CN205253044U - Continuous granulation system of high -load thermal sensitivity surface -activeagent - Google Patents
Continuous granulation system of high -load thermal sensitivity surface -activeagent Download PDFInfo
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- CN205253044U CN205253044U CN201521116745.0U CN201521116745U CN205253044U CN 205253044 U CN205253044 U CN 205253044U CN 201521116745 U CN201521116745 U CN 201521116745U CN 205253044 U CN205253044 U CN 205253044U
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- feeding machine
- extruder
- discharge valve
- delivery pump
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Abstract
The utility model discloses a continuous granulation system of high -load thermal sensitivity surface -activeagent, include the delivery pump of being connected with the feed jar, the delivery pump other end with scrape film -type evaporator and be connected, the roll -type tablet press of scraping film -type evaporator and being connected with rotatory discharge valve is connected, rotatory discharge valve send pipeline and air conveying system to be connected through wind, air conveying system links to each other with the feeding machine that is equipped with the extruder, the extruder is connected with needle -like conveyor belt, needle -like conveyor belt is connected with the vibratory liquefaction bed, the vibratory liquefaction bed links to each other with the needle -like baling line feeding machine that is equipped with the shale shaker, needle -like baling line feeding machine is connected with package system, the utility model discloses product quality is good, and it is even to distribute, does not have yellow, stain, and the moisture content is low, is difficult for the moisture absorption, does not contain powder dress, cubic product, simultaneously can continuous production, both raised the efficiency, and can also reduce unnecessary energy resource consumption and pollution.
Description
Technical field
The utility model relates to a kind of high-load heat-sensitive surfactant continuous granulation system.
Background technology
Lauryl sodium sulfate is a kind of thermal sensitivity, steeps stickum more, in industry, it carried out to dry condition very harsh. If color and luster can occur when baking temperature is too high to be deepened, easily decomposes; Temperature is too low can cause again that viscosity is higher, difficult decomposes, and makes can not reach the drying effect of stability and high efficiency in industrial production. Existing dry lauryl sodium sulfate adopts drying process with atomizing conventionally, this technology utilization hot-air is as drying medium, but material just starts to decompose coking for 4 hours under 100 DEG C of conditions, cause occurring yellow, stain have a strong impact on product quality, and material being again viscosity powder in white powder, easily be bonded on spray tower tower wall, therefore after driving 10 hours, essential parking purge column wall, affects production efficiency at every turn, produces a large amount of washes.
Utility model content
The purpose of this utility model is to provide a kind of high-load heat-sensitive surfactant continuous granulation system.
The technical solution adopted in the utility model is:
A kind of high-load heat-sensitive surfactant continuous granulation system, comprise and the tank connected delivery pump of feed, the delivery pump other end is connected with luwa evaporator, described luwa evaporator is connected with the roller-type sheet-pressing machine that is connected with rotary discharge valve, described rotary discharge valve is connected with blast system by air delivery pipe, blast system is connected with the feeding machine that is provided with extruder, described extruder is connected with needle-like belt conveyor, described needle-like belt conveyor is connected with vibrated fluidized bed, described vibrated fluidized bed is connected with the needle-like baling line feeding machine that is provided with vibratory sieve, described needle-like baling line feeding machine is connected with packaging system.
Advantage of the present utility model: good product quality, be evenly distributed, there is no yellow point, stain, moisture is low, is difficult for the moisture absorption,, containing powder dress, bulk product, can not produce continuously simultaneously, both raises the efficiency, and can also reduce unnecessary energy resource consumption and pollution.
Brief description of the drawings
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Fig. 1 is structural representation of the present utility model.
Wherein: 1, gravitation tank; 2, charging pump; 3, luwa evaporator; 4, roller-type sheet-pressing machine; 5, rotary discharge valve; 6, air delivery pipe; 7, blast system; 8, feeding hopper; 9, extruder; 10, needle-like belt conveyor; 11, vibrated fluidized bed; 12, vibratory sieve; 13, needle-like baling line feeding hopper; 14, packaging system.
Detailed description of the invention
As shown in Figure 1, a kind of high-load heat-sensitive surfactant continuous granulation system, comprise the delivery pump 2 being connected with gravitation tank 1, delivery pump 2 other ends are connected with luwa evaporator 3, luwa evaporator 3 is connected with the roller-type sheet-pressing machine 4 that is connected with rotary discharge valve 5, rotary discharge valve 5 is connected with blast system 7 by air delivery pipe 6, blast system 7 is connected with the feeding machine 8 that is provided with extruder 9, extruder 9 is connected with needle-like belt conveyor 10, needle-like belt conveyor 10 is connected with vibrated fluidized bed 11, vibrated fluidized bed 11 is connected with the needle-like baling line feeding machine 13 that is provided with vibratory sieve 12, needle-like baling line feeding machine 13 is connected with packaging system 14.
When the utility model uses, to in gravitation tank, the temperature of the lauryl sodium sulfate of moisture content 30% be controlled to 50 ° ~ 70 °, under 0.2 ~ 0.6Mpa pressure, make material enter in luwa evaporator with delivery pump, be dried, dried material water ratio is lower than 3%, it is cooling and carry out compressing tablet by big or small roller that dried material enters roller-type sheet-pressing machine, the granule disperseing after dry is squeezed into product on chip, send rotary valve and air delivery pipe to send into blast system cyclone separator by wind the material that is cooled to sheet and carry out sedimentation separation, the material of separating enters extruder feeding hopper by material diversion, entering respectively screw extruder carries out obtaining needle-like product after granulation, needle-like product temperature is 35 DEG C of left and right, needle-like size is particle diameter φ 1.2mm, length is 2 ~ 3mm, after the little hopper of needle-like product introduction, falling into needle-like belt conveyor carries out once cooling and is transported to strap end, arriving the needle-like product of strap end falls into vibrated fluidized bed import to carry out secondary cooling and be transported to fluid bed outlet and enter vibratory sieve, now needle-like product temperature is 10 DEG C of left and right, cooled needle-like product is carried out to 2 screenings by vibratory sieve, remove the bulk in needle-like product, powder product, finally complete the packaging of product by automatic packaging line, carry and piling.
The utility model good product quality, is evenly distributed, and there is no yellow point, stain, and moisture is low, is difficult for the moisture absorption,, containing powder dress, bulk product, can not produce continuously simultaneously, both raises the efficiency, and can also reduce unnecessary energy resource consumption and pollution.
Claims (1)
1. a high-load heat-sensitive surfactant continuous granulation system, it is characterized in that: comprise and the tank connected delivery pump of feed, the delivery pump other end is connected with luwa evaporator, described luwa evaporator is connected with the roller-type sheet-pressing machine that is connected with rotary discharge valve, described rotary discharge valve is connected with blast system by air delivery pipe, blast system is connected with the feeding machine that is provided with extruder, described extruder is connected with needle-like belt conveyor, described needle-like belt conveyor is connected with vibrated fluidized bed, described vibrated fluidized bed is connected with the needle-like baling line feeding machine that is provided with vibratory sieve, described needle-like baling line feeding machine is connected with packaging system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521116745.0U CN205253044U (en) | 2015-12-30 | 2015-12-30 | Continuous granulation system of high -load thermal sensitivity surface -activeagent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521116745.0U CN205253044U (en) | 2015-12-30 | 2015-12-30 | Continuous granulation system of high -load thermal sensitivity surface -activeagent |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205253044U true CN205253044U (en) | 2016-05-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521116745.0U Active CN205253044U (en) | 2015-12-30 | 2015-12-30 | Continuous granulation system of high -load thermal sensitivity surface -activeagent |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205253044U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107014159A (en) * | 2017-04-21 | 2017-08-04 | 江苏丰益化工科技有限公司 | A kind of drying equipment and method for lauryl sodium sulfate |
| CN107033036A (en) * | 2017-04-21 | 2017-08-11 | 江苏丰益化工科技有限公司 | A kind of drying system and method for lauryl sodium sulfate |
-
2015
- 2015-12-30 CN CN201521116745.0U patent/CN205253044U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107014159A (en) * | 2017-04-21 | 2017-08-04 | 江苏丰益化工科技有限公司 | A kind of drying equipment and method for lauryl sodium sulfate |
| CN107033036A (en) * | 2017-04-21 | 2017-08-11 | 江苏丰益化工科技有限公司 | A kind of drying system and method for lauryl sodium sulfate |
| CN107033036B (en) * | 2017-04-21 | 2019-08-16 | 江苏丰益化工科技有限公司 | A kind of drying system and method for lauryl sodium sulfate |
| CN107014159B (en) * | 2017-04-21 | 2019-09-17 | 江苏丰益化工科技有限公司 | A kind of drying equipment and method for lauryl sodium sulfate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 226221 no.226 Shanghai Road, Qidong life and Health Industrial Park, Nantong City, Jiangsu Province Patentee after: Jiangsu Youyang Pharmaceutical Co.,Ltd. Address before: 226200 no.226 Shanghai Road, Binjiang fine chemical industry park, Qidong City, Nantong City, Jiangsu Province Patentee before: JIANGSU FENGYI CHEMICAL TECHNOLOGY Co.,Ltd. |
|
| CP03 | Change of name, title or address |