CN203820962U - Device for melt direct spinning production of PBT (polybutylece terephthalate) elastic filament - Google Patents
Device for melt direct spinning production of PBT (polybutylece terephthalate) elastic filament Download PDFInfo
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- CN203820962U CN203820962U CN201420100072.9U CN201420100072U CN203820962U CN 203820962 U CN203820962 U CN 203820962U CN 201420100072 U CN201420100072 U CN 201420100072U CN 203820962 U CN203820962 U CN 203820962U
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Abstract
The utility model discloses a device for melt direct spinning production of a PBT (polybutylece terephthalate) elastic filament. The device comprises a final polyethylene reactor (6). The device is characterized in that a low-viscosity melt discharge port formed in the middle of the final polyethylene reactor (6) is communicated with a melt filter (7), a low-viscosity melt is conveyed to a liquid-phase tackifying reactor (8) by the melt filter (7) through a melt pump along an insulation pipeline, and a discharge port of the liquid-phase tackifying reactor (8) is directly communicated with a feed port of a direct spinning device (9) through a conveying pipe. According to the device, the low-viscosity melt in the final polyethylene reactor is conveyed to the liquid-phase tackifying reactor, so as to be tackified, and then the low-viscosity melt is directly conveyed to the direct spinning device for spinning; when the PBT melt direct spinning is compared with PBT section spinning, the energy consumption is reduced to 38% of the section spinning process, the process flow is greatly shortened, additionally, the direct spinning device and a polyester section cannot be influenced, and the operating flexibility of the two devices is improved.
Description
Technical field
The utility model relates to the production technical field of PBT elastic filament, and the fused mass directly spinning that specifically the long distance of a kind of low sticky melt is carried, the short residence time of liquid-phase tackifying, high sticky melt distributes nearby before spinning manifold is produced the device of PBT elastic filament.
Background technology
At present, all PBT spinning all adopts section spinning process in the world.Be mainly, by three still flow processs, PTA and BDO are polymerized to the polyester fondant that inherent viscosity is 1.0dl/g left and right, through Cast Strip, cooling, pelletizing, make the section of PBT polyester.Again PBT polyester section is dried, screw rod heating melt extrudes the production of carrying out POY long filament to spinning manifold again.
The weak point of section spinning process is: PBT melt must pass through cooling and dicing → dry dewater → screw rod and heat melting operation again, be actually and experienced a repetitive process that cooling heats up again.Section needed a large amount of recirculated water (chilled water) to take away heat in producing and planting, and screw rod melting process needs again a large amount of electric power that heat is provided, and this repetitive process has been wasted mass energy, and product energy consumption is higher.And only chip drying one procedure is spun in flow process in section just needs the time of staying of 8～10hr, technological process is long, at the bottom of production efficiency.Moreover the high shear heat of the hot-air of chip drying process and spiral shell melting process all can produce harmful effect to the form and aspect of PBT and molecular weight branch, the stability of POY finished product is bad, and the repeatability of different batches product physical property is poor.
Summary of the invention
The purpose of this utility model is the shortcoming of, long flow path high for the energy consumption existing in PBT section spinning technique, unstable product quality, and the fused mass directly spinning that provide that the long distance of a kind of low sticky melt is carried, the short residence time of liquid-phase tackifying, high sticky melt distributes before spinning manifold is nearby produced the device of PBT elastic filament.
The purpose of this utility model solves by the following technical programs:
A kind of fused mass directly spinning is produced the device of PBT elastic filament, comprise connected successively slurry preparation, esterifier, preshrunk reactor, prepolymer filter, prepolymer cooler and eventually poly-reactor, it is characterized in that the low sticky melt discharging opening that poly-reactor at described end middle part arranges is connected with fondant filter, fondant filter is delivered to liquid-phase tackifying reactor by low sticky melt along utilidor by Melt Pump, and the discharging opening of liquid-phase tackifying reactor is directly connected with the charging aperture of straight spinning equipment by carrier pipe.
On the conveyance conduit at the charging aperture of described liquid-phase tackifying reactor and discharging opening place, be all provided with online Viscosity Monitoring meter.
Temperature in described utilidor is controlled at 220 ℃-250 ℃.
Described liquid-phase tackifying reactor is connected with liquid-phase tackifying vacuum system by pipeline respectively with the gaseous phase outlet of straight spinning equipment.
Described liquid-phase tackifying vacuum system comprises in trapping vapour phase easily the vapour phase condenser of solidifying component and takes in vapour phase not roots blower and the liquid rotary pump of solidifying component away, and the import of roots blower connects 2.5bar essence nitrogen to regulate the vacuum of liquid-phase tackifying vacuum system.
Fused mass directly spinning is produced a method for PBT elastic filament, it is characterized in that described method comprises the following steps:
A, load weighted raw material are put into slurry preparation carry out slurry preparation, after slurry preparation is good, put into esterifier and carry out esterification;
B, then carboxylate is dropped into and in preshrunk reactor, carry out preshrunk reaction, the prepolymer making is delivered to eventually poly-reactor successively after prepolymer filter and prepolymer cooler filter cooling processing;
The low sticky melt Conveying that the low sticky melt discharging opening at c, eventually poly-reactor middle part is 0.5～0.6dl/g by viscosity is delivered to liquid-phase tackifying reactor by low sticky melt along utilidor by Melt Pump after fondant filter filters;
D, low sticky melt be further deliming in liquid-phase tackifying reactor, generating spinning target viscosities is that M ± 0.01dl/g(M is spinning target viscosities central value, can be set as 0.8～1.1dl/g) the sticky melt of height after have gear pump to be directly delivered to straight spinning equipment to carry out spinning, can obtain PBT elastic filament.
It is 0.5～0.7h that temperature in utilidor in described step c is controlled at 225～245 ℃ and the time of delivery of low sticky melt in utilidor.
Liquid-phase tackifying reactor in described steps d is horizontal reactor, and the reaction temperature in liquid-phase tackifying reactor is that 235～255 ℃, the time of staying are that 0.5～1.3h, operating pressure are 0.15～0.20KPa/a.
The input and output material of the liquid-phase tackifying reactor in described steps d all adopts online Viscosity Monitoring meter to carry out Real-Time Monitoring.
Liquid-phase tackifying reactor in described steps d is connected with liquid-phase tackifying vacuum system by pipeline respectively with the gaseous phase outlet of straight spinning equipment, this liquid-phase tackifying vacuum system comprises in trapping vapour phase easily the vapour phase condenser of solidifying component and takes in vapour phase not roots blower and the liquid rotary pump of solidifying component away, and the import of roots blower connects 2.5bar essence nitrogen to regulate the vacuum of liquid-phase tackifying vacuum system.
The utility model has the following advantages compared to existing technology:
The utility model is by carrying out low sticky melt Conveying to the liquid-phase tackifying reactor in eventually poly-reactor directly to deliver to straight spinning equipment (spinning manifold) after tackify, for the energy consumption before straight spinning equipment, will drop to 38% of section spinning process, greatly reduce the energy consumption of product; Simultaneously by spinning material by poly-reactor eventually to the time shorten of straight spinning equipment be section spin below 20%, and straight spinning equipment conversion kind will no longer need polyester section to change the line of production, same polyester slice is changed the line of production also no longer affects straight spinning equipment operation, and two covering device operation flexibilities are all greatly improved.
Accompanying drawing explanation
Accompanying drawing 1 is structural representation of the present utility model.
Wherein: 1-slurry preparation; 2-esterifier; 3-preshrunk reactor; 4-prepolymer filter; 5-prepolymer cooler; 6-eventually poly-reactor; 7-fondant filter; 8-liquid-phase tackifying reactor; 9-straight spinning equipment; 10-liquid-phase tackifying vacuum system.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment, the utility model is further described.
As shown in Figure 1: a kind of fused mass directly spinning is produced the device of PBT elastic filament, comprise connected successively slurry preparation 1, esterifier 2, preshrunk reactor 3, prepolymer filter 4, prepolymer cooler 5 and eventually poly-reactor 6, the low sticky melt discharging opening arranging at eventually poly-reactor 6 middle parts is connected with fondant filter 7 and obtains low sticky melt so that discharging is filtered, fondant filter 7 is delivered to liquid-phase tackifying reactor 8 by low sticky melt along utilidor by Melt Pump, temperature in utilidor is controlled at 220 ℃-250 ℃, the discharging opening of liquid-phase tackifying reactor 8 is directly connected with the charging aperture of straight spinning equipment 9 by carrier pipe, on the conveyance conduit at the charging aperture of liquid-phase tackifying reactor 8 and discharging opening place, being all provided with online Viscosity Monitoring meter controls to realize the tandem of liquid-phase tackifying reactor 8 input and output materials, and liquid-phase tackifying reactor 8 is connected with liquid-phase tackifying vacuum system 10 by pipeline respectively with the gaseous phase outlet of straight spinning equipment 9, be subject to the restriction of spinning building structure, the liquid-phase tackifying vacuum system 10 that is positioned at spinning roof portion adopts that floor spaces are little, compact conformation, investment and the less mechanical vacuum system of operating cost, does not adopt the configuration mode of scraper condenser+jet pump+liquid rotary pump that traditional polyester uses.Because, tradition PET vaccum system relates to BD circulated sprinkling system and power steam system, particularly to involve the vacuum fluid-tight of barometric pipe, in the discrepancy in elevation of equipment, there is rigid requirement in this flow process, be difficult to realize the reasonable Arrangement in spinning building, and the energy consumption of BD circulation and power steam is also higher.Consider that viscosity at liquid-phase tackifying reactor 8 Raw melts and spinning melt rises Δ IV and only has 0.5dl/g left and right, adopt mechanical vacuum system can meet the demands completely.This liquid-phase tackifying vacuum system 10 adopts the preparing mode of vapour phase condenser+roots blower+liquid rotary pump, with vapour phase condenser, substitute most of easily solidifying component in scraper condenser trapping vapour phase, not solidifying component is taken away by roots blower and liquid rotary pump, at inlet of Roots blower, connect 2.5bar essence nitrogen with regulating system vacuum, the collection liquid of vapour phase condenser and liquid rotary pump displacement liquid send into polymeric size configuration-system according to component situation or the BDO system of refining participates in esterification, realize the full reuse of all materials, liquid rotary pump tail gas access polymerization exhaust system, after processing, send hot Media Oven to burn, realize zero-emission.
Fused mass directly spinning is produced a method for PBT elastic filament, and the method comprises the following steps: a, load weighted raw material are put into slurry preparation 1 carry out slurry preparation, put into esterifier 2 and carry out esterification after slurry preparation is good; B, then carboxylate is dropped into and in preshrunk reactor 3, carry out preshrunk reaction, the prepolymer making is delivered to eventually poly-reactor 6 successively after prepolymer filter 4 and prepolymer cooler 5 filter cooling processing; C, the low sticky melt Conveying that eventually the low sticky melt discharging opening at poly-reactor 6 middle parts is 0.5～0.6dl/g by viscosity are delivered to liquid-phase tackifying reactor 8 by low sticky melt along utilidor by Melt Pump after fondant filter 7 filters, and it is 0.5～0.7h that the temperature in utilidor is controlled at 225～245 ℃ and the time of delivery of low sticky melt in utilidor; D, liquid-phase tackifying reactor 8 are horizontal reactor, and the reaction temperature in liquid-phase tackifying reactor 8 is that 235～255 ℃, the time of staying are that 0.5～1.3h, operating pressure are 0.15～0.20KPa/a, low sticky melt is further deliming in liquid-phase tackifying reactor 8, generating spinning target viscosities is that M ± 0.01dl/g(M is spinning target viscosities central value, can be set as 0.8～1.1dl/g) the sticky melt of height after have gear pump to be directly delivered to straight spinning equipment 9 to carry out spinning, can obtain PBT elastic filament.The input and output material of liquid-phase tackifying reactor 8 all adopts online Viscosity Monitoring meter to carry out Real-Time Monitoring in addition; And liquid-phase tackifying reactor 8 is connected with liquid-phase tackifying vacuum system 10 by pipeline respectively with the gaseous phase outlet of straight spinning equipment 9, this liquid-phase tackifying vacuum system 10 comprises in trapping vapour phase easily the vapour phase condenser of solidifying component and takes in vapour phase not roots blower and the liquid rotary pump of solidifying component away, and the import of roots blower connects 2.5bar essence nitrogen to regulate the vacuum of liquid-phase tackifying vacuum system 10.
The utility model increases low sticky melt discharging opening by the correct position at poly-reactor at the end at polymerization technique 6 middle parts, by Melt Pump by the low sticky melt Conveying of the PBT of certain degree of polymerization to the liquid-phase tackifying reactor 8 that is positioned at straight spinning equipment 9 tops, on utilidor before liquid-phase tackifying reactor 8, increase online Viscosity Monitoring, the viscosity of liquid-phase tackifying reactor feedstocks melt is controlled between 0.5～0.6dl/g, viscosity is too high can aggravate the thermal degradation that the long distance of melt is carried, the too low tackifying ability that can surpass liquid-phase tackifying reactor 8, cause the outlet melt of liquid-phase tackifying reactor 8 not reach the required target viscosities requirement of spinning, this viscosity can be by regulating low cohesive end speed of agitator and the vacustat of the eventually poly-reactor 6 of polymerization technique to control, minimum for the thermal degradation in melt Conveying process is down to, the melt Conveying temperature in utilidor is strict controlled within 225～245 ℃, specifically can be by regulating melt jacket pipe heat medium temperature and melt cooling actuator temperature to realize.The low sticky melt of 0.5～0.6dl/g viscosity is further deliming in liquid-phase tackifying reactor 8, generate the higher PBT melt of the degree of polymerization, liquid-phase tackifying reactor 8 is designed to horizontal reactor, and reaction temperature is that 235～255 ℃, the time of staying are that 0.5～1.3h, operating pressure are 0.15～0.20KPa/a; Online Viscosity Monitoring is set after the discharging pump of liquid-phase tackifying reactor 8, take guarantee spinning target viscosities as M ± 0.01dl/g(M be spinning target viscosities central value, can between 0.8～1.1dl/g, set arbitrarily), the vacuum of liquid-phase tackifying reactor 8 and input and output material viscosity realize " tandem " and control on DCS, guarantee for the PBT melt viscosity of spinning steadily, the target melt after tackify is directly sent into straight spinning equipment 9 by gear pump and is carried out spinning.
PBT fused mass directly spinning of the present utility model and PBT section is spun and is compared, and greatly reduces the energy consumption of product, and following table is that the energy consumption comparison with fused mass directly spinning is spun in PBT section:
As can be seen from the above table, adopt PBT fused mass directly spinning can make power consumption decline 160Kw/t, recirculated water consumption decline 10m
3/ t(internal circulating load), technique is pressed the empty decline 220Nm that consumes
3/ t, demineralized water consumption decline 150Kg/t, but because the heating of liquid-phase tackifying reactor 8 and melt pipeline need to increase coal consumption 10Kg/t.If all energy consumption kinds are converted to standard coal (recirculated water and demineralized water calculate by coefficient of equivalent), adopt after PBT fused mass directly spinning, for the energy consumption before spinning manifold, will drop to 38% of section spinning process.
Adopt in addition PBT section to spin, from melt pelletizing → section conveying → pre-crystallized → chip drying → screw rod melting, at least need the time of staying more than 10hr.And adopt PBT fused mass directly spinning technique, the time of staying of melt Conveying to be about 0.5～0.7h (wherein, high sticky melt is at not enough 5min of the ducted time of staying), and the time of staying of liquid-phase tackifying reactor 8 is 0.5～1.3h approximately, and technological process is shortened greatly.Adopt after PBT fused mass directly spinning technique, device for spinning conversion kind will no longer need polyester section to change the line of production simultaneously, and same polyester slice is changed the line of production also no longer affects device for spinning operation, and two covering device operation flexibilities are all greatly improved.
Above embodiment is only explanation technological thought of the present utility model, can not limit protection domain of the present utility model with this, every technological thought according to the utility model proposes, any change of doing on technical scheme basis, within all falling into the utility model protection domain; The technology that the utility model does not relate to all can be realized by prior art.
Claims (5)
1. a fused mass directly spinning is produced the device of PBT elastic filament, comprise connected successively slurry preparation (1), esterifier (2), preshrunk reactor (3), prepolymer filter (4), prepolymer cooler (5) and eventually poly-reactor (6), it is characterized in that the low sticky melt discharging opening that poly-reactor (6) at described end middle part arranges is connected with fondant filter (7), fondant filter (7) is delivered to liquid-phase tackifying reactor (8) by low sticky melt along utilidor by Melt Pump, the discharging opening of liquid-phase tackifying reactor (8) is directly connected with the charging aperture of straight spinning equipment (9) by carrier pipe.
2. fused mass directly spinning according to claim 1 is produced the device of PBT elastic filament, it is characterized in that being all provided with online Viscosity Monitoring meter on the charging aperture of described liquid-phase tackifying reactor (8) and the conveyance conduit at discharging opening place.
3. fused mass directly spinning according to claim 1 is produced the device of PBT elastic filament, it is characterized in that the temperature in described utilidor is controlled at 220 ℃-250 ℃.
4. fused mass directly spinning according to claim 1 is produced the device of PBT elastic filament, it is characterized in that described liquid-phase tackifying reactor (8) is connected with liquid-phase tackifying vacuum system (10) by pipeline respectively with the gaseous phase outlet of straight spinning equipment (9).
5. fused mass directly spinning according to claim 4 is produced the device of PBT elastic filament, it is characterized in that vapour phase condenser that described liquid-phase tackifying vacuum system (10) comprises easily solidifying component in trapping vapour phase and take in vapour phase not roots blower and the liquid rotary pump of solidifying component away, the import of roots blower connects 2.5bar essence nitrogen to regulate the vacuum of liquid-phase tackifying vacuum system (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420100072.9U CN203820962U (en) | 2014-03-06 | 2014-03-06 | Device for melt direct spinning production of PBT (polybutylece terephthalate) elastic filament |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420100072.9U CN203820962U (en) | 2014-03-06 | 2014-03-06 | Device for melt direct spinning production of PBT (polybutylece terephthalate) elastic filament |
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| CN203820962U true CN203820962U (en) | 2014-09-10 |
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| CN201420100072.9U Expired - Fee Related CN203820962U (en) | 2014-03-06 | 2014-03-06 | Device for melt direct spinning production of PBT (polybutylece terephthalate) elastic filament |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105671646A (en) * | 2014-11-19 | 2016-06-15 | 无锡市兴盛新材料科技有限公司 | Improved liquid-phase tackifying vacuum system |
-
2014
- 2014-03-06 CN CN201420100072.9U patent/CN203820962U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105671646A (en) * | 2014-11-19 | 2016-06-15 | 无锡市兴盛新材料科技有限公司 | Improved liquid-phase tackifying vacuum system |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140910 Termination date: 20170306 |