CN106965957A - Cold packet system on Description on Production of Sulfaminic Acid line - Google Patents
Cold packet system on Description on Production of Sulfaminic Acid line Download PDFInfo
- Publication number
- CN106965957A CN106965957A CN201610477634.5A CN201610477634A CN106965957A CN 106965957 A CN106965957 A CN 106965957A CN 201610477634 A CN201610477634 A CN 201610477634A CN 106965957 A CN106965957 A CN 106965957A
- Authority
- CN
- China
- Prior art keywords
- cooling pipe
- production
- charging aperture
- cyclone dust
- blanking bin
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B1/00—Packaging fluent solid material, e.g. powders, granular or loose fibrous material, loose masses of small articles, in individual containers or receptacles, e.g. bags, sacks, boxes, cartons, cans, or jars
- B65B1/04—Methods of, or means for, filling the material into the containers or receptacles
- B65B1/10—Methods of, or means for, filling the material into the containers or receptacles by rotary feeders
- B65B1/12—Methods of, or means for, filling the material into the containers or receptacles by rotary feeders of screw type
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B1/00—Packaging fluent solid material, e.g. powders, granular or loose fibrous material, loose masses of small articles, in individual containers or receptacles, e.g. bags, sacks, boxes, cartons, cans, or jars
- B65B1/28—Controlling escape of air or dust from containers or receptacles during filling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G33/00—Screw or rotary spiral conveyors
- B65G33/08—Screw or rotary spiral conveyors for fluent solid materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
- B65G53/16—Gas pressure systems operating with fluidisation of the materials
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Cold packet system on Description on Production of Sulfaminic Acid line, the discharging opening of overflow spiral auger 1 and cooling pipe（2）Charging aperture communicate, the blower fan（7）Air outlet and cooling pipe（2）Air inlet communicate, cooling pipe（2）Discharging opening and cyclone dust collectors（3）Charging aperture communicate, cyclone dust collectors（3）Top exit and pulsed jet cloth filter（4）Charging aperture communicate, pulsed jet cloth filter（4）Outlet at bottom and pulsed jet cloth filter（4）Outlet and blanking bin（5）Import communicate, blanking bin（5）Outlet and conveying worm（6）Charging aperture communicate.The method have the advantages that：1st, the sulfamic acid packed by the present apparatus is better without caking；2nd, the present apparatus is utilizing the floating material recycle in production process, reduces production cost, protects working environment.
Description
Technical field
The present invention relates to Description on Production of Sulfaminic Acid line field, and in particular to the cold packet system on Description on Production of Sulfaminic Acid line.
Background technology
At present, Description on Production of Sulfaminic Acid line has substantial amounts of particulate dust floating in atmosphere in process of production, and the material of this floating finally all falls on the ground, finally it is cleaned, abandoning, this mode not only wastes material, and floating aerial particulate dust can impact to the body of people.
The content of the invention
The purpose of the present invention has substantial amounts of particulate dust floating in atmosphere in process of production aiming at current Description on Production of Sulfaminic Acid line, the material of this floating finally all falls on the ground, finally it is cleaned, abandon, this mode not only wastes material, and the deficiency that the aerial particulate dust of floating can be impacted to the body of people, and the cold packet system on Description on Production of Sulfaminic Acid line is provided.
The present invention includes overflow spiral auger, cooling pipe, cyclone dust collectors, pulsed jet cloth filter, blanking bin, conveying worm and blower fan, the cooling pipe length is 18-22m, charging aperture is provided with cooling pipe, air inlet and air outlet, the internal diameter of the cooling pipe is 150mm, overflow spiral auger discharging mouthful is communicated with the charging aperture of cooling pipe, the air outlet of the blower fan is communicated with the air inlet of cooling pipe, the discharging opening of cooling pipe is communicated with the charging aperture of cyclone dust collectors, cyclone dust collectors top exit is communicated with the charging aperture of pulsed jet cloth filter, the outlet of pulsed jet cloth filter outlet at bottom and pulsed jet cloth filter is communicated with the import of blanking bin, the outlet of blanking bin is communicated with the charging aperture of conveying worm.
The blanking bin is provided between watch window, and watch window and the charging aperture of blanking bin apart from 500-550MM.
Overflow spiral auger, cooling pipe, cyclone dust collectors, the housing of pulsed jet cloth filter, blanking bin and conveying worm use 304 stainless steel materials.
Cloth bag in the pulsed jet cloth filter uses anti-corrosion cloth bag.
The concrete technology step is as follows：
A, Description on Production of Sulfaminic Acid line discharge hole for discharge is through overflow spiral auger and enters cooling pipe, 50-60 DEG C of the discharge hole for discharge temperature of Description on Production of Sulfaminic Acid line, blower fan is to starting air blast in cooling pipe, the air quantity of blower fan is 5000M3/h, blast temperature 20-30；
After B, blower fan make cooling pipe 2 of the material for falling into cooling pipe by 20m length, temperature is down to 25-30 DEG C；
C, the material after cooling pipe cools enter cyclone dust collectors, material below 20 microns of particle diameter is discharged and entered in pocket type pulsed dust collector from top discharge mouthful by cyclone dust collectors, cyclone dust collectors discharge the material of more than 20 microns of particle diameter from bottom discharge mouthful, the discharging opening of cyclone dust collectors bottom discharge mouthful and pulse dust collector enters blanking bin, and blanking bin material is discharged through conveying worm.
The method have the advantages that：1st, the sulfamic acid packed by the present apparatus is better without caking；2nd, the present apparatus is utilizing the floating material recycle in production process, reduces production cost, protects working environment.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention.
Embodiment
As shown in Figure 1, the present invention includes overflow spiral auger 1, cooling pipe 2, cyclone dust collectors 3, pulsed jet cloth filter 4, blanking bin 5, conveying worm 6 and blower fan 7, the length of cooling pipe 2 is 18-22m, charging aperture is provided with cooling pipe 2, air inlet and air outlet, the internal diameter of the cooling pipe 2 is 150mm, the discharging opening of overflow spiral auger 1 is communicated with the charging aperture of cooling pipe 2, the air outlet of the blower fan 7 is communicated with the air inlet of cooling pipe 2, the discharging opening of cooling pipe 2 is communicated with the charging aperture of cyclone dust collectors 3, the top exit of cyclone dust collectors 3 is communicated with the charging aperture of pulsed jet cloth filter 4, the outlet of the outlet at bottom of pulsed jet cloth filter 4 and pulsed jet cloth filter 4 is communicated with the import of blanking bin 5, the outlet of blanking bin 5 is communicated with the charging aperture of conveying worm 6.
The blanking bin 5 is provided between watch window, and the charging aperture of watch window and blanking bin 5 apart from 500-550MM.
Overflow spiral auger 1, cooling pipe 2, cyclone dust collectors 3, the housing of pulsed jet cloth filter 4, blanking bin 5 and conveying worm 6 use 304 stainless steel materials.
Cloth bag in the pulsed jet cloth filter 4 uses anti-corrosion cloth bag.
The concrete technology step is as follows：
A, the discharge hole for discharge of Description on Production of Sulfaminic Acid line are through overflow spiral auger 1 and entrance cooling pipe 2,50-60 DEG C of the discharge hole for discharge temperature of Description on Production of Sulfaminic Acid line, blower fan is to starting air blast in cooling pipe 2, the air quantity of blower fan is 5000M3/h, blast temperature 20-30, preferably 25 DEG C；
After B, blower fan make cooling pipe 2 of the material for falling into cooling pipe 2 by 20m length, temperature is down to 25-30 DEG C；
C, the material after the cooling of cooling pipe 2 enter cyclone dust collectors 3, material below 20 microns of particle diameter is discharged and entered in pocket type pulsed dust collector from top discharge mouthful by cyclone dust collectors, cyclone dust collectors discharge the material of more than 20 microns of particle diameter from bottom discharge mouthful, the discharging opening of cyclone dust collectors bottom discharge mouthful and pulse dust collector enters blanking bin, and blanking bin material is discharged through conveying worm 6.
Claims (5)
1. for the cold packet system on Description on Production of Sulfaminic Acid line, it is characterised in that it includes overflow spiral auger（1）, cooling pipe（2）, cyclone dust collectors（3）, pulsed jet cloth filter（4）, blanking bin（5）, conveying worm（6）And blower fan（7）, the cooling pipe（2）Length is 18-22m, cooling pipe（2）On be provided with charging aperture, air inlet and air outlet, the cooling pipe（2）Internal diameter be 150mm, overflow spiral auger（1）Discharging opening and cooling pipe（2）Charging aperture communicate, the blower fan（7）Air outlet and cooling pipe（2）Air inlet communicate, cooling pipe（2）Discharging opening and cyclone dust collectors（3）Charging aperture communicate, cyclone dust collectors（3）Top exit and pulsed jet cloth filter（4）Charging aperture communicate, pulsed jet cloth filter（4）Outlet at bottom and pulsed jet cloth filter（4）Outlet and blanking bin（5）Import communicate, blanking bin（5）Outlet and conveying worm（6）Charging aperture communicate.
2. the cold packet system according to claim 1 on Description on Production of Sulfaminic Acid line, it is characterised in that the blanking bin（5）It is provided with watch window, and watch window and blanking bin（5）Charging aperture between apart from 500-550MM.
3. the cold packet system according to claim 1 on Description on Production of Sulfaminic Acid line, it is characterised in that overflow spiral auger（1）, cooling pipe（2）, cyclone dust collectors（3）, pulsed jet cloth filter（4）Housing, blanking bin（5）And conveying worm（6）Use 304 stainless steel materials.
4. the cold packet system according to claim 1 on Description on Production of Sulfaminic Acid line, it is characterised in that the pulsed jet cloth filter（4）Interior cloth bag uses anti-corrosion cloth bag.
5. a kind of processing technology for cold packet system on Description on Production of Sulfaminic Acid line, it is characterised in that the concrete technology step is as follows：
A, Description on Production of Sulfaminic Acid line discharge hole for discharge is through overflow spiral auger 1 and enters cooling pipe（2）, 50-60 DEG C of the discharge hole for discharge temperature of Description on Production of Sulfaminic Acid line, blower fan is to cooling pipe（2）Interior beginning air blast, the air quantity of blower fan is 5000M3/h, 20-30 DEG C of blast temperature；
B, blower fan make to fall into cooling pipe（2）Cooling pipe of the material Jing Guo 20m length（2）Afterwards, temperature is down to 25-30 DEG C；
C, by cooling pipe（2）Material after cooling enters cyclone dust collectors（3）Material below 20 microns of particle diameter is discharged and entered in pocket type pulsed dust collector from top discharge mouthful by cyclone dust collectors, cyclone dust collectors discharge the material of more than 20 microns of particle diameter from bottom discharge mouthful, the discharging opening of cyclone dust collectors bottom discharge mouthful and pulse dust collector enters blanking bin, and blanking bin material is through conveying worm（6）Discharge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610477634.5A CN106965957A (en) | 2016-06-28 | 2016-06-28 | Cold packet system on Description on Production of Sulfaminic Acid line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610477634.5A CN106965957A (en) | 2016-06-28 | 2016-06-28 | Cold packet system on Description on Production of Sulfaminic Acid line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106965957A true CN106965957A (en) | 2017-07-21 |
Family
ID=59334852
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610477634.5A Pending CN106965957A (en) | 2016-06-28 | 2016-06-28 | Cold packet system on Description on Production of Sulfaminic Acid line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106965957A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114834843A (en) * | 2022-05-20 | 2022-08-02 | 新疆征泰饲料有限公司 | Portable popped raw materials cooling material feeding unit |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3816202A1 (en) * | 1988-05-11 | 1989-11-23 | Motan Verfahrenstechnik | PLANT FOR PRODUCING AND PACKING A MULTIPLE MIXTURE |
| CN200991626Y (en) * | 2006-12-12 | 2007-12-19 | 贵阳铝镁设计研究院 | Petroleum coke calcination cooler dust-contained smoke treatment system apparatus |
| CN201105197Y (en) * | 2007-09-10 | 2008-08-27 | 杨圣保 | Fluidization dust-cleaning equipment |
| DE202008011260U1 (en) * | 2008-08-23 | 2008-11-20 | Merz Verpackungsmaschinen Gmbh | Mehrkomponent-Auger |
| CN102872963A (en) * | 2012-10-25 | 2013-01-16 | 南通新邦化工科技有限公司 | Flaky and lump stearate grinding process and equipment |
| CN103101979A (en) * | 2013-01-25 | 2013-05-15 | 清华大学 | Equipment system for producing mineral powder-grade manganous oxide by reducing low-grade manganese oxide ore through biomass |
-
2016
- 2016-06-28 CN CN201610477634.5A patent/CN106965957A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3816202A1 (en) * | 1988-05-11 | 1989-11-23 | Motan Verfahrenstechnik | PLANT FOR PRODUCING AND PACKING A MULTIPLE MIXTURE |
| CN200991626Y (en) * | 2006-12-12 | 2007-12-19 | 贵阳铝镁设计研究院 | Petroleum coke calcination cooler dust-contained smoke treatment system apparatus |
| CN201105197Y (en) * | 2007-09-10 | 2008-08-27 | 杨圣保 | Fluidization dust-cleaning equipment |
| DE202008011260U1 (en) * | 2008-08-23 | 2008-11-20 | Merz Verpackungsmaschinen Gmbh | Mehrkomponent-Auger |
| CN102872963A (en) * | 2012-10-25 | 2013-01-16 | 南通新邦化工科技有限公司 | Flaky and lump stearate grinding process and equipment |
| CN103101979A (en) * | 2013-01-25 | 2013-05-15 | 清华大学 | Equipment system for producing mineral powder-grade manganous oxide by reducing low-grade manganese oxide ore through biomass |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114834843A (en) * | 2022-05-20 | 2022-08-02 | 新疆征泰饲料有限公司 | Portable popped raw materials cooling material feeding unit |
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| Date | Code | Title | Description |
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| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170721 |
|
| WD01 | Invention patent application deemed withdrawn after publication |