CN110126136A - Utilize the technics of enhancing viscosity of Pillar recovery bottle piece processing HMLS Polyester silk - Google Patents
Utilize the technics of enhancing viscosity of Pillar recovery bottle piece processing HMLS Polyester silk Download PDFInfo
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- CN110126136A CN110126136A CN201910419372.0A CN201910419372A CN110126136A CN 110126136 A CN110126136 A CN 110126136A CN 201910419372 A CN201910419372 A CN 201910419372A CN 110126136 A CN110126136 A CN 110126136A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/06—Conditioning or physical treatment of the material to be shaped by drying
- B29B13/065—Conditioning or physical treatment of the material to be shaped by drying of powder or pellets
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B2017/001—Pretreating the materials before recovery
- B29B2017/0015—Washing, rinsing
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Abstract
The invention discloses a kind of technics of enhancing viscosity using Pillar recovery bottle piece processing HMLS Polyester silk, it is related to regenerated terylene silk processing technique field, the following steps are included: (1) crushes, (2) it cleans, (3) it dries, (4) it viscosifies, the output of (5) die head.The present invention improves the brittleness of waste polyester bottle chip by freezing processing, in favor of improving crush efficiency on the basis of guaranteeing grinding particle size, reducing pulverizer energy consumption；And using first crush clean afterwards by the way of can significantly improve cleaning efficiency, the dust and greasy dirt washed down be easier to enter cleaning waste water in；And as the tackified finish to waste and old polyester make after processing obtained by the intrinsic viscosity of PET melt significantly increase, to meet requirement of the HMLS Polyester silk to raw material.
Description
Technical field:
The present invention relates to regenerated terylene silk processing technique fields, and in particular to a kind of to process Gao Mo using Pillar recovery bottle piece
The technics of enhancing viscosity of low-shrinkage dacron thread.
Background technique:
It is the main path of the current polyester recycling and reusing in China using waste polyester bottle chip production regenerated fiber, however this
A little fibers are mainly the cotton of some low sides, filled-type product, since the expansion and homogeneity of production capacity are serious, regenerated fiber enterprise
Industry is in meagre profit state.Therefore high-endization of regenerated fiber, functionality just seem necessary.
Requirement of the HMLS Polyester silk to raw material is not achieved in the intrinsic viscosity (about 0.6dL/g) of common PET slice, and passes through
The PET melt intrinsic viscosity of PET bottle piece recycling is lower.Therefore, it in order to improve the intrinsic viscosity of PET melt, needs to recycled PET
Carry out tackified finish.At present frequently with thickening mode be PET chain extension thickening, but the Efficient Adhesive Promotion of this thickening mode is limited,
And ensuring tackifier be added will not decompose reaction during high temperature extrusion molding, otherwise will affect recycling
The recycling property energy of PET.
Summary of the invention:
Technical problem to be solved by the present invention lies in one kind is provided, operation is simple, process control parameter is clear and work
The reproducible technics of enhancing viscosity using Pillar recovery bottle piece processing HMLS Polyester silk of skill.
The following technical solution is employed for the technical problems to be solved by the invention to realize:
Utilize the technics of enhancing viscosity of Pillar recovery bottle piece processing HMLS Polyester silk, comprising the following steps:
(1) it crushes: first waste polyester bottle chip being transferred in freezing chamber and is stood, is produced after chilled processing, and through pulverizer
The particle of 1~5mm of granularity is made to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, spray cleaning in rotary drum washer
Liquid is cleaned at 300~500rpm of revolving speed, and cleaning solution is discharged after cleaning, then draws off waste and old polyester particle；
(3) it dries: once purged polyester granulate being sent into roller dryer, and at 200~400rpm of revolving speed
Water content is dried to lower than 0.5wt%；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into
Extruder carries out extrusion plasticizing, and the heating temperature in extruder is 250~260 DEG C；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and runner temperature 250~
260 DEG C, 260~270 DEG C of die head temperature.
Cryogenic temperature is 5~10 DEG C in the step (1).
The freezing processing time is 8~12h in the step (1).
Cleaning solution temperature is 45~55 DEG C in the step (2).
Scavenging period is 10~30min in the step (2).
Drying temperature is 65~75 DEG C in the step (3).
The weight ratio of polyester granulate and tackifier is 100:5~15 in the step (4).
Tackifier are pyromellitic acid anhydride in the step (4).The pyromellitic acid anhydride pair during extrusion plasticizing
PET carries out chain extension thickening, belongs to chemical thickening mode.
Trihydroxymethylpropanyltri diglycidyl ether of the tackifier by weight ratio 2:1:0.5, poly- two season penta in the step (4)
Six acrylate of tetrol and stearyl alcohol glycyrrhetin acid esters composition.The tackifier are punctured into PET molecule knot during extrusion plasticizing
In structure, belong to physics thickening mode.
Cleaning solution is dissolved in water by cleaning agent and is made in the step (2).
The cleaning agent is decyl glucoside, and dosage is that every 1kg water dissolves 0.5~5g decyl glucoside.
The cleaning agent is decyl glucoside-pyroglutamic acid carboxylate, and dosage is that every 1kg water dissolves 0.5~5g decyl
Glucoside-pyroglutamic acid carboxylate.
The decyl glucoside-pyroglutamic acid carboxylate is made of decyl glucoside, pyroglutamic acid through esterification,
Preparation method are as follows: first decyl glucoside and pyroglutamic acid are dissolved in the water respectively, are configured to decyl glucoside solution
With pyroglutamic acid solution, then the concentrated sulfuric acid is added dropwise into pyroglutamic acid solution and adjusts solution ph to 3~4, decyl Portugal is then added dropwise
Polyglycoside solution is warming up to reflux state insulation reaction after being added dropwise, after reaction be concentrated under reduced pressure be made solid content 65~
75% lotion, gained lotion are sent into freeze drier after cooled to room temperature, and dry obtained solid is through pulverizing
15~20 μm of granularity of micro mist is made to get decyl glucoside-pyroglutamic acid carboxylate in machine.
The decyl glucoside and the molar ratio of pyroglutamic acid are 1:5.
The beneficial effects of the present invention are:
(1) present invention improves the brittleness of waste polyester bottle chip by freezing processing, in favor of guaranteeing grinding particle size
On the basis of improve crush efficiency, reduce pulverizer energy consumption；And using first crush clean afterwards by the way of can significantly improve cleaning
Efficiency, the dust and greasy dirt washed down are easier to enter in cleaning waste water；
(2) present invention efficiently removes the dust and greasy dirt that adhere on waste and old polyester particle by cleaning operation, avoids ash
The presence of dirt and greasy dirt influences the regeneration of waste and old polyester particle, and mitigates cleaning institute by selecting environmental type cleaning agent
Generate the processing difficulty of waste water；
(3) present invention carries out tackified finish to waste and old polyester by two kinds of thickening modes, make after processing gained PET it is molten
The intrinsic viscosity of body significantly increases, to meet requirement of the HMLS Polyester silk to raw material.
Specific embodiment:
In order to be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, tie below
Specific embodiment is closed, the present invention is further explained.
Embodiment 1
(1) it crushes: first 25kg waste polyester bottle chip being transferred in 5~10 DEG C of freezing chambers and is stood, turn after 12h freezing processing
Out, and through pulverizer the particle of 3~5mm of granularity is made to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, 100kg is sprayed in rotary drum washer
50~55 DEG C of cleaning solutions clean 10min at revolving speed 500rpm, cleaning solution are discharged after cleaning, then draws off waste and old polyester
Particle；Cleaning solution is dissolved in water by cleaning agent and is made, and cleaning agent is decyl glucoside, and dosage is that every 1kg water dissolves 5g decyl Portugal
Polyglycoside；
(3) it dries: once purged polyester granulate being sent into 70~75 DEG C of roller dryers, and in revolving speed 300rpm
Under be dried to water content lower than 0.5wt%；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into
Extruder carries out extrusion plasticizing, and the heating temperature in extruder is 255~260 DEG C；Polyester granulate and tackifier Pyromellitic Acid
The weight ratio of dianhydride is 100:10；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and runner temperature 250~
255 DEG C, 260~265 DEG C of die head temperature.
Embodiment 2
(1) it crushes: first 25kg waste polyester bottle chip being transferred in 5~10 DEG C of freezing chambers and is stood, turn after 12h freezing processing
Out, and through pulverizer the particle of 3~5mm of granularity is made to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, 100kg is sprayed in rotary drum washer
50~55 DEG C of cleaning solutions clean 10min at revolving speed 500rpm, cleaning solution are discharged after cleaning, then draws off waste and old polyester
Particle；Cleaning solution is dissolved in water by cleaning agent and is made, and cleaning agent is decyl glucoside, and dosage is that every 1kg water dissolves 5g decyl Portugal
Polyglycoside；
(3) it dries: once purged polyester granulate being sent into 70~75 DEG C of roller dryers, and in revolving speed 300rpm
Under be dried to water content lower than 0.5wt%；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into
Extruder carries out extrusion plasticizing, and the heating temperature in extruder is 255~260 DEG C；The weight ratio of polyester granulate and tackifier is
100:10, trihydroxymethylpropanyltri diglycidyl ether, dipentaerythrite six acrylate of the tackifier by weight ratio 2:1:0.5
It is formed with stearyl alcohol glycyrrhetin acid esters；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and runner temperature 250~
255 DEG C, 260~265 DEG C of die head temperature.
Embodiment 3
(1) it crushes: first 25kg waste polyester bottle chip being transferred in 5~10 DEG C of freezing chambers and is stood, turn after 12h freezing processing
Out, and through pulverizer the particle of 3~5mm of granularity is made to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, 100kg is sprayed in rotary drum washer
50~55 DEG C of cleaning solutions clean 10min at revolving speed 500rpm, cleaning solution are discharged after cleaning, then draws off waste and old polyester
Particle；Cleaning solution is dissolved in water by cleaning agent and is made, and cleaning agent is decyl glucoside-pyroglutamic acid carboxylate, and dosage is every
1kg water dissolves 5g decyl glucoside-pyroglutamic acid carboxylate；
Decyl glucoside-pyroglutamic acid carboxylate preparation: first respectively by 1mol decyl glucoside and 5mol Jiao Gu
Propylhomoserin is dissolved in the water, and is configured to decyl glucoside solution and pyroglutamic acid solution, then is added dropwise into pyroglutamic acid solution dense
Then sulfuric acid regulation solution pH value is added dropwise decyl glucoside solution, reflux state heat preservation is warming up to after being added dropwise to 3~4
Reaction, is concentrated under reduced pressure the lotion that solid content 65~75% is made after reaction, and gained lotion is sent after cooled to room temperature
Enter in freeze drier, 15~20 μm of granularity of micro mist is made through micronizer to get decyl glucose in dry obtained solid
Glycosides-pyroglutamic acid carboxylate；
(3) it dries: once purged polyester granulate being sent into 70~75 DEG C of roller dryers, and in revolving speed 300rpm
Under be dried to water content lower than 0.5wt%；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into
Extruder carries out extrusion plasticizing, and the heating temperature in extruder is 255~260 DEG C；The weight ratio of polyester granulate and tackifier is
100:10, trihydroxymethylpropanyltri diglycidyl ether, dipentaerythrite six acrylate of the tackifier by weight ratio 2:1:0.5
It is formed with stearyl alcohol glycyrrhetin acid esters；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and runner temperature 250~
255 DEG C, 260~265 DEG C of die head temperature.
Reference examples 1
It is control with embodiment 2, the reference examples 1 for not adding stearyl alcohol glycyrrhetin acid esters in tackifier is set.
(1) it crushes: first 25kg waste polyester bottle chip being transferred in 5~10 DEG C of freezing chambers and is stood, turn after 12h freezing processing
Out, and through pulverizer the particle of 3~5mm of granularity is made to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, 100kg is sprayed in rotary drum washer
50~55 DEG C of cleaning solutions clean 10min at revolving speed 500rpm, cleaning solution are discharged after cleaning, then draws off waste and old polyester
Particle；Cleaning solution is dissolved in water by cleaning agent and is made, and cleaning agent is decyl glucoside, and dosage is that every 1kg water dissolves 5g decyl Portugal
Polyglycoside；
(3) it dries: once purged polyester granulate being sent into 70~75 DEG C of roller dryers, and in revolving speed 300rpm
Under be dried to water content lower than 0.5wt%；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into
Extruder carries out extrusion plasticizing, and the heating temperature in extruder is 255~260 DEG C；The weight ratio of polyester granulate and tackifier is
100:10, trihydroxymethylpropanyltri diglycidyl ether of the tackifier by weight ratio 2:1, six acrylate group of dipentaerythrite
At；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and runner temperature 250~
255 DEG C, 260~265 DEG C of die head temperature.
Reference examples 2
It is control with embodiment 2, the reference examples 2 for not adding six acrylate of dipentaerythrite in tackifier is set.
(1) it crushes: first 25kg waste polyester bottle chip being transferred in 5~10 DEG C of freezing chambers and is stood, turn after 12h freezing processing
Out, and through pulverizer the particle of 3~5mm of granularity is made to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, 100kg is sprayed in rotary drum washer
50~55 DEG C of cleaning solutions clean 10min at revolving speed 500rpm, cleaning solution are discharged after cleaning, then draws off waste and old polyester
Particle；Cleaning solution is dissolved in water by cleaning agent and is made, and cleaning agent is decyl glucoside, and dosage is that every 1kg water dissolves 5g decyl Portugal
Polyglycoside；
(3) it dries: once purged polyester granulate being sent into 70~75 DEG C of roller dryers, and in revolving speed 300rpm
Under be dried to water content lower than 0.5wt%；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into
Extruder carries out extrusion plasticizing, and the heating temperature in extruder is 255~260 DEG C；The weight ratio of polyester granulate and tackifier is
100:10, tackifier are made of the trihydroxymethylpropanyltri diglycidyl ether and stearyl alcohol glycyrrhetin acid esters of weight ratio 2:0.5；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and runner temperature 250~
255 DEG C, 260~265 DEG C of die head temperature.
Reference examples 3
It is control with embodiment 2, the reference examples 3 for not adding trihydroxymethylpropanyltri diglycidyl ether in tackifier is set.
(1) it crushes: first 25kg waste polyester bottle chip being transferred in 5~10 DEG C of freezing chambers and is stood, turn after 12h freezing processing
Out, and through pulverizer the particle of 3~5mm of granularity is made to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, 100kg is sprayed in rotary drum washer
50~55 DEG C of cleaning solutions clean 10min at revolving speed 500rpm, cleaning solution are discharged after cleaning, then draws off waste and old polyester
Particle；Cleaning solution is dissolved in water by cleaning agent and is made, and cleaning agent is decyl glucoside, and dosage is that every 1kg water dissolves 5g decyl Portugal
Polyglycoside；
(3) it dries: once purged polyester granulate being sent into 70~75 DEG C of roller dryers, and in revolving speed 300rpm
Under be dried to water content lower than 0.5wt%；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into
Extruder carries out extrusion plasticizing, and the heating temperature in extruder is 255~260 DEG C；The weight ratio of polyester granulate and tackifier is
100:10, tackifier are made of six acrylate of dipentaerythrite and stearyl alcohol glycyrrhetin acid esters of weight ratio 1:0.5；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and runner temperature 250~
255 DEG C, 260~265 DEG C of die head temperature.
Reference examples 4
It is control with embodiment 3, setting cleaning agent selects the decyl glucoside and pyroglutamic acid mixture of molar ratio 1:5
Reference examples 4.
(1) it crushes: first 25kg waste polyester bottle chip being transferred in 5~10 DEG C of freezing chambers and is stood, turn after 12h freezing processing
Out, and through pulverizer the particle of 3~5mm of granularity is made to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, 100kg is sprayed in rotary drum washer
50~55 DEG C of cleaning solutions clean 10min at revolving speed 500rpm, cleaning solution are discharged after cleaning, then draws off waste and old polyester
Particle；Cleaning solution is dissolved in water by cleaning agent and is made, and cleaning agent is decyl glucoside-pyroglutamic acid carboxylate, and dosage is every
The molar ratio of 1kg water dissolution 5g decyl glucoside and pyroglutamic acid, decyl glucoside and pyroglutamic acid is 1:5；
(3) it dries: once purged polyester granulate being sent into 70~75 DEG C of roller dryers, and in revolving speed 300rpm
Under be dried to water content lower than 0.5wt%；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into
Extruder carries out extrusion plasticizing, and the heating temperature in extruder is 255~260 DEG C；The weight ratio of polyester granulate and tackifier is
100:10, trihydroxymethylpropanyltri diglycidyl ether, dipentaerythrite six acrylate of the tackifier by weight ratio 2:1:0.5
It is formed with stearyl alcohol glycyrrhetin acid esters；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and runner temperature 250~
255 DEG C, 260~265 DEG C of die head temperature.
Embodiment 4
It is utilized respectively embodiment 1-3, reference examples 1-4 and carries out tackified finish, and determination step to batch waste polyester bottle chip
(4) intrinsic viscosity (using Ubbelohde viscometer) and step (2) drawn off waste and old polyester of gained PET melt in extruder
The dust oil removal rate of grain, the results are shown in Table 1.
Treatment effect of the technics of enhancing viscosity of the present invention of table 1 to waste polyester bottle chip
As shown in Table 1, the present invention can be significantly improved using decyl glucoside-pyroglutamic acid carboxylate as cleaning agent
Dust oil removal rate, and use trihydroxymethylpropanyltri diglycidyl ether, six acrylate of dipentaerythrite and stearyl alcohol
Glycyrrhetin acid esters can make the intrinsic viscosity of gained PET melt reach 1dL/g or more as the physics thickening mode of tackifier.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (10)
1. utilizing the technics of enhancing viscosity of Pillar recovery bottle piece processing HMLS Polyester silk, which comprises the following steps:
(1) it crushes: first waste polyester bottle chip being transferred in freezing chamber and is stood, is produced after chilled processing, and be made through pulverizer
The particle of 1~5mm of granularity is to get waste and old polyester particle；
(2) it cleans: gained waste and old polyester particle is sent into rotary drum washer, cleaning solution is sprayed in rotary drum washer,
It is cleaned under 300~500rpm of revolving speed, cleaning solution is discharged after cleaning, then draw off waste and old polyester particle；
(3) it dries: once purged polyester granulate being sent into roller dryer, and is dried at 200~400rpm of revolving speed
It is lower than 0.5wt% to water content；
(4) it viscosifies: tackifier being added into polyester granulate after drying, and uniform in stirrer for mixing, enter back into extrusion
Machine carries out extrusion plasticizing, and the heating temperature in extruder is 250~260 DEG C；
(5) die head exports: the material after plasticizing is sent into die head through runner, exports sheet material through die head, and 250~260 DEG C of runner temperature,
260~270 DEG C of die head temperature.
2. the technics of enhancing viscosity according to claim 1 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: cryogenic temperature is 5~10 DEG C in the step (1).
3. the technics of enhancing viscosity according to claim 1 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: the freezing processing time is 8~12h in the step (1).
4. the technics of enhancing viscosity according to claim 1 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: cleaning solution temperature is 45~55 DEG C in the step (2).
5. the technics of enhancing viscosity according to claim 1 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: scavenging period is 10~30min in the step (2).
6. the technics of enhancing viscosity according to claim 1 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: drying temperature is 65~75 DEG C in the step (3).
7. the technics of enhancing viscosity according to claim 1 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: the weight ratio of polyester granulate and tackifier is 100:5~15 in the step (4).
8. the technics of enhancing viscosity according to claim 1 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: tackifier are pyromellitic acid anhydride in the step (4).
9. the technics of enhancing viscosity according to claim 1 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: cleaning solution is dissolved in water by cleaning agent and is made in the step (2).
10. the technics of enhancing viscosity according to claim 9 using Pillar recovery bottle piece processing HMLS Polyester silk, feature
Be: the cleaning agent is decyl glucoside, and dosage is that every 1kg water dissolves 0.5~5g decyl glucoside.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112609316A (en) * | 2020-12-11 | 2021-04-06 | 山东滨州波涛化纤制品有限公司 | Method for manufacturing fabric by weaving PET cast film and slitting and stretching all-in-one machine |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63202408A (en) * | 1987-02-18 | 1988-08-22 | Toshiba Mach Co Ltd | Production equipment of reclaimed pellet of waste pet resin film or the like |
| EP0492043A2 (en) * | 1990-12-27 | 1992-07-01 | Taiyo Electric Industry Co., Ltd | Method for recycling treatment of refuse of plastic molded articles and apparatus therefor |
| CN103422182A (en) * | 2013-08-19 | 2013-12-04 | 大连恒源纤维科技有限公司 | Regenerated polyester short-cut fiber |
| CN109651775A (en) * | 2018-12-25 | 2019-04-19 | 南通新帝克单丝科技股份有限公司 | A kind of chemical thickening method of reuse polyethylene terephthalate |
-
2019
- 2019-05-20 CN CN201910419372.0A patent/CN110126136B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63202408A (en) * | 1987-02-18 | 1988-08-22 | Toshiba Mach Co Ltd | Production equipment of reclaimed pellet of waste pet resin film or the like |
| EP0492043A2 (en) * | 1990-12-27 | 1992-07-01 | Taiyo Electric Industry Co., Ltd | Method for recycling treatment of refuse of plastic molded articles and apparatus therefor |
| CN103422182A (en) * | 2013-08-19 | 2013-12-04 | 大连恒源纤维科技有限公司 | Regenerated polyester short-cut fiber |
| CN109651775A (en) * | 2018-12-25 | 2019-04-19 | 南通新帝克单丝科技股份有限公司 | A kind of chemical thickening method of reuse polyethylene terephthalate |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112609316A (en) * | 2020-12-11 | 2021-04-06 | 山东滨州波涛化纤制品有限公司 | Method for manufacturing fabric by weaving PET cast film and slitting and stretching all-in-one machine |
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