CN207170961U - A kind of fast reaction prepares the device of nano material or nano composite material - Google Patents

A kind of fast reaction prepares the device of nano material or nano composite material Download PDF

Info

Publication number
CN207170961U
CN207170961U CN201721066790.9U CN201721066790U CN207170961U CN 207170961 U CN207170961 U CN 207170961U CN 201721066790 U CN201721066790 U CN 201721066790U CN 207170961 U CN207170961 U CN 207170961U
Authority
CN
China
Prior art keywords
storage container
pressure
nano
reaction
temperature control
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201721066790.9U
Other languages
Chinese (zh)
Inventor
万军喜
敖洪亮
戴金洲
周学楷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shenzhen Geluo New Material Technology Co., Ltd.
Original Assignee
Shenzhen City Grid Photoelectric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shenzhen City Grid Photoelectric Co Ltd filed Critical Shenzhen City Grid Photoelectric Co Ltd
Priority to CN201721066790.9U priority Critical patent/CN207170961U/en
Application granted granted Critical
Publication of CN207170961U publication Critical patent/CN207170961U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

The utility model provides the device that a kind of fast reaction prepares nano material or nano composite material, and it includes pressure materials storage container, knock-on reaction device and temperature control reaction vessel, and the knock-on reaction device is located at the upper opening of temperature control reaction vessel;Knock-on reaction device includes the centre gangway positioned at middle part, the honeycomb duct of even, symmetric is being provided with around centre gangway, angle between symmetrical honeycomb duct is 30 ~ 150 °, pressure materials storage container at least two, the entrance of one of pressure materials storage container and centre gangway is connected, and the symmetrical honeycomb duct of each two is connected with other pressure materials storage container respectively;The honeycomb duct, the extended line of centre gangway intersect at the lower section of knock-on reaction device and in the middle part of the cavitys of temperature control reaction vessel.The technical solution of the utility model, obtained nano material or the particle size distribution of nano composite material are narrow, pattern is homogeneous, reunite less, stability and uniformity are good.

Description

A kind of fast reaction prepares the device of nano material or nano composite material
Technical field
The utility model belongs to nano material preparation facilities technical field, more particularly to a kind of fast reaction prepares nanometer material The device of material or nano composite material.
Background technology
Nano material receives extensive concern because it has the unexistent unique physical of block materials, chemical property, profit With these characteristics, nano material can be widely used in including biological medicine, environmental treatment, catalysis, new energy, electric Deng the almost all industrial circle including field.According to statistics, global nanometer technology relevant market scale just reached in 2009 91,000,000,000 dollars, and the related product quantity of every 3 years nano materials and related practitioner will double, to 2020 Year, market scale is estimated up to 3 trillion dollars, and provides about 6,000,000 work positions, therefore countries in the world are all attached great importance to receive The industrialization of rice material.
The performance of nano material, price and application are largely relevant with its preparation method, by researching and developing for many years, people Have been able to prepare the nano material of different morphologies and structure using a variety of methods under lab.Wherein with atom, divide Son is elementary cell, and the wet chemistry method route of nano material is prepared by atom, the aggregation of molecule and assembling, has equipment letter Single, raw material is readily available, purity is high, uniformity is good, chemical composition control is accurate, is easy to the advantages that amplification, becomes current reality Test the preparation method of nano material widely used in room and industrial production.
Generally, wet chemistry method prepares nano material and all carried out in a kettle, is added successively into reactor various Reaction raw materials, under mechanical stirring material hybrid reaction prepare nano material.For a chemical reaction process, three pass That is momentum transmission, heat transfer and mass transfer, and an anti-i.e. chemical reaction influences each other and interwoveness.For some reactions Speed is slow, three pass less demanding reaction, is suitable using still reaction.And reacted for those in less than one minute just Carry out for complete fast reaction, three biography speed of still reaction just obviously do not catch up with reaction speed, so that prepared obtain Nano material have that serious Size Distribution is wide, the problems such as serious, stability and uniformity difference of reuniting.
In the reaction of reduction method for preparing nanometer silver, such as using sodium borohydride or hydrazine hydrate as reducing agent, with silver nitrate Solution reaction prepares silver nano-grain, sodium borohydride or hydrazine hydrate solution once being contacted with silver nitrate solution, will react rapidly And release substantial amounts of bubble.Nano-Ag particles, the boron of addition are prepared using this method if in the reactor of big volume Sodium hydride or hydrazine hydrate solution may not realize the uniform mixing in silver nitrate solution before starting the reaction, may result in The nano-Ag particles first reflected are as seed, and the nano-Ag particles that subsequent reaction product makes to have generated constantly are grown up, So that final product particle size distribution is wide, pattern heterogeneity.
In addition, in the course of reaction of nano-Ag particles is prepared using chemical reduction method, it is easy in the device of reaction vessel One layer of fine and close silver layer of attachment generation, the presence of silver layer can influence the progress of following reaction on wall so that newly-generated silver is preferential It is attached on the silver layer, with the lasting progress of reaction, the silver layer progressive additive, and under the continuous impact of reaction liquid stream, into The stripping of piece comes off, and seriously affects the stability and uniformity of final product.The materials such as conventional glass, metal, silver It is easy to be attached to above, therefore, how selects manufacture silver to be unable to the reaction vessel just always Nano Silver preparation of apposition growth During the biggest problem.
Therefore, very high requirement, product and easy apposition growth on the wall are passed quickly, to three for this kind of reaction speed Simple-substance nano silvery or silver composite material reaction for, to realize to the stably and controllable of reaction, and large-scale industry is raw Production, it is necessary to research and develop the reaction unit and method of novelty.
Utility model content
For above technical problem, the utility model discloses a kind of fast reaction to prepare nano material or nano combined material The device of material, solve the three of fast reaction and pass and hit the reaction that crosses with the unmatched problem of reaction speed, another aspect liquid stream Area does not contact among container cavity with wall, solves the problems, such as that reaction product is attached on wall well, is particularly suitable for The large-scale production of simple-substance nano silvery or argentum nano composite material.
On the other hand, the technical solution adopted in the utility model is:
A kind of fast reaction prepares the device of nano material or nano composite material, it include pressure materials storage container, Knock-on reaction device and temperature control reaction vessel, the knock-on reaction device are located at the upper opening of temperature control reaction vessel;The shock Reactor includes the centre gangway positioned at middle part, the honeycomb duct of even, symmetric is being provided with around centre gangway, relatively Honeycomb duct between angle be referred to as 30 ~ 150 °, the pressure materials storage container at least two, one of pressure materials The entrance of storage container and centre gangway connect, the symmetrical honeycomb duct of each two respectively with other pressure materials storage container Connection;The honeycomb duct, the extended line of centre gangway intersect at the lower section of knock-on reaction device and positioned at the chambers of temperature control reaction vessel In the middle part of body, the side wall of the temperature control reaction vessel is provided with steam vent.Wherein, the honeycomb duct at least two.
Wherein, pressure materials storage container is used for storage reaction raw material, and keeps certain pressure, enable reaction raw materials with Certain speed is mutually hit.Further, the pressure materials storage container can be with the dress equipped with high voltage protective gas Connection is put, to keep certain pressure.
The knock-on reaction device is the core component for guiding knock-on reaction to occur.The passage in center is a kind of reaction mass Honeycomb duct, even number honeycomb duct is symmetrically furnished with the circle apart from centre gangway certain distance, as another or other are a variety of The honeycomb duct of reaction mass.If a variety of reaction masses, then a variety of reaction mass arranged for interval.Wherein, centre gangway is corresponding One pressure materials storage container, the corresponding pressure materials storage container of the symmetrical honeycomb duct of edge each two, and it is symmetrical Angle between water conservancy diversion duct so collects in knock-on reaction device between 30 ~ 150 ° by a variety of reaction masses of honeycomb duct Below, between 30 ~ 150 °, liquid stream crosses with reaction zone among the cavity of temperature control reaction vessel liquid stream intersection angle, would not be with Reactor wall contacts.Reaction mass mixes in liquid stream confluence high-speed impact, while completes to react.Hit due to several bursts of liquid streams and The region distance wall of reaction farther out, therefore will not be disturbed by wall, can be considered that homogeneous nucleation is reacted.Continuous reaction side Formula ensure that the continual and steady progress of reaction, it is easy to realize scale volume production.And relatively spacious knock-on reaction region with And the presence of steam vent, for heat release and there is the reaction of gaseous volatilization can also be compatible.
Further, the product of fast ram reaction falls on the bottom of temperature control reaction vessel, makees in the stirring of agitating device Under, make the complete material reaction of unreacted complete, while stirring action also prevents product from settling and reuniting.Reaction Complete product is flowed into product storage container, through further ripening, you can filtering, washing obtain final nanometer Material or nano composite material.
Above-mentioned technical proposal use liquid stream knock-on reaction mode on the one hand solve well fast reaction three pass and The unmatched problem of reaction speed, another aspect liquid stream are hit and cross reaction zone among container cavity, do not contacted with wall, are solved The problem of reaction product of having determined is attached on wall.
The reaction unit have reaction speed is fast, simple to operate, controllability is strong, it is applied widely, amplification easily etc. it is a variety of Advantage, a variety of nano materials or nano composite material, including but not limited to nanometer are prepared particularly suitable for industrialization fast reaction Metal simple-substance particle, nano-oxide and nano composite material etc..
As further improvement of the utility model, the angle between symmetrical honeycomb duct is 60 ~ 120 °.
As further improvement of the utility model, the bottom of the temperature control reaction vessel is provided with agitating device.Using this Technical scheme, by the further hybrid reaction of agitation of agitating device and scattered, reactant is fully reacted and prevent from reuniting.
As further improvement of the utility model, the fast reaction prepares the dress of nano material or nano composite material Put and be provided with discharging opening, the product storage container and discharging opening including product storage container, the bottom of the temperature control reaction vessel Connection.Temperature control reaction vessel can carry out appropriate control to the temperature of conversion zone, expand the scope of application of the present apparatus.Instead Complete product is answered to be flowed into product storage container, through further ripening, you can filtering, washing obtain final receive Rice material or nano composite material.
Further, the bottom of the temperature control reaction vessel is concave surface, and product can also be collected.Temperature control reaction is held The bottom of device is plane at the agitating paddle of agitating device.
As further improvement of the utility model, the fast reaction prepares the dress of nano material or nano composite material Put including high voltage protective gas container, raw storage container, the high voltage protective gas container respectively by air gauge with least Two pressure materials storage container connections, the quantity of the raw storage container are not less than the quantity of pressure materials storage container, The raw storage container is connected with pressure materials storage container respectively.
Wherein, high voltage protective gas container is used to provide the gas with certain pressure, for assigning and keeping pressure former Expect that the pressure in storage container is constant, enable centre gangway of the reaction precursor solution with higher flow velocity in knock-on reaction device With high-speed impact, while complete to mix and react at an angle under the guiding of honeycomb duct.Pressure materials storage container is used for Storage reaction raw material, and be connected with high voltage protective gas container to keep certain pressure, enable reaction raw materials with certain Speed is mutually hit.Air gauge is used for the pressure for monitoring and adjusting gas.
As further improvement of the utility model, the raw storage container includes the first raw storage container and second Raw storage container, the pressure materials storage container includes first pressure raw storage container and the storage of second pressure raw material is held Device, first raw storage container are connected with first pressure raw storage container, second raw storage container and second Pressure materials storage container is connected, and the first pressure raw storage container is connected with centre gangway, the second pressure raw material Storage container is connected with the symmetrical honeycomb duct of centrally located channel circumference.
As further improvement of the utility model, the raw storage container is held by peristaltic pump and pressure materials storage Device connects.Wherein, the peristaltic pump is used for realizing continuously transmitting for material.
As further improvement of the utility model, agitating device is provided with the raw storage container.
Using said apparatus when carrying out nano material or prepared by nano composite material, comprise the following steps:
Step S1, the mixture of metal salt solution or metal salt and nano particle and surfactant is added to the In one raw storage container;Reducing agent or precipitating reagent are added in the second raw storage container;
Step S2, the temperature control system of temperature control reaction vessel is opened, is maintained at the temperature of temperature control reaction vessel interior Required temperature;
Step S3, the first raw storage container, the raw material in the second raw storage container is set to separately flow into first pressure original Expect in storage container and second pressure raw storage container, and open high voltage protective gas container simultaneously, make high voltage protective gas Respectively enter in first pressure raw storage container and second pressure raw storage container;
The liquid of step S4, first pressure raw storage container and second pressure raw storage container enters under pressure Enter knock-on reaction device, by the centre gangway of knock-on reaction device, honeycomb duct with certain speed knock-on reaction device lower section phase Mutually hit concurrently raw reaction;After reaction, product drops to the bottom of temperature control reaction vessel.
Further, the fluid pressure in the pressure stock chest is maintained at 0.2 ~ 0.5MPa.
Further, the metal salt includes silver nitrate, silver acetate, gold chloride, chlorine palladium acid, chloroplatinic acid, copper sulphate, sulfuric acid One or more mixtures in nickel, nickel nitrate, nickel chloride, copper nitrate, copper chloride;The nano particle be carbon nanomaterial, One or more in metal oxide nano-material, metal nano material, polymer nano material and composite nano materials Mixture;The surfactant includes PVP(Polyvinyl pyrrolidone, polyvinylpyrrolidone)、CTAB (Cetyltrimethyl Ammonium Bromide, cetyl trimethyl ammonium)、CTAC (Cetyltrimethylammonium chloride, cetyltrimethylammonium chloride), it is sodium citrate, F127, P123, thin One or more mixture therein such as born of the same parents' cellulose, aliphatic acid, oleic acid;The reducing agent include sodium borohydride, hydrazine hydrate, One or more mixtures in formaldehyde, citric acid, potassium borohydride, ascorbic acid, the precipitating reagent include sodium hydroxide, ammonia One or more mixtures in water, potassium hydroxide, sodium carbonate, sodium acid carbonate.Wherein, P123 and F127 is that three block is gathered Compound, full name are polyoxyethylene-poly-oxypropylene polyoxyethylene, and its molecular formula is PEO-PPO-PEO.
It should be noted that the above method is illustrated by taking two kinds of reaction masses as an example, but it is not intended that this practicality is new Type is only applicable to include the preparation method of two kinds of reaction masses, increases corresponding raw material tank diameter, peristaltic pump, pressure stock chest simultaneously It is equipped with the nano material preparation that suitable multi-pore channel knock-on reaction device goes for two or more materials.
Compared with prior art, the beneficial effects of the utility model are:
The technical solution of the utility model, using continuous production mode, simple to operate, controllability is strong, amplification is easy, uses Liquid stream knock-on reaction mode on the one hand solve well fast reaction three pass and the unmatched problem of reaction speed, it is another Aspect liquid stream is hit and crosses reaction zone among container cavity, is not contacted with wall, solves reaction product well and be attached to The problem of on wall.The nano material or the particle size distribution of nano composite material that are obtained using the device are narrow, pattern is homogeneous, Reunite less, stability and uniformity it is good.
The apparatus and method are applied to a variety of nano materials that fast reaction can be used to prepare, including but not limited to nanometer Metal simple-substance particle, nano-oxide and nano composite material etc.;Particularly suitable for simple-substance nano silvery or silver nanoparticle composite wood The production of material.
Brief description of the drawings
Fig. 1 is that the structure for the device that a kind of fast reaction of the present utility model prepares nano material or nano composite material is shown It is intended to.
Fig. 2 is the knock-on reaction device diagrammatic cross-section involved by utility model.
Fig. 3 is the knock-on reaction device schematic top plan view of utility model embodiment 2, and wherein knock-on reaction device is 7 ducts.
Fig. 4 is that the pod apertures reaction mass of Fig. 3 knock-on reaction device arranges schematic diagram.
Fig. 5 is the stereoscan photograph of the silver nano-grain prepared by embodiment 3.
Fig. 6 is using the stereoscan photograph of the silver nano-grain prepared by 5L reactors in comparative example 1.
Reference includes:1- high pressure inert gas cylinders, 2- gas gauges, 3- the first raw material tank diameters, the raw materials of 4- second Tank diameter, 5- peristaltic pumps, 6- first pressure stock chests, 7- second pressure stock chests, 8- knock-on reaction devices, 9- steam vents, 10- Temperature control reaction vessel, 11- agitators, 12- product holding tanks;21- centre gangways, 22- honeycomb ducts, 23- cross impingement region.
Embodiment
Below by specific embodiment and with reference to accompanying drawing, the utility model is described in further detail.Following examples Only it is that the utility model is further detailed, should not be understood as to limitation of the present utility model.
Embodiment 1
As shown in Fig. 1 ~ Fig. 2, a kind of fast reaction prepares the device of nano material or nano composite material, and it includes high pressure Inertia gas cylinder 1, gas gauge 2, raw material tank diameter, peristaltic pump 5, pressure stock chest, knock-on reaction device 8, temperature control reaction vessel 10th, product holding tank 12, the knock-on reaction device 8 are located at the upper opening of temperature control reaction vessel 10;The knock-on reaction device 8 Including the centre gangway 21 positioned at middle part, the honeycomb duct 22 of even, symmetric is being provided with around centre gangway 21, relatively Honeycomb duct 22 between angle be referred to as 30 ~ 150 °, the raw material tank diameter includes the first raw material tank diameter 3 and the second raw material and stirred Groove 4 is mixed, the pressure stock chest includes first pressure stock chest 6 and second pressure stock chest 7, the first raw material tank diameter 3 It is connected by peristaltic pump 5 with first pressure stock chest 6, the second raw material tank diameter 4 passes through peristaltic pump 5 and second pressure storing Groove 7 connects.The high pressure inert gas cylinder 1 is connected by gas gauge 2 with two pressure stock chests respectively.The first pressure Stock chest 6 is connected with centre gangway 21, the symmetrical honeycomb duct around the second pressure stock chest 7 and centrally located passage 21 22 connections.
The honeycomb duct 22, the extended line of centre gangway 21 intersect at the lower section of knock-on reaction device 8 and reacted positioned at temperature control In the middle part of the cavity of container 10, the impingement region 23 that crosses is formed.The side wall of the temperature control reaction vessel 10 is provided with steam vent 9, the temperature The bottom of control reaction vessel 10 is provided with agitator 11.The bottom of the temperature control reaction vessel 10 is provided with discharging opening, the discharging opening It is connected with product holding tank 12.Agitating device is provided with the raw material tank diameter.
Each device links together as shown in Figure 1 by more than, just constitutes a set of suitable for fast reaction preparation nanometer material The process units of material or nano composite material.
The method that nano material or nano composite material are prepared using said apparatus fast reaction, is comprised the following steps:
Step S1, the temperature control system of temperature control reaction vessel 10 is opened, protects the temperature inside temperature control reaction vessel 10 Hold in required temperature;
Step S2, the mixture of metal salt solution or metal salt and nano particle and surfactant is added to the In one raw material tank diameter 3;Reducing agent or precipitating reagent are added in the second raw material tank diameter 4;
Step S3, the first raw material tank diameter 3, the material in the second raw material tank diameter 4 is set to separately flow into first pressure storing In groove 6 and second pressure stock chest 7, and high pressure inert gas cylinder 1 is opened simultaneously, high voltage protective gas is respectively enterd first pressure In stock chest 6 and second pressure stock chest 7;
The material of step S4, first pressure stock chest 6 and second pressure stock chest 7 enters knock-on reaction under pressure Device 8, crossed and hit in the lower section of knock-on reaction device 8 with certain speed by the centre gangway 21 of knock-on reaction device 8, honeycomb duct 22 Area 23 is hit mutually to hit and react;After reaction, product drops to the bottom of temperature control reaction vessel 10.Fast ram reaction Product falls on the bottom of temperature control reaction vessel 10, under the stirring action of agitator 11, makes the complete material reaction of unreacted complete Entirely, while stirring action also prevents product from settling and reuniting.React complete product and be flowed into product holding tank 12 In, through further ripening, you can filtering, washing obtain final nano material or nano composite material.
Wherein, the metal salt include silver nitrate, silver acetate, gold chloride, chlorine palladium acid, chloroplatinic acid, copper sulphate, nickel sulfate, One or more mixtures in nickel nitrate, nickel chloride, copper nitrate, copper chloride.The nano particle is carbon nanomaterial, metal It is one or more mixed in oxide-based nanomaterial, metal nano material, polymer nano material and composite nano materials Compound.The surfactant includes PVP, CTAB, CTAC, sodium citrate, F127, P123, cell cellulose, aliphatic acid, oil One or more mixture therein such as acid.The reducing agent includes sodium borohydride, hydrazine hydrate, formaldehyde, citric acid, hydroboration One or more mixtures in potassium, ascorbic acid, the precipitating reagent include sodium hydroxide, ammoniacal liquor, potassium hydroxide, carbonic acid One or more mixtures in sodium, sodium acid carbonate.
Embodiment 2
On the basis of embodiment 1, as shown in Figure 3 and Figure 4, the knock-on reaction device 8 includes leading to positioned at the center at middle part Road 21, around centre gangway 21 be provided with even, symmetric honeycomb duct 22, the honeycomb duct 22 totally 6, two-by-two with It is symmetrical arranged centered on centre gangway 21, the angle between symmetrical honeycomb duct 22 is 30 ~ 150 °.
When being produced using said apparatus, the symmetrical honeycomb duct 22 of each two is respectively used to a kind of stream of material Enter, knock-on reaction device 8 one as shown in Figure 4 shares six honeycomb ducts 22, and 4 kinds of materials are can be used for together with centre gangway 21 Flow into, i.e., centre gangway 21 is used for material 1, and six honeycomb ducts 22 are symmetrically used for material 2, material 3 and material 4 two-by-two.
Embodiment 3
The continuous reaction system and method provided using embodiment 1 prepares silver nanoparticle colloidal sol, comprises the following steps:
The mixed solution of a certain amount of silver nitrate, PVP is added in the first raw material tank diameter 3, by a certain amount of boron hydrogen Change sodium solution to be poured into the second raw material tank diameter 4, start agitator 11 and be thoroughly mixed.Open peristaltic pump 5, the first raw material Liquid in tank diameter 3, the second raw material tank diameter 4 is flowed into first pressure stock chest 6 and second pressure stock chest 7.It is same with this When open high pressure inert gas cylinder 1 and gas is entered in first pressure stock chest 6 and second pressure stock chest 7, make pressure stock chest In fluid pressure be maintained at 0.2MPa.Before experiment starts, the temperature control device of temperature control reaction vessel 10 is opened, makes reactor area Temperature be maintained at 25 DEG C.
Raw material enters knock-on reaction device 8, by centre gangway 21 and honeycomb duct 22 with certain speed in knock-on reaction device 8 The impingement region 23 that crosses of lower section mutually hit and react.After reaction, product drops to the bottom of temperature control reaction vessel 10, By the further hybrid reaction of agitation of agitator 11 and scattered, reactant is fully reacted and prevent from reuniting, flow ultimately into production In thing holding tank 12, silver nano-grain colloidal sol has been obtained.Fig. 5 is the stereoscan photograph of prepared silver nano-grain, it is seen that chi Very little narrowly distributing, pattern are homogeneous.In addition, the metal nanoparticle such as nanogold, Platinum Nanoparticles, Technique of Nano Pd can also pass through this device Prepared with method.
Comparative example 1
As a comparison, in 5L stirred autoclave, using reactant concentration similarly to Example 2 and proportioning, three In the case that leaf formula twisted stir paddle rotating speed is 350rpm, to silver nitrate, PVP mixed solution and dripping sodium borohydride solution, The stereoscan photograph of reaction product is shown in Fig. 6, and its nanoparticle agglomerates is serious, and pattern is complicated, and uniformity is poor.
Contrast by Fig. 5 and Fig. 6 is visible, and the silver nanoparticle sol size obtained using the technical scheme of embodiment 2 is distributed Narrow, pattern is homogeneous.
Embodiment 4
The continuous reaction system and method provided using embodiment 1 prepares silver cladding nickel Nano sol, and it includes following step Suddenly:
The mixed solution of a certain amount of silver nitrate, hydroxyethyl cellulose and nano nickel particles is added to the stirring of the first raw material In groove 3, a certain amount of formalin is poured into the second raw material tank diameter 4, opens stirring.Open peristaltic pump 5, the first raw material Liquid in tank diameter 3, the second raw material tank diameter 4 is flowed into first pressure stock chest 6 and second pressure stock chest 7.It is same with this When open high pressure inert gas cylinder 1 and gas is entered in first pressure stock chest 6 and second pressure stock chest 7, store up first pressure Fluid pressure in hopper 6 and second pressure stock chest 7 is maintained at 0.35MPa.Before experiment, the temperature of temperature control reaction vessel 10 is opened Device is controlled, the temperature of reactor area is maintained at 30 DEG C.
Raw material enters in knock-on reaction device 8, by centre gangway 21 and honeycomb duct 22 with certain speed in knock-on reaction The impingement region 23 that crosses of the lower section of device 8 mutually hits and reacted.After reaction, product drops to the bottom of temperature control reaction vessel 10 Portion, by the further hybrid reaction of agitation of agitator 11 and scattered, reactant is fully reacted and prevent from reuniting, flow ultimately into In product holding tank 12, the nuclear-shell structured nano-composite material of silver-colored coating nickel nano-particle has been obtained.In addition, silver cladding Copper, silver cladding gold, silver cladding carbon black, silver-colored enveloped carbon nanometer tube, other metals such as silver-colored coated graphite alkene, Yi Jijin, platinum, copper, nickel Nano composite material of cladding etc. can also be prepared by this apparatus and method.
Embodiment 5
The continuous reaction system and method provided using embodiment 1 prepares silver cladding tin oxide rice grain colloidal sol, including such as Lower step:
The mixed solution of a certain amount of silver nitrate, sodium citrate and tin oxide nanoparticles is added to the stirring of the first raw material In groove 3, a certain amount of hydrazine hydrate solution is poured into the second raw material tank diameter 4, opens stirring.Peristaltic pump 5 is opened, first is former Expect that the liquid in tank diameter 3, the second raw material tank diameter 4 is flowed into first pressure stock chest 6 and second pressure stock chest 7.With this Opening high pressure inert gas cylinder 1 simultaneously makes gas enter in first pressure stock chest 6 and second pressure stock chest 7, makes first pressure Fluid pressure in stock chest 6 and second pressure stock chest 7 is maintained at 0.5MPa.Before experiment, temperature control reaction vessel 10 is opened Temperature control device, the temperature of reactor area is set to be maintained at 30 DEG C.
Raw material enters in knock-on reaction device 8, by centre gangway 21 and honeycomb duct 22 with certain speed in knock-on reaction The impingement region 23 that crosses of device 8 mutually hits and reacted.After reaction, product drops to the bottom of temperature control reaction vessel 10, by The further hybrid reaction of agitation of agitator 11 and scattered, makes reactant fully react and prevents from reuniting, flow ultimately into product In holding tank 12, the colloidal sol of silver-colored cladding tin oxide rice grain has been obtained.In addition, silver-colored coating zinc oxide, silver-colored coated aluminum oxide, Silver cladding zirconium oxide, silver-colored carbon coated cerium oxide, silver cladding silica etc., other metallic cover nanometers such as Yi Jijin, platinum, copper, nickel Nano composite material of oxide particle etc. can also be prepared by this apparatus and method.
Above content is to combine specific preferred embodiment further detailed description of the utility model, it is impossible to Assert that specific implementation of the present utility model is confined to these explanations.For the ordinary skill of the utility model art For personnel, without departing from the concept of the premise utility, some simple deduction or replace can also be made, should all be regarded To belong to the scope of protection of the utility model.

Claims (8)

1. a kind of fast reaction prepares the device of nano material or nano composite material, it is characterised in that:It includes pressure materials Storage container, knock-on reaction device and temperature control reaction vessel, the knock-on reaction device are located at the upper opening of temperature control reaction vessel; The knock-on reaction device includes the centre gangway positioned at middle part, and the water conservancy diversion of even, symmetric is being provided with around centre gangway Road, the angle between symmetrical honeycomb duct is 30 ~ 150 °, the pressure materials storage container at least two, one of them The entrance of pressure materials storage container and centre gangway connect, the symmetrical honeycomb duct of each two respectively with other pressure materials Storage container connects;The honeycomb duct, the extended line of centre gangway intersect at the lower section of knock-on reaction device and reacted positioned at temperature control In the middle part of the cavity of container, the side wall of the temperature control reaction vessel is provided with steam vent.
2. fast reaction according to claim 1 prepares the device of nano material or nano composite material, it is characterised in that: Angle between symmetrical honeycomb duct is 60 ~ 120 °.
3. fast reaction according to claim 1 prepares the device of nano material or nano composite material, it is characterised in that: The bottom of the temperature control reaction vessel is provided with agitating device.
4. fast reaction according to claim 3 prepares the device of nano material or nano composite material, it is characterised in that: It includes product storage container, and the bottom of the temperature control reaction vessel is provided with discharging opening, the product storage container and discharging opening Connection.
5. fast reaction according to claim 1 prepares the device of nano material or nano composite material, it is characterised in that: It includes high voltage protective gas container, raw storage container, the high voltage protective gas container respectively by air gauge with least Two pressure materials storage container connections, the quantity of the raw storage container are not less than the quantity of pressure materials storage container, The raw storage container is connected with pressure materials storage container respectively.
6. fast reaction according to claim 5 prepares the device of nano material or nano composite material, it is characterised in that: The raw storage container includes the first raw storage container and the second raw storage container, the pressure materials storage container bag First pressure raw storage container and second pressure raw storage container are included, first raw storage container is former with first pressure Expect storage container connection, second raw storage container is connected with second pressure raw storage container, and the first pressure is former Material storage container is connected with centre gangway, and the second pressure raw storage container is led with the symmetrical of centrally located channel circumference Runner connects.
7. fast reaction according to claim 5 prepares the device of nano material or nano composite material, it is characterised in that: The raw storage container is connected by peristaltic pump with pressure materials storage container.
8. fast reaction according to claim 5 prepares the device of nano material or nano composite material, it is characterised in that: Agitating device is provided with the raw storage container.
CN201721066790.9U 2017-08-24 2017-08-24 A kind of fast reaction prepares the device of nano material or nano composite material Active CN207170961U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721066790.9U CN207170961U (en) 2017-08-24 2017-08-24 A kind of fast reaction prepares the device of nano material or nano composite material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721066790.9U CN207170961U (en) 2017-08-24 2017-08-24 A kind of fast reaction prepares the device of nano material or nano composite material

Publications (1)

Publication Number Publication Date
CN207170961U true CN207170961U (en) 2018-04-03

Family

ID=61738773

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721066790.9U Active CN207170961U (en) 2017-08-24 2017-08-24 A kind of fast reaction prepares the device of nano material or nano composite material

Country Status (1)

Country Link
CN (1) CN207170961U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107398565A (en) * 2017-08-24 2017-11-28 深圳市格络光电有限公司 A kind of fast reaction prepares the apparatus and method of nano material or nano composite material
CN109530713A (en) * 2018-12-30 2019-03-29 北京康普锡威科技有限公司 A kind of device preparing composite metal powder, method and composite metal powder

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107398565A (en) * 2017-08-24 2017-11-28 深圳市格络光电有限公司 A kind of fast reaction prepares the apparatus and method of nano material or nano composite material
CN109530713A (en) * 2018-12-30 2019-03-29 北京康普锡威科技有限公司 A kind of device preparing composite metal powder, method and composite metal powder

Similar Documents

Publication Publication Date Title
CN102019431B (en) Metallic nano cluster/silicon dioxide hollow nuclear shell structured nanoparticles and preparation method thereof
CN102554258B (en) Method for preparing metal silver nanostructure in water solution
CN108941599A (en) A kind of continuous preparation method of Nanometer Copper
CN107398565A (en) A kind of fast reaction prepares the apparatus and method of nano material or nano composite material
CN207170961U (en) A kind of fast reaction prepares the device of nano material or nano composite material
CN108409979A (en) A kind of cuprous oxide-metal organic frame composite material and preparation method
CN108941609A (en) Solar cell conductive silver paste high performance spherical super fine silver powder and preparation method thereof
CN104795558B (en) Continuous synthesis method of nickel-cobalt-manganese ternary hydroxide for lithium battery
CN104070177B (en) Preparation method for silver and gold nano-particles
CN106563811B (en) A kind of method that sea urchin shape Ag-ZnO nano-particles are continuously prepared using micro passage reaction
CN104743613B (en) Method for continuously preparing large-particle-size spherical cobalt carbonate
CN107377993B (en) A kind of metal nanometer line, dispersion liquid and preparation method thereof
CN107252896A (en) A kind of synthetic method of single dispersing thorn-like gold nano grain
CN101154493A (en) Superparamagnetism microsphere and method for manufacturing the same
CN109718775A (en) A kind of CuCo2O4The preparation method of nano spinel catalyst
CN107309439A (en) A kind of 3-dimensional metal nano wire and preparation method thereof
CN105013479A (en) Core-shell structure nanometer material for silver cores/platinum shells and preparation method of core-shell structure nanometer material
CN108031475A (en) A kind of preparation method of gold load ferric oxide nano photochemical catalyst
CN108115150A (en) A kind of preparation method of the nano silver of size adjustable
CN114436272A (en) Mesoporous silica nanosheet with high specific surface area and preparation method thereof
CN108356276A (en) A kind of the hypergravity preparation method and device of cellulose modified nano zero valence iron
CN100402145C (en) Catalyst in use for hydrogenation reaction of benzene selection, preparartion method and application
CN107552808B (en) Large-scale continuous preparation device and method for nano nickel powder
CN110586957B (en) Preparation method of porous Pd hollow nanospheres in ionic liquid aqueous solution
CN207237950U (en) A kind of knock-on reaction device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 518000 Shenzhen Nanshan District Guangdong Province Yuehai Street 10 High-tech Nanjiu Road Shenzhen Bay Science and Technology Eco-Park 10 Skirt Building 5 Floor 14-A

Patentee after: Shenzhen Geluo New Material Technology Co., Ltd.

Address before: Room 201, Building A, Qianhai Road, Qianhai Shenzhen-Hong Kong Cooperation Zone, Shenzhen, Guangdong 518000

Patentee before: Shenzhen city grid photoelectric Co., Ltd.