CN203021046U - Triamine spiral discharging system - Google Patents
Triamine spiral discharging system Download PDFInfo
- Publication number
- CN203021046U CN203021046U CN 201220704653 CN201220704653U CN203021046U CN 203021046 U CN203021046 U CN 203021046U CN 201220704653 CN201220704653 CN 201220704653 CN 201220704653 U CN201220704653 U CN 201220704653U CN 203021046 U CN203021046 U CN 203021046U
- Authority
- CN
- China
- Prior art keywords
- discharging
- triamine
- spiral
- discharging system
- auger loader
- 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 - Fee Related
Links
Images
Abstract
The utility model relates to a spiral discharging system, in particular to a triamine spiral discharging system. The triamine spiral discharging system comprises a trap, wherein a discharge opening is formed at the lower portion of the trap, the discharge opening is connected with one end of a spiral conveyor, the other end of the spiral conveyor is connected with a discharging tank, and the spiral conveyor is connected with a motor. The length of the spiral conveyor is 7.5-8.5m, the diameter of the discharging tank is 3-3.5m, and the height of the discharging tank is 3-3.5. The spiral conveyor is added, so that the triamine spiral discharging system solves the problem of discharging speed, increases the size of the discharging tank, enables finished triamine articles to form material seal after stored at a certain height in the discharging tank, solves the problem of process gas brought by an original discharging system, and not only is low in ammonia consumption, but also reduces production cost.
Description
Technical field
The utility model relates to a kind of spiral discharging system, is specifically related to a kind of triamine spiral discharging system.
Background technology
The direct connection diameter of pressure spiral discharging mouth is the discharge tank of 0.6m, and discharge tank lower part outlet material enters the discharging pipeline from the discharge tank bottom.Because former discharge tank small volume, need continuous blowing, so very easily cause process gas to run into the discharging pipeline, cause ammonia consume high, cost of product increases and cause environmental pollution; The material situation if collapsing appears in crystallizer or drip catcher, to such an extent as to cause the large blocking pipeline of moment load, therefore discharge system also can be forced to stop, and causes the decline of production efficiency.
The utility model content
According to above deficiency of the prior art, the technical problems to be solved in the utility model is: provide a kind of ammonia to consume low, as to have reduced productive costs triamine spiral discharging system.
The technical scheme that its technical matters that solves the utility model adopts is:
Described triamine spiral discharging system, comprise drip catcher, the drip catcher bottom arranges discharging opening, discharging opening is connected with an end of auger loader, the auger loader other end connects discharge tank, and auger loader is connected with motor, and the length of auger loader is 7.5-8.5m, the discharge tank diameter is 3-3.5m, is highly 3-3.5m.
The preferred 7.5m of the length of described auger loader, the auger loader of setting up can be regulated discharging speed.
The preferred 3m of described discharge tank diameter, highly preferred 3m.
The utility model has solved the problem of discharging speed and discharge system band process gas by the size of setting up auger loader and increase discharge tank.Before transformation, discharge system triamine per ton is taken away 65kg ammonia, and after transformation, discharge system is not with ammonia.By 2.5 ten thousand tons of every annual output triamines, the annual ammonia 1625t that saves.Per ton by the liquefied ammonia price is 3100 yuan of calculations, 503.75 ten thousand yuan of annual escapable costs.
The beneficial effect that the utility model has is:
The utility model has solved the problem of discharging speed by setting up auger loader, the size that increases discharge tank makes finished product triamine material form the material envelope after discharge tank accumulates certain altitude, avoided the problem of former discharge system band process gas, not only ammonia consumes low but also has reduced productive costs.
Description of drawings
Fig. 1 is the utility model structural representation;
In figure: 1, drip catcher; 2, discharge tank; 3, auger loader; 4, motor; 5, discharging opening.
The specific embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described further:
As shown in Figure 1, described triamine spiral discharging system comprises drip catcher 1, and drip catcher 1 bottom arranges discharging opening 5, and discharging opening 5 is connected with an end of auger loader 3, and auger loader 3 other ends connect discharge tanks 2, and auger loader 3 is connected with motor 4.The preferred 7.5m of the length of auger loader 3, the auger loader 3 of setting up can be regulated discharging speed.The discharge tank 2 preferred 3m of diameter, highly preferred 3m.
The utility model has solved the problem of discharging speed and discharge system band process gas by the size of setting up auger loader 3 and increase discharge tank 2.Before transformation, discharge system triamine per ton is taken away 65kg ammonia, and after transformation, discharge system is not with ammonia.By 2.5 ten thousand tons of every annual output triamines, the annual ammonia 1625t that saves.Per ton by the liquefied ammonia price is 3100 yuan of calculations, 503.75 ten thousand yuan of annual escapable costs.The utility model has solved the problem of discharging speed by setting up auger loader 3, the size that increases discharge tank 2 makes finished product triamine material form the material envelope after discharge tank 2 accumulates certain altitude, avoided the problem of former discharge system band process gas, not only ammonia consumes low but also has reduced productive costs.
The length of the auger loader 3 in the present embodiment is 8m, and discharge tank 2 diameters are 3.5m, is highly 3m, all the other constructional features such as embodiment 1.
The length of the auger loader 3 in the present embodiment is 8.5m, and discharge tank 2 diameters are 3.5m, is highly 3.5m, all the other constructional features such as embodiment 1.
Claims (3)
1. triamine spiral discharging system, comprise drip catcher (1), it is characterized in that: drip catcher (1) bottom arranges discharging opening (5), discharging opening (5) is connected with an end of auger loader (3), auger loader (3) other end connects discharge tank (2), and auger loader (3) is connected with motor (4), and the length of auger loader (3) is 7.5-8.5m, discharge tank (2) diameter is 3-3.5m, is highly 3-3.5m.
2. triamine spiral discharging according to claim 1 system, it is characterized in that: the length of described auger loader (3) is 7.5m.
3. triamine spiral discharging according to claim 1 system, it is characterized in that: described discharge tank (2) diameter is 3m, is highly 3m.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220704653 CN203021046U (en) | 2012-12-18 | 2012-12-18 | Triamine spiral discharging system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220704653 CN203021046U (en) | 2012-12-18 | 2012-12-18 | Triamine spiral discharging system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203021046U true CN203021046U (en) | 2013-06-26 |
Family
ID=48645044
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220704653 Expired - Fee Related CN203021046U (en) | 2012-12-18 | 2012-12-18 | Triamine spiral discharging system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203021046U (en) |
-
2012
- 2012-12-18 CN CN 201220704653 patent/CN203021046U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201694807U (en) | Bottle cover conveying device of beverage filling cover screwing machine | |
| CN203320022U (en) | Discharging system | |
| CN203021046U (en) | Triamine spiral discharging system | |
| CN202188302U (en) | Loxygen recovery and reuse system for space division machine | |
| CN201302037Y (en) | Liquid chlorine packaging tail gas recovery unit | |
| CN103672395A (en) | Method for recycling emptying residual gas of high purity gas transportation and storage tank | |
| CN201890838U (en) | Air supply device of bottle making machine | |
| CN203726733U (en) | Novel mold runner structure | |
| CN202146759U (en) | Pressurized reactor | |
| CN203615061U (en) | Emptied gas recycling device for gas transportation storage tank | |
| CN203615062U (en) | Recycle device for depressurizing and emptying gas-liquid storage tank | |
| CN203612683U (en) | Dust-free environment-friendly material conveying and feeding system | |
| CN202115805U (en) | High-viscosity raw material discharging device | |
| CN201916259U (en) | Water pumping device used for water storage tank in plastic production | |
| CN203305416U (en) | Vulcanization device for producing organic-silicon-modified polyether adhesive | |
| CN202201355U (en) | Resin pot with pressurized discharging mechanism | |
| CN202239482U (en) | Sand warehouse moulding sand delivering structure | |
| CN202557804U (en) | Simple packaging equipment | |
| CN201672243U (en) | Device of LNG filling station with automatic pressure reducing function | |
| CN204528651U (en) | A kind of device of reinforced glass conveying | |
| CN203333283U (en) | Liquid sealing and transferring device | |
| CN201721660U (en) | Medicine outer package flatting device | |
| CN202414183U (en) | Cosmetic cream semi-finished product conveying and feeding device | |
| CN202449832U (en) | Dimethoxymethane gas-liquid separation buffer for production of polyformaldehyde | |
| CN204454905U (en) | A kind of formaldehyde discharge system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: HELI TECHNOLOGY CO., LTD. Free format text: FORMER NAME: SHANDONG UNITED CHEMICAL INDUSTRY CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 256100 No. 36 Dongfeng Road, Yiyuan County, Shandong, Zibo Patentee after: SHANDONG LIAHERD CHEMICAL INDUSTRY CO., LTD. Address before: 256100 No. 36 Dongfeng Road, Yiyuan County, Shandong, Zibo Patentee before: Shandong United Chemical Industry Co., Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171106 Address after: Yiyuan County Economic Development Zone 256100 Shandong city of Zibo province (county Yihe Road No. 1329) Patentee after: Shandong Heli Chemical Co., Ltd. Address before: 256100 No. 36 Dongfeng Road, Yiyuan County, Shandong, Zibo Patentee before: SHANDONG LIAHERD CHEMICAL INDUSTRY CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130626 Termination date: 20181218 |