be 1 drop/s, heating to 50-53 ℃ after dropwise adding, carrying out reflux reaction for 10-15h, reacting to room temperature after the reaction is finished, then adding concentrated hydrochloric acid, controlling the adding rate to be 1mL/min, then continuing stirring for 30-50min, carrying out reduced pressure evaporation to remove the solvent, carrying out vacuum suction filtration, washing a filter cake with distilled water for 2-3 times, drying, and then recrystallizing with a mixed solution to obtain an intermediate 3;
the reaction principle is as follows:
Figure BDA0003192179960000061
a14: adding the intermediate 3, 4' -difluorodiphenyl sulfone, anhydrous potassium carbonate, sulfolane and xylene into a three-neck flask provided with a stirrer, a gas-guide tube and a reflux condenser tube, introducing nitrogen for protection, heating to enable a solid solvent, then heating to 150-;
the reaction principle is as follows:
Figure BDA0003192179960000071
a15: adding temperature-resistant resin into chloroform, stirring and dissolving for 1-2h under the condition that the stirring speed is 300-;
a16: distilling the dispersion liquid for 2-3h under the protection of nitrogen gas at the temperature of 52-56 ℃, and then distilling for 30-60min under the condition of heating to 60-62 ℃ to obtain the temperature-resistant emulsion.
As a further scheme of the invention: the dosage ratio of the anisole, the acetic anhydride, the anhydrous aluminum chloride and the concentrated hydrochloric acid in the step A11 is 0.5 mol: 0.5-0.6 mol: 160 g: 10-20mL, wherein the mass fraction of the concentrated hydrochloric acid is 35-37%, and the mass fraction of the sodium hydroxide solution is 5-10%.
As a further scheme of the invention: the using amount ratio of the intermediate 1, the absolute ethyl alcohol, the silicon tetrachloride and the deionized water in the step A12 is 100 g: 300 mL: 0.2-0.3 mol: 100-150mL, wherein the mass fraction of the sodium hydroxide solution is 10-15%, and the mass fraction of the ethanol solution is 90-95%.
As a further scheme of the invention: the amount ratio of the intermediate 2, dichloromethane, boron tribromide solution and concentrated hydrochloric acid in step a13 was 10 g: 100mL of: 100mL of: 30mL, wherein the boron tribromide solution is a solution with the molar concentration of 1mol/L formed by dissolving boron tribromide in dichloromethane, and the mixed solution is prepared from trichloromethane and absolute ethyl alcohol according to the weight ratio of 10: 1 by volume ratio.
As a further scheme of the invention: the amount ratio of the intermediate 3, 4' -difluorodiphenyl sulfone, anhydrous potassium carbonate, sulfolane and xylene in step a14 was 0.15 mol: 0.3-0.5 mol: 80-90 g: 80-100 mL: 100-.
As a further scheme of the invention: the dosage ratio of the temperature-resistant resin, chloroform, methanol and sodium dodecyl sulfate aqueous solution in the step A15 is 150 g: 350-400 mL: 10-20 mL: 450-500mL, wherein the sodium dodecyl sulfate aqueous solution is sodium dodecyl sulfate according to the weight ratio of 1 g: 30mL of a solution formed by dissolving in deionized water.
The invention has the beneficial effects that:
according to the overflowing water sterilizing device with the UVC LED light source, drinking water is introduced into an inner cavity of a slow flow bottom cylinder from a water inlet pipe, an ultraviolet LED lamp panel is started, works to release ultraviolet rays, the ultraviolet rays penetrate through a transparent waterproof shell to enter the drinking water, the drinking water is sterilized and disinfected, the drinking water is finally discharged from a water outlet pipe, heat released by the ultraviolet LED lamp panel during working is transferred to a plugging nut through a base of the LED lamp panel, and then the heat is transferred to the water through the plugging nut;
this sterilizing equipment utilizes dark ultraviolet UVC LED technique to disinfect with overflowing water, excellent in sterilization effect, and the heat transfer to the aquatic with ultraviolet LED lamp plate release in the sterilization process, realize the quick heat dissipation of ultraviolet LED lamp plate, the life and the result of use of ultraviolet LED lamp plate have been improved, realize disinfecting fast with simple cooling system, the cost of sterilization system has been reduced, and this LED submodule piece is the bolt mounting on the upper cover, be convenient for take out the change, and the lower cylinder that slowly flows, bolted connection between the upper cover, be convenient for clear up the inner chamber of the lower cylinder that slowly flows, guaranteed the drinking water can not by secondary pollution when disinfecting the drinking water.
The invention relates to an overflowing water sterilizing device of a UVC LED light source, wherein a plugging nut comprises a metal substrate and an antirust heat dissipation coating coated on the metal substrate, the antirust heat dissipation coating is formed by solidifying an antirust heat dissipation coating, anisole and acetic anhydride are used as raw materials to react to generate an intermediate 1, then the intermediate 1 reacts to generate an intermediate 2, the intermediate 2 reacts to generate an intermediate 3, the intermediate 3 contains a large amount of hydroxyl groups and can be polymerized with 4, 4' -difluorodiphenyl sulfone to form a high polymer material, namely a temperature-resistant resin, the temperature-resistant resin is composed of a large amount of benzene rings, so the temperature-resistant resin has good high temperature resistance, emulsion is formed, is mixed with polytetrafluoroethylene emulsion and a heat-conducting filler to prepare the coating by using main raw materials, the polytetrafluoroethylene contains a large amount of C-F bonds, and the C-F bonds are the largest in chemical bonds, therefore, the corrosion resistance and the weather resistance are super strong, and the heat conducting fillers are all high heat conducting materials and can quickly transfer and guide heat out; therefore, the antirust heat dissipation coating can protect a metal substrate from rusting due to water corrosion, prolong the service life of the LED sub-module, simultaneously avoid the influence of water quality due to the water rust, simultaneously quickly transfer heat generated by the LED sub-module to water through the heat conducting filler, and solve the problem that a high-power ultraviolet LED faces serious LED heating in the application process.
Drawings
The invention will be further described with reference to the accompanying drawings.
FIG. 1 is a schematic structural diagram of an overflowing water sterilizing device with a UVC LED light source in the invention;
FIG. 2 is a schematic view of the inner structure of the slow flow bottom cylinder of the present invention;
FIG. 3 is a schematic view of the assembly of an LED sub-module of the present invention;
FIG. 4 is a top view of the upper cover of the present invention;
FIG. 5 is a schematic diagram of an LED sub-module of the present invention;
FIG. 6 is a connection view of the LED lamp panel base and the ultraviolet LED lamp panel in the invention;
FIG. 7 is a schematic structural view of an LED lamp panel base according to the present invention;
fig. 8 is a schematic structural view of the blocking nut of the present invention.
In the figure: 101. a slow flow bottom cylinder; 102. an upper cover; 103. a water inlet pipe; 104. a water outlet pipe; 105. mounting holes; 106. an O-shaped sealing ring; 107. mounting grooves; 108. a connecting port; 109. a transparent waterproof shell; 110. mounting a plate; 111. plugging the nut; 112. an LED lamp panel base; 113. an ultraviolet LED lamp panel; 114. fixing grooves; 115. a threaded hole; 116. a threaded post; 117. sealing the groove.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1:
referring to fig. 1 to 8, the embodiment is an overflowing water sterilizing device of a UVC LED light source, including a slow flow cavity and an LED sub-module, where the LED sub-module is installed on the slow flow cavity;
the slow flow cavity comprises a slow flow bottom cylinder 101, an upper cover 102, a water inlet pipe 103, a water outlet pipe 104, mounting holes 105, an O-shaped sealing ring 106, mounting grooves 107 and a connecting port 108, the upper cover 102 is arranged at the top of the slow flow bottom cylinder 101, a plurality of mounting holes 105 are formed in the edge position of the upper cover 102, the upper cover 102 is connected to the top of the slow flow bottom cylinder 101 through the mounting holes 105 through bolts, the O-shaped sealing ring 106 is mounted at the connecting position of the slow flow bottom cylinder 101 and the upper cover 102, the water inlet pipe 103 and the water outlet pipe 104 are symmetrically mounted at the top of the upper cover 102, the LED sub-modules are mounted on the upper cover 102 in a penetrating mode, and the bottom ends of the LED sub-modules are located in an inner cavity of the slow flow bottom cylinder 101;
the LED submodule includes transparent waterproof case 109, mounting panel 110, shutoff nut 111, LED lamp plate base 112, ultraviolet LED lamp plate 113, fixed slot 114, screw hole 115, threaded post 116 and seal groove 117, transparent waterproof case 109's top, the sealing washer is all installed to the bottom, transparent waterproof case 109 cup joints at LED lamp plate base 112, ultraviolet LED lamp plate 113's outside, ultraviolet LED lamp plate 113 installs on LED lamp plate base 112, mounting panel 110 is installed at LED lamp plate base 112's top, LED lamp plate base 112's bottom is provided with shutoff nut 111, shutoff nut 111 includes the metal base and coats the rust-resistant heat dissipation coating on the metal base, rust-resistant heat dissipation coating is formed by the solidification of rust-resistant heat dissipation coating.
An installation groove 107 is formed in one side of the top of the upper cover 102, a connection port 108 is formed in the middle of the installation groove 107, an installation plate 110 is installed in the installation groove 107 through bolts, and a transparent waterproof case 109 penetrates through the connection port 108.
A sealing groove 117 is formed in the top of the plugging nut 111, a threaded column 116 is installed in the center of the sealing groove 117, a threaded hole 115 is formed in the bottom of the LED lamp panel base 112, the threaded column 116 is connected to an inner cavity of the threaded hole 115 in a threaded mode, a fixing groove 114 is formed in the side face of the LED lamp panel base 112, and the ultraviolet LED lamp panel 113 is connected to the fixing groove 114 through bolts.
Example 2:
the embodiment is a preparation method of temperature-resistant emulsion, which comprises the following steps:
a11: adding 0.5mol of anisole and 0.55mol of acetic anhydride into a three-neck flask provided with a stirrer, adding 160g of anhydrous aluminum chloride under stirring in an ice water bath at a stirring speed of 1500r/min, continuing stirring after the addition is finished, cooling a reaction product to room temperature, introducing the reaction product into the ice water, adding 15mL of concentrated hydrochloric acid with the mass fraction of 37%, stirring, standing for layering, extracting an aqueous phase with diethyl ether for 3 times, combining an organic phase and an extract, washing with distilled water and a sodium hydroxide solution with the mass fraction of 5% for 3 times, drying with anhydrous magnesium sulfate, distilling under reduced pressure, collecting fractions with the temperature of 138 ℃, cooling and crystallizing to obtain an intermediate 1;
a12: adding 100g of intermediate 1 and 300mL of anhydrous ethanol into a three-neck flask provided with a stirrer, a reflux condenser tube and a constant-pressure dropping funnel, dropwise adding 0.25mol of silicon tetrachloride while stirring at a stirring rate of 1500r/min, controlling the dropwise adding rate to be 1 drop/s, continuously stirring and reacting for 15h after the dropwise adding is finished, adding 150mL of deionized water, continuously stirring for 250min after the adding is finished, then adding a sodium hydroxide solution with the mass fraction of 10%, carrying out vacuum filtration on a reaction product, washing a filter cake for 3 times by using distilled water, then placing the filter cake into a vacuum drying oven, drying to constant weight at the temperature of 60 ℃, then carrying out reflux reaction for 40min by using an ethanol solution with the mass fraction of 95%, cooling the reaction product to room temperature, carrying out vacuum filtration and drying to obtain an intermediate 2;
a13: adding 10g of intermediate 2 and 100mL of dichloromethane into a three-neck flask provided with a stirrer, a gas-guide tube and a constant-pressure dropping funnel, stirring until the intermediate 2 is completely dissolved under the condition of stirring speed of 400r/min, introducing nitrogen for protection, then dropwise adding 100mL of boron tribromide solution under the condition of stirring speed of 1500r/min while stirring, controlling the dropwise adding speed to be 1 drop/s, heating to 52 ℃ after dropwise adding, carrying out reflux reaction for 12 hours, reacting to room temperature after the reaction is finished, then adding 30mL of concentrated hydrochloric acid with the mass fraction of 37%, controlling the adding speed to be 1mL/min, then continuing stirring for 40min, carrying out reduced pressure evaporation, vacuum suction filtration, washing a filter cake with distilled water for 3 times, drying, and then recrystallizing with a mixed solution to obtain an intermediate 3;
a14: adding 0.15mol of the intermediate 3, 0.4mol of 4, 4' -difluorodiphenyl sulfone, 85g of anhydrous potassium carbonate, 90mL of sulfolane and 150mL of xylene into a three-neck flask provided with a stirrer, an air guide pipe and a reflux condenser tube, introducing nitrogen for protection, heating to enable a solid solvent to be heated, heating to 160 ℃, refluxing and dehydrating for 3h under the condition that the stirring speed is 400r/min, then heating to 210 ℃, continuing stirring for reaction for 8h, pouring a reaction product into hot water at 90 ℃ when the reaction is finished, then heating to boil for 3h, filtering, placing a filter cake into a vacuum drying oven, and drying to constant weight under the condition that the temperature is 65 ℃ to obtain a temperature-resistant resin;
a15: adding temperature-resistant resin into chloroform, stirring and dissolving for 2h under the condition that the stirring speed is 400r/min, then adding methanol, then adding sodium dodecyl sulfate aqueous solution, dispersing for 3min under the condition that the stirring speed is 3500r/min, then dispersing for 3min under the condition that the stirring speed is 4000r/min, and then dispersing for 2min under the condition that the stirring speed is 4500r/min to obtain dispersion liquid;
a16: distilling the dispersion liquid for 2h under the protection of nitrogen and at the temperature of 54 ℃, and then distilling for 40min under the condition of heating to 61 ℃ to obtain the temperature-resistant emulsion.
Example 3:
the embodiment is a preparation method of an antirust heat-dissipation coating, which comprises the following steps:
a1: weighing 100 parts of temperature-resistant emulsion, 50 parts of polytetrafluoroethylene emulsion, 50 parts of deionized water, 10 parts of boron nitride, 0.2 part of defoaming agent, 1 part of flatting agent and 1 part of curing agent in the example 2 according to the parts by weight for later use;
a2: mixing the temperature-resistant emulsion, the polytetrafluoroethylene emulsion, deionized water and the heat-conducting filler, and then ultrasonically dispersing for 5min under the condition that the ultrasonic frequency is 45kHz to obtain a dispersion liquid;
a3: and adding the defoaming agent, the flatting agent and the curing agent into the dispersion liquid, and shearing for 20min under the condition that the stirring speed is 800r/min to obtain the antirust heat dissipation coating.
Example 4:
the embodiment is a preparation method of an antirust heat-dissipation coating, which comprises the following steps:
a1: weighing 125 parts of temperature-resistant emulsion, 60 parts of polytetrafluoroethylene emulsion, 75 parts of deionized water, 30 parts of carbon nanotubes, 0.8 part of defoaming agent, 3 parts of flatting agent and 5 parts of curing agent in the example 2 according to the parts by weight for later use;
a2: mixing the temperature-resistant emulsion, the polytetrafluoroethylene emulsion, deionized water and the heat-conducting filler, and then carrying out ultrasonic dispersion for 7min under the condition that the ultrasonic frequency is 55kHz to obtain dispersion liquid;
a3: and adding the defoaming agent, the flatting agent and the curing agent into the dispersion liquid, and shearing for 25min under the condition that the stirring speed is 900r/min to obtain the antirust heat dissipation coating.
Example 5:
the embodiment is a preparation method of an antirust heat-dissipation coating, which comprises the following steps:
a1: weighing 150 parts of temperature-resistant emulsion, 70 parts of polytetrafluoroethylene emulsion, 100 parts of deionized water, 50 parts of graphene, 1.5 parts of defoaming agent, 5 parts of flatting agent and 10 parts of curing agent in the example 1 according to the parts by weight for later use;
a2: mixing the temperature-resistant emulsion, the polytetrafluoroethylene emulsion, deionized water and the heat-conducting filler, and then carrying out ultrasonic dispersion for 8min under the condition that the ultrasonic frequency is 65kHz to obtain dispersion liquid;
a3: and adding the defoaming agent, the flatting agent and the curing agent into the dispersion liquid, and shearing for 30min under the condition that the stirring speed is 1000r/min to obtain the antirust heat dissipation coating.
The performance of the rust inhibitive heat dissipating coatings of examples 3-5 were tested:
thermal conductivity: the thermal conductivity of the antirust heat dissipation coating is tested by a thermal conductivity tester according to MIL-I-49456A, GB5598-85 and ASTM-D5470-12 test standards and methods;
water resistance: the antirust heat dissipation coating is placed in water at the temperature of 80 ℃ for 72 hours to form adhesive force;
high temperature resistance: and (3) the antirust heat dissipation coating is adhered to the muffle furnace after being baked.
The results are shown in the following table:
sample (I) Example 3 Example 4 Example 5
Thermal conductivity/(W/m. K) 2.043 3.124 3.856
Water resistance/80 ℃ for 72h Class 1 and coating integrity Class 1 and coating integrity Class 1 and coating integrity
High-temperature resistance of 5h at 300 DEG C Class 1 and coating integrity Class 1 and coating integrity Class 1 and coating integrity
High-temperature resistance of 5h at 500 DEG C Class 2 and coating integrity Class 1 and coating integrity Class 1 and coating integrity
Referring to fig. 1 to 8, the operation of the device for sterilizing overflowing water with the UVCLED light source in this embodiment is as follows:
drinking water is introduced into the inner cavity of the slow flow bottom cylinder 101 from the water inlet pipe 103, the ultraviolet LED lamp panel 113 is started, the ultraviolet LED lamp panel 113 works to release ultraviolet rays, the ultraviolet rays penetrate through the transparent waterproof shell 109 to enter the drinking water, the drinking water is sterilized and disinfected, and the drinking water is finally discharged from the water outlet pipe 104;
ultraviolet LED lamp plate 113 during operation release heat transmits to shutoff nut 111 through LED lamp plate base 112, later transmits to aquatic through shutoff nut 111.
The data in the above table show that the antirust heat dissipation coating has good water resistance and high temperature resistance, can efficiently transfer heat released by the ultraviolet LED lamp panel during operation into water, and cannot be damaged after long-time use, so that the plugging nut is prevented from being corroded by water and rusted, the service life is shortened, and the water quality is influenced.
In the description herein, references to the description of "one embodiment," "an example," "a specific example" or the like are intended to mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The foregoing is illustrative and explanatory only and is not intended to be exhaustive or to limit the invention to the precise embodiments described, and various modifications, additions, and substitutions may be made by those skilled in the art without departing from the scope of the invention or exceeding the scope of the claims.

Claims (10)

1. The overflowing water sterilizing device of the UVC LED light source is characterized by comprising a slow flow cavity and an LED sub-module, wherein the LED sub-module is arranged on the slow flow cavity;
the slow flow cavity comprises a slow flow bottom cylinder (101), an upper cover (102), a water inlet pipe (103), a water outlet pipe (104), mounting holes (105), O-shaped sealing rings (106), mounting grooves (107) and a connecting port (108), the top of the slow flow bottom cylinder (101) is provided with the upper cover (102), the edge position of the upper cover (102) is provided with a plurality of mounting holes (105), the upper cover (102) is connected to the top of the slow flow bottom cylinder (101) through the mounting holes (105) in a bolt mode, the O-shaped sealing rings (106) are mounted at the connecting position of the slow flow bottom cylinder (101) and the upper cover (102), the water inlet pipe (103) and the water outlet pipe (104) are symmetrically mounted at the top of the upper cover (102), the LED sub-modules are mounted on the upper cover (102) in a penetrating mode, and the bottom ends of the LED sub-modules are located in an inner cavity of the slow flow bottom cylinder (101);
the LED sub-module comprises a transparent waterproof shell (109), a mounting plate (110), a blocking nut (111), an LED lamp panel base (112), an ultraviolet LED lamp panel (113), a fixing groove (114), a threaded hole (115), a threaded column (116) and a sealing groove (117), the top and the bottom of the transparent waterproof shell (109) are both provided with a sealing ring, the transparent waterproof shell (109) is sleeved outside the LED lamp panel base (112) and the ultraviolet LED lamp panel (113), the ultraviolet LED lamp panel (113) is arranged on the LED lamp panel base (112), the top of the LED lamp panel base (112) is provided with an installation plate (110), the bottom of the LED lamp panel base (112) is provided with a plugging nut (111), the plugging nut (111) comprises a metal base body and an antirust heat dissipation coating coated on the metal base body, wherein the antirust heat dissipation coating is formed by solidifying an antirust heat dissipation coating.
2. The overflowing water sterilizing device of the UVC LED light source as claimed in claim 1, wherein said top cover (102) is opened with a mounting groove (107) on one side of the top, a connection port (108) is opened in the middle of said mounting groove (107), said mounting plate (110) is installed in said mounting groove (107) by bolts, said transparent waterproof case (109) penetrates through said connection port (108).
3. The overflowing water sterilizing device of the UVC LED light source as claimed in claim 1, wherein said blocking nut (111) is formed with a sealing groove (117) at the top, a threaded post (116) is installed at the center of said sealing groove (117), a threaded hole (115) is formed at the bottom of said LED lamp panel base (112), said threaded post (116) is screwed into the inner cavity of said threaded hole (115), a fixing groove (114) is formed on the side of said LED lamp panel base (112), and said ultraviolet LED lamp panel (113) is bolted into said fixing groove (114).
4. The overflowing water sterilizing device of the UVC LED light source as claimed in claim 1, wherein said preparation method of the antirust heat-dissipating paint comprises the following steps:
a1: weighing 100 parts of temperature-resistant emulsion 150 parts, 50-70 parts of polytetrafluoroethylene emulsion, 50-100 parts of deionized water, 10-50 parts of heat-conducting filler, 0.2-1.5 parts of defoaming agent, 1-5 parts of flatting agent and 1-10 parts of curing agent according to parts by weight for later use;
a2: mixing the temperature-resistant emulsion, the polytetrafluoroethylene emulsion, deionized water and the heat-conducting filler, and then carrying out ultrasonic dispersion for 5-8min under the condition that the ultrasonic frequency is 45-65kHz to obtain dispersion liquid;
a3: and adding the defoaming agent, the flatting agent and the curing agent into the dispersion liquid, and shearing for 20-30min under the condition that the stirring speed is 800-1000r/min to obtain the antirust heat dissipation coating.
5. The overflowing water sterilizing device of the UVC LED light source as claimed in claim 4, wherein said temperature-resistant emulsion is prepared by the following steps:
a11: adding anisole and acetic anhydride into a three-neck flask provided with a stirrer, adding anhydrous aluminum chloride while stirring under the conditions of ice-water bath and stirring speed of 1000-;
a12: adding the intermediate 1 and absolute ethyl alcohol into a three-neck flask provided with a stirrer, a reflux condenser tube and a constant-pressure dropping funnel, dropwise adding silicon tetrachloride while stirring under the condition that the stirring speed is 1000-2000r/min, controlling the dropwise adding speed to be 1 drop/s, continuously stirring and reacting for 10-20h after the dropwise adding is finished, adding deionized water, continuously stirring for 20-30min after the adding is finished, then adding a sodium hydroxide solution, carrying out vacuum filtration on a reaction product, washing a filter cake for 2-3 times by using distilled water, then placing the filter cake into a vacuum drying box, drying the filter cake to constant weight under the condition that the temperature is 50-70 ℃, then carrying out reflux reaction for 30-50min by using an ethanol solution, then cooling the reaction product to room temperature, carrying out vacuum filtration and drying to obtain an intermediate 2;
a13: adding the intermediate 2 and dichloromethane into a three-neck flask provided with a stirrer, a gas-guide tube and a constant-pressure dropping funnel, stirring at the stirring rate of 300-500r/min until the intermediate 2 is completely dissolved, introducing nitrogen for protection, then adding a boron tribromide solution dropwise under the stirring rate of 1000-2000r/min while stirring, controlling the dropwise adding rate to be 1 drop/s, heating to 50-53 ℃ after dropwise adding, carrying out reflux reaction for 10-15h, reacting to room temperature after the reaction is finished, then adding concentrated hydrochloric acid, controlling the adding rate to be 1mL/min, then continuing stirring for 30-50min, carrying out reduced pressure evaporation, vacuum suction filtration, washing a filter cake with distilled water for 2-3 times, drying, and then recrystallizing with a mixed solution to obtain an intermediate 3;
a14: adding the intermediate 3, 4' -difluorodiphenyl sulfone, anhydrous potassium carbonate, sulfolane and xylene into a three-neck flask provided with a stirrer, a gas-guide tube and a reflux condenser tube, introducing nitrogen for protection, heating to enable a solid solvent, then heating to 150-;
a15: adding temperature-resistant resin into chloroform, stirring and dissolving for 1-2h under the condition that the stirring speed is 300-500r/min, then adding methanol, then adding sodium dodecyl sulfate aqueous solution, dispersing for 2-3min under the condition that the stirring speed is 3000-3500r/min, then dispersing for 2-3min under the condition that the stirring speed is 3800-4000r/min, and then dispersing for 1-2min under the condition that the stirring speed is 4200-4500r/min to obtain dispersion liquid;
a16: distilling the dispersion liquid for 2-3h under the protection of nitrogen gas at the temperature of 52-56 ℃, and then distilling for 30-60min under the condition of heating to 60-62 ℃ to obtain the temperature-resistant emulsion.
6. The excess flow water sterilization device of the UVC LED light source of claim 5, wherein the dosage ratio of the anisole, the acetic anhydride, the anhydrous aluminum chloride and the concentrated hydrochloric acid in the step A11 is 0.5 mol: 0.5-0.6 mol: 160 g: 10-20mL, wherein the mass fraction of the concentrated hydrochloric acid is 35-37%, and the mass fraction of the sodium hydroxide solution is 5-10%.
7. The overflowing water sterilizing device of the UVC LED light source as claimed in claim 5, wherein the dosage ratio of said intermediate 1, absolute ethyl alcohol, silicon tetrachloride and deionized water in step A12 is 100 g: 300 mL: 0.2-0.3 mol: 100-150mL, wherein the mass fraction of the sodium hydroxide solution is 10-15%, and the mass fraction of the ethanol solution is 90-95%.
8. The overflowing water sterilizing device of a UVC LED light source as claimed in claim 5, wherein the dosage ratio of said intermediate 2, dichloromethane, boron tribromide solution and concentrated hydrochloric acid in step A13 is 10 g: 100mL of: 100mL of: 30mL, wherein the boron tribromide solution is a solution with the molar concentration of 1mol/L formed by dissolving boron tribromide in dichloromethane, and the mixed solution is prepared from trichloromethane and absolute ethyl alcohol according to the weight ratio of 10: 1 by volume ratio.
9. The excess flow water sterilization device of UVC LED light source of claim 5, wherein, the dosage ratio of said intermediate 3, 4' -difluoro diphenyl sulfone, anhydrous potassium carbonate, sulfolane and xylene in step A14 is 0.15 mol: 0.3-0.5 mol: 80-90 g: 80-100 mL: 100-.
10. The overflowing water sterilizing device with the UVC LED light source as claimed in claim 5, wherein the dosage ratio of said temperature-resistant resin, chloroform, methanol and sodium dodecyl sulfate aqueous solution in step A15 is 150 g: 350-400 mL: 10-20 mL: 450-500mL, wherein the sodium dodecyl sulfate aqueous solution is sodium dodecyl sulfate according to the weight ratio of 1 g: 30mL of a solution formed by dissolving in deionized water.
CN202110880745.1A 2021-08-02 2021-08-02 Water sterilization apparatus overflows of UVC LED light source Pending CN113603185A (en)

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