CN209722011U - A kind of preparation system of optical cable loose tube raw material - Google Patents

A kind of preparation system of optical cable loose tube raw material Download PDF

Info

Publication number
CN209722011U
CN209722011U CN201822195666.3U CN201822195666U CN209722011U CN 209722011 U CN209722011 U CN 209722011U CN 201822195666 U CN201822195666 U CN 201822195666U CN 209722011 U CN209722011 U CN 209722011U
Authority
CN
China
Prior art keywords
raw material
optical cable
loose tube
esterification
preparation system
Prior art date
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.)
Active
Application number
CN201822195666.3U
Other languages
Chinese (zh)
Inventor
刘贻文
黄小明
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.)
Jiangyin Echosens Burton Polymer Co Ltd
Original Assignee
Jiangyin Echosens Burton Polymer 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
Publication date
Application filed by Jiangyin Echosens Burton Polymer Co Ltd filed Critical Jiangyin Echosens Burton Polymer Co Ltd
Priority to CN201822195666.3U priority Critical patent/CN209722011U/en
Application granted granted Critical
Publication of CN209722011U publication Critical patent/CN209722011U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Polyesters Or Polycarbonates (AREA)
  • Light Guides In General And Applications Therefor (AREA)

Abstract

The utility model relates to optical fiber secondary coating raw material preparation technical fields; it discloses a kind of preparation system of optical cable loose tube raw material, including the process according to preparation be sequentially arranged Weighing device, be mixed installation, reaction kettle of the esterification, precondensation kettle, whole polycondensation vessel, for carrying out pelletizing to the whole polymers after final polycondensation reaction the pelleter of pellet, the polymerization purifying plant for carrying out polymerization purification to the pellet after pelletizing is made, for the pellet after purification screen and purified treatment is screened and purified device.The utility model improves the stability of optical cable loose tube material property, and then improves the flexibility and antiseepage oiliness of optical cable loose tube, while reducing the diameter change of long fluctuation and Loose tube more than the optical cable after optical fiber secondary coating.

Description

A kind of preparation system of optical cable loose tube raw material
Technical field
The utility model relates to optical fiber secondary coating raw material preparation technical fields, and in particular to a kind of optical cable loose tube is former The preparation system of material.
Background technique
In optical fiber secondary coating technique, filling fiber paste after the optical fiber boundling different colours is needed to enter by engineering plastic Expect in the round tube (Loose tube) extruded.Loose tube, which can play, loosely to be placed optical fiber, protects optical fiber from internal stress and outer The effect that portion's lateral pressure influences, generallys use PBT (polybutylene terephthalate (PBT)) or polypropylene (PP) etc. and is made.
Raw material currently used for extruding optical cable loose tube generallys use PBT (polybutylene terephthalate (PBT)), although PBT With outstanding processing performance, but under certain specific service conditions, the required pine set for optical fiber secondary coating The bending radius very little of pipe is easily snapped off using the optical cable loose tube that PBT is manufactured, and uses the polypropylene of polypropylene PP or modification The Loose tube of PP manufacture is then easy to appear permeability phenomenon.
Therefore there is an urgent need to find the good Loose tube raw material of a kind of more soft and antiseepage oiliness to replace for the prior art Existing PBT and polypropylene (PP) raw material.
The admissible optional scheme of one kind is using TPEE (thermoplastic polyester elastomer) raw material.Hard section in TPEE It is typically chosen high rigidity crystallinity PBT, soft segment then selects noncrystalline polyethers (such as polyglycol ether PEG, polypropylene glycol ether PPG, polybutadiene alcohol ether PTMEG etc.) or aliphatic polyester (such as polylactide PLA, polyglycolide PGA, polycaprolactone (PCL)). Using polyethers is the TPEE cold resistance of soft segment preparation, flexibility and hydrolytic resistance is preferable but fast light, heat resistance is poor;With aliphatic Polyester is the TPEE heat-resistant aging of soft segment preparation, good weatherability, but hydrolytic resistance is poor.It, can be according to TPEE in actual production Purposes select different proportions, freely design the hard and soft chain segment ratio of block copolymer.Soft, hard segment type, length Have an impact with performance of the content to TPEE.And currently there are TPEE belong to universal polyester-polyether type TPEE, Its heat resistance, lower temperature resistance, chemical-resistance and processing performance relatively balance.
But above-mentioned universal TPEE raw material is due to during the preparation process that by purification, raw material inside is not contained A small amount of small molecule object, such as p-phthalic acid PTA, 1,4-butanediol BDO, tetrahydrofuran, polyethers and small molecule chain Polybutylene terephthalate (PBT) PBT etc..The presence of these small molecule objects affects the stability of TPEE performance, leads to production Optical fiber secondary coating is had the following problems with Loose tube: first is that the shrinking percentage of material is unstable, the optical cable after leading to secondary coating Remaining long fluctuation is big;Second is that the unstable of shrinking percentage also causes Loose tube diameter fluctuation larger, to reduce the quality of Loose tube And reliability.
Utility model content
To solve the above-mentioned problems, the utility model proposes a kind of preparation systems of optical cable loose tube raw material, it is intended to improve The stability of optical cable loose tube material property, and then improve the flexibility and antiseepage oiliness of optical cable loose tube, while reducing optical cable The diameter change of long fluctuation and Loose tube more than optical cable after secondary coating.Specific technical solution is as follows:
A kind of preparation system of optical cable loose tube raw material, matches including what the process according to preparation was sequentially arranged for raw material The Weighing device of material, is used for mixed object the mixing installation for mixing the raw material after ingredient Material carries out esterification to generate the reaction kettle of the esterification of carboxylate, for carrying out prepolymerization reaction to the carboxylate after esterification To generate the precondensation kettle of prepolymer, for carrying out final polycondensation reaction to the prepolymer after prepolymerization reaction to generate whole polymers Whole polycondensation vessel, for carrying out pelletizing to the whole polymers after final polycondensation reaction the pelleter of pellet is made, for after to pelletizing Pellet carries out the polymerization purifying plant of polymerization purification, for screen to the pellet after purification and purified treatment is screened and purified Device.
Above-mentioned raw material ingredient includes the ingredient of soft segment raw material and matching for hard section raw material for participating in esterification Material.
Preferably, the Weighing device includes BDO (1,4-butanediol) metering device and DMT (terephthalic acid (TPA) two Methyl esters) metering device.
Above-mentioned preparation system increases compared with prior art is provided with polymerization purifying plant, polymerize to the pellet after pelletizing Purification, the small molecule object after polymerization purification in its pellet are therefrom precipitated, and which thereby enhance optical cable loose tube material property Stability, and then reduce the diameter change of long fluctuation and Loose tube more than the optical cable after optical fiber secondary coating, to improve pine The q&r of casing.
In the utility model, the catalyst feeding device for promoting esterification is connected on the reaction kettle of the esterification, Catalyst metering apparatus is provided on the catalyst feeding device.
Preferably, the catalyst feeding device includes butyl titanate feeding device and magnesium acetate feeding device.
Preferably, the polymerization purifying plant is rotative nickel reactor.
Preferably, described is stainless steel revolving reaction kettle.
Preferably, the device that is screened and purified is fluidized bed.
The above-mentioned device that is screened and purified is using fluidized bed, and available particle is uniform and the higher optical cable loose tube of degree of purification is former The pellet of material.
A kind of preparation system of optical cable loose tube raw material of the utility model further includes being arranged in described to be screened and purified device Baling press later.
Using the preparation system of above-mentioned optical cable loose tube raw material, its preparation process flow is as follows:
(1) ingredient: taking 1,4-butanediol BDO, dimethyl terephthalate (DMT) DMT and catalyst for esterification reaction is material, is made Ingredient is carried out with Weighing device;Wherein the molar ratio of BDO and DMT is 1.7:1~2:1;
(2) mixing: mixing and blending machine is used, BDO is uniformly mixed with DMT;
(3) it is esterified: adding mixture into reaction kettle of the esterification, and esterification is added using catalyst feeding device and urges Agent carries out esterification, obtains carboxylate;Wherein, the weight of catalyst for esterification reaction is the 0.12 of BDO and DMT total weight ~0.20%;
(4) pre-polymerization: the carboxylate Jing Guo esterification is transferred in precondensation kettle, is carried out prepolymerization reaction, is obtained pre- Polymers;
(5) poly- eventually: prepolymer being transferred in whole polycondensation vessel, final polycondensation reaction is carried out, obtains whole polymers;
(6) pelletizing: whole polymers is transferred to pelleter, is cut into pellet;
(7) it purifies: pellet being transferred to purified reaction kettle, carries out polymerization purification, so that the small molecule object in pellet is therefrom It is precipitated;
(8) it screens: using fluidized bed, screening and purified treatment are carried out to the pellet after purification.
It is excellent by rational proportion BDO (1,4-butanediol) and DMT (dimethyl terephthalate (DMT)) in above-mentioned preparation process The hard and soft chain segment ratio for having changed block copolymer, improves the comprehensive performance of optical cable loose tube raw material, so that the optical cable produced Loose tube has both good flexibility and antiseepage oiliness.
(9) it is packaged: the optical cable loose tube raw material after screening being packaged using baling press.
Wherein, in the esterification step, the technological parameter of esterification are as follows: 240~245 DEG C of temperature, pressure 40~ 50Kpa, the time 2.0~2.5 hours.
Wherein, in the pre-polymerization process, the technological parameter of prepolymerization reaction are as follows: 245~248 DEG C of temperature, pressure 20~ 25Kpa, the time 0.75~0.8 hour.
Wherein, in the end poly- process, the technological parameter of final polycondensation reaction are as follows: 242~248 DEG C of temperature, pressure 100~ 120pa, the time 3.0~3.5 hours.
Wherein, in the purification process, it polymerize the technological parameter of purification are as follows: 190~200 DEG C of temperature, pressure 0~ 2Kpa, the time 3.0~3.5 hours.
Wherein, the catalyst for esterification reaction is titanium system catalyst for esterification reaction.
Preferably, titanium system catalyst for esterification reaction is butyl titanate, or is butyl titanate and magnesium acetate Mixture.
The beneficial effects of the utility model are:
First, a kind of preparation system of optical cable loose tube raw material of the utility model increases and is provided with polymerization purifying plant, Polymerization purification is carried out to the pellet after pelletizing, the small molecule object after polymerization purification in its pellet is therefrom precipitated, and thus improves The stability of optical cable loose tube material property, and then reduce long fluctuation and Loose tube more than the optical cable after optical fiber secondary coating Diameter change, to improve the q&r of Loose tube.
Second, a kind of preparation system of optical cable loose tube raw material of the utility model is screened and purified device and uses fluidized bed, Available particle is uniform and the pellet of the higher optical cable loose tube raw material of degree of purification.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of the preparation system of optical cable loose tube raw material of the utility model.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is further described.Implement below Example is only used for clearly illustrating the technical solution of the utility model, and cannot be used as a limitation the protection model of limitation the utility model It encloses.
Embodiment 1:
It is as shown in Figure 1 a kind of embodiment of the preparation system of optical cable loose tube raw material of the utility model, including according to The process of preparation be sequentially arranged for the Weighing device of raw material ingredient, for the raw material after ingredient to be mixed Mixing installation, for mixed material to be carried out esterification to generate the reaction kettle of the esterification of carboxylate, be used for pair Carboxylate after esterification carry out prepolymerization reaction to generate the precondensation kettle of prepolymer, for pre- after prepolymerization reaction Polymers carry out final polycondensation reaction with generate whole polymers whole polycondensation vessel, for after final polycondensation reaction whole polymers carry out pelletizing with The pelleter of pellet, the polymerization purifying plant for carrying out polymerization purification to the pellet after pelletizing is made, for after to purification Pellet carries out screening and purified treatment is screened and purified device.
Above-mentioned raw material ingredient includes the ingredient of soft segment raw material and matching for hard section raw material for participating in esterification Material.
Preferably, the Weighing device includes BDO (1,4-butanediol) metering device and DMT (terephthalic acid (TPA) two Methyl esters) metering device.
Above-mentioned preparation system increases compared with prior art is provided with polymerization purifying plant, polymerize to the pellet after pelletizing Purification, the small molecule object after polymerization purification in its pellet are therefrom precipitated, and which thereby enhance optical cable loose tube material property Stability, and then reduce the diameter change of long fluctuation and Loose tube more than the optical cable after optical fiber secondary coating, to improve pine The q&r of casing.
This carries out being connected with the catalyst for promoting esterification on the reaction kettle of the esterification in screening and purified treatment Feeding device is provided with catalyst metering apparatus on the catalyst feeding device.
Preferably, the catalyst feeding device includes butyl titanate feeding device and magnesium acetate feeding device.
Preferably, the polymerization purifying plant is rotative nickel reactor.
Preferably, described is stainless steel revolving reaction kettle.
Preferably, the device that is screened and purified is fluidized bed.
The above-mentioned device that is screened and purified is using fluidized bed, and available particle is uniform and the higher optical cable loose tube of degree of purification is former The pellet of material.
This preparation system for carrying out a kind of optical cable loose tube raw material of screening and purified treatment further includes being arranged in the sieve Select the baling press after purification device.
Embodiment 2:
Using a kind of preparation system of optical cable loose tube raw material of embodiment 1, its preparation process flow is as follows:
(1) ingredient: taking 1,4-butanediol BDO, dimethyl terephthalate (DMT) DMT and catalyst for esterification reaction is material, is made Ingredient is carried out with Weighing device;Wherein the molar ratio of BDO and DMT is 1.7:1~2:1;
(2) mixing: mixing and blending machine is used, BDO is uniformly mixed with DMT;
(3) it is esterified: adding mixture into reaction kettle of the esterification, and esterification is added using catalyst feeding device and urges Agent carries out esterification, obtains carboxylate;Wherein, the weight of catalyst for esterification reaction is the 0.12 of BDO and DMT total weight ~0.20%;
(4) pre-polymerization: the carboxylate Jing Guo esterification is transferred in precondensation kettle, is carried out prepolymerization reaction, is obtained pre- Polymers;
(5) poly- eventually: prepolymer being transferred in whole polycondensation vessel, final polycondensation reaction is carried out, obtains whole polymers;
(6) pelletizing: whole polymers is transferred to pelleter, is cut into pellet;
(7) it purifies: pellet being transferred to purified reaction kettle, carries out polymerization purification, so that the small molecule object in pellet is therefrom It is precipitated;
(8) it screens: using fluidized bed, screening and purified treatment are carried out to the pellet after purification.
It is excellent by rational proportion BDO (1,4-butanediol) and DMT (dimethyl terephthalate (DMT)) in above-mentioned preparation process The hard and soft chain segment ratio for having changed block copolymer, improves the comprehensive performance of optical cable loose tube raw material, so that the optical cable produced Loose tube has both good flexibility and antiseepage oiliness.
(9) it is packaged: the optical cable loose tube raw material after screening being packaged using baling press.
Wherein, in the esterification step, the technological parameter of esterification are as follows: 240~245 DEG C of temperature, pressure 40~ 50Kpa, the time 2.0~2.5 hours.
Wherein, in the pre-polymerization process, the technological parameter of prepolymerization reaction are as follows: 245~248 DEG C of temperature, pressure 20~ 25Kpa, the time 0.75~0.8 hour.
Wherein, in the end poly- process, the technological parameter of final polycondensation reaction are as follows: 242~248 DEG C of temperature, pressure 100~ 120pa, the time 3.0~3.5 hours.
Wherein, in the purification process, it polymerize the technological parameter of purification are as follows: 190~200 DEG C of temperature, pressure 0~ 2Kpa, the time 3.0~3.5 hours.
Wherein, the catalyst for esterification reaction is titanium system catalyst for esterification reaction.
Preferably, titanium system catalyst for esterification reaction is butyl titanate, or is butyl titanate and magnesium acetate Mixture.
Embodiment 3:
The optical cable loose tube raw material prepared using embodiment 1 and embodiment 2 is extruded into outer with the speed of production of 300m/min Diameter is the optical cable loose tube of φ 1.8mm, is then measured to caliber (outer diameter) variable quantity of the optical cable loose tube extruded out, and It is compared with the optical cable loose tube extruded out using universal TPEE raw material, as a result as follows:
The present invention Universal TPEE
Caliber (outer diameter) and variable quantity φ1.8±0.1mm φ1.8±0.2mm
Embodiment 4:
Optical cable loose tube is made using embodiment 3, carries out bending failure test, still maintains intact after detecting its bending Minimum bending radius, and be compared with the optical cable loose tube extruded out using universal TPEE raw material, it is as a result as follows:
The present invention Universal TPEE
Minimum bending radius 25~35mm 50~80mm
Embodiment 5:
Optical cable loose tube is made using embodiment 3, carries out optical fiber secondary coating test, the light after detecting optical fiber secondary coating Long change rate more than cable, and be compared with the optical cable loose tube extruded out using universal TPEE raw material, it is as a result as follows:
The present invention Universal TPEE
Remaining long change rate 0.1-0.3% Greater than 1.2%
The above is only the preferred embodiment of the utility model, it is noted that for the common skill of the art For art personnel, without deviating from the technical principle of the utility model, several improvements and modifications can also be made, these change It also should be regarded as the protection scope of the utility model into retouching.

Claims (7)

1. a kind of preparation system of optical cable loose tube raw material, which is characterized in that the use being sequentially arranged including the process according to preparation In the Weighing device of raw material ingredient, for the raw material after ingredient to be mixed mixing installation, be used for by Mixed material carries out esterification to generate the reaction kettle of the esterification of carboxylate, for carrying out to the carboxylate after esterification Prepolymerization reaction with generate prepolymer precondensation kettle, for after prepolymerization reaction prepolymer carry out final polycondensation reaction with life At the whole polycondensation vessel of whole polymers, for the pelleter of pellet to be made to the whole polymers progress pelletizing after final polycondensation reaction, is used for The polymerization purifying plant of polymerization purification is carried out, for carrying out screening and purified treatment to the pellet after purification to the pellet after pelletizing Be screened and purified device.
2. a kind of preparation system of optical cable loose tube raw material according to claim 1, which is characterized in that the Weighing Device includes BDO metering device and DMT metering device.
3. a kind of preparation system of optical cable loose tube raw material according to claim 1, which is characterized in that the esterification It is connected with the catalyst feeding device for promoting esterification on kettle, is provided with catalyst gauge on the catalyst feeding device Measure device.
4. a kind of preparation system of optical cable loose tube raw material according to claim 3, which is characterized in that the catalyst adds Expect that device includes butyl titanate feeding device and magnesium acetate feeding device.
5. a kind of preparation system of optical cable loose tube raw material according to claim 1, which is characterized in that the polymerization purification Device is rotative nickel reactor.
6. a kind of preparation system of optical cable loose tube raw material according to claim 1, which is characterized in that described to be screened and purified Device is fluidized bed.
7. a kind of preparation system of optical cable loose tube raw material according to claim 1, which is characterized in that further include being arranged in The baling press being screened and purified after device.
CN201822195666.3U 2018-12-26 2018-12-26 A kind of preparation system of optical cable loose tube raw material Active CN209722011U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201822195666.3U CN209722011U (en) 2018-12-26 2018-12-26 A kind of preparation system of optical cable loose tube raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201822195666.3U CN209722011U (en) 2018-12-26 2018-12-26 A kind of preparation system of optical cable loose tube raw material

Publications (1)

Publication Number Publication Date
CN209722011U true CN209722011U (en) 2019-12-03

Family

ID=68677833

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201822195666.3U Active CN209722011U (en) 2018-12-26 2018-12-26 A kind of preparation system of optical cable loose tube raw material

Country Status (1)

Country Link
CN (1) CN209722011U (en)

Similar Documents

Publication Publication Date Title
CN100506880C (en) High IV melt phase polyester polymer catalyzed with antimony containing compounds
US3420801A (en) Process for the manufacture of polyethylene terephthalate
CN1363002A (en) Poly (trimethylene terephthalate) yarn
CN102504217B (en) Method for preparing special polybutylene terephthalate for high-speed spinning
CN104403091B (en) Polyester production equipment and technology
DE1745296A1 (en) Continuous polymerization of terephthalate polyesters at higher rates using terephthalic acid
US11560450B2 (en) Aliphatic-aromatic polyester having elevated whiteness index
US4675378A (en) Process control system
CN101787584A (en) Method for preparing continuous polymerization directly-spun high-shrinkage polyester staple fibers
JP2005314674A (en) Polybutylene terephthalate
CN1962716A (en) Low-melting point polyester synthesis method
CN209722011U (en) A kind of preparation system of optical cable loose tube raw material
CN115651171B (en) Continuous preparation method of polycaprolactone polyol
JP3112943B2 (en) Co-condensed polyetherester elastomer having a hard fraction of poly- (1,3-propylene-4,4-diphenyldicarboxylate)
CN113817148B (en) Polylactic acid copolymer, preparation method and application thereof, and preparation method of blend film
CN106916286A (en) The semi continuous preparation method of Biodegradable polyester resin
CN1631933A (en) Process for continuous polycondensation preparation of fibrous polyethylene terephthalate
CN109836562A (en) A kind of preparation process of optical cable loose tube raw material
CN109206597A (en) Polybutylene terephthalate (PBT) resin and preparation method thereof
EP2657269B1 (en) Method for producing aliphatic polyester having increased molecular weight
CN1098872C (en) Preparation of violet ray resistant polyester
WO2005012391A1 (en) Polybutylene terephthalate
DE60106591T2 (en) METHOD OF PREPARING ALIPHATIC POLYESTER CARBONATE
CN106700040A (en) Method for preparing polylactic acid through twin screw reactive extrusion method and ring open polymerization method
EP2614100A1 (en) Method for producing polyester alcohols

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant