CN206646195U - The packaged type melt spinning machine of cold, heat and electricity triple supply - Google Patents
The packaged type melt spinning machine of cold, heat and electricity triple supply Download PDFInfo
- Publication number
- CN206646195U CN206646195U CN201720161577.XU CN201720161577U CN206646195U CN 206646195 U CN206646195 U CN 206646195U CN 201720161577 U CN201720161577 U CN 201720161577U CN 206646195 U CN206646195 U CN 206646195U
- Authority
- CN
- China
- Prior art keywords
- melt spinning
- temperature
- spinning machine
- heat
- packaged type
- 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
Links
Classifications
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
- Y02P70/62—Manufacturing or production processes characterised by the final manufactured product related technologies for production or treatment of textile or flexible materials or products thereof, including footwear
Landscapes
- Fuel Cell (AREA)
Abstract
It the utility model is related to processing of high molecular material technical field, more particularly to the packaged type melt spinning machine of cold, heat and electricity triple supply, its structure includes the screw extruder set gradually, manifold, cooling chamber and collecting chamber, also include methanol-water preparing hydrogen, generating power system, the system includes methanol-water storage container, delivery pump, reformer, separation chamber, fuel cell and control device, packaged type melt spinning machine is provided with high-temperature gas loop and refrigerating circuit, high-temperature gas collection device is provided with high-temperature gas loop, the high temperature residual air that high-temperature gas in high-temperature gas collection device is isolated from separation chamber.The utility model makes full use of caused heat energy and electric energy in methanol-water reformation hydrogen production and power generation process, and it is combined with conventional melt spinning-drawing machine, by intelligentized cold, heat and electricity three-way control to realize the efficient utilization of the energy, and power supply mode of the tradition by external power supply power supply is changed, melt spinning machine is turned into Portable mobile equipment.
Description
Technical field
It the utility model is related to processing of high molecular material technical field, and in particular to a kind of cold, heat and electricity triple supply may move
Formula melt spinning machine.
Background technology
Melt spinning machine is to heat polymer to melt, and is extruded by spinneret orifice, cooling and solidifying forms fiber in atmosphere
Process equipment.In the prior art, melt spinning owner will include screw extruder, manifold, for melt cooling solidification
Cooling chamber, coiler device and heater and cooling device.During work, polymer is heated through screw extruder and melted, then
Melt is extruded into manifold and by spinneret, after melt enters cooling chamber cooling and solidifying, then is wound by coiler device
Spinning.Wherein, temperature is the major influence factors of melt spinning, and screw extruder and manifold are required to heating and obtain melt institute
The high temperature (about 180~280 DEG C) needed, need to be passed through cold wind in cooling chamber and maintain low temperature (about 20~35 needed for curing molding
℃).In the prior art, one mainly uses electric heater to the mode that screw extruder and manifold heat, most common
It is powerful resistance heater, its drawback is：Because the temperature needed for melt is up to more than 200 degree, it fully relies on outer
Connect power supply, cause that power consumption is big, cost is high, and Resistant heating reach predetermined temperature it is time-consuming it is longer, efficiency is low, heating not
Uniformly；Furthermore resistance wire is fragile, service life is short；Secondly the mode of cooling and solidifying mainly adopts air conditioner refrigerating or water cooling, together
The mode of sample air conditioner refrigerating or water cooling can produce extra energy consumption.And it is difficult to carry out energy-conservation to change on heat energy and electric energy at present
Make, energy-conservation truly and environmental protection can not be realized.In addition, according to intrinsic design, the transmission of existing melt spinning machine
The device that device and other needs are powered, can only fully rely on external power supply, not only cause the power consumption of whole equipment huge
Greatly, and external power supply must use in fixed venue, and therefore, the removable convenience of existing melt spinning machine receives greatly
Limit.
With the development of new energy technology, it is developed gradually using the technology of first alcohol and water reformation hydrogen production, it can be reduced
Energy consumption in Chemical Manufacture and reduce cost, and be expected to alternative electric energy consumption especially electrolysis hydrogen producing process.Chinese invention
(the applicant of patent 201310340475.0：Shanghai Hejide Dynamic Hydrogen Machine Co., Ltd.) disclose a kind of methanol-water hydrogen manufacturing system
System, methanol and vapor at a temperature of 350-570 DEG C, under 1-5MPa pressure condition, are being catalyzed in the reformer chamber of reformer
In the presence of agent, methanol decomposition reaction and the transformationreation of carbon monoxide occurs, generates hydrogen and carbon dioxide, this is more than one
Component, the gas solid catalytic reaction system reacted more.Reactional equation is as follows：(1)CH3OH→CO+2H2；(2)H2O+CO →CO2+H2；
(3)CH3OH+H2O→CO2+3H2, the H of reforming reaction generation2And CO2, then by separation chamber palladium membrane separator by H2And CO2Point
From obtaining high-purity hydrogen.(the applicant of Chinese invention application 201410622203.4：Shanghai, which is closed, must both move the limited public affairs of hydrogen machine
Department), a kind of generator and its electricity-generating method based on Methanol water hydrogen production system are disclosed, the generator uses fuel cell conduct
Generating equipment, the high-purity hydrogen that above-mentioned Methanol water hydrogen production system obtains are delivered to the fuel cell, hydrogen and the oxygen in air
Generation electrochemical reaction is so as to producing electric energy.In above-mentioned methanol-water hydrogen manufacturing and electricity generation system, the reformation system of methanol and vapor
During hydrogen reacts, due to needing to maintain 350-570 DEG C of temperature, the H of methanol-water reforming reaction generation in reformer2And CO2,
After palladium membrane separator isolates hydrogen, remaining CO2And unreacted steam is discharged from system, these are discharged remaining
Gas has very high heat, its temperature is generally between 300-600 DEG C, if be directly emitted, serious waste is big
The heat energy of amount, make methanol-water raw material availability relatively low.
Therefore, how using methanol-water preparing hydrogen, generating power technology the characteristics of, and apply it to traditional melt spinning machine with
Realize to conventional melt spinning-drawing machine in high energy consumption, be completely dependent on external power supply, using the improvement limited by place etc., will be
Break through the new research direction of intrinsic thinking.
The content of the invention
Above-mentioned technical problem be present for prior art, the purpose of this utility model is to provide a kind of cold, heat and electricity triple supply
Packaged type melt spinning machine, it is realized molten using caused heat energy and electric energy in methanol-water reformation hydrogen production and power generation process
The hot cold electric trilogy supply of body spinning-drawing machine and the Intelligentized regulating and controlling of temperature and humidity, realize energy-conserving and environment-protective, and independent of tradition
External power supply, turn into Portable mobile equipment.
To achieve the above object, the utility model provides following technical scheme：
There is provided cold, heat and electricity triple supply packaged type melt spinning machine, including set gradually screw extruder, manifold,
Cooling chamber and collecting chamber, wherein：The screw extruder includes machine barrel and screw rod, is provided with spinneret in the manifold, institute
State and coiler device is provided with collecting chamber, the packaged type melt spinning machine also includes methanol-water preparing hydrogen, generating power system, described
Methanol-water preparing hydrogen, generating power system includes methanol-water storage container, delivery pump, reformer, fuel cell and control device, described heavy
Whole device includes reformer chamber, separation chamber and the electric heater for reformer chamber heating, and methanol-water raw material is delivered to reformation through delivery pump
The reformation hydrogen production reaction of first alcohol and water occurs in reformer for device, first alcohol and water, is made mixed based on carbon dioxide and hydrogen
Gas is closed, the mixed gas isolates hydrogen and high temperature residual air through separation chamber, and the hydrogen is delivered to fuel cell and produces electric energy, and one
Part electric energy is delivery pump and the electric heater power supply of methanol-water preparing hydrogen, generating power system, and a part of electric energy is its of melt spinning machine
His power supply for electrical equipment；Fuel cell discharges Cryogenic air during producing electric energy；The control device include control mainboard,
Electric supply installation and electric power output port, the control mainboard control methanol-water preparing hydrogen, generating power system work, the electric supply installation are
Power itself in methanol-water reformation hydrogen production electricity generation system start-up course, the electric power output port are used for outside output power；
The packaged type melt spinning machine also includes being used to make the air inducing system that the melt cooling in the cooling chamber solidifies
System, the induced draught system include Cryogenic air blender, humidifier and blower unit, wherein：The fuel cell is discharged low
Warm air, outside air, the humidifier are connected by pipeline with the air inlet of the Cryogenic air blender respectively, described low
The gas outlet of warm air blender is connected by compressor with the air inlet of the blower unit, and the blower unit is provided with more
Individual air channel, the side of the cooling chamber are provided with multiple blowing mouths corresponding with the air channel along melt flows directional spreding,
The direction of the air channel and the blowing mouth is each perpendicular to the melt in cooling chamber；
The packaged type melt spinning machine is provided with high-temperature gas loop, and high temperature is provided with the high-temperature gas loop
Gas collector, the high temperature residual air that the high-temperature gas in the high-temperature gas collection device is isolated from the separation chamber,
The temperature of the high temperature residual air is 300~600 DEG C；The high-temperature gas loop includes at least one for adjusting barrel zone temperature
First high-temperature gas loop and the second high-temperature gas loop for adjusting spinning the temperature inside the box；
Be provided with temperature sensor in the machine barrel, the manifold and the cooling chamber, the temperature sensor with
The control device electrical connection.
Wherein, the packaged type melt spinning machine is additionally provided with the refrigerating circuit for cooling down machine barrel, described to freeze back
Cooling device is provided with road.
Wherein, the packaged type melt spinning machine includes at least one first heat exchanger, and the refrigerating circuit passes through
At least one first heat exchanger transfers heat to the corresponding high-temperature gas loop.
Wherein, the packaged type melt spinning machine includes second heat exchanger, and the refrigerating circuit passes through described second
Heat exchanger and the Cryogenic air of fuel cell discharge carry out heat exchange.
Wherein, flow control valve, the flow control are provided with the high-temperature gas loop and the refrigerating circuit
Valve electrically connects with the control device.
Wherein, reversal valve is provided with the connecting line between the separation chamber and the high-temperature gas collection device,
In melt spinning machine mixing process, the high temperature residual air that separation chamber isolates enters high-temperature gas collection device through reversal valve；Molten
In body spinning-drawing machine cooling procedure, the high temperature residual air that separation chamber isolates is arranged outwardly through reversal valve.
Wherein, the machine barrel and the manifold are provided with electric heater unit, and the electric heater unit includes electric heating film,
The electric heating film is arranged at the inwall of the machine barrel and the tank surface of the manifold.
Wherein, the Cryogenic air blender is provided with temperature-detecting device and humidity detector, the temperature detection
Device and humidity detector electrically connect with the control device respectively.
Wherein, the electric supply installation is rechargeable battery.
Wherein, heat exchanger is provided with transfer pipeline between the methanol-water storage container and the reformer, low temperature
First alcohol and water raw material carries out heat exchange with the high-temperature hydrogen that separation chamber isolates.
The beneficial effects of the utility model：
Compared with the melt spinning machine of prior art, the utility model has advantages below：
(1) the packaged type melt spinning machine of cold, heat and electricity triple supply of the present utility model, one, reformed and made using methanol-water
300~600 DEG C of high temperature residual air caused by hydrogen and power generation process is used as high temperature heat source after the collection of high-temperature gas collection device,
It is that screw extruder and manifold heat by high-temperature gas loop, there is provided polymer melting, temperature needed for melt is extruded into,
Circulation of the high temperature residual air through high-temperature gas loop and form the stable thermal source of even heat and uniform heat distribution；Secondly, utilize
40~60 DEG C of the Cryogenic air discharged during fuel cell power generation is mixed to form as low-temperature heat source, and with outside air
20~35 DEG C of mixing air provides required temperature when being cooled and solidified for the melt in cooling chamber；Thirdly, in methanol-water
In reformation hydrogen production start-up course, it is not necessary to external power supply is powered, and can be system power itself by the electric supply installation of itself, etc.
Operation of fuel cells produce electric energy after, then for its own system power and be melt spinning machine all power supply for electrical equipment, by
This changes the power supply mode that conventional melt spinning-drawing machine relies on external power supply completely, and realize unrestricted makes in any place
With making melt spinning machine turn into Portable mobile equipment.Therefore, the utility model breaches intrinsic thinking, makes full use of first
Caused high temperature heat, low temperature heat energy and electric energy in alcohol water reformation hydrogen production and power generation process, and by itself and conventional melt spinning-drawing machine
It is combined, realizes cold, heat and electricity triple supply, can be according to the work(of the electrical equipments such as the temperature needed for melt spinning each stage, motor
Methanol usage, caused heat energy and electric energy needed for rate and methanol-water reformation hydrogen production electricity generation system carry out the permanent calculation of energy, lead to
The intelligent cold, heat and electricity three-way control of melt spinning-drawing machine is crossed to realize the efficient utilization of the energy, so as to provide a kind of brand-new section
Can, packaged type open one's minds, it has wide commercial application prospect；
(2) temperature that generation high temperature residual air in hydrogen production process is reset due to methanol-water is up to 300~600 DEG C, this part
Heat energy fully meets the temperature (generally 180~280 DEG C) needed for polymer melting formation melt), on the other hand, fuel cell
The mixing air that 40~60 DEG C of Cryogenic air of discharge is mixed to form with outside air, meets needed for melt curing molding just
Low temperature (about 20~35 DEG C), it is so main that using methanol-water reformation hydrogen production and power generation process, caused waste heat heats in itself
Or cooling melt, the utilization rate of methanol-water raw material is not only improved, and no longer rely on the electrical heating of conventional melt spinning-drawing machine merely
Device, air conditioner refrigerating or water cooling plant are heated or freezed, and thus greatly reduce the electric energy energy consumption of whole equipment, and energy-conservation subtracts
Arrange significant effect；
(3) electric energy of methanol-water reformation hydrogen production electricity generation system of the present utility model output is direct current, therefore melt spinning
The motor used in machine equipment can use direct current generator, and it does not need high-power start, no power waste compared to alternating current generator；
(4) the utility model has important breakthrough in energy-conservation and environmental protection, on the one hand, raw material of the present utility model is methanol
With the mixed liquor of water, low raw-material cost (cost of 1kg methanol is about 2 yuan), the water of discharge and a small amount of carbon dioxide are to environment
It is pollution-free；On the other hand from energy consumption cost, the cost of commercial power is that 1 degree of electricity is about 1 yuan at present, the required heat of 1 degree of electricity
Amount is equivalent to 860kcal；But methanol-water preparing hydrogen, generating power system of the present utility model, the generated energy of 1kg methanol is about 2 degree of electricity,
I.e. required heat is 2*860kcal=1720kcal, and heat caused by methanol there remains 3380kcal equivalent to 5kcal
Heat, that is to say, that except caused 2 degree of electricity can be supplied to melt during methanol-water preparing hydrogen, generating power of the present utility model
Outside the electrical equipment of spinning-drawing machine, the heat energy (temperature is up to 300~600 DEG C) of 3380kcal high-quality and low product can be also produced
The heat energy of matter, the thermal source and low-temperature receiver that this partial heat energy and can is further compensate for heating as melt and cooling is required use, according to
The mode of hot and cold, electric trilogy supply is converted, and is produced the cost of electricity-generating of 1 degree of electricity and is only needed about 0.4 yuan, compared to current industry
Electric cost saves the high cost and energy consumption being more than half, and this has in industry and environmental protection and had very great significance.
Brief description of the drawings
Fig. 1 is the structural representation of the packaged type melt spinning machine of cold, heat and electricity triple supply of the present utility model.
Reference：
Screw extruder 1, machine barrel 11, screw rod 12, manifold 2, spinneret 21, cooling chamber 3, collecting chamber 4, coiler device
41；
Methanol-water preparing hydrogen, generating power system 5, methanol-water storage container 51, delivery pump 52, reformer 53, reformer chamber 531, electricity add
Hot device 532, separation chamber 533, fuel cell 54, heat exchanger 55, control device 56；
High-temperature gas collection device 6, cooling device 7, reversal valve 8；
Induced draught system 9, Cryogenic air blender 91, humidifier 92, blower unit 93, air channel 931, compressor 94；
First high-temperature gas loop 10a, the second high-temperature gas loop 10, refrigerating circuit 20, first heat exchanger 40, second
Heat exchanger 50, first flow control valve 60, second flow control valve 70, the 3rd flow control valve 80, valve 90.
Embodiment
The utility model is described in detail below in conjunction with specific embodiment and accompanying drawing.
The packaged type melt spinning machine of cold, heat and electricity triple supply, as shown in figure 1, including set gradually screw extruder 1,
Manifold 2, cooling chamber 3 and collecting chamber 4, wherein：Screw extruder includes machine barrel 11 and screw rod 12, and spray is provided with manifold 2
Filament plate 21, coiler device 41 is provided with collecting chamber 4.During work, polymer is heated through screw extruder 1 and melted, subsequently into
Manifold 2 is simultaneously extruded into melt by spinneret 21, and melt enters after cooling chamber 3 cools and solidifies and enters collecting chamber 4, then by rolling up
Winding apparatus 41 winds spinning.(this part operation principle is identical with the melt spinning machine of prior art).
The packaged type melt spinning machine of cold, heat and electricity triple supply of the present utility model and the melt spinning machine of prior art
Difference is：
The packaged type melt spinning machine of cold, heat and electricity triple supply also includes methanol-water preparing hydrogen, generating power system 5, methanol-water hydrogen manufacturing
Electricity generation system 5 includes methanol-water storage container 51, delivery pump 52, reformer 53, fuel cell 54 and control device 56, reformer
53 include reformer chamber 531, separation chamber 533 and the electric heater 532 heated for reformer chamber 531, the system hydrogen manufacturing and generating
Operation principle is：The mixed material of first alcohol and water is delivered to reformer 53 through delivery pump 52, and electric heater 532 is that reformer 53 carries
For required heat, make first alcohol and water reforming reaction under catalyst action in reformer chamber 531, be made with carbon dioxide and hydrogen
Mixed gas based on gas, the mixed gas isolate hydrogen and high temperature residual air through separation chamber 533, and wherein hydrogen passes through heat exchanger
55 with after the heat exchange of the methanol-water of low temperature, methanol-water evaporation gasification enters reformer 53, and the hydrogen of high temperature is delivered to after cooling
Fuel cell 54 is used to produce electric energy, and a part of electric energy is the delivery pump 52 and electric heater 532 of methanol-water preparing hydrogen, generating power system 5
Power supply, a part of electric energy are all power supply for electrical equipment of melt spinning machine；Fuel cell 54 is discharged during producing electric energy
Cryogenic air.Above-mentioned methanol-water preparing hydrogen, generating power system 5 constantly cyclically produces high temperature residual air, Cryogenic air and output electric energy, from
And the cold, heat and electricity triple supply of melt spinning machine is realized, it is specific as follows：
(1) power：
Control device 56 includes control mainboard, electric supply installation and electric power output port, wherein：Control mainboard controls methanol-water
Preparing hydrogen, generating power system 5 works, and electric supply installation can be rechargeable battery, in the start-up course of methanol-water reformation hydrogen production electricity generation system
In, rechargeable battery be power itself (mainly powered for electric heater 532, with into reformer 53 provide reformation hydrogen production it is anti-
Answer required heat), so as to quickly start reformer 53, make first alcohol and water reforming reaction hydrogen manufacturing.Electric power output port be used for
Outer output power.In above-mentioned methanol-water reformation hydrogen production start-up course, it is not necessary to which external power supply is powered, and is filled by the power supply of itself
It can be system power itself to put, and after waiting the work of fuel cell 54 to produce electric energy, then for its own system power supply and be that melt is spun
All electrical equipments (such as screw extruder 1, the power-equipment of coiler device 41) power supply of silk machine, so as to change biography completely
The melt spinning machine of uniting relies on the power supply mode of external power supply, unrestricted can be used in any place, make melt spinning machine into
For the equipment of Portable mobile.
(2) UTILIZATION OF VESIDUAL HEAT IN of Cryogenic air：
Packaged type melt spinning machine also includes being used to make the induced draught system 9 that the melt cooling in cooling chamber 3 solidifies, air inducing
System 9 includes Cryogenic air blender 91, humidifier 92 and blower unit 93, wherein：The Cryogenic air of the discharge of fuel cell 54,
Outside air and humidifier 92 are connected by pipeline with the air inlet of Cryogenic air blender 91 respectively, Cryogenic air blender
91 gas outlet is connected by compressor 94 with the air inlet of blower unit 93, and blower unit 93 is provided with multiple air channels 931,
The side of cooling chamber 3 is provided with multiple blowing mouths corresponding with air channel 931 along melt flows directional spreding.The induced draught system 9
40~60 DEG C of the Cryogenic air by the use of the discharge of the power generation process of fuel cell 54 mixes shape as low-temperature heat source, and with outside air
It is delivered into 20~35 DEG C of mixing airs in the air channel 931 of blower unit 93, subsequently into making high-temperature fusant cold in cooling chamber 3
But solidify.The melt being each perpendicular to due to the direction in air channel 931 and the blowing mouth of cooling chamber 3 in cooling chamber 3, can effectively improve spinning
The quality of silk.Humidifier 92 is used for the humidity for adjusting mixing air in Cryogenic air blender 91.Cryogenic air blender 91 is set
Temperature-detecting device and humidity detector are equipped with, temperature-detecting device and humidity detector are electrically connected with control device respectively
Connect, intelligent temperature and humidity in cooling chamber 3 can be regulated and controled.
(3) UTILIZATION OF VESIDUAL HEAT IN of high temperature residual air：
Packaged type melt spinning machine is provided with high-temperature gas loop, and high-temperature gas loop includes being used to adjust machine barrel 11 not
The second high-temperature gas loop with two the first high-temperature gas loop 10a of regional temperature and for adjusting temperature in manifold 2
10, be provided with high-temperature gas collection device 6 in high-temperature gas loop, the high-temperature gas in high-temperature gas collection device 6 from point
The high temperature residual air isolated from room 533, the temperature of high temperature residual air is 300~600 DEG C.High temperature residual air is followed through high-temperature gas loop
Ring and form the stable thermal source of even heat, so as to quickly be heated to machine barrel 11 and manifold 2.Because the temperature of high temperature residual air reaches
To 300~600 DEG C, this part high-quality heat energy is fully able to meet the heating-up temperature (generally 180~280 needed for melt
DEG C), caused waste heat in methanol-water reformation hydrogen production and power generation process is so not only taken full advantage of, improves the profit of methanol-water raw material
With rate, and no longer heated by the electric heater unit of conventional melt spinning-drawing machine merely, thus greatly reduce the electric energy of complete machine
Energy consumption, effects of energy saving and emission reduction are notable.Each high-temperature gas loop is provided with first flow control valve 60, first flow control valve
60 electrically connect with control device 56.Control device 56 adjusts corresponding high-temperature gas loop high temperature by first flow control valve 60
The flow of residual air is to realize the regulation to machine barrel 11 and the heating-up temperature of manifold 2.
Packaged type melt spinning machine be additionally provided with for cool down machine barrel 11 and manifold 2 refrigerating circuit 20 (Fig. 1 with
Exemplified by machine barrel 11, the refrigerating circuit 20 for cooling down machine barrel 11 is only depicted, the refrigerating circuit 20 for cooling down manifold 2 is not drawn
Go out).Cooling device 7 is provided with refrigerating circuit 20.The 3rd flow control valve 80, the 3rd flow control are also set up in refrigerating circuit 20
Valve 80 processed electrically connects with control device 56.When machine barrel 11 or manifold 2 need cooling, cooling device 7 by freezing accordingly
Loop 20 conveys cooling medium so that machine barrel 11 and manifold 2 cool rapidly.
Packaged type melt spinning machine includes two first heat exchangers 40, and it is separately positioned on corresponding first High Temperature Gas
On body loop 10a return line.Refrigerating circuit 20 transfers heat to corresponding first high temperature by first heat exchanger 40
Gas return path 10a.During this is due to polymer melting, heats required temperature and be generally 180~280 DEG C, and more than high temperature
The heat of gas is up to 300~600 DEG C, to prevent the rising of the temperature of machine barrel 11 and manifold 2 is too fast from exceeding required heating temperature
Degree, now refrigerating circuit 20 can be made to carry out heat exchange with high-temperature gas loop, to adjust respectively by first heat exchanger 40
The temperature of machine barrel 11 and manifold 2.In Fig. 1, towards the pipeline of each first heat exchanger 40 on be provided with second flow control
Valve 70 processed, for controlling the high-temperature gas flow by first heat exchanger 40, so as to adjust corresponding high-temperature gas loop and system
Heat transfer between cold loop 20.Meanwhile controllable valve 90 is provided with each refrigerating circuit 20, for controlling cooling medium
Towards the path of first heat exchanger 40 or the manifold 2 of machine barrel 11/.When in heating process, it is necessary to adjust certain by cooling medium
During the temperature in individual high-temperature gas loop, then valve 90 leads to the path opening in the direction of first heat exchanger 40；When heating terminate and
When being cooled down, then valve 90 leads to the path closing of first heat exchanger 40, and valve 90 leads to the road of the manifold 2 of machine barrel 11/
Footpath is opened, and cooling medium cools to the manifold 2 of machine barrel 11/.
Reversal valve 8 is provided with connecting line between separation chamber 533 and high-temperature gas collection device 6, works as melt spinning
When machine works, the high temperature residual air that separation chamber 533 isolates enters high-temperature gas collection device 6 through reversal valve 8, and then passes through high temperature
Gas return path is heated to machine barrel 11 and manifold 2；When melt spinning machine is stopped, more than the high temperature that separation chamber 533 isolates
Through the row of reversal valve 8 outwardly, cooling device 7 conveys cooling medium so that machine barrel 11 and manifold 2 are fast to gas by refrigerating circuit 20
Prompt drop temperature.
In the present embodiment, packaged type melt spinning machine also includes second heat exchanger 50, and refrigerating circuit 20 passes through second
Heat exchanger 50 carries out heat exchange with the Cryogenic air that fuel cell 54 is discharged.When mixing air in Cryogenic air blender 91
When temperature is too high, the temperature that mixing air can be adjusted by second heat exchanger 50 is maintained at the required temperature of melt cooling solidification
20~35 DEG C.
In the present embodiment, temperature sensor, temperature sensor and control are provided with machine barrel 11, manifold 2 and cooling chamber 3
Device 56 processed electrically connects.Control device 56 controls first according to the feedback signal of each temperature sensor and temperature-detecting device
Flow control valve 60, the flow control valve 80 of second flow control valve 70 and the 3rd are with realization to machine barrel 11, manifold 2 and cooling chamber
The Intelligentized regulating and controlling of 3 temperature.
Intelligentized hot and cold, electric three joint control of packaged type melt spinning machine can be achieved in work above.In addition, melt is spun
Silk machine adjusts the heating-up temperature of machine barrel 11 and manifold 2 using caused high temperature residual air in methanol-water reformation hydrogen production power generation process
Although realizing energy-conservation, it is difficult to accurately control by Thermoregulation temperature merely, is machine barrel 11 in this present embodiment
Electric heater unit is additionally provided with manifold 2, electric heater unit electrically connects with power output end, i.e., electric heater unit is also by fuel
The electric energy power supply that battery 54 exports, it is not necessary to external power supply.Specifically, electric heater unit uses electric heating film, the electric heating film
It is arranged at the inwall of machine barrel 11 and the tank surface of manifold 2.The electric heating film of the preferred silicon carbide material of electric heating film, due to electricity
Heating film has the advantages of high temperature resistant, energy-conservation, fast heat transfer rate, is easy to precise control of temperature.For example, the temperature needed for melt heating
Spend for 250 DEG C, during work, first with heat energy caused by itself during methanol-water reformation hydrogen production to machine barrel 11 and manifold 2 plus
Heat, when the temperature of the two reaches 200 DEG C of basal temperature, restart electric heating film and continue to heat to machine barrel 11 and manifold 2
To 250 DEG C and then realize accurate control to temperature.Therefore, melt spinning machine-to-machine cylinder 11 of the present utility model and manifold 2
Temperature control can also realize thermoelectricity joint control, according to the requirement of material technology to be processed, can arbitrarily select machine barrel 11 and spin
The temperature adjusting mode of silk case 2 and the accuracy of regulation and control.
Compared with prior art, the utility model breaches intrinsic thinking, makes full use of methanol-water reformation hydrogen production to generate electricity
Caused heat energy and electric energy in journey, and it is combined with conventional melt spinning-drawing machine, it is intelligentized cold and hot by melt spinning machine
Electric three joint controls are to realize the efficient utilization of the energy.Therefore, the utility model provides a kind of brand-new energy-conservation, the wound of packaged type
New approaches, it has wide commercial application prospect.
Finally it should be noted that above example is only illustrating the technical solution of the utility model, rather than to this reality
With the limitation of novel protected scope, although being explained with reference to preferred embodiment to the utility model, this area it is general
It is logical it will be appreciated by the skilled person that can be modified to the technical solution of the utility model or equivalent substitution, without departing from this
The spirit and scope of utility model technical scheme.
Claims (10)
1. the packaged type melt spinning machine of cold, heat and electricity triple supply, including set gradually screw extruder, manifold, cooling chamber
And collecting chamber, wherein：The screw extruder includes machine barrel and screw rod, and spinneret, the collection are provided with the manifold
Interior is provided with coiler device, it is characterised in that：The packaged type melt spinning machine also includes methanol-water preparing hydrogen, generating power system,
The methanol-water preparing hydrogen, generating power system includes methanol-water storage container, delivery pump, reformer, fuel cell and control device, institute
Stating reformer includes reformer chamber, separation chamber and the electric heater for reformer chamber heating, and methanol-water raw material is delivered to through delivery pump
The reformation hydrogen production reaction of first alcohol and water occurs in reformer, is made based on carbon dioxide and hydrogen for reformer, first alcohol and water
Mixed gas, the mixed gas isolates hydrogen and high temperature residual air through separation chamber, and the hydrogen is delivered to fuel cell and produces electricity
Can, a part of electric energy is delivery pump and the electric heater power supply of methanol-water preparing hydrogen, generating power system, and a part of electric energy is melt spinning
Other power supply for electrical equipment of machine；Fuel cell discharges Cryogenic air during producing electric energy；The control device includes control
Mainboard, electric supply installation and electric power output port processed, the control mainboard control methanol-water preparing hydrogen, generating power system work, the power supply
Device is power itself in methanol-water reformation hydrogen production electricity generation system start-up course, and the electric power output port is used to outwards export electricity
Power；
The packaged type melt spinning machine also includes being used to make the induced draught system that the melt cooling in the cooling chamber solidifies, institute
Stating induced draught system includes Cryogenic air blender, humidifier and blower unit, wherein：The low temperature of the fuel cell discharge is empty
Gas, outside air, the humidifier are connected by pipeline with the air inlet of the Cryogenic air blender respectively, and the low temperature is empty
The gas outlet of gas blender is connected by compressor with the air inlet of the blower unit, and the blower unit is provided with multiple wind
Road, the side of the cooling chamber is provided with multiple blowing mouths corresponding with the air channel along melt flows directional spreding, described
The direction of air channel and the blowing mouth is each perpendicular to the melt in cooling chamber；
The packaged type melt spinning machine is provided with high-temperature gas loop, and high-temperature gas is provided with the high-temperature gas loop
Collection device, the high temperature residual air that the high-temperature gas in the high-temperature gas collection device is isolated from the separation chamber are described
The temperature of high temperature residual air is 300~600 DEG C；The high-temperature gas loop includes at least one for adjusting the first of barrel zone temperature
High-temperature gas loop and the second high-temperature gas loop for adjusting spinning the temperature inside the box；
Be provided with temperature sensor in the machine barrel, the manifold and the cooling chamber, the temperature sensor with it is described
Control device electrically connects.
2. the packaged type melt spinning machine of cold, heat and electricity triple supply according to claim 1, it is characterised in that：It is described removable
Dynamic formula melt spinning machine is additionally provided with the refrigerating circuit for cooling down machine barrel, and cooling device is provided with the refrigerating circuit.
3. the packaged type melt spinning machine of cold, heat and electricity triple supply according to claim 2, it is characterised in that：It is described removable
Dynamic formula melt spinning machine includes at least one first heat exchanger, and the refrigerating circuit passes through at least one first heat exchange
Device transfers heat to the corresponding high-temperature gas loop.
4. the packaged type melt spinning machine of cold, heat and electricity triple supply according to claim 2, it is characterised in that：It is described removable
Dynamic formula melt spinning machine includes second heat exchanger, and the refrigerating circuit is discharged by the second heat exchanger and fuel cell
Cryogenic air carry out heat exchange.
5. the packaged type melt spinning machine of the cold, heat and electricity triple supply according to Claims 2 or 3 or 4, it is characterised in that：Institute
State and flow control valve is provided with high-temperature gas loop and the refrigerating circuit, the flow control valve and the control device
Electrical connection.
6. the packaged type melt spinning machine of cold, heat and electricity triple supply according to claim 1, it is characterised in that：The separation
Reversal valve is provided with connecting line between room and the high-temperature gas collection device, in melt spinning machine mixing process,
The high temperature residual air that separation chamber isolates enters high-temperature gas collection device through reversal valve；In melt spinning machine cooling procedure, point
Arranged outwardly through reversal valve from the high temperature residual air that room is isolated.
7. the packaged type melt spinning machine of cold, heat and electricity triple supply according to claim 1, it is characterised in that：The machine barrel
The manifold is provided with electric heater unit, the electric heater unit includes electric heating film, and the electric heating film is arranged at institute
State the inwall of machine barrel and the tank surface of the manifold.
8. the packaged type melt spinning machine of cold, heat and electricity triple supply according to claim 1, it is characterised in that：The low temperature
Air mixer is provided with temperature-detecting device and humidity detector, temperature-detecting device and the humidity detector difference
Electrically connected with the control device.
9. the packaged type melt spinning machine of cold, heat and electricity triple supply according to claim 1, it is characterised in that：The power supply
Device is rechargeable battery.
10. the packaged type melt spinning machine of cold, heat and electricity triple supply according to claim 1, it is characterised in that：The first
Heat exchanger, the first alcohol and water raw material of low temperature and separation chamber are provided between alcohol water storage container and the reformer on transfer pipeline
The high-temperature hydrogen isolated carries out heat exchange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720161577.XU CN206646195U (en) | 2017-02-22 | 2017-02-22 | The packaged type melt spinning machine of cold, heat and electricity triple supply |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720161577.XU CN206646195U (en) | 2017-02-22 | 2017-02-22 | The packaged type melt spinning machine of cold, heat and electricity triple supply |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206646195U true CN206646195U (en) | 2017-11-17 |
Family
ID=60280780
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720161577.XU Active CN206646195U (en) | 2017-02-22 | 2017-02-22 | The packaged type melt spinning machine of cold, heat and electricity triple supply |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206646195U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6539802B1 (en) * | 2018-12-21 | 2019-07-03 | 三井化学株式会社 | Cooling system and separation method |
-
2017
- 2017-02-22 CN CN201720161577.XU patent/CN206646195U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6539802B1 (en) * | 2018-12-21 | 2019-07-03 | 三井化学株式会社 | Cooling system and separation method |
| WO2020129255A1 (en) * | 2018-12-21 | 2020-06-25 | 三井化学株式会社 | Cooling system and separation method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105084311B (en) | The methanol-water hydrogen production system employing reforming technology and its application and hydrogen production process of a kind of zero carbon emission | |
| CN106898794B (en) | A kind of electricity-generating method and power generator based on methanol steam reforming system | |
| CN101170187A (en) | A method and device for low-temperature start of the fuel battery | |
| CN109346748A (en) | A kind of fuel cell started quickly at low temperature system and starting method | |
| CN105293432A (en) | Methanol water reforming hydrogen production machine and hydrogen production method thereof | |
| CN115418656A (en) | Skid-mounted hydrogen production, solid-state hydrogen storage and hydrogen fuel cell integrated system and operation method | |
| CN108550877A (en) | A kind of fuel cell pile distribution cold-starting device, system and method | |
| CN109958882A (en) | A kind of water electrolysis hydrogen production and alloy hydrogen storage integrated control system | |
| CN206870240U (en) | The packaged type micro foaming injection moulding machine of cogeneration | |
| CN206646195U (en) | The packaged type melt spinning machine of cold, heat and electricity triple supply | |
| CN113328123A (en) | Fuel cell stack shell purging device and control method | |
| CN204778810U (en) | Methanol -water reformation hydrogen manufacturing machine | |
| CN114105096B (en) | Methanol-water reforming hydrogen production system and hydrogen production method thereof | |
| CN108453994A (en) | The packaged type micro foaming injection moulding machine of cogeneration | |
| CN110875711B (en) | Fuel preparation system and method based on photovoltaic and solid oxide fuel cell | |
| CN108456945A (en) | The packaged type melt spinning machine of cold, heat and electricity triple supply | |
| CN206870318U (en) | The packaged type extruding machine of cogeneration | |
| CN207262996U (en) | One kind is variable to flow to formula solid heat storage device | |
| CN111532688A (en) | Screw feeder and screw heating conveying type thermochemical energy storage system | |
| CN108454044A (en) | The packaged type injection molding machine of cogeneration | |
| CN206870310U (en) | The packaged type injection machine of cogeneration | |
| CN206873202U (en) | Energy-saving mobile three-roller calendar | |
| CN206870350U (en) | The packaged type blow moulding machine of cogeneration | |
| CN102723514B (en) | Solid oxide fuel cells power generating system and methane vapor reforming unit thereof | |
| CN206870171U (en) | The packaged type banbury of cogeneration |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20210918 Granted publication date: 20171117 |