CN204263398U - A kind of Super Absorbent Polymer Particles tinuous production - Google Patents

A kind of Super Absorbent Polymer Particles tinuous production Download PDF

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Publication number
CN204263398U
CN204263398U CN201420720222.6U CN201420720222U CN204263398U CN 204263398 U CN204263398 U CN 204263398U CN 201420720222 U CN201420720222 U CN 201420720222U CN 204263398 U CN204263398 U CN 204263398U
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CN
China
Prior art keywords
separator
fluid bed
bed dryer
polymer particles
super absorbent
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Expired - Fee Related
Application number
CN201420720222.6U
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Chinese (zh)
Inventor
尹立华
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Caim High Water Absorbing Material (tianjin) Co Ltd
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Caim High Water Absorbing Material (tianjin) Co Ltd
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Priority to CN201420720222.6U priority Critical patent/CN204263398U/en
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Publication of CN204263398U publication Critical patent/CN204263398U/en
Expired - Fee Related legal-status Critical Current
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Abstract

The utility model relates to a kind of Super Absorbent Polymer Particles tinuous production, comprise reactor, polyplant, colloid mill, drier, separator, screening machine, pulverizer and feed bin, drier is made up of one-level fluid bed dryer and secondary fluid bed dryer, discharge nozzle is connected at reactor discharging opening, discharge nozzle is placed in the feed end of polyplant, the discharge end of polyplant is relative with the feed hopper of colloid mill, the discharging opening of colloid mill is connected with the charging aperture of one-level fluid bed dryer by the pipeline connecting air-introduced machine, the discharging opening of one-level fluid bed dryer is relative with the charging aperture of secondary fluid bed dryer, the discharging opening of secondary fluid bed dryer is relative with material pond, the suction pipe connecting separator is provided with in material pond, screening machine and pulverizer is set gradually in separator bottom, splicing case is placed in the discharge outlet of pulverizer, this splicing case is connected with feed bin by suction pipe.The utility model has that labour intensity is little, production efficiency is high, avoid the advantages such as material deterioration.

Description

A kind of Super Absorbent Polymer Particles tinuous production
Technical field
The utility model relates to a kind of production line, particularly a kind of Super Absorbent Polymer Particles tinuous production.
Background technology
Super absorbent resin is a kind of novel macromolecular material, and it can absorb own wt the hundred times even moisture of several thousand times, has nontoxic, harmless, pollution-free, that water absorbing capacity is strong, water holding capacity is high feature.The processing technology of Super Absorbent Polymer Particles generally will through operations such as batch mixing, polymerization shaping, grinding, drying, separation, screening and pulverizing.
Owing to there is no a set ofly can to make Super Absorbent Polymer Particles quantity-produced production equipment in prior art, so when producing, per pass process equipment in technique is all separated from each other, material often completes a step processing, just need manually to send it in subsequent processing, labour intensity is large, production efficiency is low.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of and has that labour intensity is little, production efficiency is high, the Super Absorbent Polymer Particles tinuous production of compact conformation.
The utility model solves its technical problem and is achieved through the following technical solutions:
A kind of Super Absorbent Polymer Particles tinuous production, comprise reactor, polyplant, colloid mill, drier, separator, screening machine, pulverizer and feed bin, it is characterized in that: described drier is made up of one-level fluid bed dryer and secondary fluid bed dryer, also comprise a material pond, a discharge nozzle is connected in the discharge outlet of described reactor, this discharge nozzle is placed in the feed end of polyplant, the discharge end of polyplant is relative with the feed hopper of colloid mill, the discharge outlet of colloid mill is connected with the charging aperture of one-level fluid bed dryer by the pipeline connecting air-introduced machine, the discharging opening of one-level fluid bed dryer is relative with the charging aperture of secondary fluid bed dryer, the discharging opening of secondary fluid bed dryer is relative with the material pond that its underpart is arranged, the suction pipe that one is connected to separator is provided with in material pond, the bottom of separator is provided with screening machine, the bottom of screening machine is provided with pulverizer, a splicing case is placed with in the discharge outlet of pulverizer, this splicing case is connected with the feed bin that whole level separator is installed at top by the suction pipe placed in it.
And, also comprise an installing rack, be equipped with separator at the top layer of installing rack, in installing rack, be provided with screening machine, be equipped with pulverizer at the bottom of installing rack.
And, the described separator be positioned on installing rack top layer is 3, be respectively primary separator, second-stage separator and three grades of separators, discharging opening bottom primary separator is connected with the charging aperture of second-stage separator by pipeline, discharging opening bottom second-stage separator is connected by the charging aperture of pipeline with three grades of separators, and the discharging opening of three grades of separator bottom is led directly on the screening machine of its lower floor of case by pipeline.
And described material pond is made up of base and pond body, and base is embedded with pond body, laid on the surface of pond body have the stainless sheet steel fitted with its inwall.
And described screening machine is rotation sieve.
And, described polyplant is provided with ventilation shaft.
And, described one-level fluid bed dryer and secondary fluid bed dryer are all provided with pump-line.
Advantage of the present invention and beneficial effect are:
1. this Super Absorbent Polymer Particles tinuous production, by the production equipment in each operation is linked together through discharge nozzle or the attachment such as pipeline or suction pipe, achieve super absorbent resin quantity-produced object, improve production efficiency, reduce cost and the labour intensity of artificial conveyance; By expecting the setting in pond, because material is after fluid bed dryer top discharge, its humidity and temperature can not meet the requirement of separation, so need first blanking to ventilate in material pond, when temperature and humidity meet separation requirement, be delivered in separator by suction pipe and be separated, the setting in this material pond makes Super Absorbent Polymer Particles in quantity-produced situation, can also ensure the quality of production.By drier is designed to two-stage drying, material carries out the drying in material table face on one-level fluid bed dryer, secondary fluid bed dryer carries out the drying of internal batch, dry through this two-stage, make the dry standard that material reaches required in technique.
2. this Super Absorbent Polymer Particles tinuous production; by by separator designs being primary separator, second-stage separator, three grades of separators; and at the whole level separator of the upper design of feed bin; material is separated through four times; make the Super Absorbent Polymer Particles particle diameter that obtains evenly, purity is higher; avoid the confusion of different-grain diameter, affect product quality.
3. this Super Absorbent Polymer Particles tinuous production, by the laid stainless sheet steel fitted with its inwall on the surface of material pond, pond body, avoids material and touches rusty stain and rotten problem.
4. this Super Absorbent Polymer Particles tinuous production, by installing ventilation shaft on polyplant, the setting of this ventilation shaft can make air flow method in polyplant even, accelerates polymerisation.
5. this Super Absorbent Polymer Particles tinuous production, by installing pump-line on one-level fluid bed dryer and secondary fluid bed dryer, the moisture in drying machine can siphon away by this pump-line, accelerates drying efficiency.
6. the utility model scientific structure design is reasonable, and having that labour intensity is little, production efficiency is high, compact conformation, avoid material deterioration, be easy to the advantage that realizes, is a kind of Super Absorbent Polymer Particles tinuous production with higher innovation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Description of reference numerals:
1-reactor, 2-discharge nozzle, 3-polyplant, 4-ventilation shaft, 5-feed hopper, 6-colloid mill, 7-one-level fluid bed dryer, 8-pump-line, the discharging opening of 9-one-level fluid bed dryer, the charging aperture of 10-secondary fluid bed dryer, 11-secondary fluid bed dryer, 12-expects pond, 13-suction pipe, 14-installing rack, 15-primary separator, 16-second-stage separator, 17-tri-grades of separators, 18-feed bin, the whole level separator of 19-, 20-splicing case, 21-pulverizer, 22-screening machine.
Detailed description of the invention
Below by specific embodiment, the utility model is described in further detail, and following examples are descriptive, is not determinate, can not limit protection domain of the present utility model with this.
A kind of Super Absorbent Polymer Particles tinuous production, comprise reactor 1, polyplant 3, colloid mill 6, drier, separator, screening machine 22, pulverizer 21 and feed bin 18, its innovation is: described drier is made up of one-level fluid bed dryer 7 and secondary fluid bed dryer 11, also comprise a material pond 12, a discharge nozzle 2 is connected in the discharge outlet of described reactor, this discharge nozzle is placed in the feed end of polyplant, the discharge end of polyplant is relative with the feed hopper 5 of colloid mill, the discharge outlet of colloid mill is connected with the charging aperture of one-level fluid bed dryer by the pipeline connecting air-introduced machine, the discharging opening 9 of one-level fluid bed dryer is relative with the charging aperture 10 of secondary fluid bed dryer, the discharging opening of secondary fluid bed dryer is relative with the material pond that its underpart is arranged, the suction pipe 13 that one is connected to separator is provided with in material pond, the bottom of separator is provided with screening machine, the bottom of screening machine is provided with pulverizer, a splicing case 20 is placed with in the discharge outlet of pulverizer, this splicing case is connected with the feed bin that whole level separator 19 is installed at top by the suction pipe placed in it.
Also comprise an installing rack 14, be equipped with separator at the top layer of installing rack, in installing rack, be provided with screening machine, be equipped with pulverizer at the bottom of installing rack.
The described separator be positioned on installing rack top layer is 3, be respectively primary separator 15, second-stage separator 16 and three grades of separators 17, discharging opening bottom primary separator is connected with the charging aperture of second-stage separator by pipeline, discharging opening bottom second-stage separator is connected by the charging aperture of pipeline with three grades of separators, and the discharging opening of three grades of separator bottom is led directly on the screening machine of its lower floor of case by pipeline.
Described material pond is made up of base and pond body, and base is embedded with pond body, and laid on the surface of pond body have the stainless sheet steel fitted with its inwall.
Described screening machine is rotation sieve.
Described polyplant is provided with ventilation shaft 4.
Described one-level fluid bed dryer and secondary fluid bed dryer are all provided with pump-line 8.
Operation principle:
Liquid material is delivered on polyplant by the discharge nozzle that reactor discharge outlet is arranged, liquid material is solidified into block on polyplant, then become the material of block to fall in colloid mill and grind to form fritter, by the pipeline of air-introduced machine, piece material is delivered to drier subsequently, dry through two-stage, material falls into material pond and ventilates, the separation carrying out different-grain diameter material in primary separator is delivered to again by suction pipe, enter second-stage separator subsequently to be again separated, then enter three grades of separators to continue to be separated, entered on screening machine by isolated material bottom three grades of separators and sieve, the material of different-grain diameter drops on pulverizer by pipeline corresponding on screening machine, pulverizer as requested, after particle diameter needed for crushing material is become, be delivered to intermediate separator by suction pipe and carry out last separation, end product is fallen by feed bin.
Although disclose embodiment of the present utility model and accompanying drawing for the purpose of illustration, but it will be appreciated by those skilled in the art that: in the spirit and scope not departing from the utility model and claims, various replacement, change and amendment are all possible, therefore, scope of the present utility model is not limited to the content disclosed in embodiment and accompanying drawing.

Claims (7)

1. a Super Absorbent Polymer Particles tinuous production, comprise reactor, polyplant, colloid mill, drier, separator, screening machine, pulverizer and feed bin, it is characterized in that: described drier is made up of one-level fluid bed dryer and secondary fluid bed dryer, also comprise a material pond, a discharge nozzle is connected in the discharge outlet of described reactor, this discharge nozzle is placed in the feed end of polyplant, the discharge end of polyplant is relative with the feed hopper of colloid mill, the discharge outlet of colloid mill is connected with the charging aperture of one-level fluid bed dryer by the pipeline connecting air-introduced machine, the discharging opening of one-level fluid bed dryer is relative with the charging aperture of secondary fluid bed dryer, the discharging opening of secondary fluid bed dryer is relative with the material pond that its underpart is arranged, the suction pipe that one is connected to separator is provided with in material pond, the bottom of separator is provided with screening machine, the bottom of screening machine is provided with pulverizer, a splicing case is placed with in the discharge outlet of pulverizer, this splicing case is connected with the feed bin that whole level separator is installed at top by the suction pipe placed in it.
2. a kind of Super Absorbent Polymer Particles tinuous production according to claim 1, is characterized in that: also comprise an installing rack, is equipped with separator, in installing rack, is provided with screening machine at the top layer of installing rack, be equipped with pulverizer at the bottom of installing rack.
3. a kind of Super Absorbent Polymer Particles tinuous production according to claim 2, it is characterized in that: described in the separator be positioned on installing rack top layer be 3, be respectively primary separator, second-stage separator and three grades of separators, discharging opening bottom primary separator is connected with the charging aperture of second-stage separator by pipeline, discharging opening bottom second-stage separator is connected by the charging aperture of pipeline with three grades of separators, and the discharging opening of three grades of separator bottom is led directly on the screening machine of its lower floor of case by pipeline.
4. a kind of Super Absorbent Polymer Particles tinuous production according to claim 1, is characterized in that: described material pond is made up of base and pond body, and base is embedded with pond body, and laid on the surface of pond body have the stainless sheet steel fitted with its inwall.
5. a kind of Super Absorbent Polymer Particles tinuous production according to claim 1, is characterized in that: described screening machine is rotation sieve.
6. a kind of Super Absorbent Polymer Particles tinuous production according to claim 1, is characterized in that: on described polyplant, be provided with ventilation shaft.
7. a kind of Super Absorbent Polymer Particles tinuous production according to claim 1, is characterized in that: on described one-level fluid bed dryer and secondary fluid bed dryer, be all provided with pump-line.
CN201420720222.6U 2014-11-25 2014-11-25 A kind of Super Absorbent Polymer Particles tinuous production Expired - Fee Related CN204263398U (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105109776A (en) * 2015-09-06 2015-12-02 河北尚华塑料科技有限公司 High-molecular pellet screening and packaging equipment
CN105170028A (en) * 2015-09-25 2015-12-23 河北尚华塑料科技有限公司 Crosslinked polyethylene production equipment
CN106861867A (en) * 2015-12-10 2017-06-20 上海电信工程有限公司 A kind of optical cable binding agent Preparation equipment
CN109482319A (en) * 2017-04-21 2019-03-19 宁夏天绿健知识产权运营有限公司 Equipment for colloidal grinding homogeneous

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105109776A (en) * 2015-09-06 2015-12-02 河北尚华塑料科技有限公司 High-molecular pellet screening and packaging equipment
CN105170028A (en) * 2015-09-25 2015-12-23 河北尚华塑料科技有限公司 Crosslinked polyethylene production equipment
CN106861867A (en) * 2015-12-10 2017-06-20 上海电信工程有限公司 A kind of optical cable binding agent Preparation equipment
CN106861867B (en) * 2015-12-10 2019-06-07 上海电信工程有限公司 A kind of optical cable binder Preparation equipment
CN109482319A (en) * 2017-04-21 2019-03-19 宁夏天绿健知识产权运营有限公司 Equipment for colloidal grinding homogeneous

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

Granted publication date: 20150415

Termination date: 20151125