阅读说明：本技术 一种通过振动混合实现超快速无团聚真空冷冻干燥的装置 (Device for realizing ultra-fast agglomeration-free vacuum freeze drying through vibration mixing ) 是由 谯志强 屈延阳 于 2021-08-12 设计创作，主要内容包括：本发明公开了一种通过振动混合实现超快速无团聚真空冷冻干燥的装置,其包括：干燥釜,用于盛装物料；高加速度振动控制系统,用于对所述干燥釜施加高加速度振动,使干燥釜内部物料处于高加速度振动状态；冷却加热循环系统,用于对干燥釜提供外循环冷却和加热；冷凝系统,与所述干燥釜连通；真空泵机组,真空泵机组与冷凝系统连接,用于使干燥釜内部处于高真空状态。针对传统的预冷冻-真空升华冷冻干燥方法和已有的改进型冷冻干燥方法所具有的干燥时间长、能耗高、产物难以避免团聚需要二次分散等缺点,本发明提出了一种在高频振动和高真空下,使湿态物料以无挤压的方式进行快速预冻成“冰沙”、然后对“冰沙”升温从而实现超快速升华干燥的装置。(The invention discloses a device for realizing ultra-fast agglomeration-free vacuum freeze drying by vibration mixing, which comprises: the drying kettle is used for containing materials; the high-acceleration vibration control system is used for applying high-acceleration vibration to the drying kettle to enable the materials in the drying kettle to be in a high-acceleration vibration state; the cooling and heating circulating system is used for providing external circulating cooling and heating for the drying kettle; the condensation system is communicated with the drying kettle; and the vacuum pump unit is connected with the condensing system and used for enabling the inside of the drying kettle to be in a high vacuum state. Aiming at the defects of long drying time, high energy consumption, difficult avoidance of agglomeration of products, secondary dispersion and the like of the traditional pre-freezing-vacuum sublimation freeze-drying method and the existing improved freeze-drying method, the invention provides a device for quickly pre-freezing wet materials into 'ice sand' in a non-extrusion mode under high-frequency vibration and high vacuum and then heating the 'ice sand' so as to realize ultra-quick sublimation drying.)

1. The utility model provides a device that realizes super quick no reunion vacuum freeze-drying through vibration mixing which characterized in that includes:

the drying kettle is used for containing materials;

the high-acceleration vibration control system is used for applying high-acceleration vibration to the drying kettle to enable the materials in the drying kettle to be in a high-acceleration vibration state;

the cooling and heating circulating system is used for providing external circulating cooling and heating for the drying kettle;

the condensation system is communicated with the drying kettle;

and the vacuum pump unit is connected with the condensing system and used for enabling the inside of the drying kettle to be in a high vacuum state.

2. The apparatus of claim 1, wherein the high acceleration vibration control system comprises: shaking table, shaking table movable coil and vibration control system, the inside both sides of shaking table are equipped with the spring shaft subassembly respectively, and the shaking table movable coil sets firmly on the spring shaft subassembly, is equipped with the clamping device who is used for fixed drying kettle on the shaking table movable coil, is equipped with between two spring shaft subassemblies to be used for driving the spring shaft subassembly and be the magnetic coil part electric connection of high acceleration vibration, vibration control system and magnetic coil part.

3. The apparatus of claim 2, further comprising a sensor fixed to the moving coil of the vibration table and connected to the vibration control system via a data line.

4. The apparatus of claim 2, wherein the magnetic coil assembly comprises a current coil and magnetic assemblies disposed on opposite sides of the current coil.

5. The apparatus of claim 2, wherein the spring shaft assembly comprises a spring and a guiding column disposed inside the spring for guiding, and the top of the guiding column is lower than the lowest position of the moving coil of the vibration table when the moving coil performs high acceleration vibration motion.

6. The device for realizing ultrafast agglomeration-free vacuum freeze-drying through vibratory mixing according to any one of claims 1 to 5, wherein the drying kettle comprises a kettle body and a kettle cover buckled on the kettle body, and a temperature control adjusting part which is matched with the cooling and heating circulating system and used for adjusting the temperature inside the kettle body is arranged on the side wall of the kettle body; the kettle body is internally provided with an isolating device which is movably connected.

7. The apparatus of claim 6, wherein the cooling and heating circulation system is connected to the temperature control adjustment unit through a cooling medium hose.

8. The apparatus for ultra-fast agglomeration-free vacuum freeze-drying according to claim 6, wherein the temperature-controlled regulating member is a jacket or an internal coil.

9. The device for realizing ultrafast agglomeration-free vacuum freeze-drying through vibration mixing as claimed in any one of claims 1 to 5, wherein the condensing system comprises a condenser, a condensing coil arranged in the condenser and a compression refrigerating unit respectively connected with two ends of the condensing coil, one end of the condenser is hermetically connected with the drying kettle through a vacuum hose, and the other end of the condenser is hermetically connected with the vacuum pump unit.

10. The apparatus for ultra-fast agglomeration-free vacuum freeze-drying by vibratory mixing as claimed in claim 9, wherein the vacuum hose is a vacuum bellows; the bottom of the condenser is provided with a drain valve.

Technical Field

The invention relates to the technical field of chemical production of superfine materials, nano materials, pharmacy and the like, in particular to a freeze drying device which can pre-freeze a solid-liquid mixed wet material into 'ice sand' under high acceleration vibration and high vacuum, then heat the 'ice sand' under the high acceleration vibration and high vacuum to ensure that the 'ice sand' is quickly sublimated into steam, and finally obtain a dry material through vacuumizing and removing. More particularly to a device for realizing ultra-fast agglomeration-free vacuum freeze drying by vibration mixing.

Background

Freeze drying is a drying method in which moisture or a liquid phase in a wet material frozen into a solid phase is directly sublimated into vapor and removed without being melted under a high vacuum environment by using the principle of ice crystal sublimation. The drying method can be carried out at normal temperature and low temperature, and meets the requirements of drying heat-sensitive materials; meanwhile, the osmotic pressure which is generated by changing liquid state into gas state and enables the material to agglomerate and reunite is eliminated, the hard agglomeration of the material can be avoided to a certain extent, and the porous structure of the material is kept. Therefore, freeze drying and equipment thereof are widely used in the fields of pharmacy, food processing, powder or nano material preparation and the like.

However, in the conventional tray type freeze-drying apparatus (such as the apparatus disclosed in JP1988173852, JP1995197775, etc.), a prefreezing process is required to freeze the wet material containing the liquid phase into a solid phase, and the wet material contained in the tray is subjected to a partial extrusion during the prefreezing process, because the freezing process advances layer by layer from outside to inside, the material dispersed in the liquid phase is easily agglomerated into a block-shaped porous structure. Therefore, materials (especially powder materials, nano materials and the like) obtained by the traditional pre-freezing-sublimation freeze drying method are always in a porous soft agglomerated block structure on the microscopic scale, and are not beneficial to subsequent direct use; particularly in the pharmaceutical industry, the freeze-dried bulk drug powder often needs to be further dispersed into highly dispersible powder, which increases the risks of contamination and operation safety during the dispersion process.

Another disadvantage of conventional tray freeze-drying devices is that the larger volume of ice formed by the pre-freezing process tends to be left standing in the vacuum system as it sublimes under high vacuum. The essence of sublimation under high vacuum is that heat is transferred from the surface of the ice to the inside layer by layer, and the heat is transferredThe speed is limited by the small surface area and the static state of the ice blocks, so that the heat transfer efficiency is low, the sublimation speed is slow, the process time for executing the freeze drying process is usually dozens of hours, the rapid production is not facilitated, and simultaneously, the energy consumption and the CO in the whole freeze drying process are greatly increased₂And (5) discharging.

Some improved freeze-drying methods, such as KR1020180028233A, which propose a freeze-drying method using liquid nitrogen as coolant, although the material can be prevented from being extruded and agglomerated during the pre-freezing process to some extent by the rapid freezing of liquid nitrogen, the sublimation drying process is still slow, and more energy is consumed because the pre-freezing uses a large amount of liquid nitrogen.

Although patent EP 1601919B 1, patent WO2004/073845 A3 and patent WO2004/073845 a2 propose a rapid vacuum freeze-drying device and method under stirring conditions, which can reduce the volume of ice crystals and achieve rapid sublimation drying, the ice crystals are gradually reduced by stirring, the volume is still large, and the introduction of stirring brings about the problem of sealing under high vacuum, which makes the equipment expensive.

USP7188993, EP2018783465, EP2018867320, RU2016117488, and chinese patent ZL201610320677.2, etc. although various forms of designs of vibration devices for solid-liquid, solid-solid material mixing are proposed, there is no provision of how to design a device for freeze-drying of wet material under vibration for rapid sublimation drying.

Disclosure of Invention

The invention aims to provide a device for realizing ultra-fast agglomeration-free vacuum freeze drying by vibration mixing, which aims to solve the problems in the prior art.

In order to achieve the purpose, the invention adopts the following technical scheme:

an apparatus for ultra-fast agglomeration-free vacuum freeze-drying by vibratory mixing, comprising: the drying kettle is used for containing materials; the high-acceleration vibration control system is used for applying high-acceleration vibration to the drying kettle to enable the materials in the drying kettle to be in a high-acceleration vibration state; the cooling and heating circulating system is used for providing external circulating cooling and heating for the drying kettle; the condensation system is communicated with the drying kettle; and the vacuum pump unit is connected with the condensing system and used for enabling the inside of the drying kettle to be in a high vacuum state.

In some embodiments, the high acceleration vibration control system comprises: shaking table, shaking table movable coil and vibration control system, the inside both sides of shaking table are equipped with the spring shaft subassembly respectively, and the shaking table movable coil sets firmly on the spring shaft subassembly, is equipped with the clamping device who is used for fixed drying kettle on the shaking table movable coil, is equipped with between two spring shaft subassemblies to be used for driving the spring shaft subassembly and be the magnetic coil part electric connection of high acceleration vibration, vibration control system and magnetic coil part.

In some embodiments, the vibration control device further comprises a sensor, wherein the sensor is fixed on the moving coil of the vibration table and is connected with the vibration control system through a data line.

In some embodiments, the magnetic coil assembly includes a current coil and magnetic assemblies disposed on either side of the current coil.

In some embodiments, the spring shaft assembly comprises a spring and a guide post arranged in the spring for guiding, wherein the top of the guide post is lower than the lowest position of the moving coil of the vibration table when the moving coil of the vibration table performs high-acceleration vibration motion.

In some embodiments, the drying kettle comprises a kettle body and a kettle cover buckled on the kettle body, and a temperature control adjusting part which is matched with the cooling and heating circulating system and used for adjusting the temperature inside the kettle body is arranged on the side wall of the kettle body; the kettle body is internally provided with an isolating device which is movably connected.

In some embodiments, the cooling and heating cycle system is connected to the temperature-controlled regulation part through a cooling medium hose.

In some embodiments, the temperature-controlled regulating member is a jacket or an internal coil.

In some embodiments, the condensing system comprises a condenser, a condensing coil arranged in the condenser and a compression refrigerating unit respectively connected with two ends of the condensing coil, one end of the condenser is hermetically connected with the drying kettle through a vacuum hose, and the other end of the condenser is hermetically connected with a vacuum pump unit.

In some embodiments, the vacuum hose is a vacuum bellows; the bottom of the condenser is provided with a drain valve.

Drawings

FIG. 1 is a schematic diagram of an apparatus for ultra-fast agglomeration-free vacuum freeze-drying by vibratory mixing according to some embodiments of the present application;

FIG. 2 is a schematic diagram of a high acceleration vibration control system of an apparatus for ultra-fast agglomeration-free vacuum freeze-drying via vibrational mixing according to some embodiments of the present application;

FIG. 3 is a schematic diagram of the configuration of the drying vessel of an apparatus for ultra-fast agglomeration-free vacuum freeze-drying by vibratory mixing according to some embodiments of the present disclosure;

FIG. 4 is a schematic diagram of a condensing system of an apparatus for ultra-fast agglomeration-free vacuum freeze-drying by vibrational mixing according to some embodiments of the present application;

FIG. 5a is a photograph showing the appearance of a freeze-dried product obtained by using the apparatus of the present invention;

fig. 5b is a picture of the appearance of a freeze-dried product obtained using a conventional tray-type freeze dryer;

the labels in the figure are: 101-high acceleration vibration control system, 102-cooling and heating circulation system, 103-drying kettle, 104-vacuum pump unit, 105-condensation system, 106-cold and hot medium hose, 107-vacuum hose, 108-vacuum valve, 109-air release valve, 110-water discharge valve, 201-vibration table, 202-spring shaft assembly, 203-magnetic assembly, 204-current coil, 205-vibration table moving coil, 206-data line, 207-sensor, 208-clamping device, 209-vibration control system, 301-jacket, 302-kettle body, 303-isolation device, 304-kettle cover, 305-vacuum tube, 306-material, 401-compression refrigeration unit, 402-condenser, 403-condensation coil.

Detailed Description

In order to make the objects, technical solutions and advantages of the present application more apparent, the present application is described in further detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the present application and are not intended to limit the present application.

On the contrary, this application is intended to cover any alternatives, modifications, equivalents, and alternatives that may be included within the spirit and scope of the application as defined by the appended claims. Furthermore, in the following detailed description of the present application, certain specific details are set forth in order to provide a better understanding of the present application. It will be apparent to one skilled in the art that the present application may be practiced without these specific details.

The apparatus for ultra-fast agglomeration-free vacuum freeze-drying by vibration mixing according to the embodiments of the present application will be described in detail with reference to fig. 1 to 5. It is to be noted that the following examples are only for explaining the present application and do not constitute a limitation to the present application.

In an embodiment of the present application, the apparatus for performing ultra-fast agglomeration-free vacuum freeze-drying by vibration mixing as shown in fig. 1 to 3 may include: a drying kettle 103 for containing the material 306; the high-acceleration vibration control system 101 is used for applying high-acceleration vibration to the drying kettle 103 to enable the materials in the drying kettle 103 to be in a high-acceleration vibration state; a cooling and heating circulation system 102 for providing external circulation cooling and heating to the drying kettle 103; a condensing system 105 in communication with the drying vessel 103; and a vacuum pump unit 104, wherein the vacuum pump unit 104 is connected with the condensing system 105 and is used for keeping the interior of the drying kettle 103 in a high vacuum state.

The device provided by the invention can pre-freeze wet materials mixed by solid and liquid phases into ice sand under high acceleration vibration and high vacuum, then heat the ice sand under the high acceleration vibration and high vacuum to ensure that the ice crystal is directly sublimated into vapor at ultra high speed, further remove the vapor from the materials by vacuumizing, and re-coagulate into solid in the condenser 402, and finally obtain the novel freeze drying device of the dry materials. The device can avoid the extrusion of the materials in the pre-freezing process, avoid the agglomeration of the materials into porous materials, and directly obtain high-dispersion powder materials by combining sublimation drying under vibration; meanwhile, the device can greatly reduce the freeze drying time, and realize the rapid, high-efficiency and energy-saving process.

The apparatus of the present invention for solving the technical problems is a system having functions of providing high acceleration vibration, material cooling and heating, ice crystal sublimation, high vacuum and vapor desublimation, as shown in fig. 1, in terms of being able to provide a device suitable for ultra-fast agglomeration-free vacuum freeze-drying by high acceleration vibration. The wet material may be pre-frozen to "smoothie" simultaneously under high acceleration vibration and high vacuum, and then the vapor removed by sublimation of the "smoothie". The system comprises 5 core components of a high-acceleration vibration and control system, a cooling and heating circulation system 102, a drying kettle 103, a vacuum pump unit 104 and a condensing system 105, and auxiliary components such as a cold and heat medium hose 106, a vacuum bellows, a vent valve 109, a drain valve 110 and the like.

By adopting the device with the structure, due to the existence of the high-acceleration vibration and control system, the drying kettle 103 connected with the device and the materials inside the drying kettle can be in a high-acceleration vibration state, so that the materials can be formed into 'ice sand' with small volume and large surface area in the pre-freezing process; and the sublimation process is carried out with the drying kettle 103 by continuous movement, thereby accelerating the heat exchange and accelerating the sublimation process.

Due to the existence of the cooling and heating circulation system 102 and the connected cold and heat medium hose 106, the connected drying kettle 103 and the materials inside the drying kettle can be cooled and heated, so that the wet materials can be pre-cooled to be near the ice crystal point in the pre-freezing process, and the icing state of the ice sand is kept before high vacuum is applied; and the drying kettle 103 and the 'ice sand' inside the drying kettle can be heated by slow heating in the high vacuum sublimation drying process so as to accelerate the heat exchange and sublimation drying process.

Due to the presence of the drying kettle 103, the wet material can be pre-frozen, heated and sublimated, and liquid and solid materials are prevented from entering the vacuum pipeline 305.

Due to the existence of the vacuum pump unit 104, a high vacuum state can be applied to the drying kettle 103, the cavity of the condensing system 105 and the vacuum pipe 305, and vapor generated by sublimation from the drying kettle 103 in the drying process can be extracted. Due to the existence of the condensing system 105, the vapor generated by sublimation from the drying kettle 103 can be de-sublimated into solid again, so that the vapor is prevented from entering the vacuum pump unit 104 to pollute the pump oil and influence the continuous and stable operation of the system.

Because the existence of the cooling and heating medium hose 106 and the vacuum hose 107 are both hoses, the independent high-frequency free vibration of the drying kettle 103 connected with the hoses is not influenced. Due to the presence of the purge valve 109 and the drain valve 110, the vacuum conditions within the drying vessel 103 and the condensing system 105 can be controlled as required by the process steps. Due to the water discharge valve 110, after the drying process is finished, the ice desublimated in the condensing system 105 is melted into liquid and then discharged out of the condensing system 105 for the next drying.

In some embodiments, the high acceleration vibration control system 101 is a system that can achieve high acceleration vibration by adjusting the current magnitude and frequency, as shown in fig. 2. The high acceleration vibration control system 101 includes: the vibration table 201, the vibration table moving coil 205, the vibration control system 209 and the sensor 207 are arranged, the spring shaft assemblies 202 are respectively arranged on two sides inside the vibration table 201, the vibration table moving coil 205 is fixedly arranged on the spring shaft assemblies 202, the vibration table moving coil 205 is provided with a clamping device 208 for fixing the drying kettle 103, a magnetic coil assembly for driving the spring shaft assemblies 202 to vibrate at high acceleration is arranged between the two spring shaft assemblies 202, and the vibration control system 209 is electrically connected with the magnetic coil assembly. The sensor 207 is fixed to the oscillating table moving coil 205 and is connected to the oscillation control system 209 via a data line 206. The magnetic coil component includes a current coil 204 and magnetic assemblies 203 disposed on both sides of the current coil 204. The spring shaft assembly 202 includes a spring and a guiding post disposed inside the spring for guiding, wherein the top of the guiding post is lower than the lowest position of the vibrating table moving coil 205 when performing high-acceleration vibrating motion.

In some embodiments, the sensor 207 is fixed to the vibrating table coil 205 and is connected to the vibration control system 209 through the data line 206, the current coil 204 is also connected to the vibration control system 209 through the electric line, and the drying kettle 103 is connected to and held fixed by the vibrating table coil 205 through the holding device 208. The magnetic component 203 may be a permanent magnet, such as a magnet, or an electromagnetic coil with current.

With the adoption of the high-acceleration vibration control system 101 with the structure, the drying kettle 103 and the vibration table moving coil 205 connected with the drying kettle can be supported due to the existence of the vibration table 201; due to the existence of the spring shaft assembly 202, the vibration table moving coil 205 connected with the spring shaft assembly can vibrate up and down; due to the presence of the magnetic assembly 203 and the current coil 204, a pair of adjustable interaction forces can be generated between the two and cause the spring to vibrate.

In the present embodiment, the presence of the sensor 207 fixed on the vibrating table moving coil 205, the vibration control system 209 can obtain the vibration frequency and amplitude of the vibrating table moving coil 205 through the data line 206; due to the clamping device 208, the vibration table moving coil 205 and the drying kettle 103 can be kept in fixed connection and vibrate at the same amplitude and frequency.

In this embodiment, due to the existence of the vibration control system 209, the frequency and amplitude data of the vibration table 201 can be analyzed, and the magnitude and frequency of the current flowing through the current coil 204 can be adjusted, so as to control the vibration state, the vibration frequency range of the high acceleration vibration and the output of the control system is 1.0Hz to 2000Hz, wherein the optimized vibration frequency range is 10Hz to 1000Hz, and the acceleration range which can be provided is 10g to 100 g.

In the present embodiment, the cooling and heating cycle system 102 is a device capable of providing an external cycle cooling and heating function, and the cooling and heating control, the temperature display, the temperature reduction and rise program setting, the external cycle start, and the like can be controlled through a control panel or a computer of the cooling and heating cycle system 102 itself. The cooling temperature range that can be provided is lower than the ice crystal point temperature of the medium to be dried, taking the drying of the water-containing material as an example, the cooling temperature range that the cooling and heating circulation system 102 can provide is-30 to 0 ℃, and the optimized cooling temperature range is-10 to 0 ℃. The heating temperature that can be provided is higher than the liquid boiling temperature of the medium to be dried in the high vacuum state, taking the drying water-containing material as an example, the heating temperature range that the cooling and heating circulation system 102 can provide is 0-60 ℃, and the optimized heating temperature range is 0-30 ℃.

In some embodiments, the drying kettle 103 comprises a kettle body 302 and a kettle cover 304 buckled on the kettle body 302, and a temperature control regulating component which is matched with the cooling and heating circulation system 102 and used for regulating the temperature inside the kettle body 302 is arranged on the side wall of the kettle body 302; an isolating device 303 which is movably connected is arranged in the kettle body 302. The cooling and heating circulation system 102 is connected with a temperature control adjustment component through a cold and hot medium hose 106. The temperature control adjusting part is a jacket 301 or an internal coil.

The drying kettle 103 is a reaction kettle device capable of containing wet materials, pre-freezing and sublimation drying the materials, and preventing the dry and wet materials from entering the vacuum tube 305, and as shown in fig. 3, mainly comprises a kettle body 302 with a jacket 301 (which may be a built-in coil), an isolating device 303, a kettle cover 304 and the vacuum tube 305. With the drying kettle 103 with the structure, due to the existence of the jacket 301 (or the built-in coil), the cooling medium and the heating medium in the cooling and heating medium hose 106 connected with the jacket can cool and heat the materials in the kettle;

the isolation device 303 is a removable and cleanable device having a plurality of small holes or mesh structures and being in close contact with the inner wall of the vessel, and functions to prevent liquid or solid dust (gas) from entering the vacuum tube 305 under high acceleration vibration. Due to the existence of the kettle body 302, the kettle cover 304 and the vacuum tube 305, the kettle body 302 and the kettle cover 304 can be opened and closed to carry out operations of containing materials, keeping a high vacuum state, taking out materials and the like.

In some embodiments, the condensing system 105 includes a condenser 402, a condensing coil 403 disposed in the condenser 402, and a compression refrigeration unit 401 connected to two ends of the condensing coil 403, wherein one end of the condenser 402 is hermetically connected to the drying kettle 103 through a vacuum hose 107, and the other end of the condenser 402 is hermetically connected to the vacuum pump unit 104.

The condensing system 105 is a device capable of performing multi-stage compression refrigeration and desublimating the drawn low-pressure vapor to a solid by the flow of low-temperature coolant, and, as shown in fig. 4, mainly includes a compression refrigeration unit 401 and a condenser 402 having a condensing coil 403 provided therein. The condensation system 105 with the structure can compress and refrigerate the refrigerant and reduce the temperature range of the cooling liquid circulating in the condensation coil 403 to-80 ℃ to-10 ℃ due to the existence of the compression refrigeration unit 401, wherein the optimized temperature range of the cooling liquid is-60 ℃ to-30 ℃. Due to the presence of the condenser 402 and the internal condenser coil 403, the vapor drawn out of the drying kettle 103 can be desublimated into a solid in the cavity of the condenser 402. In addition, the condenser 402 is connected to the vacuum assembly and through vacuum line 305, which may include vacuum valve 108, to maintain and control high vacuum operation; the bottom of the condenser 402 is provided with a drain valve 110 to facilitate the solid ice in the cavity to be melted into liquid and drained after drying.

The vacuum pump assembly 104 is a vacuum pump device capable of providing a high vacuum state or a series, parallel combination thereof. The unit is used for providing a high vacuum state in the range of 1 Pa-1000 Pa for the drying kettle 103 and the vacuum pipe 305, wherein the optimized high vacuum state has the pressure range of 10 Pa-40 Pa.

As an improvement of the apparatus for ultra-fast agglomeration-free vacuum freeze-drying by vibratory mixing according to the present invention, the apparatus may further comprise additional, optional auxiliary devices for ease of operation, process control and maintenance.

If a gas mixing valve is arranged on the vacuum pipe 305 connected with the drying kettle 103 or the drying kettle 103, protective gas is released after drying is finished, pressure balance is realized in the kettle, and then the drying kettle 103 is opened to take out materials; a computer control system may also be provided to start and stop the cooling and heating cycle system 102, the compression and refrigeration unit 401, the vacuum pump unit 104, and the valves by setting programs.

A vacuum gauge and a temperature sensor 207 can also be arranged in the drying kettle 103 and are connected with a control computer so as to measure the temperature and the vacuum degree of the materials in the drying kettle 103; a catalyst filtering system can be arranged on the vacuum pipe 305 connected with the vacuum pump unit 104 to prevent residual steam from polluting vacuum pump oil; an oil pumping filtering self-cleaning system can be additionally arranged on the vacuum pump; a valve can be additionally arranged on a pipeline between the compression refrigeration unit 401 and the condenser 402 to control the flow of the refrigerant; the types of the valves, such as electromagnetic valves, pneumatic valves and the like, can be changed, so that the on-off control of the valves can be realized by adopting different control modes.

The working principle of the device of the present invention is explained in detail below by freeze-drying a wet nano triaminotrinitrobenzene material having a water content of about 40%:

step 1, filling 1.0kg of a nanometer triamino trinitrobenzene wet material with the water content of about 40 percent into a drying kettle 103 of a device for realizing ultra-fast agglomeration-free vacuum freeze drying through high-acceleration vibration shown in figure 1, then sequentially installing an isolation device 303, covering a kettle cover 304 for sealing, and then fixing the drying kettle 103 on a vibrating table moving coil 205 through a clamping device 208.

And 2, starting the cooling circulation function of the cooling and heating circulation system 102, enabling cooling liquid to flow into the jacket 301 to refrigerate the drying kettle 103, and cooling the wet material in the drying kettle to 0-0.3 ℃.

And 3, starting the vibration control system 209, loading alternating current to the current coil 204 according to the frequency from small to large to cause the vibration of the vibration table moving coil 205, transmitting the vibration frequency and amplitude data back to the vibration control system 209 by the sensor 207 fixed on the vibration table moving coil 205 to find out the frequency with the maximum corresponding amplitude, and setting the frequency as the output resonance frequency by a program.

Step 4, start the compression refrigeration unit 401 of the condensing system 105, reduce the temperature inside the condenser 402 to below-30 ℃, and maintain continuous cooling operation until step 8.

And 5, enabling the vibration control system 209 to output alternating current to the current coil 204 under the output resonance frequency searched in the step 3 so as to enable the material in the drying kettle 103 to move in the optimal vibration state. Then starting the vacuum pump unit 104 and opening the vacuum valve 108 and the vacuum valve 108 in sequence to make the vacuum degree in the drying kettle 103 quickly drop below 200Pa and make the wet material boil, and the material in the cavity will quickly drop in temperature and quickly form fine 'ice sand' under the vibration of high acceleration. Meanwhile, the cooling and heating circulation system 102 is continuously adopted to further cool and reduce the temperature, so that the temperature of the materials in the kettle is reduced to about minus 10 ℃.

And 6, after the wet materials in the drying kettle 103 are completely converted into the 'ice sand' (less than or equal to 10min), maintaining the vibration state, further reducing the vacuum degree to (10-40 Pa) and continuously operating, sublimating the 'ice sand' formed in the drying kettle 103 under the high vacuum and high acceleration vibration, pumping away the generated water vapor, and cooling and sublimating around the condensing coil 403 in the condenser 402 to form solid ice.

And 7, switching the cooling circulation mode of the cooling and heating circulation system 102 into a heating circulation mode, and heating the drying kettle 103 under high-acceleration vibration according to the heating rate of 1.0 ℃/min to accelerate the heat exchange between the 'ice sand' and the kettle body 302, so that the sublimation drying process of the 'ice sand' is completed more quickly. After about 30-40 min, the temperature of the material in the drying kettle 103 rises to 30.0 ℃, at this time, all the "ice sand" is completely sublimated, and the nano triamino trinitrobenzene wet material becomes completely dry high-dispersion material.

And 8, after drying is finished, firstly closing the vacuum valve 108, then closing the vacuum pump unit 104, the compression refrigeration unit 401 and the cooling and heating circulation system 102, stopping vibration through the vibration control system 209, then opening the air release valve 109 to enable gas to slowly enter the drying kettle 103, after pressure is balanced, sequentially opening the kettle cover 304 and the isolation device 303, and taking out the dried material to obtain about 600g of dry and highly dispersed nano triamino trinitrobenzene powder.

And 9, opening the drain valve 110, heating and melting the solid ice in the condenser 402, completely discharging the solid ice, and then closing the drain valve 110 for the next freeze drying.

The nanometer triamino trinitrobenzene which is subjected to ultra-fast freeze drying by adopting the method provided by the invention and wet nanometer triamino trinitrobenzene with the water content of about 40 percent are put into a tray and are pre-frozen by adopting a common refrigerator, then sublimation drying is carried out in a traditional tray type freeze dryer, the specific surface area of the obtained product is tested by adopting a nitrogen adsorption and desorption method, and a camera is used for shooting the appearance picture of the product. The results of the comparative tests are shown in Table 1, and the photographs of the appearance of the products are compared as shown in FIG. 5a and FIG. 5b below.

TABLE 1 comparison of the present invention with conventional freeze-drying for the treatment of wet nano triaminotrinitrobenzene material

The device for realizing ultra-fast agglomeration-free vacuum freeze drying by high-acceleration vibration can greatly reduce energy consumed by freeze drying, reduce process time, improve production efficiency and improve specific surface area and dispersity of products.

The device for ultra-fast agglomeration-free vacuum freeze-drying by vibration mixing disclosed in the present application may bring about the following beneficial effects including but not limited to: aiming at the defects of long drying time, high energy consumption, difficult avoidance of agglomeration of products, secondary dispersion and the like of the traditional pre-freezing-vacuum sublimation freeze-drying method and the existing improved freeze-drying method, the invention provides a device for quickly pre-freezing wet materials into 'ice sand' in a non-extrusion mode under high-acceleration vibration and high vacuum and then heating the 'ice sand' so as to realize ultra-quick sublimation drying. The device can greatly reduce the time and energy consumption required by the freeze drying process, and directly obtain highly dispersed powder without secondary crushing. The device and the using method can be widely applied to the fields of pharmaceutical technology, superfine powder material preparation, nanometer material preparation and the like.

The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents and improvements made within the spirit and principle of the present invention are intended to be included within the scope of the present invention.