CN203611376U - Multistage burdening equipment for producing regenerated polypropylene - Google Patents
Multistage burdening equipment for producing regenerated polypropylene Download PDFInfo
- Publication number
- CN203611376U CN203611376U CN201320869172.3U CN201320869172U CN203611376U CN 203611376 U CN203611376 U CN 203611376U CN 201320869172 U CN201320869172 U CN 201320869172U CN 203611376 U CN203611376 U CN 203611376U
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- distribution line
- feed
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- burdening
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- 239000004743 Polypropylene Substances 0.000 title claims abstract description 25
- -1 polypropylene Polymers 0.000 title claims abstract description 23
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 23
- 239000000463 material Substances 0.000 claims abstract description 141
- 230000007246 mechanism Effects 0.000 claims abstract description 34
- 238000009826 distribution Methods 0.000 claims description 70
- 239000000835 fiber Substances 0.000 claims description 19
- 230000008929 regeneration Effects 0.000 claims description 17
- 238000011069 regeneration method Methods 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 15
- 238000013329 compounding Methods 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 239000000654 additive Substances 0.000 claims description 9
- 230000000996 additive effect Effects 0.000 claims description 9
- 238000007599 discharging Methods 0.000 claims description 7
- 238000002156 mixing Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract 1
- 239000004033 plastic Substances 0.000 description 7
- 229920003023 plastic Polymers 0.000 description 7
- 239000002699 waste material Substances 0.000 description 7
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007380 fibre production Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005491 wire drawing Methods 0.000 description 1
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- Preliminary Treatment Of Fibers (AREA)
Abstract
Multistage burdening equipment for producing regenerated polypropylene comprises a first-level burdening device, a second-level burdening device and a third-level burdening device; the first-level burdening device comprises multiple first burdening lines for mixing first-level materials into second-level materials; the second-level burdening device comprises multiple second burdening lines for mixing the second-level materials into third-level materials; the third-level burdening device comprises multiple third burdening lines for mixing the third-level materials into fourth-level materials; the first-level materials are sent to the first burdening lines for mixing and burdening by a first feeding mechanism of each first burdening line; each first-level burdening line sends the second-level materials to the multiple second burdening lines by second charging mechanisms for mixing and burdening; each second-level burdening line sends the third-level materials to each corresponding third burdening line by third charging mechanisms for mixing and burdening. After the multistage burdening equipment is adopted, the automation of the burdening is realized, the burdening efficiency is improved, a more uniform effect is realized after the three levels of burdening and the quality of polypropylene yarns is improved.
Description
Technical field
The utility model relates to regeneration polypropylene fibre production equipment field, refers to specifically the multiple stage material compounding equipment that regeneration polypropylene fibre is produced that is applied to.
Background technology
Along with the development of regeneration techniques, many waste or used plastics can be reused for the production of polypropylene fibre, and this has not only reduced the production cost of enterprise, and can greatly reduce environmental pollution.While utilizing waste or used plastics to regenerate polypropylene fibre production, waste or used plastics needs the operations such as cutting, cleaning, dewatered drying, batching, melting, finally carries out wire drawing again and forms product.
In the burden process of producing at regeneration polypropylene fibre, multiple waste or used plastics need to be carried out to mix equably, and then carry out melting after adding additive.The burden process that existing regeneration polypropylene fibre is produced is to adopt the mode of artificial batching that multiple waste or used plastics and additive are carried out to mix, but adopt the mode of artificial batching to exist following deficiency: the one, operating efficiency is low, and adopt the mode of artificial batching to need a large amount of manpowers, so just indirectly improved production cost; The 2nd, prepare burden inhomogeneous, have a strong impact on the quality of polypropylene fiber silk.
Utility model content
The utility model provides the multiple stage material compounding equipment that regeneration polypropylene fibre is produced that is applied to, and its main purpose is to overcome existing regeneration polypropylene fibre and prepares burden that efficiency is lower, the inhomogeneous problem of preparing burden in producing.
In order to solve above-mentioned technical problem, the utility model adopts following technical scheme:
Be applied to the multiple stage material compounding equipment that regeneration polypropylene fibre is produced, comprise one-level proportioner, B grade mixture material device and three gradating material devices, described one-level proportioner comprises many first distribution line that one-level material are mixed into secondary material, described B grade mixture material device comprises many second distribution line that secondary material are mixed into three grades of material, and described three gradating material devices comprise that many articles add additive to be mixed into the 3rd distribution line of level Four material in three grades of material; Described every first distribution line is delivered to one-level material in the first distribution line, to carry out mix by the first feed mechanism, described every first distribution line is delivered to secondary material in described many second distribution line and is carried out mix by the second feed mechanism, and described every second distribution line is delivered to three grades of material in every corresponding the 3rd distribution line and carried out mix by the 3rd feed mechanism.
Described every first distribution line comprises multiple the first feed bins that are set up in parallel and is positioned at the first material conveyer belt under multiple the first feed bins, the top of each the first feed bin is provided with the first charging aperture, the bottom of each the first feed bin is provided with the first discharging opening, one end of described the first material conveyer belt is the first feed end, its other end is the first discharge end, and described the second feed mechanism is located at the first discharge end place.
Described the first feed mechanism comprise the first material pipe and with multiple the first feed bins one by one corresponding and be communicated with multiple Celloco fractionator Cellocos, each Celloco fractionator Celloco be located at the first corresponding feed bin directly over, each Celloco fractionator Celloco is communicated with the first material pipe, and each Celloco fractionator Celloco is provided with the one-level material in the first material pipe is drawn to the first suction blower fan in Celloco fractionator Celloco, and the plurality of the first suction blower fan is controlled by one first controller.
Described every second distribution line comprises multiple the second feed bins that are set up in parallel and is positioned at the second material conveyer belt under the plurality of the second feed bin, the top of each the second feed bin is provided with the second charging aperture, the bottom of each the second feed bin is provided with the second discharging opening, one end of described the second material conveyer belt is the second feed end, its other end is the second discharge end, described the 3rd feed mechanism is located at the second discharge end place, the number of the second feed bin in described every second distribution line is identical with the number of the first distribution line, the second feed bin of described many second distribution line is multiple lines and multiple rows and arranges.
The second material pipe that described the second feed mechanism comprises the second suction bucket and is communicated with the second suction bucket, this the second suction bucket is provided with the second induced-draught fan, every the second material pipe is communicated with each the second charging aperture on every row the second feed bin, each the second charging aperture is provided with the second suction blower fan, and the second suction blower fan on every row the second feed bin is controlled by a second controller.
Described every the 3rd distribution line comprises a 3 material conveyer belt, one end of this 3 material conveyer belt is the 3rd feed end, its other end is the 3rd discharge end, described the 3rd feed end is communicated with the 3rd feed mechanism, described the 3rd discharge end place is provided with suction funnel, this suction funnel is communicated with the batch can that is contained with additive by tube connector, and described suction funnel is controlled by one the 3rd controller.
The 3 material pipeline that described the 3rd feed mechanism comprises the 3rd suction bucket and is communicated with the 3rd suction bucket, the 3rd suction bucket is provided with the 3rd induced-draught fan, and described 3 material pipeline is communicated with the 3rd feed end of 3 material conveyer belt.
To description of the present utility model, compared to the prior art, the utlity model has following advantage from above-mentioned:
The utility model is reasonable in design, be skillfully constructed, one-level material is again mixed rear formation secondary material by described every first distribution line, this secondary material is delivered in many second distribution line by the second feed mechanism, because the first distribution line has many, in every second distribution line, just there is so the multiple secondary material of bringing from many first distribution line, this multiple secondary material forms three grades of material after the second distribution line is mixed, these three grades of material are delivered in the 3rd corresponding distribution line by the 3rd feed mechanism, in every the 3rd distribution line, add additive three grades of material can be mixed into level Four material, then this level Four material just can be for melting.Adopt the utility model to prepare burden not only to realize batching automation, improved batching efficiency, and batching is more even after three grades of mixing, thereby has improved the quality of polypropylene fiber silk.
Accompanying drawing explanation
Fig. 1 is schematic top plan view of the present utility model.
Fig. 2 is that schematic diagram is looked on a left side for the utility model the first distribution line.
Fig. 3 is that schematic diagram is looked on the right side of the utility model the second distribution line.
The specific embodiment
With reference to Fig. 1.Be applied to the multiple stage material compounding equipment that regeneration polypropylene fibre is produced, comprise one-level proportioner 1, B grade mixture material device 2 and three gradating material devices 3, described one-level proportioner 1 comprises many first distribution line 11 that one-level material are mixed into secondary material, described B grade mixture material device 2 comprises many second distribution line 21 that secondary material are mixed into three grades of material, and described three gradating material devices 3 comprise that many articles add additive to be mixed into the 3rd distribution line 31 of level Four material in three grades of material.Described every first distribution line 11 is delivered to one-level material in the first distribution line 11 and is carried out mix by the first feed mechanism 12, described every first distribution line 11 is delivered to secondary material in described many second distribution line 21 and is carried out mix by the second feed mechanism 13, and described every second distribution line 21 is delivered to three grades of material in every corresponding the 3rd distribution line 31 and carried out mix by the 3rd feed mechanism 22.
See figures.1.and.2.Described every first distribution line 11 comprises multiple the first feed bins 111 that are set up in parallel and is positioned at the first material conveyer belt 112 under multiple the first feed bins 111, the top of each the first feed bin 111 is provided with the first charging aperture 1111, the bottom of each the first feed bin 111 is provided with the first discharging opening 1112, one end of described the first material conveyer belt 112 is the first feed end 1121, its other end is the first discharge end 1122, and described the second feed mechanism 13 is located at the first discharge end 1122 places.Described the first feed mechanism 12 comprise the first material pipe 121 and with multiple the first feed bins 111 one by one corresponding and be communicated with multiple Celloco fractionator Cellocos 122.Each Celloco fractionator Celloco 122 be located at the first corresponding feed bin 111 directly over, the bottom of each fiber separation 122 devices is provided with material outlet, each Celloco fractionator Celloco 122 is communicated with the first material pipe 121, and each Celloco fractionator Celloco 122 is provided with the one-level material in the first material pipe 121 is drawn to the first suction blower fan 123 in Celloco fractionator Celloco 122, and the plurality of the first suction blower fan 123 is controlled by one first controller (not shown in FIG.).
See figures.1.and.2.Multiple the first suction blower fans 123 that described the first controller (not shown in FIG.) is controlled in every first distribution line 11 are worked along the direction of the first discharge end 1122 successively by the first feed end 1121 of the first material conveyer belt 112, now one-level material just can fall into the first feed bin 111 from Celloco fractionator Celloco 122, and then drops down onto the first material conveyer belt 112 from the first discharging opening 1112.In the time that the one-level material on the first material conveyer belt 112 is transported to the below of next the first feed bin 111, the first controller (not shown in FIG.) is controlled next the first suction blower fan 123 and is worked, the first controller (not shown in FIG.) is controlled in such a manner the first feed bin 111 and is worked, and the material that is transported to like this first discharge end 1122 is the secondary material being mixed by multilayer one-level material.
With reference to Fig. 1 and Fig. 3.Described every second distribution line 21 comprises multiple the second feed bins 211 that are set up in parallel and is positioned at the second material conveyer belt 212 under the plurality of the second feed bin 211, the top of each the second feed bin 211 is provided with the second charging aperture 2111, and the bottom of each the second feed bin 211 is provided with the second discharging opening 2112.One end of described the second material conveyer belt 212 is the second feed end 2121, and its other end is the second discharge end 2122, and described the 3rd feed mechanism 22 is located at the second discharge end 2122 places.The number of the second feed bin 211 in described every second distribution line 21 is identical with the number of the first distribution line 11, and the second feed bin 211 of described many second distribution line 21 is multiple lines and multiple rows and arranges.The second material pipe 132 that described the second feed mechanism 13 comprises the second suction bucket 131 and is communicated with the second suction bucket 131, this the second suction bucket 131 is provided with the second induced-draught fan 133, every the second material pipe 131 is communicated with each the second charging aperture 2111 on every row the second feed bin 211, each the second charging aperture 2111 is provided with the second suction blower fan 134, and the second suction blower fan 134 on every row the second feed bin 211 is controlled by a second controller (not shown in FIG.).
With reference to Fig. 1 and Fig. 3.Described each the second feed mechanism 13 can be delivered to the secondary material in every first distribution line 11 in every row the second feed bin 211, and the secondary material in many first distribution line 11 just can be delivered in every second distribution line 21 like this.The same with the working method of the first distribution line, the second suction blower fan 134 that second controller (not shown in FIG.) is controlled in every second distribution line 21 is worked along the direction of the second discharge end 2122 by the second feed end 2121 of the second material conveyer belt 212, and the material that is transported to like this second discharge end 2122 is three grades of material that mixed by multilayer secondary material.
With reference to Fig. 1.Described every the 3rd distribution line 31 comprises a 3 material conveyer belt 311, one end of this 3 material conveyer belt 311 is the 3rd feed end 3111, its other end is the 3rd discharge end 3112, described the 3rd feed end 3111 is communicated with the 3rd feed mechanism 22, described the 3rd discharge end 3112 places are provided with suction funnel 312, this suction funnel 312 is communicated with two batch cans 313,314 that are contained with additive by tube connector 315, and this two batch can 313,314 is equipped with respectively look mother and cooling particulate.Described suction funnel 312 is controlled by one the 3rd controller (not shown in FIG.), and the 3rd controller (not shown in FIG.) is controlled the suction amount of suction funnel 312.The 3 material pipeline 222 that described the 3rd feed mechanism 22 comprises the 3rd suction bucket 221 and is communicated with the 3rd suction bucket 221, the 3rd suction bucket 221 is provided with the 3rd induced-draught fan 223, and described 3 material pipeline 222 is communicated with the 3rd feed end 3111 of 3 material conveyer belt 311.
With reference to Fig. 1.Described the 3rd feed mechanism 22 is delivered to three grades of material in every second distribution line 21 in the 3rd corresponding distribution line 31, these three grades of material are delivered to the 3rd discharge end 3112 by the feed end 3111 of 3 material conveyer belt 311, on the 3rd discharge end 3112, in three grades of material, add look mother and cooling particulate three grades of material can be mixed into level Four material, this level Four material just can be for melting.
With reference to Fig. 1.According to need of production, one-level material in many first distribution line 11 can be waste or used plastics of the same race or waste or used plastics not of the same race, as the one-level material in first distribution line 11 can be for the one-level material in PP rope class, another first distribution line 11 can be PP particle, the one-level material in another first distribution line 11 can be banded class again.In addition, the number of the first distribution line 11, the second distribution line 21 and the 3rd distribution line 31 can be selected according to need of production.
Above are only the specific embodiment of the present utility model, but design concept of the present utility model is not limited to this, allly utilizes this design to carry out the change of unsubstantiality to the utility model, all should belong to the behavior of invading the utility model protection domain.
Claims (7)
1. be applied to the multiple stage material compounding equipment that regeneration polypropylene fibre is produced, it is characterized in that: comprise one-level proportioner, B grade mixture material device and three gradating material devices, described one-level proportioner comprises many first distribution line that one-level material are mixed into secondary material, described B grade mixture material device comprises many second distribution line that secondary material are mixed into three grades of material, and described three gradating material devices comprise that many articles add additive to be mixed into the 3rd distribution line of level Four material in three grades of material; Described every first distribution line is delivered to one-level material in the first distribution line, to carry out mix by the first feed mechanism, described every first distribution line is delivered to secondary material in described many second distribution line and is carried out mix by the second feed mechanism, and described every second distribution line is delivered to three grades of material in every corresponding the 3rd distribution line and carried out mix by the 3rd feed mechanism.
2. the multiple stage material compounding equipment that is applied to the production of regeneration polypropylene fibre as claimed in claim 1, it is characterized in that: described every first distribution line comprises multiple the first feed bins that are set up in parallel and is positioned at the first material conveyer belt under multiple the first feed bins, the top of each the first feed bin is provided with the first charging aperture, the bottom of each the first feed bin is provided with the first discharging opening, one end of described the first material conveyer belt is the first feed end, its other end is the first discharge end, and described the second feed mechanism is located at the first discharge end place.
3. the multiple stage material compounding equipment that is applied to the production of regeneration polypropylene fibre as claimed in claim 2, it is characterized in that: described the first feed mechanism comprise the first material pipe and with multiple the first feed bins one by one corresponding and be communicated with multiple Celloco fractionator Cellocos, each Celloco fractionator Celloco be located at the first corresponding feed bin directly over, each Celloco fractionator Celloco is communicated with the first material pipe, and each Celloco fractionator Celloco is provided with the one-level material in the first material pipe is drawn to the first suction blower fan in Celloco fractionator Celloco, and the plurality of the first suction blower fan is controlled by one first controller.
4. the multiple stage material compounding equipment that is applied to the production of regeneration polypropylene fibre as claimed in claim 1, it is characterized in that: described every second distribution line comprises multiple the second feed bins that are set up in parallel and is positioned at the second material conveyer belt under the plurality of the second feed bin, the top of each the second feed bin is provided with the second charging aperture, the bottom of each the second feed bin is provided with the second discharging opening, one end of described the second material conveyer belt is the second feed end, its other end is the second discharge end, described the 3rd feed mechanism is located at the second discharge end place, the number of the second feed bin in described every second distribution line is identical with the number of the first distribution line, the second feed bin of described many second distribution line is multiple lines and multiple rows and arranges.
5. the multiple stage material compounding equipment that is applied to the production of regeneration polypropylene fibre as claimed in claim 4, it is characterized in that: the second material pipe that described the second feed mechanism comprises the second suction bucket and is communicated with the second suction bucket, this the second suction bucket is provided with the second induced-draught fan, every the second material pipe is communicated with each the second charging aperture on every row the second feed bin, each the second charging aperture is provided with the second suction blower fan, and the second suction blower fan on every row the second feed bin is controlled by a second controller.
6. the multiple stage material compounding equipment that is applied to the production of regeneration polypropylene fibre as claimed in claim 1, it is characterized in that: described every the 3rd distribution line comprises a 3 material conveyer belt, one end of this 3 material conveyer belt is the 3rd feed end, its other end is the 3rd discharge end, described the 3rd feed end is communicated with the 3rd feed mechanism, described the 3rd discharge end place is provided with suction funnel, and this suction funnel is communicated with the batch can that is contained with additive by tube connector, and described suction funnel is controlled by one the 3rd controller.
7. the multiple stage material compounding equipment that is applied to the production of regeneration polypropylene fibre as claimed in claim 6, it is characterized in that: the 3 material pipeline that described the 3rd feed mechanism comprises the 3rd suction bucket and is communicated with the 3rd suction bucket, the 3rd suction bucket is provided with the 3rd induced-draught fan, and described 3 material pipeline is communicated with the 3rd feed end of 3 material conveyer belt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320869172.3U CN203611376U (en) | 2013-12-27 | 2013-12-27 | Multistage burdening equipment for producing regenerated polypropylene |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320869172.3U CN203611376U (en) | 2013-12-27 | 2013-12-27 | Multistage burdening equipment for producing regenerated polypropylene |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203611376U true CN203611376U (en) | 2014-05-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320869172.3U Expired - Lifetime CN203611376U (en) | 2013-12-27 | 2013-12-27 | Multistage burdening equipment for producing regenerated polypropylene |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203611376U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103707430A (en) * | 2013-12-27 | 2014-04-09 | 福建三宏再生资源科技有限公司 | Multistage dispensing equipment applied to production of regenerative polypropylene |
| CN109809206A (en) * | 2017-11-21 | 2019-05-28 | 宁波大发化纤有限公司 | Automatic premixing storage device |
-
2013
- 2013-12-27 CN CN201320869172.3U patent/CN203611376U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103707430A (en) * | 2013-12-27 | 2014-04-09 | 福建三宏再生资源科技有限公司 | Multistage dispensing equipment applied to production of regenerative polypropylene |
| CN103707430B (en) * | 2013-12-27 | 2016-04-20 | 福建三宏再生资源科技有限公司 | Be applied to the multiple stage material compounding equipment that regeneration polypropylene fibre is produced |
| CN109809206A (en) * | 2017-11-21 | 2019-05-28 | 宁波大发化纤有限公司 | Automatic premixing storage device |
| CN109809206B (en) * | 2017-11-21 | 2020-08-18 | 宁波大发化纤有限公司 | Automatic premixing and storing device |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
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Granted publication date: 20140528 |
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| CX01 | Expiry of patent term |