CN216536956U - Laboratory is with small-size low pressure flash drying device - Google Patents
Laboratory is with small-size low pressure flash drying device Download PDFInfo
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- CN216536956U CN216536956U CN202120868134.0U CN202120868134U CN216536956U CN 216536956 U CN216536956 U CN 216536956U CN 202120868134 U CN202120868134 U CN 202120868134U CN 216536956 U CN216536956 U CN 216536956U
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- 238000001035 drying Methods 0.000 title claims abstract description 42
- 239000000463 material Substances 0.000 claims abstract description 39
- 238000001704 evaporation Methods 0.000 claims abstract description 27
- 230000008020 evaporation Effects 0.000 claims abstract description 23
- 238000000227 grinding Methods 0.000 claims description 37
- 238000005192 partition Methods 0.000 claims description 13
- 238000007789 sealing Methods 0.000 claims description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 1
- 229910052796 boron Inorganic materials 0.000 claims 1
- 239000011521 glass Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 6
- 238000004140 cleaning Methods 0.000 abstract description 5
- 239000000203 mixture Substances 0.000 abstract description 5
- 235000011837 pasties Nutrition 0.000 abstract description 5
- 238000002347 injection Methods 0.000 abstract 1
- 239000007924 injection Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 description 12
- 239000010425 asbestos Substances 0.000 description 8
- 238000005485 electric heating Methods 0.000 description 8
- 229910052895 riebeckite Inorganic materials 0.000 description 8
- 230000002572 peristaltic effect Effects 0.000 description 7
- 238000001694 spray drying Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 238000005070 sampling Methods 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 description 1
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229960000074 biopharmaceutical Drugs 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007603 infrared drying Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000010092 rubber production Methods 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
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- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to a small low-pressure flash drying device for a laboratory, which comprises an evaporation bottle and a functional round cover. The evaporation bottle provides a place for drying and receives the dried material. The functional round cover is provided with three ports, namely a low-pressure port, a feed port and an air release port. The low-pressure port is connected with a vacuum pump to meet the requirement of low-pressure environment in the device; feeding different sample injection instruments into the device through the feed inlet; the air leakage port is used for balancing the air pressure in the device after drying is finished. The lower part of the functional dome is connected with two vertical clapboards to prevent a few materials from being carried out by airflow in the drying process. The device has the advantages of simple structure, convenient operation, short time consumption and easy cleaning, and is suitable for preliminary drying or thorough drying of mixed system substances such as laboratory powder-water mixtures, pasty substances, colloidal substances and the like.
Description
Technical Field
The utility model relates to the field of laboratory material drying.
Background
With the development of modern fine chemistry technology, the various chemicals and biologicals we developed can be applied in different fields, and each of them is usually dried in different drying ways due to its unique properties. The main drying methods today are forced air drying, reduced pressure drying, infrared drying, spray drying, flash drying, etc.
When the materials are dried by air blowing or low pressure, the materials at the bottom cannot be completely dried if the drying time is too short, and the experimental time is prolonged if the drying time is too long. However, the powder-water mixture, the paste-like material, the gel-like material, etc. have problems that separation and drying are difficult. If drying is directly performed or drying is performed after filtering, the problem of agglomeration is inevitable, and the development of subsequent experiments is influenced to a certain extent.
Spray drying and flash drying applied in a factory on a large scale can dry materials such as liquid, pasty materials, turbid liquid, pressed powder and the like, the obtained materials have good appearance and uniform particle size distribution, and related equipment is widely applied. In patent CN212578982U, a spray drying device applied in the rubber production process is introduced, which saves the drying time; in patent CN204952303U, a spray drying device applicable to starch sugar production is introduced, the product has better properties, and the dust content in the tail gas is low; in patent CN2903853Y, a spray drying device for maltose powder is introduced, which corrects the disadvantages of the prior art; in patent CN112592728A, a flash evaporation device applied to crude oil separation is introduced, which has good effect in the decontamination process after crude oil separation; in patent CN212566654U, a high-efficiency rotary flash evaporation dryer is introduced, which solves the problem of uneven drying of materials at the bottom of a common drying box; in patent CN112010381A, a device for preparing hot distilled water by multi-stage flash evaporation is introduced, which reduces the cost of preparing hot purified water.
In a laboratory, generally, the obtained materials are relatively few, and by applying the two drying modes, although the materials with good appearance and uniform particle size distribution can be obtained, the loss of the materials such as wall adhesion and the like can be avoided, and the equipment has the advantages of complex structure, large occupied area, large loss and difficulty in cleaning.
The utility model designs a small-sized low-pressure flash drying device for a laboratory, solves the problems of less material and long drying time under laboratory conditions, and can be used for primarily drying or completely drying materials in a mixed system such as a powder-water mixture, a pasty material, a colloidal material and the like to obtain a material with good appearance and uniform particle size. The device has the advantages of simple assembly, convenient operation, rapid drying, easy disassembly and easy cleaning.
Disclosure of Invention
Aiming at the defects, the utility model provides the small-sized low-pressure flash drying device for the laboratory, which can dry substances in a mixed system such as powder-water mixture, pasty substances and the like, and has the advantages of simple operation, exquisite structure, convenient sample introduction and sampling, small volume, easy cleaning, safety, reliability, energy conservation and no pollution.
In order to achieve the purpose, the utility model adopts the following technical scheme.
The utility model relates to a small low-pressure flash drying device for a laboratory, which comprises an evaporation bottle and a functional round cover.
The device can be heated by a flexible heating asbestos sleeve, and can also be heated by a common electric heating sleeve.
The evaporation bottle provides a place for drying and receives the dried material, and the evaporation bottle is connected with the functional circular cover in a grinding sealing mode.
The radius ratio of the upper end face to the lower end face of the functional circular cover is 1.2: 1-1.3: 1; the ratio of the thickness of the functional round cover to the height of a standard inner grinding opening (reference GB/T21297-2007) of the feed inlet is 2: 1; the upper opening is three openings which penetrate through the round cover. One port of the device is a low-pressure port, the design requires that the upper part of the low-pressure port is designed as a standard inner grinding port (refer to GB/T21297-2007), the middle part is designed to be smooth, the radius ratio of the upper part to the middle part is 4: 1-5: 1, the lower part is designed to be conical, the conicity is 45-60 degrees, the device plays a role of cyclone separation when in work and prevents materials from blocking the low-pressure port, the height ratio of the three parts is 1:1:1, and an outer grinding port air-extracting grinding plug which has the same grinding port number as that of the low-pressure port in the device can be connected with a vacuum pump, so that the requirement of a low-pressure environment in the device is met; one opening of the device is a feed inlet, the design requires that the upper part of the feed inlet is designed as a standard inner grinding opening (refer to GB/T21297-2007), the lower part of the feed inlet is designed to be smooth, the radius ratio of the upper part to the lower part is 2.5: 1-3.0: 1, the height ratio of the upper part to the lower part is 1:1, and the feeding mode (feeding by an injector and feeding by a peristaltic pump) can be determined according to the specific environmental requirements; one opening of the air release device is an air release opening, the design requires that the upper part of the air release opening is designed as a standard inner grinding opening (refer to GB/T21297-2007), the lower part of the air release opening is designed to be smooth, the radius ratio of the upper part to the lower part is 2.5: 1-3.0: 1, the height ratio of the upper part to the lower part is 1:1, the air release valve can be matched with an outer grinding opening air release valve and an air release opening with the same grinding opening mark number in the air release opening for use, and the air pressure in the device is balanced after drying is finished.
Two partition plates are arranged below the functional round cover to prevent a few materials from being carried out by air flow in the drying process, the central angle corresponding to the arc length of the lower portion of each partition plate is 30-35 degrees, the ratio of the thickness of each partition plate to the thickness of the functional round cover is 0.2: 1-0.3: 1, the ratio of the contact length of each partition plate and the lower end face of the functional cover plate to the diameter of the lower end face of the functional cover plate is 0.7: 1-0.8: 1, the ratio of the height of each partition plate to the height of the evaporation bottle is 0.5: 1-0.6: 1, one partition plate is arranged between the low-pressure port and the feed port, and the other partition plate is arranged between the feed port and the air release port.
The utility model has the following beneficial effects.
1. The device has the advantages of simple operation, exquisite structure, small volume, convenient sample introduction and sampling, safety, reliability, rapid drying, easy disassembly and easy cleaning.
2. The utility model is suitable for the requirement of a laboratory on drying a small amount of materials, can obtain materials with better appearance and uniform particle size, and is better suitable for the primary drying or the complete drying of mixed system materials such as powder-water mixtures, pasty materials and the like.
3. The utility model can reasonably select heating modes (flexible heating asbestos covers, common electric heating covers and the like) according to actual conditions; the injector feeding or the peristaltic pump feeding can be reasonably selected according to actual conditions.
Drawings
FIG. 1 is a full sectional view of the present invention.
FIG. 2 is a top view of the functional dome of the present invention.
FIG. 3 is an enlarged view of the functional dome of the present invention.
FIG. 4 is a diagram of an application example 1 of the present invention.
FIG. 5 is a diagram of an example 2 of the present invention.
In the figure: 1-an evaporation bottle; 2-functional dome; 3-low pressure port; 4-a feed inlet; 5-air leakage port; 6-a separator.
Detailed Description
The following detailed description of embodiments of the utility model refers to the accompanying drawings.
As shown in figure 1, a small-sized low-pressure flash drying device for a laboratory comprises an evaporation bottle 1 and a functional round cover 2. The functional round cover 2 is provided with three openings, namely a low pressure opening 3, a feed inlet 4 and an air leakage opening 5, and the lower part of the functional round cover 2 is connected with two vertical clapboards 6. During the use, place in electric jacket or other heating instrument with evaporating flask 1, put evaporating flask 1 with function dome 2 on, both realize that the mill mouthful is sealed, it is even with low pressure port 3 internal mill mouthful of the unanimous mill of mill mouthful mark and low pressure port 3 to bleed off the grinding stopper with the vacuum pump through the external mill mouth, select suitable grinding stopper and feed inlet 4 to link to each other according to specific feeding mode, the installation links to each other with disappointing 5 internal mill mouthful atmospheric valve that the mill mouthful mark is unanimous and disappointing 5, and the adjustment external mill mouthful atmospheric valve is open state. And (4) turning on an electric heating jacket or other heating instruments, setting the temperature, turning on a vacuum pump, and turning off the vent valve of the outer grinding opening after about ten seconds. When the temperature and the pressure meet the requirements, feeding is carried out to the device through the feeding hole 4 according to a specific feeding mode, the dried material falls to the lower part of the evaporation bottle 1, after the material is completely dried, the electric heating sleeve or other heating instruments are closed, after the temperature in the device is stable, the vent valve of the outer grinding port is opened, the air pressure inside and outside the device is balanced, the vacuum pump is closed after the air pressure is balanced, the vent valve of the outer grinding port, the air-extracting grinding plug, the sampling instrument and the related grinding plug are taken down, the functional round cover 2 is taken down, and the material in the evaporation bottle 1 is taken out. After the end, the device is cleaned for the next use. During operation, the hot air drawn off by the vacuum pump can be cooled by a cooling device.
Application example 1: when the amount of the materials is small. As shown in fig. 3, firstly put the evaporating flask 1 into the flexible heating asbestos sleeve (electric jacket), put the functional round cover 2 on the evaporating flask 1, connect the vacuum pump with the low pressure port 3 through the exhaust grinding plug, connect the rubber plug of the outer grinding port with the same mark number as the grinding port in the feed port 4 with the feed port 4, install the vent valve of the outer grinding port and connect with the air escape port 5, and adjust the vent valve of the outer grinding port to be open. And (3) opening the flexible heating asbestos (an electric heating sleeve) and setting the temperature, opening the vacuum pump, and closing the vent valve of the outer grinding opening after about ten seconds. When temperature and pressure reach the requirement, the syringe feeds into the device through the rubber buffer of the external mill mouth, the dry material falls to 1 lower part of the evaporation flask, after the material is dry in the syringe finishes, close the flexible heating asbestos cover (electric jacket), after the temperature is stable in the device, open the atmospheric pressure of the external mill mouth, the inside and outside air pressure of the balancing unit, close the vacuum pump after waiting to the atmospheric pressure balance, take off the atmospheric valve of the external mill mouth, bleed and grind the stopper, syringe and rubber buffer of the external mill mouth, take off the function dome 2, take out the material in the evaporation flask 1. After the end, the device is cleaned for the next use.
Application example 2: when more materials are available. As shown in fig. 2, firstly, the evaporation bottle 1 is put into a flexible heating asbestos sleeve (an electric heating sleeve), the functional round cover 2 is put on the evaporation kettle 1, the vacuum pump is connected with the low-pressure port 3 through the air exhaust grinding plug, the peristaltic pump is connected with the feed port 4 through the outer grinding port switching port with the same grinding port mark number as that of the feed port 4, the outer grinding port vent valve is installed to be connected with the air leakage port 5, and the outer grinding port vent valve is adjusted to be in an open state. The flexible heating asbestos (electric heating sleeve) 1 is opened, the temperature is set, the vacuum pump is opened, and the external grinding opening vent valve is closed after about ten seconds. When the temperature and the pressure meet the requirements, the peristaltic pump is opened to feed materials into the device, the dried materials fall to the lower part of the evaporation bottle 1, after all the materials in the peristaltic pump are dried, the peristaltic pump is closed, the flexible heating asbestos sleeve (electric heating sleeve) is closed, after the temperature in the device is stable, the vent valve of the outer grinding opening is opened, the air pressure inside and outside the device is balanced, the vacuum pump is closed after the air pressure is balanced, the vent valve of the outer grinding opening, the air extraction grinding plug, the peristaltic pump and the outer grinding opening switching opening are taken down, the functional round cover 2 is taken down, and the materials in the evaporation bottle 1 are taken out. After the end, the device is cleaned for the next use.
Although the embodiments of the present invention have been described with reference to the accompanying drawings, the present invention is not limited thereto
The technical scheme of the utility model, such as the limitation of the novel protection range, the change, the perfection and the like, is covered in the protection range of the utility model.
Claims (4)
1. A small-sized low-pressure flash drying device for a laboratory is characterized by comprising an evaporation bottle and a functional round cover, wherein the evaporation bottle is in ground sealing connection with the functional round cover; the functional round cover is provided with three openings, namely a low-pressure opening, a feed inlet and an air release opening, and the lower part of the functional round cover is connected with two vertical clapboards; the radius ratio of the upper end face to the lower end face of the functional circular cover is 1.2: 1-1.3: 1; the ratio of the thickness of the functional round cover to the standard internal grinding height of the feed inlet is 2: 1.
2. A small-sized low-pressure flash drying apparatus for laboratory use according to claim 1, wherein: the upper part of the low-pressure port is designed as a standard internal grinding port, the middle part of the low-pressure port is designed as a smooth part, the radius ratio of the upper part to the middle part is 4: 1-5: 1, the lower part of the low-pressure port is designed as a taper, the taper is 45-60 degrees, and the height ratio of the three parts is 1:1: 1; the upper part of the feed inlet is designed as a standard inner grinding opening, the lower part of the feed inlet is designed to be smooth, the radius ratio of the upper part to the lower part is 2.5: 1-3.0: 1, and the height ratio of the upper part to the lower part is 1: 1; the upper part of the air leakage opening is designed as a standard inner grinding opening, the lower part of the air leakage opening is designed as a smooth part, the radius ratio of the upper part to the lower part is 2.5: 1-3.0: 1, and the height ratio of the upper part to the lower part is 1: 1.
3. A small-sized low-pressure flash drying apparatus for laboratory use according to claim 1, wherein: the central angle corresponding to the arc length of the lower part of the partition plate is 30-35 degrees, the ratio of the thickness of the partition plate to the thickness of the functional circular cover is 0.2: 1-0.3: 1, the ratio of the contact length of the partition plate and the lower end face of the functional cover plate to the diameter of the lower end face is 0.7: 1-0.8: 1, the ratio of the height of the partition plate to the height of the evaporation bottle is 0.5: 1-0.6: 1, one partition plate is arranged between the low-pressure port and the feed port, and the other partition plate is arranged between the feed port and the air release port.
4. A small-sized low-pressure flash drying apparatus for laboratory use according to claim 1, wherein: the material of the evaporation bottle and the functional circular cover is quartz glass or high boron glass.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202120868134.0U CN216536956U (en) | 2021-04-26 | 2021-04-26 | Laboratory is with small-size low pressure flash drying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN202120868134.0U CN216536956U (en) | 2021-04-26 | 2021-04-26 | Laboratory is with small-size low pressure flash drying device |
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Publication Number | Publication Date |
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CN216536956U true CN216536956U (en) | 2022-05-17 |
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CN202120868134.0U Expired - Fee Related CN216536956U (en) | 2021-04-26 | 2021-04-26 | Laboratory is with small-size low pressure flash drying device |
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CN (1) | CN216536956U (en) |
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2021
- 2021-04-26 CN CN202120868134.0U patent/CN216536956U/en not_active Expired - Fee Related
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CF01 | Termination of patent right due to non-payment of annual fee | ||
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Granted publication date: 20220517 |