CN201366334Y - Freeze drying granulation device - Google Patents
Freeze drying granulation device Download PDFInfo
- Publication number
- CN201366334Y CN201366334Y CNU200920001134XU CN200920001134U CN201366334Y CN 201366334 Y CN201366334 Y CN 201366334Y CN U200920001134X U CNU200920001134X U CN U200920001134XU CN 200920001134 U CN200920001134 U CN 200920001134U CN 201366334 Y CN201366334 Y CN 201366334Y
- Authority
- CN
- China
- Prior art keywords
- spray tower
- tower
- utility
- model
- spray
- 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
Links
- 238000004108 freeze drying Methods 0.000 title claims abstract description 13
- 238000005469 granulation Methods 0.000 title description 8
- 230000003179 granulation Effects 0.000 title description 8
- 239000007921 spray Substances 0.000 claims abstract description 43
- 239000000463 material Substances 0.000 claims abstract description 19
- 238000007710 freezing Methods 0.000 claims abstract description 5
- 230000008014 freezing Effects 0.000 claims abstract description 5
- 241000282326 Felis catus Species 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 3
- 238000002844 melting Methods 0.000 abstract description 3
- 230000008018 melting Effects 0.000 abstract description 3
- 238000005507 spraying Methods 0.000 abstract 2
- 230000009977 dual effect Effects 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 238000001035 drying Methods 0.000 description 5
- 239000011344 liquid material Substances 0.000 description 4
- 239000003595 mist Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种造粒装置,具体地说,是涉及一种成本低廉且可提高成品产量的冷冻干燥造粒装置。The utility model relates to a granulation device, in particular to a freeze-drying granulation device with low cost and which can increase the output of finished products.
背景技术 Background technique
目前,各行业广泛存在有液体物料干燥而成粉末状最终产品的需求,为此人们发明了众多的干燥工艺,适用于各种不同温度、酸碱度、纯度、易燃等产品的干燥,其中使用喷雾塔干燥工艺,具有连续生产、干燥速度块、产品易收集、粉尘小等优点。现有的冷冻喷雾塔的工作原理是:使液体物料先经高压泵输送至喷头,再由喷头呈雾状喷出,随后,将经过预泠处理的冷冻风由送风机从喷雾塔的顶部送进喷雾塔内,对雾状物料进行冷却处理。雾状物料经过冷却后变硬形成粉末状颗粒,于喷雾塔的底部被收集包装即为成品。At present, there is a wide demand for drying liquid materials into powdery final products in various industries. For this reason, many drying processes have been invented, which are suitable for drying products with different temperatures, pH, purity, and flammability. Among them, spray The tower drying process has the advantages of continuous production, fast drying speed, easy collection of products, and small dust. The working principle of the existing refrigerated spray tower is: the liquid material is transported to the nozzle by the high-pressure pump first, and then sprayed out in the form of mist by the nozzle, and then the refrigerated air that has been pre-cooled is sent from the top of the spray tower by the blower. In the spray tower, the mist material is cooled. After cooling, the mist material hardens to form powder particles, which are collected and packaged at the bottom of the spray tower to become the finished product.
然而,在传统的冷冻喷雾造粉技术中,喷雾塔中一般只设置一个喷头。而且,成品的产量要求越大,成品颗粒要求越小,则喷雾塔的体积要求也就越大。因此,如果需要加大成品的产量,通常的做法是加大喷雾塔的直径和高度,而且还需加大相应的配套系统,从而大幅度增加了物料的造粒成本。However, in the traditional freeze-spray pulverization technology, generally only one nozzle is arranged in the spray tower. Moreover, the greater the output requirement of the finished product and the smaller the particle size requirement of the finished product, the greater the volume requirement of the spray tower. Therefore, if it is necessary to increase the output of finished products, the usual practice is to increase the diameter and height of the spray tower, and also increase the corresponding supporting system, which greatly increases the granulation cost of materials.
实用新型内容Utility model content
有鉴于上述技术问题,本实用新型的目的在于克服现有技术的不足与缺陷,并且提供一种既可提高成品产量,又不会造成设备的投资成本大幅度增加的冷冻干燥造粒装置。In view of the above-mentioned technical problems, the purpose of this utility model is to overcome the deficiencies and defects of the prior art, and provide a freeze-drying and granulating device that can increase the output of finished products without greatly increasing the investment cost of the equipment.
本实用新型的上述目的是通过采用这样的技术方案实现的:The above-mentioned purpose of the utility model is achieved by adopting such technical scheme:
一种冷冻干燥造粒装置,它至少包括喷雾塔、与喷雾塔底部相连的旋风分离器及通过旋风分离器连接至所述喷雾塔的底部的抽风机。此外,该冷冻干燥造粒装置还包括:两个用于输送物料到塔顶的高压泵,两个水平设置于喷雾塔的顶部且分别与高压泵的其中之一相连接的喷头,以及通过排风管与所述喷雾塔的顶部相连的排风机。A freeze-drying and granulating device at least includes a spray tower, a cyclone separator connected to the bottom of the spray tower, and an exhaust fan connected to the bottom of the spray tower through the cyclone separator. In addition, the freeze-drying and granulating device also includes: two high-pressure pumps for transporting materials to the top of the tower, two spray heads arranged horizontally on the top of the spray tower and respectively connected to one of the high-pressure pumps, and The air duct is an exhaust fan connected to the top of the spray tower.
在本实用新型的另一个优选实施方式中,该冷冻干燥造粒装置还包括通过冷冻风管连接至所述喷雾塔的中部的送风机。In another preferred embodiment of the present utility model, the freeze-drying and granulating device further includes a blower connected to the middle of the spray tower through a freezing air pipe.
与现有技术相比,本实用新型具有以下优点:Compared with the prior art, the utility model has the following advantages:
1、在本实用新型中,由于在喷雾塔的顶部水平设置了两个喷头,因此可增大成品的产量;而且于喷雾塔的顶部连接有排风机,所以其不仅可排走大部分从喷头喷出的物料的热量,而且还可延缓物料在塔内沉降的速度,以使物料造粒的效果更佳;1. In the utility model, since two nozzles are arranged horizontally on the top of the spray tower, the output of finished products can be increased; and an exhaust fan is connected to the top of the spray tower, so it can not only discharge most of the nozzles from the nozzles The heat of the ejected material can also slow down the settling speed of the material in the tower, so that the effect of material granulation is better;
2、本实用新型于喷雾塔的中部通过冷冻风管连接有送风机,该冷冻风可对下降至喷雾塔中部的物料进行再次冷却。2. In the utility model, the central part of the spray tower is connected with a blower through a refrigerated air pipe, and the refrigerated air can re-cool the materials falling to the central part of the spray tower.
附图说明 Description of drawings
图1是根据本实用新型的一个具体实施方式的造粒装置的总体结构示意图。Fig. 1 is a schematic diagram of the overall structure of a granulation device according to a specific embodiment of the present invention.
具体实施方式 Detailed ways
为详细说明本实用新型的技术内容、构造特征,以下将结合具体实施方式并配合附图予以详细说明。In order to illustrate the technical content and structural features of the present utility model in detail, the following will describe in detail in conjunction with specific embodiments and accompanying drawings.
图1示出了根据本实用新型的一个具体实施方式的造粒装置的总体结构示意图。该冷冻干燥造粒装置至少包括喷雾塔12、与喷雾塔12底部相连的旋风分离器13及抽风机14,其中,所述抽风机14通过旋风分离器13连接至所述喷雾塔12的底部。该冷冻干燥造粒装置装置还进一步包括:两个用于输送物料到塔顶的高压泵11,两个水平设置于所述喷雾塔12的顶部,且分别与所述高压泵11的其中之一相连的喷头121,以及通过排风管151与所述喷雾塔12的顶部相连的排风机15。Fig. 1 shows a schematic diagram of the overall structure of a granulation device according to a specific embodiment of the present invention. The freeze-drying and granulating device at least includes a
另外,如图1所示,所述冷冻干燥造粒装置装置还包括通过冷冻风管161连接至所述喷雾塔12的中部的送风机16。In addition, as shown in FIG. 1 , the freeze-drying and granulating device further includes a
该冷冻干燥造粒装置的工作原理如下:The working principle of the freeze-drying granulation device is as follows:
首先,温度大致为100℃左右的低溶点液体状物料由两个高压泵输送到塔顶,然后借物料本身的重力及喷头的压力将物料以雾状从两个水平设置的喷头中喷出至喷雾塔内。此时,物料的大部分热量就会先经由塔顶抽风机排出塔外,可使物料的温度降至40℃左右。当物料继续下降至塔的中部时,物料被中部送入的冷冻风进一步冷却,经过热交换的热空气可由喷雾塔下部的抽风机抽走,排出塔外,呈粉末状的物料最终由喷雾塔底部的出料口中排出。First, the liquid material with a low melting point at a temperature of about 100°C is transported to the top of the tower by two high-pressure pumps, and then the material is sprayed out from two horizontally arranged nozzles in the form of mist by the gravity of the material itself and the pressure of the nozzles. into the spray tower. At this time, most of the heat of the material will be discharged out of the tower through the exhaust fan on the top of the tower, which can reduce the temperature of the material to about 40°C. When the material continues to descend to the middle of the tower, the material is further cooled by the refrigerated air sent from the middle, and the hot air after heat exchange can be sucked away by the exhaust fan at the lower part of the spray tower and discharged out of the tower, and the powdery material is finally discharged from the spray tower Discharge from the discharge port at the bottom.
本实用新型只需在传统的喷雾塔中水平增设一个喷头,并在喷雾塔的顶部和中部分别增设排风机及送风机,即可对低溶点液体状物料进行双重冷冻处理,不仅成品的产量能够得到大幅度的增加,而且成品的处理效果更佳。The utility model only needs to add a nozzle horizontally in the traditional spray tower, and add an exhaust fan and a blower to the top and middle of the spray tower respectively, so that the low melting point liquid material can be subjected to double freezing treatment, not only the output of the finished product can be reduced It has been greatly increased, and the processing effect of the finished product is better.
以上所述仅为本实用新型的较佳实施例,并非用来限定本实用新型的实施范围;凡是依本实用新型所作的等效变化与修改,都被本实用新型的专利范围所覆盖。The above descriptions are only preferred embodiments of the present utility model, and are not intended to limit the implementation scope of the present utility model; all equivalent changes and modifications made according to the present utility model are covered by the patent scope of the present utility model.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200920001134XU CN201366334Y (en) | 2009-01-15 | 2009-01-15 | Freeze drying granulation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200920001134XU CN201366334Y (en) | 2009-01-15 | 2009-01-15 | Freeze drying granulation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201366334Y true CN201366334Y (en) | 2009-12-23 |
Family
ID=41485235
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU200920001134XU Expired - Lifetime CN201366334Y (en) | 2009-01-15 | 2009-01-15 | Freeze drying granulation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201366334Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103180037A (en) * | 2010-10-29 | 2013-06-26 | 株式会社爱发科 | Vacuum freeze drying apparatus and frozen particle manufacturing method |
| CN105597622A (en) * | 2016-03-09 | 2016-05-25 | 苏州大学 | Freezing temperature-controllable spray freezing tower for preparing micron-sized ice ball particles |
| CN106732172A (en) * | 2016-12-09 | 2017-05-31 | 华东理工大学 | Bioactive agents solidification equipment and application method based on spray chilling technology |
-
2009
- 2009-01-15 CN CNU200920001134XU patent/CN201366334Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103180037A (en) * | 2010-10-29 | 2013-06-26 | 株式会社爱发科 | Vacuum freeze drying apparatus and frozen particle manufacturing method |
| CN103180037B (en) * | 2010-10-29 | 2015-05-06 | 株式会社爱发科 | Vacuum freeze drying apparatus and frozen particle manufacturing method |
| CN105597622A (en) * | 2016-03-09 | 2016-05-25 | 苏州大学 | Freezing temperature-controllable spray freezing tower for preparing micron-sized ice ball particles |
| CN105597622B (en) * | 2016-03-09 | 2017-11-21 | 苏州大学 | The controllable spray chilling tower for being used to prepare micron order ice hockey particle of freezing temperature |
| CN106732172A (en) * | 2016-12-09 | 2017-05-31 | 华东理工大学 | Bioactive agents solidification equipment and application method based on spray chilling technology |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201255558Y (en) | Spray drying device | |
| CN204297498U (en) | A kind of conveying belt loading material air cooling system | |
| CN201366334Y (en) | Freeze drying granulation device | |
| CN205235429U (en) | Spray drying tower of airing exhaust on vertical | |
| CN107940900A (en) | The multilevel drying method and drying device of a kind of potassium fluoride in high activity | |
| CN201337869Y (en) | Dust removal unit for urea cooling fluidized bed | |
| CN210410597U (en) | Counter-flow pressure spray drying granulation system | |
| CN100560195C (en) | High-temperature spray concentration and low-temperature boiling granulation drying process and its combined device | |
| CN201676671U (en) | Urea fluidization and dust removal device | |
| CN207313454U (en) | A kind of amino acid waste liquor prepares the process units of fertilizer | |
| CN205613226U (en) | Dust -removing recovery device | |
| CN204495114U (en) | A kind of full-cream seasoning milk powder fluid bed cooler | |
| CN103028343A (en) | Production method for pelletoidal calcium chloride dihydrate | |
| CN202366673U (en) | Atomizing drying device | |
| CN103900350B (en) | Method for preventing sodium gluconate wet crystals from caking in drying process | |
| CN216704274U (en) | System for utilize high concentration calcium liquid production pellet form calcium chloride | |
| CN204594158U (en) | A kind of high-performance solid powder drying device | |
| CN103896929A (en) | Triglycidyl isocyanurate dry powder extruding and pelletizing production line and triglycidyl isocyanurate dry powder extruding and pelletizing production technology | |
| CN203728743U (en) | Full-automatic potassium sorbate production line | |
| CN203577343U (en) | Spray drying device of ceramic tile raw materials | |
| CN203803295U (en) | Molecular distillation monostearin enclosed circulating dusting system | |
| CN202709642U (en) | Distribution plate of vibrated fluidized bed | |
| CN206980666U (en) | A kind of spray granulation plant | |
| CN206045962U (en) | High tower spray crystallization system | |
| CN204672249U (en) | A kind of spraying dry and low temperature cold spray grain integrated apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: NANFANG XINYUAN FOOD BIOENGINEERING CO., LTD., ZHO Free format text: FORMER OWNER: LIU GAOFENG Effective date: 20101111 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 528436 TORCH HEALTH TECHNOLOGY PARK (YANJIANG EAST ROAD 2), ZHONGSHAN CITY, GUANGDONG PROVINCE TO: 528436 YANJIANG EAST ROAD 2, NATIONAL HEALTH TECHNOLOGY PARK, TORCH DEVELOPMENT AREA, ZHONGSHAN CITY, GUANGDONG PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20101111 Address after: 528436 national health base of Torch Development Zone, Guangdong, Zhongshan Province, two east along the river Patentee after: Nanfang Xinyuan Food Bioengineering Co., Ltd., Zhongshan City Address before: 528436 torch Health Science and technology industrial base, Zhongshan, Guangdong province (two East River Road) Patentee before: Liu Gaofeng |
|
| CX01 | Expiry of patent term |
Granted publication date: 20091223 |
|
| CX01 | Expiry of patent term |