CN202876729U - Emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation - Google Patents

Emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation Download PDF

Info

Publication number
CN202876729U
CN202876729U CN201220422452.5U CN201220422452U CN202876729U CN 202876729 U CN202876729 U CN 202876729U CN 201220422452 U CN201220422452 U CN 201220422452U CN 202876729 U CN202876729 U CN 202876729U
Authority
CN
China
Prior art keywords
emulsification
chamber
emulsification chamber
tap
cavity
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.)
Expired - Lifetime
Application number
CN201220422452.5U
Other languages
Chinese (zh)
Inventor
张锋
戴圣阳
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.)
Nuoyi Fluid Science & Technology (shanghai) Co Ltd
Original Assignee
Nuoyi Fluid Science & Technology (shanghai) 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 Nuoyi Fluid Science & Technology (shanghai) Co Ltd filed Critical Nuoyi Fluid Science & Technology (shanghai) Co Ltd
Priority to CN201220422452.5U priority Critical patent/CN202876729U/en
Application granted granted Critical
Publication of CN202876729U publication Critical patent/CN202876729U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Colloid Chemistry (AREA)

Abstract

The utility model relates to the technical field of high-voltage homogeneous emulsifying equipment, and particularly relates to an emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation. The emulsification cavity device comprises a hydraulic plunger pump, a feeding cup, a one-way valve, a pressure meter, a heat exchanger and a discharging opening, and is characterized in that the hydraulic plunger pump is connected with one end of a main pipeline; one end of a tap of the main pipeline is connected with a laying-off hole of the funnel-shaped feeding cup through the one-way valve; the other end of the main pipeline is connected with an inlet of an emulsification cavity; a pressure meter is arranged at one end of an upper tap on the main pipeline between the one-way valve and the emulsification cavity; a diamond nozzle and a five-stage ceramic reaction cavity are arranged inside the emulsification cavity; an outlet of the emulsification cavity is arranged at one end of a tap between the diamond nozzle to a first-level ceramic reaction cavity; and the outlet of the emulsification cavity is connected with the heat exchanger. The emulsification cavity device provided by the utility model is novel in structure; materials are uniformly and stably mixed through the five-stage ceramic serial-connection reaction cavity; and the dispersion grain size of particles is greatly reduced, the peak width is reduced, and the product stability is improved through working pressure of 3100 bars.

Description

The emulsification chamber device that is used for the high-pressure homogeneous emulsifying device of nanometer beign preparation
[technical field]
The utility model relates to high-pressure homogeneous emulsifying device technical field, and a kind of emulsification chamber device of the high-pressure homogeneous emulsifying device for nanometer beign preparation is mainly used in nano liposomes specifically, Fat Emulsion, and suspension, the nanometers such as chemical materials are disperseed preparation.
[background technology]
Liquid is emulsification with the process that atomic droplet is evenly dispersed in immiscible another kind of liquid, and it is the liquid-liquid interface phenomenon.
In industrial production, the plant equipment that realizes above-mentioned emulsion process mainly is mulser, the type of mulser mainly contains three kinds at present: emulsifying mixer, colloid mill and homogenizer, dissimilar mulsers has different structures and performance, and the size (dispersiveness) of the emulsion particulate of acquisition and the quality (stability) of emulsion are also not identical.
Generally at the widely used stirring type emulsifying machine of Cosmetics Plant, its bad dispersibility of prepared emulsion, particulate is large and coarse, stability is also relatively poor, also easily produce and pollute, but it is made simply, low price, as long as the Rational structure of attentional selection machine, use properly, also be to produce the popular cosmetics that generally conform to quality requirements; Colloid mill is relative preferably emulsifying device with homogenizer, but in recent years along with the arrival in nanometer epoch, traditional mulser can not be realized nano level decentralized standard.
Be homogenizing valve such as traditional valve formula structure, by valve seat, spool, back-up ring consists of, material is tungsten carbide, relies on the gap length of manual adjustments valve seat and spool, comes controlled pressure, to reach the emulsifying to material, though this kind structural design is simple, accuracy is not high, so pressure is relatively low, abroad high energy reaches 1500bar, domestic owing to the machining accuracy problem, at present general maximum working pressure is lower, generally at 1000bar, so large department uses and also only is confined to milk, food emulsification.
[summary of the invention]
The purpose of this utility model is to overcome the deficiencies in the prior art, a kind of high pressure operation is provided, realizes the emulsifier unit that the material nanoscale disperses.
For achieving the above object, design a kind of emulsification chamber device of the high-pressure homogeneous emulsifying device for nanometer beign preparation, equipment comprises hydraulic planger pump, feed cup, check valve, Pressure gauge, heat exchanger, discharging opening, it is characterized in that the hydraulic plunger pump plunger is connected with equipment trunk line one end, trunk line tap one end is connected with the blanking hole of funnel type feed cup by a check valve, the other end of trunk line connects emulsification chamber import, tap one end is provided with Pressure gauge on the trunk line between check valve and the emulsification chamber, inside, described emulsification chamber is provided with a diamond nozzle and Pyatyi pottery reaction chamber, be provided with the outlet of emulsification chamber at diamond nozzle to tap one end between the first order pottery reaction chamber, the outlet of described emulsification chamber links to each other with heat exchanger, and described heat exchanger is provided with water inlet, delivery port and discharging opening.
Diamond charging hole connection device trunk line one end in the emulsification chamber, the discharge opening of diamond nozzle connects the charging hole in the Pyatyi pottery emulsion reaction chamber of being made by ceramic material, uniformly-spaced connect on the reaction chamber pipeline and set up in described Pyatyi pottery emulsification chamber, hydraulic planger pump pushes through diamond nozzle with material, and the injection stream that forms flank speed enters Pyatyi pottery emulsification chamber.
The aperture of diamond nozzle is 100 μ m.
The utility model compared with prior art, novel structure, the chamber design of the Pyatyi that shuts peculiar end pottery cascade reaction, make material from Pyatyi cascade reaction chamber contrary exhaust chamber, clash with newly advancing material flow, so that mixing of materials stable homogeneous more; Adamantine high accuracy processing, so that it can bear the operating pressure of the highest 3100bar, the pressure that reaches considerably beyond prior art, high pressure is so that the average grain diameter of nanoparticulate dispersed reduces, reduces peak width greatly, the targeting preparation preparation obtains unprecedented effect, improves the stability of its product.
[description of drawings]
Fig. 1 is the utility model structural representation;
Fig. 2 is flow direction of material schematic diagram in the utility model Pyatyi pottery cascade reaction chamber;
Fig. 3 be sample of the same race in conventional valve formula homogenizer under the 1000bar pressure, the material particular diameter survey map that circulates and obtain for 5 times;
Fig. 4 be sample of the same race in the utility model device under the 1000bar pressure, the material particular diameter survey map that circulates and obtain for 5 times;
1. hydraulic planger pumps, 2. feed cup, 3. check valves, 4. Pressure gauges, 5. diamond nozzles, 6. emulsification chambeies, 7. heat exchangers, 8. discharging openings among the figure.
[specific embodiment]
By reference to the accompanying drawings the utility model is further elaborated, its product configurations and method can realize for a person skilled in the art.
The design of the utility model structure is based on two technical problems, one, and conventional emulsification equipment pressure control mode can't realize high operating pressure; Its two, the conventional emulsification material particular diameter can't reach nanoscale to be disperseed.
Therefore the emulsification chamber internal structure of existing high-pressure homogeneous emulsifying device is improved, set up the diamond nozzle in 100 μ m apertures and the Pyatyi ceramic reaction chamber structure of connecting.
High-pressure homogeneous emulsifying device after the improvement as shown in Figure 1, comprise hydraulic planger pump 1, check valve 3, Pressure gauge 4, emulsification chamber 6, heat exchanger 7, feed cup 2, discharging opening 8, hydraulic planger pump 1 plunger is connected with equipment trunk line one end, trunk line tap one end is connected with the blanking hole of funnel type feed cup 2 by a check valve 3, the other end of trunk line connects emulsification chamber 6 imports, tap one end is provided with Pressure gauge 4 on the trunk line between check valve 3 and the emulsification chamber 6, inside, described emulsification chamber is provided with a diamond nozzle 5 and Pyatyi pottery reaction chamber, be provided with the outlet of emulsification chamber at diamond nozzle to tap one end between the first order pottery reaction chamber, the outlet of described emulsification chamber links to each other with heat exchanger, and described heat exchanger is provided with water inlet, delivery port and discharging opening.
Internal structure its internal part shown in Fig. 1 enlarged drawing in emulsification chamber is a type and arranges, the diamond nozzle straight line in 100 μ m apertures connects the import of one-level pottery reaction chamber, one-level pottery reaction chamber outlet straight line connects the import of secondary pottery reaction chamber, secondary pottery reaction chamber outlet straight line connects three grades of ceramic reaction chamber imports, by that analogy, the outlet of Pyatyi pottery reaction chamber connects the tail end sealing in emulsification chamber.The flow direction of material in reaction chamber as shown in Figure 2, because reaction chamber afterbody sealing, therefore material injects one-level pottery reaction chamber by diamond nozzle, flows to successively secondary to Pyatyi pottery reaction chamber, is backflowed by Pyatyi and flows out the emulsification chamber to one-level pottery reaction chamber and enter heat exchanger.
The power that said apparatus provides by the hydraulic plunger pump head drives plunger and moves reciprocatingly, utilize the turnover of check valve control material, plunger is squeezed into micropore nozzle to the high pressure that material provides with material, the void effect that forms behind the micropore is passed in utilization, shearing effect, collision effect reduces material particular diameter, enter the reaction chamber of Pyatyi series connection when material, the material homogenizing effect arrives best, shut described reaction chamber end, material is contrary exhaust chamber from Pyatyi cascade reaction chamber, clash with the liquid stream of coming in, this device work maximum pressure is 3100bar, and nanoparticulate dispersed is good.
In order to show intuitively advantage of the present utility model, identical Fat Emulsion sample is carried out emulsification treatment with conventional valve formula homogenizer and this device respectively, use identical setting parameter (pressure, number of processes) during processing, the material that obtains is carried out grain diameter measurement with the model NICOMP380 instrument of U.S. particle diameter analytical system Co., Ltd, and with measurement result with the formal intuition of particle diameter distribution map express, and mutually contrast, specifically as shown in Figure 3, Figure 4:
Fig. 3 characterizes sample in conventional valve formula homogenizer under the 1000bar pressure, the material particular diameter survey map that circulates and obtain for 5 times, and the particle diameter distribution situation that from figure, characterizes, the gained material particular diameter focuses mostly at 250nm;
Fig. 4 characterizes sample in this device under the 1000bar pressure, the material particular diameter survey map that circulates and obtain for 5 times, and the particle diameter distribution situation that from figure, characterizes, the gained material particular diameter focuses mostly at 150nm;
Visible this device is to Fat Emulsion from above-mentioned contrast, liposome, and nanosuspension prepares than conventional apparatus emulsify well, and the sample average particle diameter reduces greatly, the peak width reduction, product stability is better.

Claims (3)

1. emulsification chamber device that is used for the high-pressure homogeneous emulsifying device of nanometer beign preparation, equipment comprises hydraulic planger pump, feed cup, check valve, Pressure gauge, heat exchanger, discharging opening, it is characterized in that the hydraulic plunger pump plunger is connected with equipment trunk line one end, trunk line tap one end is connected with the blanking hole of funnel type feed cup by a check valve, the other end of trunk line connects emulsification chamber import, tap one end is provided with Pressure gauge on the trunk line between check valve and the emulsification chamber, inside, described emulsification chamber is provided with a diamond nozzle and Pyatyi pottery reaction chamber, be provided with the outlet of emulsification chamber at diamond nozzle to tap one end between the first order pottery reaction chamber, the outlet of described emulsification chamber links to each other with heat exchanger, and described heat exchanger is provided with water inlet, delivery port and discharging opening.
2. the emulsification chamber device of a kind of high-pressure homogeneous emulsifying device for nanometer beign preparation as claimed in claim 1, it is characterized in that diamond charging hole connection device trunk line one end in the emulsification chamber, the discharge opening of diamond nozzle connects the charging hole in the Pyatyi pottery emulsion reaction chamber of being made by ceramic material, uniformly-spaced connects on the reaction chamber pipeline and set up in described Pyatyi pottery emulsification chamber.
3. the emulsification chamber device of a kind of high-pressure homogeneous emulsifying device for nanometer beign preparation as claimed in claim 1, the aperture that it is characterized in that diamond nozzle is 100 μ m.
CN201220422452.5U 2012-08-23 2012-08-23 Emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation Expired - Lifetime CN202876729U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201220422452.5U CN202876729U (en) 2012-08-23 2012-08-23 Emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201220422452.5U CN202876729U (en) 2012-08-23 2012-08-23 Emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation

Publications (1)

Publication Number Publication Date
CN202876729U true CN202876729U (en) 2013-04-17

Family

ID=48068195

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201220422452.5U Expired - Lifetime CN202876729U (en) 2012-08-23 2012-08-23 Emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation

Country Status (1)

Country Link
CN (1) CN202876729U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102814137A (en) * 2012-08-23 2012-12-12 诺泽流体科技(上海)有限公司 Emulsifying cavity device of high-pressure homogeneous emulsifying equipment used for nanocrystallization preparation and method for emulsifying cavity device
CN107661985A (en) * 2016-12-28 2018-02-06 贵安新区瑞诚生物工程有限公司 Nano metal material and preparation method thereof and microfluidizer

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102814137A (en) * 2012-08-23 2012-12-12 诺泽流体科技(上海)有限公司 Emulsifying cavity device of high-pressure homogeneous emulsifying equipment used for nanocrystallization preparation and method for emulsifying cavity device
CN102814137B (en) * 2012-08-23 2014-07-30 诺泽流体科技(上海)有限公司 Emulsifying cavity device of high-pressure homogeneous emulsifying equipment used for nanocrystallization preparation and method for emulsifying cavity device
CN107661985A (en) * 2016-12-28 2018-02-06 贵安新区瑞诚生物工程有限公司 Nano metal material and preparation method thereof and microfluidizer

Similar Documents

Publication Publication Date Title
CN207169595U (en) The mixing system of fracturing blender truck
CN102794119B (en) Method for preparing monodisperse emulsion
CN107159046A (en) The mixing system and its compounding method of fracturing fluid
CN106422955B (en) It is a kind of quickly, the device and method of a large amount of, continuous production nanoemulsions or nano suspending liquid
CN106582340B (en) High-pressure homogenizer
CN204395795U (en) Gas-liquid or liquid liquid mixing nano-bubble generating apparatus
CN109261036B (en) Microstructure mixer for mixing high-viscosity fluid
CN202036960U (en) Continuous emulsifying system
CN202876729U (en) Emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation
CN103816970B (en) The preparation facilities of liquid nano solution and preparation method
CN202762376U (en) Emulsifying cavity device relevant to high pressure homogeneous emulsifying device
CN102814137B (en) Emulsifying cavity device of high-pressure homogeneous emulsifying equipment used for nanocrystallization preparation and method for emulsifying cavity device
CN202343133U (en) Coating homogenization system
CN203042961U (en) Device continuously producing microspheres
CN209519621U (en) A kind of dynamic mixer of adjustable shear intensity and degree of mixing
CN209005568U (en) A kind of venturi emulsion dispenser of the perforation with venturi ejection structure
CN102806038A (en) Emulsifying cavity device for high-pressure homogenizing emulsification equipment and method for emulsifying cavity device
CN209123695U (en) A kind of emulsifier unit of Almightiness type hydrophile amino silicon oil
JPH1142431A (en) Atomizing method and device therefor
CN204522939U (en) A kind of concrete additive processing unit (plant)
CN109499410A (en) A kind of venturi emulsion device for formulating of the perforation of the ejection structure containing venturi
CN203577677U (en) Cutting emulsification device with premixing device
CN202366628U (en) Medicament preparing device
CN212348742U (en) Solid-liquid homogeneous mixing pump matched multi-tube reactor
CN203783865U (en) Pressurization control device of high-pressure nanometer homogenizer

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20130417