CN100395500C - Drying process of rubber additives - Google Patents
Drying process of rubber additives Download PDFInfo
- Publication number
- CN100395500C CN100395500C CNB2005100450023A CN200510045002A CN100395500C CN 100395500 C CN100395500 C CN 100395500C CN B2005100450023 A CNB2005100450023 A CN B2005100450023A CN 200510045002 A CN200510045002 A CN 200510045002A CN 100395500 C CN100395500 C CN 100395500C
- Authority
- CN
- China
- Prior art keywords
- drying
- flash dryer
- sent
- dryer
- rubber additives
- 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
Images
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
本发明公开了一种橡胶助剂的干燥工艺。它解决了目前橡胶助剂干燥工艺中物料干燥率低,物料干燥不充分的问题,具有干燥效果好,热效率高,产品粒度小,投资少等优点。其工艺过程为:送料、闪蒸干燥机加气流干燥机烘干、除尘收集后尾气排空,其特征是:湿物料经加料机送入闪蒸干燥机,闪蒸干燥机对物料进行打散、干燥,然后半干物料在气流内进行二次烘干,干燥好的物料送入布袋除尘器除尘收集,尾气排空。
The invention discloses a drying process for rubber additives. It solves the problems of low material drying rate and insufficient material drying in the current drying process of rubber additives, and has the advantages of good drying effect, high thermal efficiency, small product particle size, and low investment. The process is as follows: feeding, drying with flash dryer plus airflow dryer, exhausting after dust removal and collection, the characteristics are: the wet material is sent into the flash dryer through the feeder, and the flash dryer breaks up the material , drying, and then the semi-dry material is dried twice in the air flow, and the dried material is sent to the bag filter for dust collection, and the tail gas is emptied.
Description
技术领域 technical field
本发明涉及一种橡胶助剂的干燥工艺。The invention relates to a drying process for rubber additives.
背景技术 Background technique
现有的橡胶助剂干燥工艺为双级气流烘干过程,其存在的缺点为干燥气流速度高,物料停留时间短,干燥效果差,产品含水量容易波动;在干燥过程中,橡胶助剂有粘性,湿物料容易在气流管上粘壁,粘壁后清理困难。同时,双级气流工艺路线复杂,干燥风量和压头大,动力消耗高,能量利用率低,热效率低,运行成本高;除尘系统复杂,设备占地面积大,投资高,出料点多,操作困难,工人劳动强度大。The existing drying process of rubber additives is a two-stage airflow drying process, which has the disadvantages of high drying air velocity, short material residence time, poor drying effect, and easy fluctuation of product moisture content; during the drying process, rubber additives have Viscous, wet materials are easy to stick to the wall of the air flow pipe, and it is difficult to clean up after sticking to the wall. At the same time, the two-stage air flow process route is complicated, the drying air volume and pressure head are large, the power consumption is high, the energy utilization rate is low, the thermal efficiency is low, and the operating cost is high; the dust removal system is complex, the equipment occupies a large area, high investment, and many discharge points. The operation is difficult and the labor intensity of the workers is high.
发明内容 Contents of the invention
本发明的目的就是为了解决目前橡胶助剂干燥工艺中物料干燥率低,物料干燥不充分的问题,提供一种采用闪蒸干燥机与其流干燥机组合进行两次干燥,这种干燥工艺具有干燥效果好,热效率高,产品粒度小,投资少等优点。The purpose of the present invention is to solve the problem of low material drying rate and insufficient material drying in the current drying process of rubber additives, and to provide a combination of a flash dryer and a flow dryer for two times of drying. This drying process has the advantages of drying Good effect, high thermal efficiency, small product size, less investment and so on.
为实现上述目的,本发明采用了如下技术方案:一种橡胶助剂的干燥工艺,它的工艺过程为,送料、闪蒸干燥机加气流干燥机烘干、除尘收集后尾气排空,其特征是:湿物料经加料机送入闪蒸干燥机,闪蒸干燥机对物料进行打散、干燥,然后半干物料在气流内进行二次烘干,干燥好的物料送入布袋除尘器除尘收集,尾气排空。In order to achieve the above object, the present invention adopts the following technical scheme: a drying process for rubber additives. Its process is as follows: feeding, drying in a flash dryer plus an airflow dryer, and exhausting the tail gas after dust removal and collection. Yes: the wet material is sent into the flash dryer through the feeder, the flash dryer disperses and dries the material, and then the semi-dry material is dried twice in the air flow, and the dried material is sent to the bag filter for dust collection , the exhaust gas is emptied.
所述闪蒸干燥机连通加热的工艺空气,工艺空气经过过滤器及换热器加热后,经管道送入闪蒸干燥机。The flash dryer is connected with the heated process air, and the process air is sent into the flash dryer through a pipeline after being heated by a filter and a heat exchanger.
所述布袋除尘器通过管路与风机连接,布袋除尘后的工艺空气由风机排空。The bag filter is connected to the fan through pipelines, and the process air after bag dust removal is exhausted by the fan.
本发明在现有气流干燥工艺的基础上,将闪蒸干燥机干燥和气流干燥工艺结合起来,形成两次干燥,从而充分提高了物料的干燥效率;同时由于闪蒸干燥机内有高速旋转的粉碎机构,不仅可以将大块的物料打散、粉碎,还可以加强气流与湿物料的扰动,提高干燥强度,减小设备体积,从而节省设备投资。本干燥工艺可延长物料干燥停留时间,干燥效率高;打散后的物料颗粒小,为100目以上,可以通过控制风速的方法实现产品的分级,不粘壁,不影响设备连续运行,整个工艺投资小,占地面积小。On the basis of the existing airflow drying process, the present invention combines flash dryer drying and airflow drying process to form two times of drying, thereby fully improving the drying efficiency of materials; The crushing mechanism can not only disperse and crush large pieces of materials, but also strengthen the disturbance of airflow and wet materials, improve drying strength, and reduce equipment volume, thereby saving equipment investment. This drying process can prolong the drying residence time of the material, and the drying efficiency is high; the particle size of the dispersed material is small, more than 100 mesh, and the classification of the product can be realized by controlling the wind speed. It does not stick to the wall and does not affect the continuous operation of the equipment. The whole process Small investment, small footprint.
附图说明 Description of drawings
图1为本发明的工艺流程图。Fig. 1 is a process flow diagram of the present invention.
其中,1.过滤器,2.换热器,3.加料机,4.闪蒸干燥机,5.气流干燥机,6.布袋除尘器,7.风机。Among them, 1. Filter, 2. Heat exchanger, 3. Feeding machine, 4. Flash dryer, 5. Airflow dryer, 6. Bag filter, 7. Fan.
具体实施方式 Detailed ways
下面结合附图与实施例对本发明作进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
图1中,湿物料经过加料机3进入闪蒸干燥机4,由空气、冷凝水和饱和蒸汽构成的工艺空气经过滤器1和换热器2后也送入闪蒸干燥4机。闪蒸干燥机4将物料打散后与高温工艺空气混合干燥,然后物料送入气流干燥机5进行第二次干燥,干燥好的物料送入布袋除尘器6进行除尘收集,布袋除尘器6与风机7连接,布袋除尘后的工艺空气进入风机7排空,成品送出即可。In Figure 1, the wet material enters the flash dryer 4 through the feeder 3, and the process air composed of air, condensed water and saturated steam is also sent to the flash dryer 4 after passing through the
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100450023A CN100395500C (en) | 2005-11-01 | 2005-11-01 | Drying process of rubber additives |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100450023A CN100395500C (en) | 2005-11-01 | 2005-11-01 | Drying process of rubber additives |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1786634A CN1786634A (en) | 2006-06-14 |
| CN100395500C true CN100395500C (en) | 2008-06-18 |
Family
ID=36784185
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100450023A Expired - Lifetime CN100395500C (en) | 2005-11-01 | 2005-11-01 | Drying process of rubber additives |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100395500C (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103445065B (en) * | 2013-09-02 | 2015-03-25 | 河南黄国粮业股份有限公司 | Vortex air flow drying method for glutinous rice |
| CN105180624B (en) * | 2015-08-31 | 2017-10-27 | 无锡华虹信息科技有限公司 | A kind of low speed flow drying equipment |
| CN105195283A (en) * | 2015-10-29 | 2015-12-30 | 天紫环保装备制造(天津)有限公司 | Pressure relief device of garbage flash blasting equipment |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3930318A (en) * | 1973-04-23 | 1976-01-06 | Continental Can Company, Inc. | Ultraviolet curing machine |
| CN2081516U (en) * | 1990-10-19 | 1991-07-24 | 张维屏 | Bulk material vibrating flowing dryer |
| CN2322107Y (en) * | 1998-01-22 | 1999-06-02 | 王家忠 | Double-agitating stair type secondary drying machine |
| WO2000067970A1 (en) * | 1999-05-06 | 2000-11-16 | Slrg Drying Co Pty Ltd | Method and apparatus for drying material |
-
2005
- 2005-11-01 CN CNB2005100450023A patent/CN100395500C/en not_active Expired - Lifetime
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3930318A (en) * | 1973-04-23 | 1976-01-06 | Continental Can Company, Inc. | Ultraviolet curing machine |
| CN2081516U (en) * | 1990-10-19 | 1991-07-24 | 张维屏 | Bulk material vibrating flowing dryer |
| CN2322107Y (en) * | 1998-01-22 | 1999-06-02 | 王家忠 | Double-agitating stair type secondary drying machine |
| WO2000067970A1 (en) * | 1999-05-06 | 2000-11-16 | Slrg Drying Co Pty Ltd | Method and apparatus for drying material |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1786634A (en) | 2006-06-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203454660U (en) | Drying house for drying agricultural and sideline products through air energy heat pump | |
| CN201897365U (en) | Vibration fluidized bed microwave drying system for vapor compression heat energy recirculation | |
| WO2016201665A1 (en) | Rotary drying device | |
| CN103256791B (en) | A kind of atlapulgite drying system | |
| CN207501560U (en) | Microwave drying vibrated fluidized bed | |
| CN203534103U (en) | Pneumatic drying device | |
| CN206207958U (en) | A kind of spray drying tower | |
| CN203447786U (en) | A superheated steam closed circuit spray dryer | |
| CN100395500C (en) | Drying process of rubber additives | |
| CN101876501B (en) | Material concurrent flow and jigging drying device and process | |
| CN103322773B (en) | System and method for drying sodium sulfite materials | |
| CN204329538U (en) | A kind of high-efficiency and energy-saving type kudzu-vine root powder pneumatic drier | |
| CN203053181U (en) | Hot blast pulse flow drying device for expansible graphite | |
| CN206056225U (en) | A kind of flash dryer circulation of tail gas application system | |
| CN102679704B (en) | High-temperature heat pump energy-saving system of industrial drum dryer | |
| CN103697673B (en) | Air energy airflow drying equipment | |
| CN205425621U (en) | Fluidized bed dryer automatic feed device | |
| CN203454664U (en) | Corn protein powder drying system | |
| CN103512313A (en) | Combined type moist material fluidized bed superheated steam drying system | |
| CN203848610U (en) | Impact type eucommia key-fruit shell drying device | |
| CN210463769U (en) | Heat source recycling device | |
| CN206974106U (en) | A kind of hot-air drying unit of large-size particles | |
| CN209877487U (en) | Coal grinds pipeline drying system | |
| CN202648354U (en) | High temperature heat pump energy saving system for industrial tumble dryer | |
| CN206235087U (en) | A kind of flash evaporation drying device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: SHANDONG TIANLI DRYING CO., LTD. Free format text: FORMER NAME: TIANLI DRYING EQUIPMENT CO., LTD., SHANDONG |
|
| CP03 | Change of name, title or address |
Address after: 250101, Shandong Province, Ji'nan hi tech Zone, No. 554 Feng Feng Road, environmental science and Technology Park, building 8, Feng Feng building, room 230 Patentee after: SHANDONG TIANLI DRYING TECHNOLOGY AND EQUIPMENT Co.,Ltd. Address before: 250014 Shandong Province, Lixia District of Ji'nan city ten Road East Shouke Hospital Road No. 19 Patentee before: Shandong Tianli Drying Equipment Co.,Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20080618 |
|
| CX01 | Expiry of patent term |