CN213055511U - Production system for graphene polypropylene master batches - Google Patents

Production system for graphene polypropylene master batches Download PDF

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Publication number
CN213055511U
CN213055511U CN202020642723.2U CN202020642723U CN213055511U CN 213055511 U CN213055511 U CN 213055511U CN 202020642723 U CN202020642723 U CN 202020642723U CN 213055511 U CN213055511 U CN 213055511U
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production system
kettle
screw conveyor
feed inlet
discharge port
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刘少华
任国峰
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Beijing Yingchuanglihe Electronic Technology Co ltd
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Abstract

The utility model relates to the field of machinary, concretely relates to production system. The utility model provides a production system for graphite alkene polypropylene master batch, includes a production system, and production system includes first stirred tank, and a freeze dryer is passed through the pipe connection to the discharge gate of first stirred tank. The utility model discloses a this design provides a production system for graphite alkene polypropylene master batch, the operation of having simplified in this design, and through screw conveyer transport raw materials, has reduced the storage and the transportation step of raw and other materials, has improved production efficiency, is applicable to the large-scale production and uses.

Description

Production system for graphene polypropylene master batches
Technical Field
The utility model relates to the field of machinary, specifically, relate to production system.
Background
The polypropylene master batch is a chemical master batch with low cost, good performance and extremely wide application, but the traditional polypropylene master batch does not have functionality, along with the social development, the traditional polypropylene can not meet the requirements of people on functional textiles, the graphene polypropylene master batch has good antibacterial property, far infrared, ultraviolet resistance and other functions, the original polymerized graphene polypropylene functionality is permanent, the condition that the functionality is weakened along with the increase of washing times is avoided, the application range of the traditional polypropylene is expanded, the added value of products is improved, the requirements of people on healthy and environment-friendly functional textiles are met, however, the existing production system for producing the polypropylene master batch can not be directly used for producing the graphene polypropylene master batch, multiple devices are required to be operated, the operation is complex, the devices are dispersed, the raw materials are inconvenient to transport, and the production efficiency is low, can not be produced and used in large scale.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a production system for graphite alkene polypropylene master batch to solve above-mentioned at least one technical problem.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the production system for the graphene polypropylene master batches comprises a production system and is characterized by comprising a first stirring kettle, wherein a discharge port of the first stirring kettle is connected with a freeze dryer through a pipeline, a feed port of the freeze dryer is connected with the pipeline, and a first spiral conveyor and a second stirring kettle are arranged on one side of the freeze dryer;
the feed inlet of the first spiral conveyor is connected with the discharge outlet of the freeze dryer, and the discharge outlet of the first spiral conveyor is connected with the feed inlet of the second stirring kettle;
a second screw conveyor and a polymerization kettle are arranged on one side of the second stirring kettle, a feed port of the second screw conveyor is connected with a discharge port of the second stirring kettle, and a discharge port of the second screw conveyor is connected with a feed port of the polymerization kettle;
and a third screw conveyor and a granulator are arranged on one side of the polymerization kettle, a feed inlet of the third screw conveyor is connected with a discharge outlet of the polymerization kettle, and a discharge outlet of the third screw conveyor is connected with a feed inlet of the granulator.
The feed inlet of the freeze dryer is provided with a pump body.
The top of second stirred tank is equipped with a first storage case that is the bucket form, the lower part of first storage case is equipped with first drain hole, the upper portion of second stirred tank is equipped with first auxiliary material feed inlet, first drain hole with first auxiliary material feed inlet links to each other, first drain hole department ann has first valve.
The top of polymeric kettle is equipped with a second storage case that is the bucket form, the lower part of second storage case is equipped with the second drain hole, polymeric kettle's upper portion is equipped with the second auxiliary material feed inlet, the second drain hole with the second auxiliary material feed inlet links to each other, second drain hole department ann has the second valve.
The first valve and the second valve are both electromagnetic valves. The upper parts of the first storage box and the second storage box are both provided with a turnover cover.
The utility model discloses a this design provides a production system for graphite alkene polypropylene master batch, the operation of having simplified in this design, and through screw conveyer transport raw materials, has reduced the storage and the transportation step of raw and other materials, has improved production efficiency, is applicable to the large-scale production and uses.
Drawings
Fig. 1 is a schematic view of a part of the structure of the present invention.
Detailed Description
The following description will further describe embodiments of the present invention with reference to the accompanying drawings.
As shown in fig. 1, a production system for graphene polypropylene master batches comprises a production system, wherein the production system comprises a first stirring kettle 1, a discharge port of the first stirring kettle is connected with a freeze dryer 3 through a pipeline 2, a feed port of the freeze dryer is connected with the pipeline, and a first screw conveyor 4 and a second stirring kettle 6 are arranged on one side of the freeze dryer; the feed inlet of the first spiral conveyor is connected with the discharge outlet of the freeze dryer, and the discharge outlet of the first spiral conveyor is connected with the feed inlet of the second stirring kettle; a second screw conveyor 7 and a polymerization kettle 9 are arranged on one side of the second stirring kettle, a feed inlet of the second screw conveyor is connected with a discharge outlet of the second stirring kettle, and a discharge outlet of the second screw conveyor is connected with a feed inlet of the polymerization kettle; one side of the polymerization kettle is provided with a third screw conveyor 10 and a granulator 11, a feed inlet of the third screw conveyor is connected with a discharge outlet of the polymerization kettle, and a discharge outlet of the third screw conveyor is connected with a feed inlet of the granulator. The utility model discloses a this design provides a production system for graphite alkene polypropylene master batch, the operation of having simplified in this design, and through screw conveyer transport raw materials, has reduced the storage and the transportation step of raw and other materials, has improved production efficiency, is applicable to the large-scale production and uses.
When the modified graphene oxide master batch is used, raw materials are placed into a first stirring kettle to prepare modified graphene oxide slurry, the prepared modified graphene oxide slurry is conveyed to a freeze dryer to be subjected to freeze drying, modified graphene oxide powder is obtained and conveyed to a second stirring kettle through a first spiral conveyer, the modified graphene oxide powder and propylene materials fed from an auxiliary material feeding port above the second stirring kettle are mixed and stirred, the stirred mixture is conveyed to a polymerization kettle through the second spiral conveyer and is subjected to polymerization reaction with catalysts fed from the auxiliary material feeding port above the polymerization kettle, and finally the discharged material is conveyed to a granulator through the second spiral conveyer to be granulated, so that the graphene polypropylene master batch is obtained.
The feed inlet of the freeze dryer is provided with a pump body. Modified graphene oxide slurry prepared by the first stirring kettle is conveniently conveyed to a freeze dryer for freeze drying.
The top of second stirred tank is equipped with a first storage case 5 that is the bucket form, and the lower part of first storage case is equipped with first drain hole, and the upper portion of second stirred tank is equipped with first auxiliary material feed inlet, and first drain hole links to each other with first auxiliary material feed inlet, and first drain hole department ann has first valve. The first storage box can be used for storing propylene materials. The top of polymeric kettle is equipped with a second storage case 8 that is the bucket form, and the lower part of second storage case is equipped with the second drain hole, and polymeric kettle's upper portion is equipped with the second auxiliary material feed inlet, and the second drain hole links to each other with the second auxiliary material feed inlet, and second drain hole department ann has the second valve. The second storage tank may be used to store catalyst. The first valve and the second valve are both electromagnetic valves. The upper parts of the first storage box and the second storage box are both provided with a turnover cover. The user can supplement the raw materials to the first storage box and the second storage box at regular time and quantity through the turnover cover.
The inner wall of the first stirring kettle and the inner wall of the pipeline are both coated with an anticorrosive coating. The anticorrosive coating adopts a ceramic anticorrosive coating. So as to ensure the operation of the equipment and reduce the damage of the oxidized graphite powder residual strong acid to the kettle body and the pipeline.
In order to facilitate the control of a user on the production system, the production system comprises a control end, and the control end is in control connection with a first stirring kettle, a freeze dryer, a first screw conveyor, a second stirring kettle, a second screw conveyor, a polymerization kettle, a third screw conveyor and a granulator. A singlechip is arranged in the control end and controls and connects the power supply modules of the first stirring kettle, the freeze dryer, the first screw conveyor, the second stirring kettle, the second screw conveyor, the polymerization kettle, the third screw conveyor and the granulator. And the singlechip controls and connects the valve arranged at the first discharge port and the valve arranged at the second discharge port.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described in the foregoing embodiments, or equivalents may be substituted for elements thereof. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (6)

1. The production system for the graphene polypropylene master batches comprises a production system and is characterized by comprising a first stirring kettle, wherein a discharge port of the first stirring kettle is connected with a freeze dryer through a pipeline, a feed port of the freeze dryer is connected with the pipeline, and a first spiral conveyor and a second stirring kettle are arranged on one side of the freeze dryer;
the feed inlet of the first spiral conveyor is connected with the discharge outlet of the freeze dryer, and the discharge outlet of the first spiral conveyor is connected with the feed inlet of the second stirring kettle;
a second screw conveyor and a polymerization kettle are arranged on one side of the second stirring kettle, a feed port of the second screw conveyor is connected with a discharge port of the second stirring kettle, and a discharge port of the second screw conveyor is connected with a feed port of the polymerization kettle;
and a third screw conveyor and a granulator are arranged on one side of the polymerization kettle, a feed inlet of the third screw conveyor is connected with a discharge outlet of the polymerization kettle, and a discharge outlet of the third screw conveyor is connected with a feed inlet of the granulator.
2. The production system of claim 1, wherein a pump is disposed at a feed inlet of the freeze dryer.
3. The production system of claim 1, wherein a first hopper-shaped storage tank is arranged above the second stirring tank, a first discharge port is arranged at the lower part of the first storage tank, a first auxiliary material feed port is arranged at the upper part of the second stirring tank, the first discharge port is connected with the first auxiliary material feed port, and a first valve is arranged at the first discharge port.
4. The production system of claim 3, wherein a second storage tank in a hopper shape is arranged above the polymerizer, a second discharge port is arranged at the lower part of the second storage tank, a second auxiliary material feed port is arranged at the upper part of the polymerizer, the second discharge port is connected with the second auxiliary material feed port, and a second valve is installed at the second discharge port.
5. The production system for graphene polypropylene master batches according to claim 4, wherein the first valve and the second valve are both solenoid valves.
6. The production system of claim 4, wherein the upper portions of the first storage tank and the second storage tank are both provided with a flip cover.
CN202020642723.2U 2020-04-24 2020-04-24 Production system for graphene polypropylene master batches Active CN213055511U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202020642723.2U CN213055511U (en) 2020-04-24 2020-04-24 Production system for graphene polypropylene master batches

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202020642723.2U CN213055511U (en) 2020-04-24 2020-04-24 Production system for graphene polypropylene master batches

Publications (1)

Publication Number Publication Date
CN213055511U true CN213055511U (en) 2021-04-27

Family

ID=75551288

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202020642723.2U Active CN213055511U (en) 2020-04-24 2020-04-24 Production system for graphene polypropylene master batches

Country Status (1)

Country Link
CN (1) CN213055511U (en)

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Effective date of registration: 20230707

Address after: 100176 701, Floor 7, Building 42, Yard 1, Jinghai 5th Road, Beijing Economic-Technological Development Area (Tongzhou), Daxing District, Beijing

Patentee after: Beijing yingchuanglihe Electronic Technology Co.,Ltd.

Address before: 063000 Room 401, 5 / F, deyuanli building, Xuzhuang community, Beixin Xidao, Lubei District, Tangshan City, Hebei Province

Patentee before: Ren Guofeng