CN107599221A - A kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process - Google Patents

A kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process Download PDF

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Publication number
CN107599221A
CN107599221A CN201710957329.0A CN201710957329A CN107599221A CN 107599221 A CN107599221 A CN 107599221A CN 201710957329 A CN201710957329 A CN 201710957329A CN 107599221 A CN107599221 A CN 107599221A
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CN
China
Prior art keywords
overlay film
eps
expanded beads
rotary kiln
separation
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Pending
Application number
CN201710957329.0A
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Chinese (zh)
Inventor
宋红旗
董红霞
赵宝玉
李红武
郭永刚
任安安
李文燕
郭东荣
赵永亭
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SHANXI SIXTH CONSTRUCTION GROUP CO Ltd
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SHANXI SIXTH CONSTRUCTION GROUP CO Ltd
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Priority to CN201710957329.0A priority Critical patent/CN107599221A/en
Publication of CN107599221A publication Critical patent/CN107599221A/en
Pending legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Building Environments (AREA)
  • Paints Or Removers (AREA)

Abstract

Of the invention is specially a kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process, solves the problems, such as that existing EPS particles have heat conductivility and the poor easily initiation fire of fire resistance.A, EPS particles are foamed;B, inorganic overlay film liquid is configured:12 parts of binding agent, 15 parts of curing agent, 3 20 parts of fire retardant, 7 12 parts of water;C, EPS expanded beads are inserted into gas and hangs overlay film storehouse;D, EPS expanded beads are suspended in into gas to hang in overlay film storehouse;E, then inorganic overlay film liquid and EPS expanded beads are suspended and stirs overlay film;F, separation is granulated cooling after the completion of overlay film.Manufacturing process of the present invention is close to neutrality, and without harmful substances such as formaldehyde, and the apparent density that particle is made reaches 150 500 ㎏/m3, thermal conductivity factor reaches 0.035 0.045w/m2.k, the particles compress into its fire resistance of sheet material up to B2 level above flame retardant effects.

Description

A kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process
Technical field
The present invention relates to the prilling process of EPS particles, specially a kind of EPS particles suspension overlay film solidification rotary kiln separation is granulated Method.
Background technology
At present, foaming EPS particles compress to form warming plate and spread out in factory floor by overcoating overlay film liquid through hot setting Product, it is impossible to be applied independently in separately as particle beyond factory.
At present, the insulation material used both at home and abroad uses eps foam plate, using foam grain process bonding Into this particle board heat insulation effect is good, and foamed plastic is due to the property feature of itself, the heat conductivility of EPS particles and fire-retardant Performance can not all meet requirement, and disaster hidden-trouble is larger, easily trigger fire.
The content of the invention
The present invention in order to solve the problems, such as existing EPS particles exist heat conductivility and fire resistance it is poor easily trigger fire, Provide a kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process.
The present invention adopts the following technical scheme that realization:A kind of EPS particles suspension overlay film solidification rotary kiln separation granulation side Method, using following steps:A, the EPS particles of same particle diameter are foamed in high temperature foaming cabin, forms EPS expanded beads; B, inorganic overlay film liquid is configured, what inorganic overlay film liquid was made up of the raw material of following mass fraction:Binding agent 1-2 parts, curing agent 1-5 Part, fire retardant 3-20 parts, water 7-12 parts;C, EPS expanded beads are inserted into gas and hangs overlay film storehouse, the density of EPS expanded beads is 8- 10 KG/m3;D, the bottom that overlay film storehouse is hanged in gas leads to the steam that pressure is 0.5-1.5MPa and EPS expanded beads are suspended in into gas hanged In overlay film storehouse;E, inorganic overlay film liquid is then sprayed into gas by atomizer and hangs the stirring that suspended in overlay film storehouse with EPS expanded beads Overlay film, overlay film thickness are 0.1-0.4mm;F, enter after the completion of overlay film in tilted-putted rotary kiln, through rotary kiln rotary rolling, separation Be granulated and further solidification dry after lean on from reenter grate-cooler cooling, completion EPS particles granulation.
The uniformity of particle surface liquid attachment, while hot setting are ensure that in the present invention using the technique of suspension overlay film Particle is formed, as grain density change and hot setting effect rely on deadweight to sink to entering rotary kiln;Separated and be granulated using rotary kiln Technique causes particle rapid solidification and effectively to avoid inter-adhesive under high-temperature vapor effect, and prevents particle surface overlay film liquid Body and equipment container adhesion, overcome existing EPS particles and heat conductivility and fire resistance poor the problem of easily triggering fire be present.
Bonding agent is dispersed latex powder, and curing agent is accelerator or water soluble phenol resin, and fire retardant is silicate cement The mixture or desulfurated plaster of mud, aluminium hydroxide and graphite.
EPS particles suspension overlay film solidification rotary kiln separation prilling process manufacturing process of the present invention is free of close to neutrality The harmful substances such as formaldehyde, and the apparent density that particle is made reaches 150-500 ㎏/m3, thermal conductivity factor reaches 0.035- 0.045w/m2.k, the particles compress improves compression strength and answered into its fire resistance of sheet material up to B2 level above flame retardant effects With more extensive.
Embodiment
Embodiment 1
A kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process, using following steps:A, by EPS of same particle diameter Grain is foamed in high temperature foaming cabin, forms EPS expanded beads;B, inorganic overlay film liquid is configured, inorganic overlay film liquid is by as follows The raw material composition of mass fraction:1 part of binding agent, 2 parts of curing agent, 10 parts of fire retardant, 7 parts of water;C, EPS expanded beads are inserted Gas hangs overlay film storehouse, and the density of EPS expanded beads is 8KG/m3;D, the bottom that overlay film storehouse is hanged in gas leads to the steam that pressure is 0.5MPa EPS expanded beads are suspended in into gas to hang in overlay film storehouse;E, inorganic overlay film liquid is then sprayed into gas by atomizer and hangs overlay film storehouse Interior suspended with EPS expanded beads stirs overlay film, and overlay film thickness is 0.3mm;F, enter after the completion of overlay film in tilted-putted rotary kiln, Leaned on after rotary kiln rotary rolling, separation are granulated and further solidification is dried from grate-cooler cooling is reentered, complete making for EPS particles Grain.
Bonding agent is dispersed latex powder, and curing agent is accelerator, and fire retardant is portland cement.
Embodiment 2
A kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process, using following steps:A, by EPS of same particle diameter Grain is foamed in high temperature foaming cabin, forms EPS expanded beads;B, inorganic overlay film liquid is configured, inorganic overlay film liquid is by as follows The raw material composition of mass fraction:1 part of binding agent, 5 parts of curing agent, 3 parts of fire retardant, 12 parts of water;C, EPS expanded beads are inserted Gas hangs overlay film storehouse, and the density of EPS expanded beads is 10 KG/m3;D, the bottom that overlay film storehouse is hanged in gas leads to the steam that pressure is 1MPa EPS expanded beads are suspended in into gas to hang in overlay film storehouse;E, inorganic overlay film liquid is then sprayed into gas by atomizer and hangs overlay film storehouse Interior suspended with EPS expanded beads stirs overlay film, and overlay film thickness is 0.1mm;F, enter after the completion of overlay film in tilted-putted rotary kiln, Leaned on after rotary kiln rotary rolling, separation are granulated and further solidification is dried from grate-cooler cooling is reentered, complete making for EPS particles Grain.
Bonding agent is dispersed latex powder, and curing agent is water soluble phenol resin, and fire retardant is aluminium hydroxide and graphite Mixture.
Graphite is one of crystalline mineral of carbon, has lubricity, chemical stability, heat-resisting quantity and screening characteristics, tool There are anti-flammability carefully and heat reflection performance, together filled with aluminium hydroxide, play good fire resistance.To improving organic material The fire resistance of material plays good effect, is individually present in mixed liquor with form of suspension, insoluble in mixed liquor, long-time Stand easily precipitation.
Embodiment 3
A kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process, using following steps:A, by EPS of same particle diameter Grain is foamed in high temperature foaming cabin, forms EPS expanded beads;B, inorganic overlay film liquid is configured, inorganic overlay film liquid is by as follows The raw material composition of mass fraction:2 parts of binding agent, 1 part of curing agent, 20 parts of fire retardant, 10 parts of water;C, EPS expanded beads are put Enter gas and hang overlay film storehouse, the density of EPS expanded beads is 8.8 KG/m3;D, gas hang overlay film storehouse bottom lead to pressure be 1.5MPa Steam by EPS expanded beads be suspended in gas hang overlay film storehouse in;E, inorganic overlay film liquid then is sprayed into gas by atomizer to hang Suspend stirring overlay film in overlay film storehouse with EPS expanded beads, and overlay film thickness is 0.4mm;F, enter after the completion of overlay film tilted-putted In rotary kiln, leaned on after rotary kiln rotary rolling, separation are granulated and further solidification is dried from grate-cooler cooling is reentered, complete EPS The granulation of particle.
Bonding agent is dispersed latex powder, and curing agent is accelerator, and fire retardant is desulfurated plaster.
In specific implementation process, the angle of inclination of rotary kiln is 15 °.
Unified during inorganic overlay film liquid sprinkling using lateral two pipe and put pressure spray process, one of inorganic overlay film liquid of Pipeline transport, Another Pipeline transport curing agent, ensure that the attachment of particle surface liquid is uniform, while hot setting forms particle, with particle Variable density and hot setting effect rely on deadweight to sink to entering rotary kiln.
The mass ratio of EPS expanded beads and inorganic mixed liquor is 5:2-3, scale parameter is adjusted by overlay film thickness.
Dosed in architectural engineering using obtained particle as aggregate into foam cement or lightweight concrete, site pumping Pour to flooring or roofing, as insulation bed course, play insulation, it is heat-insulated, look for slope, waterproof action, its compression strength More than 5Mpa is can reach, thermal conductivity factor is no more than 0.045w/km;Also can by obtained particle with curing agent mixed liquor with certain Ratio stirs, and curing molding insulation, fire-retardant, thermal insulation plate are applied to engineering insulation and light wall material.

Claims (2)

  1. A kind of 1. EPS particles suspension overlay film solidification rotary kiln separation prilling process, it is characterised in that:Using following steps:A, will be same The EPS particles of one particle diameter are foamed in high temperature foaming cabin, form EPS expanded beads;B, inorganic overlay film liquid is configured, it is inorganic to cover Film liquid is made up of the raw material of following mass fraction:Binding agent 1-2 parts, curing agent 1-5 parts, fire retardant 3-20 parts, water 7-12 Part;C, EPS expanded beads are inserted into gas and hangs overlay film storehouse, the density of EPS expanded beads is 8-10 KG/m3;D, overlay film is hanged in gas The bottom in storehouse leads to the steam that pressure is 0.5-1.5MPa and EPS expanded beads is suspended in the outstanding overlay film storehouse of gas;E, then will be inorganic Overlay film liquid sprays into gas by atomizer and hangs the stirring overlay film that suspended in overlay film storehouse with EPS expanded beads, and overlay film thickness is 0.1- 0.4mm;F, enter after the completion of overlay film in tilted-putted rotary kiln, be granulated through rotary kiln rotary rolling, separation and further solidification is done Leaned on after dry from grate-cooler cooling is reentered, complete the granulation of EPS particles.
  2. A kind of 2. EPS particles suspension overlay film solidification rotary kiln separation prilling process according to claim 1, it is characterised in that: Bonding agent is dispersed latex powder, and curing agent is accelerator or water soluble phenol resin, and fire retardant is portland cement, hydroxide The mixture or desulfurated plaster of aluminium and graphite.
CN201710957329.0A 2017-10-16 2017-10-16 A kind of EPS particles suspension overlay film solidification rotary kiln separation prilling process Pending CN107599221A (en)

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Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB900120A (en) * 1959-10-06 1962-07-04 Dow Chemical Co Intumescent coating composition and method of making combustible materials fire retardant
US20040035318A1 (en) * 2000-01-27 2004-02-26 Henry Gang Flame inhibiting and retarding chemical process and system for general use on multiple solid surfaces
CA2123209C (en) * 1991-11-07 2004-06-22 Akbar Ghahary Granite-like coating
CN101560308A (en) * 2009-06-02 2009-10-21 吉林大学 One-step preparation method for synthesizing black expandable polystyrene particles
CN102655128A (en) * 2011-03-03 2012-09-05 硕恩科技股份有限公司 Porous graphite radiator and preparation method of porous graphite
CN102977402A (en) * 2012-12-18 2013-03-20 辽宁工程技术大学 Preparation method of coated halogen-free flame-retardant foamable polystyrene
CN104191632A (en) * 2014-08-07 2014-12-10 洛阳佳一机电设备有限公司 Light particle lamination production system and production method thereof
CN104194031A (en) * 2014-08-26 2014-12-10 北京工商大学 Preparation method of flame-retardant-containing expandable polystyrene granules
CN105936728A (en) * 2016-06-21 2016-09-14 河北见喜新材料科技股份有限公司 Manufacturing method of ultra-dispersed flame-retardant master batch
US9682888B2 (en) * 2011-10-10 2017-06-20 Certainteed Corporation Coated granules for construction applications

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB900120A (en) * 1959-10-06 1962-07-04 Dow Chemical Co Intumescent coating composition and method of making combustible materials fire retardant
CA2123209C (en) * 1991-11-07 2004-06-22 Akbar Ghahary Granite-like coating
US20040035318A1 (en) * 2000-01-27 2004-02-26 Henry Gang Flame inhibiting and retarding chemical process and system for general use on multiple solid surfaces
CN101560308A (en) * 2009-06-02 2009-10-21 吉林大学 One-step preparation method for synthesizing black expandable polystyrene particles
CN102655128A (en) * 2011-03-03 2012-09-05 硕恩科技股份有限公司 Porous graphite radiator and preparation method of porous graphite
US9682888B2 (en) * 2011-10-10 2017-06-20 Certainteed Corporation Coated granules for construction applications
CN102977402A (en) * 2012-12-18 2013-03-20 辽宁工程技术大学 Preparation method of coated halogen-free flame-retardant foamable polystyrene
CN104191632A (en) * 2014-08-07 2014-12-10 洛阳佳一机电设备有限公司 Light particle lamination production system and production method thereof
CN104194031A (en) * 2014-08-26 2014-12-10 北京工商大学 Preparation method of flame-retardant-containing expandable polystyrene granules
CN105936728A (en) * 2016-06-21 2016-09-14 河北见喜新材料科技股份有限公司 Manufacturing method of ultra-dispersed flame-retardant master batch

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