CN203092820U - Antistatic master batch production system - Google Patents

Antistatic master batch production system Download PDF

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Publication number
CN203092820U
CN203092820U CN 201320087267 CN201320087267U CN203092820U CN 203092820 U CN203092820 U CN 203092820U CN 201320087267 CN201320087267 CN 201320087267 CN 201320087267 U CN201320087267 U CN 201320087267U CN 203092820 U CN203092820 U CN 203092820U
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CN
China
Prior art keywords
master batch
antistatic master
production system
batch production
exchange device
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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
Application number
CN 201320087267
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Chinese (zh)
Inventor
章德永
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HANGZHOU BEISHENG POLYMERMATERIAL CO Ltd
Original Assignee
HANGZHOU BEISHENG POLYMERMATERIAL CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
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Priority to CN 201320087267 priority Critical patent/CN203092820U/en
Application granted granted Critical
Publication of CN203092820U publication Critical patent/CN203092820U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to an antistatic master batch production system. The antistatic master batch production system comprises a weightless feeding device, a feeding hopper, an internal mixer, a two-screw extruder, a cooling water tank, a drying device, a granulator and a vibrating screen which are sequentially connected. The antistatic master batch production system is characterized in that a heat exchange device is arranged in the cooling water tank, one end of the heat exchange device is connected with an air blasting pipeline, and the other end of the heat exchange device is connected with a hot air pipeline; an air blower is used for blowing air into the heat exchange device through the air blasting pipeline; and one end of the hot air pipeline is connected with the heat exchange device, and the other end of the hot air pipeline is connected with the drying device. The antistatic master batch production system has the advantages that the production efficiency is high by adopting assembly line work, heat generated by cooling extruded strip antistatic master batches in the cooling water tank is used for drying the cooled strip antistatic master batches, and therefore, the purposes of energy conservation and environmental protection are achieved.

Description

A kind of antistatic master batch production system
Technical field
The utility model relates to the masterbatch manufacture field of plastic sheeting, more particularly, relates to a kind of antistatic master batch production system.
Background technology
Plastic products are in processing and use, and its surface electrostatic can endanger product safety, also can bring inconvenience to the user, even can initiating failure.
Use antistatic additive (antistatic master batch) can play antistatic effect.
Antistatic master batch also has certain inside and outside lubricated and demoulding effect, can reduce the wearing and tearing of material and equipment, especially for the equipment that uses enhancing, toughness reinforcing, inserts, can play the certain protection effect.Therefore, the demand to the production system of antistatic master batch grows with each passing day on the market.
The utility model content
The purpose of this utility model provides a kind of antistatic master batch production system, comprises continuous weightless drawing-in device, feed hopper, banbury, double screw extruder, bosh, drying device, pelleter and the vibratory sieve of order successively; It is characterized in that: be provided with a heat-exchange device in described bosh, an end of this heat-exchange device links to each other with blowing line, and other end place links to each other with hot gas duct; One air blast is blown into air in the described heat-exchange device by described blowing line; One end of hot gas duct links to each other with described heat-exchange device, and the other end links to each other with described drying device.
Preferably, in described hot gas duct, be provided with the Electric radiant Heating Film device, in order to the gas through described hot gas duct is carried out post bake.
Preferably, the porch of described hot gas duct on described drying device is relative with the direction that antistatic master batch enters described drying device.
Preferably, described drying device is a tank structure.
Preferably, described pelleter is provided with accumulator tank, the particle separation of the off size requirement after the pelletizing can be come out return processing.
The beneficial effects of the utility model are:
1, the utility model adopts pipelining, production efficiency height.
2, the utility model adopts banbury raw material to be mixed good mixing effect.
3, the strip antistatic master batch extruded of the utility model utilization cools off the heat that is produced and cooled strip antistatic master batch is carried out drying, energy-conserving and environment-protective in bosh.
4, the utility model has adopted the Electric radiant Heating Film device, when the shortage of heat in the bosh during with the cooled antistatic master batch of drying, starts described Electric radiant Heating Film device, and gas is heated, and power consumption is few.
5, drying device of the present utility model adopts tank structure, can make full use of the hot gas that transports from hot gas duct and antistatic master batch be carried out drying, the drying effect height.
Description of drawings
Fig. 1 is the structural representation of antistatic master batch production system of the present utility model.
Reference numerals list
Weightless drawing-in device 1; Feed hopper 2; Banbury 3; Double screw extruder 4; Bosh 5; Drying device 6; Pelleter 7; Vibratory sieve 8; Air blast 9; Blowing line 10; Heat-exchange device 11; Hot gas duct 12; Electric radiant Heating Film device 13; Accumulator tank 14; Discharging opening 15.
The specific embodiment
Below, will be elaborated to antistatic master batch production system of the present utility model in conjunction with the accompanying drawings and embodiments.
Antistatic master batch production system as shown in Figure 1 comprises the continuous weightless drawing-in device 1 of order successively; Feed hopper 2; Banbury 3; Double screw extruder 4; Bosh 5; Drying device 6; Pelleter 7; With vibratory sieve 8.
During production and processing, vector resin and the weightless drawing-in device 1 of antistatic additive utilization are joined the banbury 3 from feed hopper 2.In banbury 3, vector resin and antistatic additive are mixed, enter double screw extruder 4 afterwards.Extrude the strip antistatic master batch from double screw extruder 4 and enter bosh 5 and carry out immersion cooling, enter drying device 6 then and carry out drying.Strip antistatic master batch after dry enters pelleter 7 pelletizings, enters vibratory sieve 8 then.Pelleter 7 is provided with accumulator tank 14, reclaim in order to underproof antistatic master batch particle is passed through accumulator tank 14, and qualified particle is by being arranged on discharging opening 15 packings on the vibratory sieve 8.
Drying device 6 of the present utility model has made full use of the heat that water temperature that bosh 5 causes owing to cooling extruded antistatic master batch raises and produced, and cooled antistatic master batch is carried out drying, and is specific as follows.
At first, air blast 9 is blown into the heat-exchange device 11 that is arranged in the bosh 5 with air by blowing line 10.The heat that the water temperature that heat-exchange device 11 utilizes bosh 5 to cause owing to cooling extruded antistatic master batch raises and produced will heat from the gas of blowing line 10 inputs.Gas after the heating enters drying device 6 by hot gas duct 12.
Wherein, in hot gas duct 12, be provided with Electric radiant Heating Film device 13, to carrying out post bake, can carry out drying to antistatic master batch thereby make gas in the hot gas duct 12 have enough heats through the gas of hot gas duct 12.
Drying device 6 is a tank structure, can make full use of the hot gas that transports from hot gas duct 12 like this, and antistatic master batch is carried out abundant drying, reaches desirable drying effect.Do not set out gas port in drying device 6 separately, gas promptly can be discharged from the position that antistatic master batch enters drying device 6.When the energy of the hot gas in the heat-exchange device 11 enough carries out drying to antistatic master batch, can start Electric radiant Heating Film device 13.
To the foregoing description of the disclosed embodiments, make those skilled in the art can realize or use the utility model.Obviously, described embodiment only is a part of embodiment of the present utility model, but not all.Make those skilled in the art in form and details and do not making all other change or modifications that obtained under the creative work prerequisite, all belong to the scope of the utility model protection.

Claims (6)

1. an antistatic master batch production system comprises continuous weightless drawing-in device, feed hopper, banbury, double screw extruder, bosh, drying device, pelleter and the vibratory sieve of order successively; It is characterized in that:
Be provided with a heat-exchange device in described bosh, an end of this heat-exchange device links to each other with blowing line, and other end place links to each other with hot gas duct; One air blast is blown into air in the described heat-exchange device by described blowing line;
One end of hot gas duct links to each other with described heat-exchange device, and the other end links to each other with described drying device.
2. antistatic master batch production system according to claim 1 is characterized in that, is provided with the Electric radiant Heating Film device in described hot gas duct, in order to the gas through described hot gas duct is carried out post bake.
3. antistatic master batch production system according to claim 1 is characterized in that, the porch of described hot gas duct on described drying device is relative with the direction that antistatic master batch enters described drying device.
4. antistatic master batch production system according to claim 1 is characterized in that, described drying device is a tank structure.
5. antistatic master batch production system according to claim 1 is characterized in that described pelleter is provided with accumulator tank, so that the particle separation of the off size requirement after the pelletizing is come out to return processing.
6. according to any one described antistatic master batch production system of claim 1 to 5, it is characterized in that described vibratory sieve is provided with discharging opening.
CN 201320087267 2013-02-26 2013-02-26 Antistatic master batch production system Expired - Fee Related CN203092820U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320087267 CN203092820U (en) 2013-02-26 2013-02-26 Antistatic master batch production system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320087267 CN203092820U (en) 2013-02-26 2013-02-26 Antistatic master batch production system

Publications (1)

Publication Number Publication Date
CN203092820U true CN203092820U (en) 2013-07-31

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201320087267 Expired - Fee Related CN203092820U (en) 2013-02-26 2013-02-26 Antistatic master batch production system

Country Status (1)

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CN (1) CN203092820U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110341072A (en) * 2019-07-16 2019-10-18 昆山科信橡塑机械有限公司 Screw mixing extruder
CN111283896A (en) * 2020-02-25 2020-06-16 浙江巨创新材料科技有限公司 Prilling granulator is used in production of modified nanometer master batch

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110341072A (en) * 2019-07-16 2019-10-18 昆山科信橡塑机械有限公司 Screw mixing extruder
CN111283896A (en) * 2020-02-25 2020-06-16 浙江巨创新材料科技有限公司 Prilling granulator is used in production of modified nanometer master batch

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130731

Termination date: 20150226

EXPY Termination of patent right or utility model