CN206870171U - The packaged type banbury of cogeneration - Google Patents

The packaged type banbury of cogeneration Download PDF

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Publication number
CN206870171U
CN206870171U CN201720161236.2U CN201720161236U CN206870171U CN 206870171 U CN206870171 U CN 206870171U CN 201720161236 U CN201720161236 U CN 201720161236U CN 206870171 U CN206870171 U CN 206870171U
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temperature
banbury
temperature gas
methanol
chamber
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Chinese (zh)
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向华
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Guangdong Hydrogen Energy Science and Technology Co Ltd
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Guangdong Hydrogen Energy Science and Technology Co Ltd
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/22—Component parts, details or accessories; Auxiliary operations
    • B29B7/28—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control
    • B29B7/283—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control measuring data of the driving system, e.g. torque, speed, power
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/22—Component parts, details or accessories; Auxiliary operations
    • B29B7/28—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control
    • B29B7/286—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control measuring properties of the mixture, e.g. temperature, density
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/80—Component parts, details or accessories; Auxiliary operations
    • B29B7/82—Heating or cooling
    • B29B7/823—Temperature control
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/80—Component parts, details or accessories; Auxiliary operations
    • B29B7/82—Heating or cooling
    • B29B7/826—Apparatus therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/18—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/183—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft having a casing closely surrounding the rotors, e.g. of Banbury type
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476—Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7495—Systems, i.e. flow charts or diagrams; Plants for mixing rubber

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Fuel Cell (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

It the utility model is related to processing of high molecular material technical field, more particularly to the packaged type banbury of cogeneration, its structure includes banburying chamber, hydraulic means and turning device, the rotor of two relative revolutions is provided with banburying 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, each rotor and banburying chamber are 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 traditional banbury, by the intelligentized thermoelectricity joint control of banbury to realize the efficient utilization of the energy, and power supply mode of the tradition by external power supply power supply is changed, banbury is turned into Portable mobile equipment.

Description

The packaged type banbury of cogeneration
Technical field
It the utility model is related to processing of high molecular material technical field, and in particular to a kind of packaged type of cogeneration is close Mill.
Background technology
Banbury, also known as masticator, mainly by a pair of given shapes simultaneously with respect to the rotor turned round, in adjustable temperature and pressure Intermittence polymeric material is plasticated and is kneaded under the air-tight state of power.In the prior art, the side to banburying chamber's heating Formula mainly has two kinds, and one kind is that electric heater (mainly resistance heater) heating is set in banburying chamber, another then be Conduction oil or water vapour are passed through, conduction oil and water vapour are then produced by electrical heating.Disadvantage existing for above two mode of heating End is：(1) direct electro heating device heats, and it fully relies on external power supply, and power is big, power consumption is big, and cost is high, and resistance Silk heating reach predetermined temperature it is time-consuming it is longer, efficiency is low, heating is uneven, furthermore, resistance wire is fragile, service life is short；(2) Using conduction oil or the mode of heating of steam, one is needing first to heat conduction oil or heating generation water vapour, this part meeting Extra energy consumption is produced, the second is being difficult to the accurate control of temperature by Thermoregulation banburying room temperature merely.In addition, press According to intrinsic design, at present the transmission device of banbury and other need the device of electricity consumption, external power supply can only be fully relied on, this Cause the power consumption of whole equipment very big a bit, energy-conservation truly and environmental protection can not be realized, especially because outside Connecing power supply must use in fixed venue, and therefore, the removable convenience of existing banbury is significantly limited.
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 water vapour 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 H2With CO2Separation, obtains high-purity hydrogen.(the applicant of Chinese invention application 201410622203.4：It is limited that Shanghai conjunction must both move hydrogen machine Company), a kind of generator and its electricity-generating method based on Methanol water hydrogen production system are disclosed, the generator is made using fuel cell For generating equipment, the high-purity hydrogen that above-mentioned Methanol water hydrogen production system obtains is delivered to the fuel cell, hydrogen and the oxygen in air Electrochemical reaction occurs for gas so as to produce electric energy.In above-mentioned methanol-water hydrogen manufacturing and electricity generation system, the reformation of methanol and water vapour During hydrogen production reaction, due to needing to maintain 350-570 DEG C of temperature, the H of methanol-water reforming reaction generation in reformer2With CO2, after palladium membrane separator isolates hydrogen, remaining CO2And unreacted steam is discharged from system, these discharges Residual air there is very high heat, its temperature is generally between 300-600 DEG C, if be directly emitted, by serious waste Substantial amounts of heat energy, makes the methanol-water raw material availability relatively low.
Therefore, how using methanol-water preparing hydrogen, generating power technology the characteristics of, and traditional banbury is applied it to realize To traditional banbury in high energy consumption, be completely dependent on external power supply, using the improvement limited by place etc., will be break through it is intrinsic The new research direction of thinking.
The content of the invention
Above-mentioned technical problem be present for prior art, what the purpose of this utility model was to provide a kind of cogeneration can Portable banbury, it realizes banbury intelligence using caused heat energy and electric energy in methanol-water reformation hydrogen production and power generation process The thermoelectricity joint control of change, and energy-conserving and environment-protective, independent of traditional external power supply, turn into Portable mobile equipment.
To achieve the above object, the utility model provides following technical scheme：
The packaged type banbury of cogeneration, including support, banburying chamber, the hydraulic pressure dress being arranged above banburying chamber are provided The turning device put, be arranged on the outside of banburying chamber, the rotors of two relative revolutions are provided with banburying chamber, and rotor passes through shaft coupling With motor connection, it is characterised in that：Also include 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, the reformer include reformer chamber, separation chamber and are The electric heater of reformer chamber heating, methanol-water raw material are delivered to reformer through delivery pump, and first occurs in reformer for first alcohol and water The reformation hydrogen production reaction of alcohol and water, is made the mixed gas based on carbon dioxide and hydrogen, the mixed gas is through separation chamber point Hydrogen and high temperature residual air are separated out, the hydrogen is delivered to fuel cell and produces electric energy, and a part of electric energy is methanol-water preparing hydrogen, generating power system Delivery pump and the electric heater power supply of system, a part of electric energy are the power supply for electrical equipment of banbury；
The control device includes control mainboard, electric supply installation and electric power output port, and the control mainboard controls methanol Water preparing hydrogen, generating power system work, the electric supply installation be methanol-water reformation hydrogen production electricity generation system start-up course in power itself, institute State electric power output port and be used for outside output power；The power output end respectively with the motor, the hydraulic means and institute State turning device electrical connection；
The banburying chamber and each rotor are provided with high-temperature gas loop and refrigerating circuit for adjusting heating-up temperature, Wherein：It is provided with high-temperature gas collection device in the high-temperature gas loop, the High Temperature Gas in the high-temperature gas collection device The high temperature residual air that body is isolated from the separation chamber, the temperature of the high temperature residual air is 300~600 DEG C；The high-temperature gas Flow control valve is provided with loop and the refrigerating circuit, the flow control valve electrically connects with the control device；Institute State and cooling device is provided with refrigerating circuit.
Wherein, the banbury also includes heat exchanger, and the refrigerating circuit is by the heat exchanger by heat transfer To the high-temperature gas loop.
Wherein, temperature sensor, the TEMP are provided with the high-temperature gas loop and the refrigerating circuit Device 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 banbury mixing process, the high temperature residual air that separation chamber isolates enters high-temperature gas collection device through reversal valve；In banbury In cooling procedure, the high temperature residual air that separation chamber isolates is arranged outwardly through reversal valve.
Wherein, the banburying chamber and/or the rotor are provided with electric heater unit, the electric heater unit and the electric power Output end electrically connects.
Wherein, the electric heater unit includes electric heating film, the electric heating film be arranged at the banburying chamber inwall and/ Or the surface of the rotor.
Wherein, the banburying chamber and the rotor are provided with temperature-detecting device, the temperature-detecting device with it is described Control device electrically connects.
Wherein, the hydraulic means includes hydraulic pump, the hydraulic jack being connected with hydraulic pump, piston rod and floating weight, institute State hydraulic jack drives floating weight mobile to make material be pressed into banburying chamber by piston rod, the hydraulic pump and the electricity Power output end electrically connects.
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 banbury of prior art, the utility model has advantages below：
(1) the packaged type banbury of cogeneration of the present utility model, methanol-water reformation hydrogen production and hair are on the one hand utilized 300~600 DEG C of high temperature residual air caused by electric process is used as high temperature heat source after the collection of high-temperature gas collection device, passes through height Wet body loop provides temperature needed for refining glue for banburying chamber and rotor heating, 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；On the other hand, in methanol-water reformation hydrogen production start-up course, it is not required to Want external power supply to power, can be system power itself by the electric supply installation of itself, after producing electric energy etc. operation of fuel cells, Be again its own system power supply and be banbury all power supply for electrical equipment, thus change completely traditional banbury rely on it is outer Connect the power supply mode of power supply, realize it is unrestricted any place use, banbury is turned into Portable mobile equipment. Therefore, the utility model breaches intrinsic thinking, make full use of in methanol-water reformation hydrogen production and power generation process caused heat energy and Electric energy, and it is combined with traditional banbury, according to the technique of different materials to be processed, each rotor, banburying during by refining glue The power of the electrical equipment such as the temperature of heating, motor needed for indoor and the methanol needed for methanol-water reformation hydrogen production electricity generation system Dosage, caused heat energy and electric energy carry out that energy is permanent to be calculated, by the complete intelligentized thermoelectricity joint control of banbury to realize the energy Efficiently utilize, so as to provide a kind of brand-new energy-conservation, packaged type is opened one's minds, before it has wide commercial application Scape；
(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 banburying chamber and rotor heats required temperature (generally 100~180 DEG C), so not only takes full advantage of first Caused waste heat in alcohol water reformation hydrogen production and power generation process, improves the utilization rate of methanol-water raw material, and no longer needs tradition close The either extra electric-heating heat-conductive oil of the electric heater unit of mill or water vapour, thus greatly reduce the electric energy energy of whole equipment Consumption, effects of energy saving and emission reduction are notable；
(3) electric energy of methanol-water reformation hydrogen production electricity generation system output of the present utility model is direct current, therefore banbury is set The standby middle motor used 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 3380 kcal equivalent to 5kcal Heat, that is to say, that except caused 2 degree of electricity can be supplied to banburying during methanol-water preparing hydrogen, generating power of the present utility model Outside the electrical equipment of machine, the heat energy (temperature is up to 300~600 DEG C) of 3380kcal high-quality, this partial heat energy can be also produced And can is further compensate for using as the thermal source needed for banburying chamber and rotor heating, and the mode of such cogeneration is converted, Producing the cost of electricity-generating of 1 degree electricity only needs about 0.4 yuan, compared to current commercial power cost savings height be more than half into Sheet and energy consumption, 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 banbury of cogeneration of the present utility model.
Reference：
Banburying chamber 1, rotor 11, hydraulic means 2, turning device 3, motor 4；
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；
First high-temperature gas loop 10a, the second high-temperature gas loop 20a, the first refrigerating circuit 20a, the second refrigerating circuit 20b, first heat exchanger 30, second heat exchanger 40, valve 50, first flow control valve 60, second flow control valve 70, Three flow control valves 80.
Embodiment
The utility model is described in detail below in conjunction with specific embodiment and accompanying drawing.
The packaged type banbury of cogeneration, as shown in figure 1, including support, banburying chamber 1, being arranged in banburying chamber 1 The hydraulic means 2 of side, the turning device 3 for being arranged at the outside of banburying chamber 1, the rotors of two relative revolutions are provided with banburying chamber 1 11, rotor 11 is connected by shaft coupling with motor 4.Hydraulic means 2 includes hydraulic pump, the hydraulic jack being connected with hydraulic pump, work Stopper rod and floating weight, hydraulic jack drive floating weight mobile to make material be pressed into banburying chamber 1 by piston rod.Banbury During work, the rotating speed and speed ratio and the spacing of rotor 11 of two rotors 11 are first adjusted according to material to be processed, passes through hydraulic pressure After mixed material is pressed into banburying chamber 1 by device, material turns round caused shearing force by rotor 11 and carries out refining glue, and refining glue terminates Afterwards, turning device 3 overturns banburying chamber 1, sizing material is drawn off from banburying chamber 1.(the banburying of this part operation principle and prior art Machine is identical).
The difference of the packaged type banbury of cogeneration of the present utility model and the banbury of prior art is：
The packaged type banbury of cogeneration also includes methanol-water preparing hydrogen, generating power system 5, methanol-water preparing hydrogen, generating power system 5 Including methanol-water storage container 51, delivery pump 52, reformer 53, fuel cell 54 and control device 56, reformer 53 includes weight Whole room 531, separation chamber 533 and the electric heater 532 heated for reformer chamber 531, the system hydrogen manufacturing and the operation principle to generate electricity It is：The mixed material of first alcohol and water is delivered to reformer 53 through delivery pump 52, and electric heater 532 is needed for reformer 53 provides Heat, make first alcohol and water reforming reaction under catalyst action in the reformer chamber 531, be made based on carbon dioxide and hydrogen Mixed gas, the mixed gas isolates hydrogen and high temperature residual air through separation chamber 533, wherein hydrogen by heat exchanger 55 with it is low After the methanol-water heat exchange of temperature, methanol-water evaporation gasification enters reformer 53, and the hydrogen of high temperature is delivered to fuel electricity after cooling Pond 54 is used to produce electric energy, and a part of electric energy is powered for the delivery pump 52 and electric heater 532 of methanol-water preparing hydrogen, generating power system 5, A part of electric energy is all electrical equipments (such as power of motor 3, the hydraulic pump of hydraulic means 2 and turning device 3 of banbury Equipment) power supply.Whole system constantly cyclically produces hydrogen, high temperature residual air and output electric energy.
Specifically, control device 56 includes control mainboard, electric supply installation and electric power output port, wherein：Control mainboard control Methanol-water preparing hydrogen, generating power system 5 processed works, and electric supply installation can be rechargeable battery, in methanol-water reformation hydrogen production electricity generation system In start-up course, rechargeable battery is that power itself (is mainly powered, to provide weight into reformer 53 for electric heater 532 Heat needed for whole hydrogen production reaction), so as to quickly start reformer 53, make first alcohol and water reforming reaction hydrogen manufacturing.Power output end Mouth is used for outside 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 passes through itself Electric supply installation can be system power itself, wait fuel cell 54 work produce electric energy after, then for its own system power supply and For all power supply for electrical equipment of banbury, so as to change the power supply mode that traditional banbury relies on external power supply, energy completely It is enough unrestricted to be used in any place, banbury is turned into the equipment of Portable mobile.
Specifically, banburying chamber 1 and each rotor 11 are provided with high-temperature gas loop and system for adjusting heating-up temperature Cold loop.Because the structure of two rotors 11 is identical, in the present embodiment, in Fig. 1 only by taking one of rotor 11 as an example, Depict the high-temperature gas loop of rotor 11 and the schematic diagram of refrigerating circuit.Wherein：High-temperature gas loop includes being arranged at First high-temperature gas loop 10a of the inwall of banburying chamber 1 and the second high-temperature gas loop 20a for being arranged at rotor 11, refrigerating circuit Including being arranged at the first refrigerating circuit 20a of the inwall of banburying chamber 1 and being arranged at the second refrigerating circuit 20b of rotor 11.High Temperature Gas It is provided with high-temperature gas collection device 6 in body loop, the high-temperature gas in high-temperature gas collection device 6 divides from separation chamber 533 The high temperature residual air separated out, the temperature of high temperature residual air is 300~600 DEG C.Circulation of the high temperature residual air through high-temperature gas loop 10 and shape The thermal source stable into even heat, so as to quickly be heated to banburying chamber 1 and rotor 11.Cooling device is provided with refrigerating circuit 7.When banburying chamber 1 or rotor 11 need cooling when, cooling device 7 by corresponding refrigerating circuit convey cooling medium so that Banburying chamber 1 and rotor 11 cool rapidly.Because the temperature of high temperature residual air reaches 300~600 DEG C, this part high-quality heat energy is complete The heating-up temperature (generally 100~180 DEG C) needed for refining glue is disclosure satisfy that, methanol-water is so not only taken full advantage of and reforms system Caused waste heat in hydrogen and power generation process, improves the utilization rate of methanol-water raw material, and no longer needs the electricity of traditional banbury to add The either extra electric-heating heat-conductive oil of thermal or water vapour, thus greatly reduce the electric energy energy consumption of complete machine, energy-saving and emission-reduction effect Fruit is notable.
In the present embodiment, each high-temperature gas loop is provided with first flow control valve 60, first flow control valve 60 Electrically connected with control device 56.Control device 56 is adjusted high in corresponding high-temperature gas loop 10 by first flow control valve 60 The flow of warm residual air is to realize the regulation to the heating-up temperature of different rotor 11.
In the present embodiment, the packaged type banbury of cogeneration also includes first heat exchanger 30 and second heat exchanger 40, first heat exchanger 30 is arranged on the first high-temperature gas loop 10a return line, and second heat exchanger 40 is arranged on On second high-temperature gas loop 10b return line.This is due to be kneaded some plasthetics, heats required temperature and is generally 100~180 DEG C, and the heat of high temperature residual air is up to 300~600 DEG C, to prevent banburying chamber 1 and the temperature of rotor 11 from rising Exceed required heating-up temperature soon, now by heat exchanger refrigerating circuit can be made to carry out hot friendship with high-temperature gas loop Change, to adjust banburying chamber 1 and the temperature needed for rotor 11 respectively.In Fig. 1, towards the pipeline of each heat exchanger on be provided with Second flow control valve 70, for controlling the high-temperature gas flow by heat exchanger, so as to adjust corresponding high-temperature gas loop Heat transfer between refrigerating circuit.Meanwhile controllable valve 50 is provided with each refrigerating circuit, for controlling cooling medium Towards the path of heat exchanger or the rotor 11 of banburying chamber 1/.When in refining glue heating process, it is necessary to adjust high temperature by cooling medium During the temperature of gas return path, then valve 50 leads to the path opening in heat exchanger direction；When refining glue terminates and cooled down, then The path that valve 50 leads to heat exchanger is closed, and valve 50 then leads to rotor 11 and the path of banburying chamber 1 is opened, cooling medium Rotor 11 and banburying chamber 1 are cooled.
Temperature sensor, temperature sensor and control device 56 are provided with each high-temperature gas loop and refrigerating circuit Electrically connect, also set up the 3rd flow control valve 80 in refrigerating circuit, the 3rd flow control valve 80 electrically connects with control device 56.It is close Temperature-detecting device is provided with refining room 1 and rotor 11, temperature-detecting device electrically connects with control device 56, control device 56 First flow control valve 60, second flow control are controlled according to the feedback signal of each temperature sensor and temperature-detecting device The flow control valve 80 of valve 70 and the 3rd is with realization to banburying chamber 1 and the temperature adjustment of each rotor 11.
In the present embodiment, reversal valve 8 is provided with the connecting line between separation chamber 533 and high-temperature gas collection device 6, When banbury works, the high temperature residual air that separation chamber 533 isolates enters high-temperature gas collection device 6, Jin Ertong through reversal valve 8 High Temperature Gas body loop is crossed to heat rotor 11；When banbury is stopped, the high temperature residual air that separation chamber 533 isolates is through commutation Outwardly, cooling device 7 conveys cooling medium so that banburying chamber 1 and rotor 11 cool rapidly to the row of valve 8 by refrigerating circuit.
The intelligentized thermoelectricity joint control of banbury can be achieved in work above.In addition, banbury utilizes methanol-water reformation hydrogen production In power generation process although caused residual air realizes energy-conservation to adjust banburying chamber 1 and the temperature of rotor 11, but relies on heat energy merely Regulation temperature is difficult to accurately control, and is that banburying chamber 1 and/or rotor 11 are additionally provided with electric heater unit in this present embodiment, Electric heater unit is electrically connected with power output end, i.e., electric heater unit is also powered by the electric energy of fuel cell output, it is not necessary to outer Connect power supply.Specifically, electric heater unit uses electric heating film, the electric heating film is arranged at the inwall and/or rotor 11 of banburying chamber 1 Surface.The electric heating film of the preferred silicon carbide material of electric heating film, because electric heating film has high temperature resistant, energy-conservation, heat transfer rate The advantages of fast, it is easy to precise control of temperature.For example, the temperature needed for banbury heating is 120 degree, during work, first with methanol Heat energy caused by itself heats to banburying chamber 1 and rotor 11 during water reformation hydrogen production, when the temperature of the two reaches 90 degree of base During plinth temperature, restart electric heating film and continue that the accurate control to temperature is heated and then realized to banburying chamber 1 and/or rotor 11. Therefore, banbury of the present utility model can also realize thermoelectricity joint control to the temperature control of banburying chamber 1 and rotor 11, according to be added The requirement of work material technology, can in a manner of arbitrarily selecting the temperature adjusting of banburying chamber 1 and rotor 11 and regulation and control accuracy.
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 extruder, by the intelligentized thermoelectricity joint control of banbury with reality The efficient utilization of the existing energy.Therefore, the utility model provides a kind of brand-new energy-conservation, packaged type is opened one's minds, it has There is 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 banbury of cogeneration, including support, banburying chamber, the hydraulic means being arranged above banburying chamber, set The turning device being placed on the outside of banburying chamber, the rotors of two relative revolutions are provided with banburying chamber, and rotor passes through shaft coupling and electricity Machine connects, it is characterised in that：Also include methanol-water preparing hydrogen, generating power system, the methanol-water preparing hydrogen, generating power system is stored up including methanol-water Container, delivery pump, reformer, fuel cell and control device are deposited, the reformer includes reformer chamber, separation chamber and to reform The electric heater of room heating；
The control device includes control mainboard, electric supply installation and electric power output port, and the control mainboard controls methanol-water system Hydrogen electricity generation system work, the electric supply installation be methanol-water reformation hydrogen production electricity generation system start-up course in power itself, the electricity Power output port is used for outside output power；The power output end is respectively with the motor, the hydraulic means and described turning over Rotary device electrically connects；
The banburying chamber and each rotor are provided with high-temperature gas loop and refrigerating circuit for adjusting heating-up temperature, its In：It is provided with high-temperature gas collection device in the high-temperature gas loop, the high-temperature gas in the high-temperature gas collection device The high temperature residual air isolated from the separation chamber, the temperature of the high temperature residual air is 300~600 DEG C；The high-temperature gas returns Flow control valve is provided with road and the refrigerating circuit, the flow control valve electrically connects with the control device；It is described Cooling device is provided with refrigerating circuit.
2. the packaged type banbury of cogeneration according to claim 1, it is characterised in that：The banbury also includes Heat exchanger, the refrigerating circuit transfer heat to the high-temperature gas loop by the heat exchanger.
3. the packaged type banbury of cogeneration according to claim 1 or 2, it is characterised in that：The high-temperature gas Temperature sensor is provided with loop and the refrigerating circuit, the temperature sensor electrically connects with the control device.
4. the packaged type banbury of cogeneration according to claim 1, it is characterised in that：The separation chamber with it is described Reversal valve is provided with connecting line between high-temperature gas collection device, in banbury mixing process, separation chamber isolates High temperature residual air enter high-temperature gas collection device through reversal valve；In banbury cooling procedure, high temperature that separation chamber isolates Residual air is arranged outwardly through reversal valve.
5. the packaged type banbury of cogeneration according to claim 1, it is characterised in that：The banburying chamber and/or The rotor is provided with electric heater unit, and the electric heater unit electrically connects with the power output end.
6. the packaged type banbury of cogeneration according to claim 5, it is characterised in that：The electric heater unit bag Electric heating film is included, the electric heating film is arranged at the inwall of the banburying chamber and/or the surface of the rotor.
7. the packaged type banbury of cogeneration according to claim 1, it is characterised in that：The banburying chamber and described Rotor is provided with temperature-detecting device, and the temperature-detecting device electrically connects with the control device.
8. the packaged type banbury of cogeneration according to claim 1, it is characterised in that：The hydraulic means includes Hydraulic pump, the hydraulic jack being connected with hydraulic pump, piston rod and floating weight, the hydraulic jack drive floating weight by piston rod Move and then material is pressed into banburying chamber, the hydraulic pump electrically connects with the power output end.
9. the packaged type banbury of cogeneration according to claim 1, it is characterised in that：The electric supply installation is can Rechargeable battery.
10. the packaged type banbury of cogeneration according to claim 1, it is characterised in that：The methanol-water storage Heat exchanger is provided between container and the reformer on transfer pipeline, what the first alcohol and water raw material of low temperature and separation chamber isolated High-temperature hydrogen carries out heat exchange.
CN201720161236.2U 2017-02-22 2017-02-22 The packaged type banbury of cogeneration Active CN206870171U (en)

Priority Applications (1)

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CN201720161236.2U CN206870171U (en) 2017-02-22 2017-02-22 The packaged type banbury of cogeneration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720161236.2U CN206870171U (en) 2017-02-22 2017-02-22 The packaged type banbury of cogeneration

Publications (1)

Publication Number Publication Date
CN206870171U true CN206870171U (en) 2018-01-12

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Family Applications (1)

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Country Status (1)

Country Link
CN (1) CN206870171U (en)

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