CN116214880B

CN116214880B - Mechanical device for synchronously producing multi-root-single multicolor tubular objects and modified material particles by adopting multiple feed inlets

Info

Publication number: CN116214880B
Application number: CN202310501247.0A
Authority: CN
Inventors: 谭卓华; 高洪亮; 谭晓露
Original assignee: Guangzhou Lvhui New Material Research Institute Co ltd
Current assignee: Guangzhou Lvhui New Material Research Institute Co ltd
Priority date: 2023-05-06
Filing date: 2023-05-06
Publication date: 2024-02-06
Anticipated expiration: 2043-05-06
Also published as: CN116214880A

Abstract

The invention discloses a mechanical device for synchronously producing a plurality of single multicolor tubular objects and modified material particles by adopting a plurality of feed inlets. Materials with different physical properties enter a specific temperature zone of a first-stage screw extruder from different feed inlets, and enter a second-stage screw extruder and a third-stage screw extruder respectively after mixing, curing modification and melting reaction, wherein the second-stage screw extruder is provided with a multicolor mixing system and a tubular object system to produce a plurality of single multicolor tubular objects, the third-stage screw extruder is provided with a granulating system to produce modified material particles, and the tubular objects and the modified material particles are synchronously produced. The tubular material system and the discharging mould of the granulating system are replaced according to the need, and various tubular materials such as plastic pipes, medical catheters, suction pipes, stirring rods and various modified material particles are produced on a large scale, so that the method is widely applied to the fields of industry, medical use, catering, daily use, various biodegradable modified materials and the like.

Description

Mechanical device for synchronously producing multi-root-single multicolor tubular objects and modified material particles by adopting multiple feed inlets

Technical Field

The invention relates to a mechanical device for synchronously producing a plurality of single multicolor tubular objects and modified material particles by adopting a plurality of feed inlets, belongs to the field of production of tubular objects and particles by adopting an extruder, and in particular relates to a mechanical device for synchronously producing a plurality of single multicolor tubular objects and modified material particles by adopting a plurality of feed inlets.

Background

With the improvement of incomes which can be controlled by people, the life style of people is changing, the consumption scale is further enlarged, the use amount of disposable straws is larger and larger, the market scale of industry is in a trend of increasing, and related matched production equipment does not keep pace with the development of the existing market. According to data display and research, the existing production equipment for straws and tubes in the market currently has the following problems:

(1) The existing production equipment only has one feed inlet, so that the stability of the product cannot be ensured, and the new large-scale preparation cannot be met

The disposable straws in the existing market mainly comprise degradable straws and edible straws, various materials are needed for producing the degradable straws and the edible straws, different materials have different physical and chemical properties, the change and the produced effect at different stages in the extruder also have obvious differences, all materials basically enter the extruder at the same time in the existing production mode of the extruder equipment in the market, and materials with different characteristics enter the extruder at the same time, so that a plurality of uncontrollable factors can appear. The materials needing low-temperature modification and the high-temperature resistant materials are mixed together in a low-temperature area, the high-temperature resistant materials and the low-temperature resistant modified materials are not reacted or changed, but the space and the heat of the low-temperature resistant modified materials are occupied, so that the modification time of the low-temperature resistant modified materials is relatively reduced, the heating area is relatively reduced, the modification process of the low-temperature resistant modified materials is blocked to a certain extent, the low-temperature resistant modified materials cannot be completely modified, and cannot be completely resistant to high temperature, so that the low-temperature resistant modified materials are easy to carbonize after entering the high-temperature area, and finally more defective products are easy to appear; meanwhile, the effect of compatible materials is greatly reduced, the quality instability of products in normal production is caused, the problems of uneven strength, poor heat resistance and the like of tubular products are caused, the stability of the products cannot be ensured, and a new preparation method and scientific research test cannot be met, so that the preparation mode for producing degradable plastic products with stable quality and large scale production is not always available in the current market. Therefore, a special treatment mode is needed to optimize, so that the production raw materials fully play the role in the extruder, and the characteristics of various materials are better kept.

(2) The existing production equipment can only produce a single product, cannot fully exert the performance of the production equipment, has low production efficiency and causes energy waste

The existing disposable straw and tubular object production device has the advantages that the production chain is complete, industrial production is realized, but the existing extruder is basically single production, the straw and tubular object production device is not greatly improved all the time due to various reasons such as economic benefit conflict and difficult technical breakthrough, and finally, the production efficiency is not obviously improved, and the production device cannot be fully utilized

The standby performance causes energy waste.

(3) The existing production equipment can only produce single color or double colors and can not produce multicolor or mixed color

The existing disposable straws and tubes are single-color or double-color, and the disposable straws and tubes with more than two colors have not been found in the market and have not been reported. The existing market is rapidly developed, the production of disposable straws and tubes is not greatly improved, the original production style is still maintained, but the existing production style is quite single, people have visual fatigue, the propaganda attractiveness of related products using the disposable straws and tubes is reduced to a certain extent, the market vitality and prospect are deficient, the existing market demands are not kept up, the consumer view of people is always changed, the market of the disposable straws and tubes also needs to be further improved and adjusted, and the market needs the disposable straws and tubes with more styles and colors.

(4) The existing tubular product production equipment or material particle production equipment can only singly produce tubular products or singly produce material particles, and two sets of production equipment are needed for producing the tubular products and the material particles, so that not only are manpower, financial resources and energy resources wasted, but also the space is occupied

In the preparation method for producing the tubular objects, the raw materials for producing the tubular objects and the straw basically need material particles, and the tubular objects and the straw can also serve as the material particles to a certain extent, so that the tubular objects and the material particles complement each other, mutually symbiotic and mutually used. In the case of only the production equipment of the tubular objects, if the production equipment is needed, new production equipment is needed, in the case of only the production equipment of the material particles, if the production equipment is needed, new production equipment is also needed, and the new production equipment is added, more using sites, energy consumption, labor cost and the like are increased, so that certain investment repetition and cost superposition are caused, and the problems of high energy consumption, high carbon emission and the like are also caused.

(5) The existing tubular product production equipment or material particle production equipment has the defects that the temperature of a tubular product extruded from a discharge die is high, the tubular product is in a molten state, quick cooling and shaping are needed, otherwise, the phenomenon of shape deformation and adhesion can occur, normal production can be influenced, in addition, the mechanical property of a tubular product is greatly improved by quick cooling, and the packaging and selling can be carried out after cooling is needed, so that the cooling is needed. The traditional cooling equipment is mostly cooled and cooled by adding fans to a conveyor due to market influence and technical limitation and utilizes the fans to cool. But the cooling time of the fan is longer, the cooling effect is worse, the requirement of conveying equipment is longer, the occupied area is larger, the waste of large space resources is caused, the requirements on the occupied area of equipment, the number of personnel and comprehensive energy consumption are larger, the problems of high energy consumption, high carbon emission and the like are also caused, and the industrial production requirements of the existing market are not met.

The biodegradable material is a feasible and effective way for solving the problems of environmental pollution caused by plastic wastes and relieving the shortage of petroleum resources. The biodegradable material is mainly prepared by synthesizing biodegradable polymers such as thermoplastic starch plastics, polylactic acid and the like through an extruder. With the issuance of new edition of plastic limiting command, china is expected to become the global maximum biodegradable plastic consumer market in recent years. And the production equipment is behind, so that the preparation method of the degradation particles is limited to a certain extent. All materials enter the extruder at the same time in the existing production mode of extruder equipment in the market basically, but materials with different characteristics enter the extruder at the same time, so that a plurality of uncontrollable factors can appear, the phenomenon is particularly obvious when material particles are produced, the low-temperature materials and the high-temperature materials are mixed and do not react and change in a low-temperature region at the same time, but occupy the space and heat of the low-temperature materials, so that the modification time of the low-temperature materials is relatively reduced, the heated area is relatively reduced, the low-temperature materials are not completely modified, unstable quality easily appears, the particle strength is uneven, and the physical property is caused

The problems of unstable performance and the like are solved, and therefore, the material characteristics are required to be fully exerted and maintained as in the production device of the tubular product.

The advantages and disadvantages of the existing production equipment are shown in table 1:

in summary, the existing production equipment only has one feed inlet, materials can only enter the extruder once, the characteristics of different materials cannot be fully utilized, and the problems of uneven product strength, unstable physical properties and the like are easy to occur; during production, only a single tube can be produced, the production capacity of an extruder is limited, and single production can only produce single-color or double-color tubes, and multi-color or mixed-color tubes cannot be produced, so that the production style is single, and the market propaganda attractiveness is lacking.

In the preparation method for producing the tubular objects, the production raw materials basically need material particles, the tubular objects can also serve as the material particles to a certain extent, so that the tubular objects and the material particles complement each other and mutually form symbiosis, a plurality of conditions of simultaneously producing the tubular objects and the material particles are required in the existing market, and the existing equipment can only singly produce the tubular objects or singly produce the material particles and cannot meet the existing market demands.

Disclosure of Invention

In order to overcome the defects of the prior production device, the invention provides a mechanical device for synchronously producing a plurality of single multi-color tubular objects and material particles by adopting a plurality of feeding ports, so that different materials are fed simultaneously at different feeding ports, and a plurality of single multi-color tubular objects and modified material particles are synchronously produced.

In order to achieve the above purpose, the technical scheme adopted by the invention is as follows:

a mechanical device for synchronously producing a plurality of single multicolor tubular objects and modified material particles by adopting a plurality of feed inlets comprises a drying module, a feed inlet module, a screw extruder combination module, a multicolor mixing system, a tubular object system and a granulating system; the process comprises the following steps: the method comprises the steps of carrying out screw pushing reaction on low-temperature materials through a screw forced feeding device I of a buffer bin I, drying at 60 ℃ for 5min in a vacuum drying chamber, stirring and conveying, carrying out screw pushing reaction through a screw forced feeding device II of a first feeding port of a feeding port module, mixing the materials with modified materials injected through a plunger type high-precision metering pump I at high pressure in a second feeding port of the feeding port module, mixing the materials with compatible materials injected through a plunger type high-precision metering pump II at high pressure in a third feeding port of the feeding port module, carrying out compatible modification at 70-100 ℃, exhausting, mixing the materials with high-temperature materials of a screw forced feeding device III of a fourth feeding port of the feeding port module, curing at 130-230 ℃, extruding the materials to two synchronously working secondary screw extruders and three-stage screw extruders through a primary screw extruder, and synchronously producing a plurality of multi-color tubular objects and modified material particles; wherein:

(1) The two-stage screw extruder is provided with a multicolor mixing system and a tube system, and the flow is as follows: the curing material is vacuumized in a molten state, flows through a diversion system of a multicolor mixing system, a color injection machine barrel, a mixing machine barrel, a diversion system, a first mixed material, a second mixed material and a third mixed material, enters a first material tank, a second material tank and a third material tank, passes through a tubular material channel, is subjected to cross fusion reaction, is subjected to extrusion of a tubular material, is subjected to shaping sleeve of an antistatic annular cooling ring, is subjected to traction, rotary cutting, sterilization and packaging, and a plurality of single multicolor tubular materials are obtained;

(2) The three-stage screw extruder is provided with a granulating system, and the production sequence is as follows: vacuumizing the cured material in a molten state, granulating and extruding the cured material, dragging the cured material, rotary-cutting the cured material, fine-granulating the cured material, sterilizing the cured material, and packaging the cured material to obtain modified material particles;

the drying module comprises a first buffer bin, a first spiral forced feeding device, a vacuum drying chamber, a stirring and conveying device and a mold temperature machine; the buffer bin is connected with a first spiral forced feeding device which is connected with a vacuum drying chamber, and the vacuum drying chamber is connected with a stirring conveying device; the vacuum drying chamber is provided with a temperature control channel connected with a mold temperature machine; the temperature of the vacuum drying chamber is set to be 60 ℃, and the material drying time is 5 minutes;

The feed port module comprises a first feed port, a second feed port, a third feed port, a fourth feed port and an exhaust device; the first feed inlet is connected with a first machine barrel of the primary screw extruder, and is suitable for powder materials, granular materials or mixed materials of powder and granules; the second feeding port is connected with a second machine barrel of the primary screw extruder, and is suitable for liquid or semisolid flowing materials; the third feed inlet is connected with a fourth machine barrel of the primary screw extruder, and is suitable for liquid or semisolid flowing materials; the fourth feed inlet is connected with the first-stage screw extruder

Is applicable to powder materials, granular materials or mixed materials of powder and granules; the exhaust device is connected with a fifth machine barrel of the primary screw extruder, and the useless gas in the materials is discharged through the exhaust device;

the first feeding port and the fourth feeding port comprise a second buffer bin, a third buffer bin and a second spiral forced feeding device, and spirals

The first feeding device comprises a first plunger type high-precision metering pump, a second plunger type high-precision metering pump and a first feeding device;

the screw extruder combined module is divided into three stages, namely a first-stage screw extruder, a second-stage screw extruder and a third-stage screw extruder;

The screw extruder comprises a single screw extruder, a double screw extruder and a multi-shaft screw extruder; according to the preparation requirements of different products, the screw extruder combination module is provided with the following combination modes:

combining: the first-stage screw extruder is a double-screw extruder, the second-stage screw extruder is a single-screw extruder, and the third-stage screw extruder is a single-screw extruder;

and (2) combining two: the first-stage screw extruder is a double-screw extruder, the second-stage screw extruder is a double-screw extruder, and the third-stage screw extruder is a double-screw extruder;

and (3) combining three: the first-stage screw extruder is a double-screw extruder, the second-stage screw extruder is a single-screw extruder, and the third-stage screw extruder is a double-screw extruder;

combination four: the first-stage screw extruder is a multi-shaft screw extruder, the second-stage screw extruder is a double-screw extruder, and the third-stage screw extruder is a double-screw extruder;

and (5) combining: the first-stage screw extruder is a multi-shaft screw extruder, the second-stage screw extruder is a single-screw extruder, and the third-stage screw extruder is a double-screw extruder;

and (3) combining six: the first-stage screw extruder is a multi-shaft screw extruder, the second-stage screw extruder is a single-screw extruder, and the third-stage screw extruder is a single-screw extruder;

The single screw extruder is provided with 5-7 sections of independent barrels to form a modularized barrel, 5-7 temperature areas are corresponding, and the temperature setting range of each temperature area is as follows: the modularized machine barrel is provided with a single screw hole at the temperature of 40-230 ℃ and is matched with a single modularized screw, and the length-diameter ratio of the screw is 26:1-40:1;

the double-screw extruder is provided with 7-9 sections of independent barrels to form a modularized barrel, 7-9 temperature areas are corresponding, and the temperature setting range of each temperature area is as follows: the modularized machine barrel is provided with double screw holes and two modularized screws, and the length-diameter ratio of the screws is 30:1-62:1.

The multi-shaft screw extruder is provided with 7-9 sections of independent barrels to form a modularized barrel, 7-9 temperature areas are corresponding, and the temperature setting range of each temperature area is as follows: the temperature of 40-230 ℃ and the modularized machine barrel is provided with a plurality of screw holes; a plurality of modularized screws are matched, and the length-diameter ratio of the screws is 30:1-62:1;

the independent machine barrel is provided with an independent temperature control channel, is connected with the mold temperature machine and is an independent temperature zone.

The die temperature machine consists of a water tank, a heating and cooling system, a power transmission system, a liquid level control system and a temperature sensor.

The modularized screw consists of a screw mandrel and a screw element, wherein the screw element is provided with thread sections with different pitches and different lengths and

The matching element, the screw mandrel and the spiral element are connected through a spline, and the spiral element is arranged according to the processing technology of materials

And the modular screw rod is formed by being arranged on the screw rod mandrel.

The multicolor mixing system comprises a diversion system, a color injection machine barrel, a mixing machine barrel and a diversion system.

The flow distribution system comprises 2-16 flow distribution channels, each flow distribution channel is connected with the color injection machine barrel, and materials enter the 2-16 color injection machine barrels through the flow distribution channels.

The color injection machine barrel, the mixing machine barrel and the flow guiding system are all provided with 2-16 material channels, each material channel of the color injection machine barrel is provided with a color injection port, multicolor materials enter the material channel of the color injection machine barrel through the color injection port, and enter the tubular object system through the flow guiding system after the mixing machine barrel and the main materials are fully mixed.

The tubular object system comprises a die mandrel plate, a first discharging plate, a second discharging plate, a third discharging plate, a discharging die I and an antistatic annular cooling ring sleeve combination.

And 1-500 die mandrels are uniformly fixed on the die mandrel plate in the vertical direction of the plate surface, and 1-500 discharge holes are correspondingly processed on the first discharge plate, the second discharge plate, the third discharge plate and the first discharge die.

The diameter size range of the die mandrel is as follows: 1-8 mm, and the diameter size range of the discharge hole: 6-12 mm.

The first discharging plate, the second discharging plate and the third discharging plate are respectively used for processing a first material groove, a second material groove and a third material groove, and are communicated with one side of each die hole, and the three material grooves are mutually independent and do not interfere with each other.

The first discharging die is provided with a temperature control channel which is connected with a die temperature machine, the temperature of the discharging die is controlled, and the temperature setting range is 40-80 ℃.

The anti-static annular cooling ring sleeve assembly comprises an anti-static annular cooling ring head die sleeve I and an anti-static annular cooling ring shaping sleeve I, the anti-static annular cooling ring head die sleeve I is arranged on the discharging die I, the discharging die I is controlled to rapidly cool, the anti-static annular cooling ring shaping sleeve I is arranged between the discharging die I and the traction system, and the produced tubular object is controlled to rapidly cool.

The granulating system comprises a discharging die II and an antistatic annular cooling ring sleeve II.

The second discharging die is provided with 1 to 500 discharging holes which are uniformly arranged on the second discharging die; the diameter size range of the discharging hole is as follows: 1-10 mm.

The anti-static annular cooling ring sleeve assembly II comprises an anti-static annular cooling ring head die sleeve II and an anti-static annular cooling ring shaping sleeve II, the anti-static annular cooling ring head die sleeve II is arranged on the discharging die II, the discharging die is controlled to cool down at a two-step speed, the anti-static annular cooling ring shaping sleeve II is arranged between the discharging die II and the traction system, and the produced modified material particles are controlled to cool down at a high speed.

The antistatic annular cooling ring is in an annular structure and comprises an air inlet, an air exchange main body, a rotating body and air outlets, wherein the number of the air inlets is even, the air inlets are uniformly distributed at the lower part or the side surface and are connected with a fan wind dividing bag through an air pipe; the wind exchange main body is a hollow shell, and the section of the wind exchange main body is a labyrinth type.

The combined module of the drying module and the screw extruder is arranged in an up-down multilayer way, the drying module is arranged at the uppermost position, and the first-stage screw extrusion is carried out

The outlet is centered, and the secondary screw extruder and the tertiary screw extruder are positioned at the lowest position.

The tube system and the granulating system are replaced according to the need, and various tubes such as plastic tubes, medical catheters, disposable straws and stirring rods, polylactic acid PLA, polycaprolactone PCL, polybutylene succinate-adipate copolymer PBSA, polybutylene adipate/terephthalate PBAT, polyhydroxyalkanoate PHA, polybutylene succinate PBS, polydioxanone PPDO, polyglycolide PGA, polypropylene carbonate or carbon dioxide/propylene oxide copolymer PPC, carbon dioxide ethylene oxide copolymer PEC, cellulose acetate CA, starch St, bio-based polyethylene Bio-PE, bio-based polypropylene Bio-PP, bio-based nylon Bio-PA, bio-based polyurethane Bio-PUR and Bio-based poly-dimethyl furan PEF biodegradable modified material particles are produced in a large scale.

The method is widely applied to the fields of industry, medical use, catering, daily use, various plastics, degradation materials and the like, is energy-saving, low-carbon and environment-friendly, has continuous and stable production process, is safe and pollution-free, and is suitable for industrialized mass production.

(1) The feed port module is provided with 4 feed ports, so that materials with different physical properties enter a specific temperature zone through different feed ports, the physical properties and characteristics of various materials are fully exerted, the mechanical properties, heat resistance and physical stability of the product are improved, and the invention is beneficial to the use and the invention of more preparation methods, as shown in figures 4 and 5. When the screw extruder in the existing market is used for producing plastic tubes or plastic particles, the adopted traditional plastic raw materials have single component raw materials and are composite, and can directly enter the screw extruder from a single feed inlet to be heated and melted, and the plastic raw materials are extruded from the screw extruder after being in a molten state.

With the increasing environmental protection requirements, new degradable plastics are commonly used;

the novel degradable plastic is required to be modified due to physical reasons and requirements of terminal products, the required production raw materials comprise materials with different physical properties such as low-temperature materials, modified materials, compatible materials and high-temperature materials, the low-temperature materials and the modified materials can reach a state of high temperature resistance after being mixed and modified, and are subjected to fusion reaction with the high-temperature materials, then in the production process, the compatible materials are added for surface modification, so that the dispersibility and compatibility of the low-temperature materials are improved, the polarity difference between the low-temperature materials and the high-temperature materials is finally overcome, the low-temperature materials are uniformly distributed in the whole high-temperature material system by virtue of intermolecular bonding force, and the incompatible two polymers are promoted to be combined together to obtain a stable blend, so that the compatibility and the dispersibility of the composite material are greatly improved;

The traditional equipment is provided with only one feed inlet, when all materials enter the screw extruder through the same feed inlet, the materials needing to be modified at low temperature and the high-temperature resistant materials are in a low temperature area, the high-temperature resistant materials do not react and change, but occupy the space and heat of the materials needing to be modified at low temperature, so that the modification time of the materials needing to be modified at low temperature is relatively reduced, the heating area is relatively reduced, the modification process of the materials needing to be modified at low temperature is blocked to a certain extent, the materials needing to be modified at low temperature cannot be completely modified, and cannot be completely resistant to high temperature, so that the materials are easy to carbonize after entering the high temperature area, and finally, more defective products are easy to appear; meanwhile, the effect of compatible materials is greatly reduced, the quality instability of products in normal production is caused, the problems of uneven strength, poor heat resistance and the like of tubular products are caused, the stability of the products cannot be ensured, and a new preparation method and scientific research test cannot be met, so that the preparation mode for producing degradable plastic products with stable quality and large scale production is not always available in the current market. Therefore, a special treatment mode is needed to optimize, so that the production raw materials fully play the role in the extruder and better keep various materials

Characteristics;

based on the reasons, the feeding port module is provided with 4 feeding ports, low-temperature materials enter through the first feeding port, modified materials enter through the second feeding port, compatible materials enter through the third feeding port, and high-temperature materials enter through the fourth feeding port. The low-temperature material enters a first-stage screw extruder through a first feed inlet, is mixed with the modified material entering through a second feed inlet, is mixed with the compatible material entering through a third feed inlet, is subjected to compatible modification in a low-temperature region of 70-100 ℃, the high-temperature resistant temperature of the modified composite material is close to the high-temperature resistant temperature of the high-temperature material, and is subjected to curing and melting reaction in a high-temperature region of 130-230 ℃ after being mixed; materials with different physical properties enter a specific temperature zone of the first-stage screw extruder through different feed inlets, so that different characteristics of various materials such as low-temperature materials, modified materials, compatible materials, high-temperature materials and the like are fully exerted, and the physical strength and the performance of a final product are improved; has the following beneficial effects:

(1) The problems of uneven product strength, unstable physical characteristics and the like of different materials after entering an extruder at the same feed inlet are solved, and meanwhile, the mechanical property, heat resistance, physical stability and the like of the product are obviously improved by matching with an advanced preparation method, so that the method is beneficial to the use and the invention of more preparation methods; experimental studies in this patent application found and verified: taking the modification of PBAT addition compatible materials as an example, by filling modified PBAT with starch, the addition of starch shifts the crystallization temperature of the blend higher than Wen Fangxiang, with a consequent decrease in crystallinity. The compatibility material is added through the test, so that not only is the dispersion effect of the starch improved, but also the compatibility between the starch and the PBAT is greatly improved; the mechanical property and the glass transition temperature of the modified material are obviously improved, the toughening modification, the stretching and the impact strength are realized, the high filling is realized, the high-temperature material consumption is reduced, the processing rheological property is improved, and the surface smoothness is improved.

(2) According to the invention, a plurality of tubular object systems are manufactured, each tubular object system is provided with 1-500 discharge holes, 2-16 tubular object systems are simultaneously produced in a concentrated manner, the production efficiency is greatly improved, and 8 tubular object systems are simultaneously produced as shown in figure 10.

When the screw extruder in the existing market is used for producing plastic tubes, the screw extruder can only be used for single production, all matched equipment can only be used for single treatment, and along with the continuous change of emerging market demands and international large environments, the problems of emission reduction, energy conservation, environmental protection and the like are more and more emphasized, and the raw material cost is continuously increased, so that the single production of the existing screw extruder is no longer suitable for the market demands.

Based on the reasons, the multi-tube system comprises 1-500 tubes, wherein 1-500 die mandrels are uniformly fixed on the die mandrel plate in the vertical direction of the plate surface, 1-500 discharge holes are respectively formed in the first discharge plate, the second discharge plate, the third discharge plate and the discharge die, and 2-16 tube systems are simultaneously produced in a concentrated mode; the tubular object system is provided with an antistatic annular cooling ring sleeve combination unit, which comprises an antistatic annular cooling ring head die sleeve I and an antistatic annular cooling ring shaping sleeve I, wherein the antistatic annular cooling ring head die sleeve I is arranged on a discharging die I, controls the discharging die I to rapidly cool down, and controls the produced tubular object to rapidly cool down; the processed 1-500 discharging holes are uniformly arranged on a first discharging die and matched with new production equipment and new preparation technology, and the process comprises the following steps: the production materials are modified, mixed, cured, melted, sleeved with a die head of an antistatic annular cooling ring, extruded by a tubular object, shaped and sleeved with an antistatic annular cooling ring, pulled, rotary cut, sterilized, packaged and obtained to obtain a plurality of tubular objects

A material; has the following beneficial effects:

(1) the method comprises the following steps The production device solves the problem that the yield of the existing tubular product production equipment in the traditional market is limited, improves the production efficiency of the tubular product, improves the utilization rate of the production equipment, fully exerts the production capacity of the extruder, reduces the production energy consumption, reduces the carbon emission, improves the production efficiency, improves the utilization rate of the production equipment, meets the industrial production requirements of the market better, and meets the national requirements in the aspects of emission reduction, energy conservation and environmental protection.

(2) The method comprises the following steps Compared with the traditional production mode in the existing market, the production capacity achieved by the method is obviously improved and improved, and the problem of the deficiency of the traditional market equipment is solved.

(3) According to the invention, a plurality of tubular objects and modified material particles are synchronously produced, so that the utilization rate of equipment is improved, and the production efficiency is greatly improved, as shown in fig. 12:

the existing screw extruder in the market can only singly produce tubular objects or singly produce material particles, along with the increasing requirements of environmental protection, the novel biodegradable materials are used more and more commonly, the novel biodegradable tubular objects are prepared by the biodegradable particles, the tubular objects can also serve as the material particles to a certain extent, the requirement of simultaneously producing the tubular objects and the material particles is met, and therefore, the tubular objects and the material particles are in a new mutual relation, and the tubular objects and the material particles complement each other and mutually form symbiosis. In the case of only the tubular object production equipment, if the production of the material particles is required, new material particle production equipment is required, in the case of only the material particle production equipment, if the production of the tubular object is required, new tubular object production equipment is required, and the new production equipment is required, more using sites, energy consumption, labor cost and the like are required to be increased, so that certain investment repetition and cost superposition are caused, and the problems of high energy consumption, high carbon emission and the like are also caused.

Based on the reasons, the screw extruder combination module is provided with the first-stage screw extruder, the second-stage screw extruder and the third-stage screw extruder, wherein the second-stage screw extruder and the third-stage screw extruder are respectively provided with a tube system and a granulating system, a plurality of single multicolor tubes and modified material particles can be synchronously produced, the extruder used for the screw extruder combination module comprises a single screw extruder, a double screw extruder, a multi-shaft screw extruder and the like, and two or three screw extruders of the single screw extruder, the double screw extruder and the multi-shaft screw extruder are adjusted to be combined according to the preparation requirements of different products.

The invention synchronously produces a plurality of tubular objects and modified material particles, and has the following beneficial effects: the invention integrates the advantages of two production devices, optimizes the device configuration, reduces the total occupied area, reduces the corresponding device cost and the corresponding worker cost, reduces the production energy consumption, reduces the carbon emission, improves the production efficiency, simultaneously improves the utilization rate of the production device, more meets the industrial production requirements of the market, and meets the national requirements in the aspects of emission reduction, energy conservation and environmental protection.

(4) The single multi-color mixing system of the invention enables the tubular object to be multi-color and greatly improves the market activity and prospect, as shown in figures 10-11.

When the existing market screw extruder is used for producing plastic tubes, only single-color or double-color is affected by primary cognition, consciousness and large environment, the single-color or double-color tubes meet most of the demands at the moment, the consumption main force army at the moment is gradually aged, the young people become new consumption main force army at present, the life is more and more rich and colorful along with the development of technology, and the single-color and double-color tubes can not meet the demands of the young people at present. The market is in urgent need of more colored products to attract young people to consume, society is developing rapidly, and the production of tubular objects is not improved greatly, the original style is single and old, the market vitality and prospect are lacking, and the market demand is not met.

For the above reasons, the multicolor mixing system of the present invention adds more colors to the production of the tube by a novel color injection. The diversion system is provided with 2-16 diversion channels, and can be connected with 2-16 sets of color injection machine barrels, mixing machine barrels, diversion systems and tubular object systems to simultaneously produce tubular objects. The color injection machine barrel, the mixing machine barrel and the flow guiding system of the multicolor mixing system are all provided with 2-16 material channels, and each material channel of the color injection machine barrel is provided with a color injection port, so that colors in 2-16 can be injected simultaneously, and the tubular product finally presents multicolor tubular products with different colors in 2-16.

The single multicolor mixing system has the following beneficial effects: solves the problem that the existing tubular objects in the market are only single color

Or the deficiency of double colors enriches the variety of the tubular objects, ensures that the colors of the tubular objects can be multi-color or multi-color mixture, improves the visual ornamental value of the tubular objects, meets the different pursuits of young people and the different demands of markets, improves the attractive force of the related products using the tubular objects to a certain extent, improves the vitality and the prospect of the markets, and meets the market demands.

(5) The invention sets the first and second anti-static annular cooling rings to cool the first and second head dies and the product at high speed, to shape the product at high efficiency, to reduce the cooling device, the using place, the energy consumption and the carbon emission, to save the cooling time, as shown in fig. 11-12, the existing tubular product producing device or material particle producing device, the tubular product and material particle product extruded from the discharging die are in molten state, to cool and shape, to deform and adhere, to affect the normal production, to improve the mechanical property of the tubular product, to cool the product after packing and selling. The traditional cooling equipment is mostly cooled and cooled by adding fans to a conveyor due to market influence and technical limitation and utilizes the fans to cool. But the cooling effect of the fan is poor, the time duration is longer, the demand of the cooling equipment is larger, the occupied area is larger, the waste of a plurality of space resources is caused, the demand on the occupied area of the equipment, the number of personnel and the comprehensive energy consumption is larger, the problems of high energy consumption, high carbon emission and the like are also caused, and the industrial production demand of the existing market is not met.

Based on the reasons, the antistatic annular cooling ring sleeve combination device is respectively arranged between the tubular object, the material particle machine head die, the discharging die and the traction system, and utilizes the high-pressure fan to generate high-speed flowing air to cool the produced tubular object products and particle products immediately and efficiently. The device is provided with a variable-frequency automatic regulating system, ensures stable and controllable wind pressure and flow, and the sleeve body adopts double-channel circulating water cooling, and the anti-static annular cooling ring sleeve combination of the invention rapidly cools and shapes the tubular objects and material particles in a molten state extruded by the discharge die, and has the following beneficial effects:

(1) the method comprises the following steps The cooling temperature can be set according to the product requirement, the product is ensured to be cooled very fast, the high-efficiency shaping is realized, and the product quality is ensured.

(2) The method comprises the following steps The problems of adhesion between products and equipment are solved, the problem of deformation of the products is also solved, and the mechanical properties of tubular products and material particles are greatly improved by rapid cooling.

(3) The method comprises the following steps The problem of even cooling can be accomplished with 1-5 meters conveying equipment only, the conveying equipment that has solved traditional heat sink and has used up to 15-20 meters and even longer installs the fan additional and carries out cooling and cooling, cooling time is longer, the inhomogeneous cooling of cooling, the great inefficiency problem of area has not only shortened the length of cooling heat sink and has reduced the area of equipment, simultaneously also reduced equipment cost, labour cost, production energy consumption and carbon emission etc. has improved production efficiency, accords with new market industrialization needs in aspects such as emission reduction, energy-conservation, environmental protection more.

(6) The invention stacks the drying module and the screw extruder combined module up and down in multiple layers, reduces the occupied area, fully utilizes the factory building space, and is shown in figure 7

The existing screw extruders basically adopt planar arrangement, if the existing screw extruders are required to be matched for use according to market development requirements, each screw extruder occupies a certain use area, the screw extruders are used in a mode of being in a front-back shape, an L shape or a T shape and the like, more space is occupied to a certain extent when the existing screw extruders are placed, the overall occupied area is large, the height space is not fully utilized, the space resource waste is caused, and the personnel arrangement and comprehensive energy consumption are also required to be large.

Based on the reasons, the drying module and the screw extruder combined module are integrally arranged in an up-down multi-layer mode, the drying module is arranged at the uppermost position, the first-stage screw extruder device is arranged at the middle position, the second-stage screw extruder and the third-stage screw extruder are arranged at the lowermost position, materials enter the first-stage screw extruder after being dried by the drying module, and enter two second-stage screw extruders and three-stage screw extruders which are respectively arranged at the lowermost position and synchronously produce a plurality of single multicolor tubular objects and modified material particles after being extruded by the first-stage screw extruder; the equipment is placed up and down compactly, the factory building space is fully utilized, the occupied area of the equipment is reduced, the number of operators is reduced to a certain extent, and the comprehensive energy consumption, carbon emission, personnel cost and the like are reduced.

The invention stacks the drying module and the screw extruder combined module up and down in multiple layers, and has the following beneficial effects: the problems of large occupied area, more labor cost, high energy consumption and the like of the equipment for producing the tubular objects and the equipment for producing the material particles are solved, the occupied area is reduced, the corresponding equipment cost and labor cost are reduced, the production energy consumption is reduced, the carbon emission is reduced, the production benefit is improved, the industrial production requirements of the existing market are met, and the national requirements on emission reduction, energy conservation, environmental protection and the like are met.

In conclusion, the invention fully plays the characteristics of each material, and improves the physical strength and performance of the product. Meanwhile, the problems of mechanical property, heat resistance, physical stability and the like of the product are improved by matching with an advanced preparation method, so that the method is beneficial to the use and the invention of more preparation methods; the invention improves the production efficiency of the tubular objects, improves the income, enriches the types of the tubular objects, ensures that the colors of the tubular objects can be mixed in multiple colors, improves the attraction of related products using the tubular objects to a certain extent, improves the market activity and prospect, and meets the current market demand.

The technology related by the invention is a typical multi-disciplinary crossed comprehensive technology, and requires the expertise of plastics processing, polymer molding machinery, physical and mechanical molds and other disciplines. The invention has excellent comprehensive performance, green and environment-friendly characteristics, and has remarkable economic value and social significance.

Drawings

The following is a further description of a mechanical apparatus for simultaneous production of a plurality of multi-color tubes and modified material particles using a plurality of feed ports, in accordance with the present invention, taken in conjunction with the accompanying drawings and detailed description:

FIG. 1 is a schematic diagram of the overall structure of the present invention;

FIG. 2 shows a sample of a multicoloured tube produced in accordance with the present invention in combination with a novel method of preparation;

FIG. 3 is a schematic diagram of a drying module according to the present invention;

FIG. 4 is a schematic view of a feed inlet module of the present invention and a combined schematic view of an antistatic annular cooling collar of the present invention;

FIG. 5 is an enlarged view of portion A of FIG. 4;

FIG. 6 is a schematic diagram of a modular barrel of the screw extruder of the present invention;

FIG. 7 is a schematic diagram of a combined module and overall placement of a screw extruder of the present invention;

FIG. 8 is a schematic view of a screw extruder of the present invention;

FIG. 9 is a schematic view of a modular screw of the screw extruder of the present invention;

FIG. 10 is a schematic illustration of the exterior of the polychromatic mixing system and tube system of the present invention;

FIG. 11 is a material path diagram of a tubular system of the present invention;

FIG. 12 is a schematic view of the discharge ports of the tube system and pelletization system of the present invention;

reference numerals: a drying module (1), a feed inlet module (2), a screw extruder combined module (3), a multicolor mixing system (4), a tube system (5) and a granulating system (6);

a first buffer bin (11), a first spiral forced feeding device (12), a vacuum drying chamber (13), a stirring and conveying device (14) and a mold temperature machine 316;

a first feed inlet (21), a second feed inlet (22), a third feed inlet (23), a fourth feed inlet (24) and an exhaust device (25);

a second buffer bin (211), a second spiral forced feeding device (212), a first plunger type high-precision metering pump (221), a first feeding device (222), a second plunger type high-precision metering pump (231), a second feeding device (232), a third buffer bin (241) and a third spiral forced feeding device (242);

a first barrel (3131), a second barrel (3132), a fourth barrel (3134), a fifth barrel (3135), a sixth barrel (3136);

a primary screw extruder (31), a secondary screw extruder (32) and a tertiary screw extruder (33);

a motor (311), a distribution box (312), a modular barrel (313), a modular screw (314); a vacuum pumping device (315) and a mold temperature machine (316);

A screw mandrel (3141), a screw element (3142);

a diversion system (41), a color injection machine barrel (42), a color injection port (421), a mixing machine barrel (43) and a diversion system (44);

a die mandrel plate (51), a first discharging plate (52), a second discharging plate (53), a third discharging plate (54), a first discharging die (55),

Antistatic annular cooling ring sleeve combination one (56), antistatic annular cooling ring nose die sleeve one (561) and antistatic annular cooling ring

A first sizing sleeve (562);

the machine comprises a discharging mold II (61), an antistatic annular cooling ring sleeve combination II (62), an antistatic annular cooling ring machine head mold sleeve II (621) and an antistatic annular cooling ring shaping sleeve II (622).

Detailed Description

A mechanical device for simultaneously producing a plurality of single multi-color tubes and modified material particles using a plurality of feed ports is described in detail below with reference to the accompanying drawings, which are provided to illustrate the present invention and not to limit the scope of the present invention;

as shown in fig. 1, the mechanical device for synchronously producing a plurality of single multicolor tubular objects and modified material particles by adopting a plurality of feed inlets comprises a drying module (1), a feed inlet module (2), a screw extruder combined module (3), a multicolor mixing system (4), a tubular object system (5) and a granulating system (6). The process comprises the following steps: the method comprises the steps of carrying out screw pushing reaction on low-temperature materials through a first screw forced feeding device (12) of a first buffer bin (11), drying at 60 ℃ for 5min in a vacuum drying chamber, stirring and conveying (14), carrying out screw pushing reaction through a second screw forced feeding device (212) of a first feed port (21) of a feed port module (2), then carrying out mixing with modified materials injected through a first plunger type high-precision metering pump (221) through a second feed port 22 of the feed port module (2), then carrying out mixing with compatible materials injected through a second plunger type high-precision metering pump (231) through a third feed port (23) of the feed port module (2), carrying out compatible modification at 70-100 ℃, exhausting, then carrying out mixing with high-temperature materials through a third screw forced feeding device (242) of a fourth feed port (24) of the feed port module (2), curing at 130-230 ℃ under high-temperature high-pressure, extruding to two synchronously working second screw extruders (32) and three-stage screw extruders (31), and producing multi-color multi-granular materials through a first screw extruder (33). Wherein:

(1) The secondary screw extruder (32) is provided with a multicolor mixing system (4) and a tube system (5), and the flow is as follows: the curing material is vacuumized in a molten state, flows through a diversion system (41) of a multicolor mixing system (4), flows through a color injecting machine barrel (42), flows through a mixing machine barrel (43), flows through a flow guiding system (44), and is formed into a first mixed material, a second mixed material and a third mixed material, enters a first material groove, a second material groove and a third material groove, passes through a tubular material channel, is subjected to cross fusion reaction, is subjected to antistatic annular cooling ring machine head die sleeve (561), is subjected to tubular material extrusion, is subjected to antistatic annular cooling ring shaping sleeve (562), is subjected to traction, is subjected to rotary cutting, is subjected to sterilization, and is packaged, so that a plurality of single multicolor tubular materials are obtained.

(2) The three-stage screw extruder (33) is provided with a granulating system (6), and the production sequence is as follows: the cured material is vacuumized, subjected to granulation extrusion, subjected to traction, subjected to rotary cutting, subjected to fine particle sterilization and packaged in a molten state to obtain modified material particles.

As shown in FIG. 2, a sample of the multicolor tubing produced in accordance with the present invention in combination with the novel preparation method is shown.

As shown in fig. 3, the drying module comprises a first buffer bin (11), a first spiral forced feeding device (12), a vacuum drying chamber (13), a stirring and conveying device (14) and a mold temperature machine (316). The first buffer bin (11) is connected with the first spiral forced feeding device (12), the first spiral forced feeding device (12) is connected with the vacuum drying chamber (13), and the vacuum drying chamber (13) is connected with the stirring conveying device (14). The vacuum drying chamber (13) is provided with a temperature control channel which is connected with a mold temperature machine (316). The set temperature of the vacuum drying chamber is 60 ℃, and the materials are dried

The time was 5 minutes.

As shown in fig. 4, 5, 6, 7 and 12, the feed port module (2) includes a first feed port (21), a second feed port (22), a third feed port (23), a fourth feed port (24) and an exhaust device (25). The first feed inlet (21) is connected with a first machine barrel (3131) of the primary screw extruder (31), and is applicable to powder materials, granular materials or mixed materials of powder and granules. The second feed inlet (22) is connected with a third machine barrel (3233) of the primary screw extruder (31), and is suitable for liquid or semi-solid flowing materials. The third feed inlet (23) is connected with a fourth machine barrel (3134) of the primary screw extruder (31), and is suitable for liquid or semi-solid flowing materials. The fourth feed inlet (24) is connected with a sixth machine barrel (3136) of the primary screw extruder (31), and is applicable to powder materials, granular materials or mixed materials of powder and granules. The exhaust device (25) is connected with a fifth machine barrel (3135) of the primary screw extruder (31), and the waste gas in the materials is discharged through the exhaust device (25).

The first feeding port (21) and the third feeding port (23) comprise a first buffering bin, a second buffering bin (211, 231) and a first spiral forced feeding device, a second spiral forced feeding device (212, 232), and the second feeding port (22) comprises a first plunger type high-precision metering pump (221) and a first feeding device (222).

As shown in fig. 7, the drying module 1 and the screw extruder combined module 3 are integrally arranged in an up-down multi-layer manner, the drying module 1 is located at the uppermost position, the first-stage screw extruder (31) is arranged at the center, the second-stage screw extruder (32) and the third-stage screw extruder (33) are located at the lowermost position, the up-down compactness is achieved, and the occupied area is reduced.

As shown in fig. 6-9, the screw extruder power of the screw extruder combined module 3 is provided by a motor (311), and the speed and power are increased and reduced through a distribution box (312) to drive a modularized screw (314) to rotate in a modularized machine barrel (313) so as to push materials forwards. The screw extruder combination module 3 is divided into three stages, namely a first-stage screw extruder (31), a second-stage screw extruder (32) and a third-stage screw extruder (33).

The screw extruder comprises a single screw extruder, a double screw extruder and a multi-shaft screw extruder. According to the preparation requirements of different products, the screw extruder combination module 3 is provided with the following combination modes:

combining: the primary screw extruder (31) is a twin screw extruder, the secondary screw extruder (32) is a single screw extruder, and the tertiary screw extruder (33) is a single screw extruder.

And (2) combining two: the primary screw extruder (31) is a twin screw extruder, the secondary screw extruder (32) is a twin screw extruder, and the tertiary screw extruder (33) is a twin screw extruder.

And (3) combining three: the primary screw extruder 31 is a twin screw extruder, the secondary screw extruder 32 is a single screw extruder, and the tertiary screw extruder 33 is a twin screw extruder.

Combination four: the primary screw extruder (31) is a multi-shaft screw extruder, the secondary screw extruder (32) is a double screw extruder, and the tertiary screw extruder (33) is a double screw extruder.

And (5) combining: the primary screw extruder (31) is a multi-shaft screw extruder, the secondary screw extruder (32) is a single screw extruder, and the tertiary screw extruder (33) is a twin screw extruder.

And (3) combining six: the primary screw extruder (31) is a multi-shaft screw extruder, the secondary screw extruder (32) is a single screw extruder, and the tertiary screw extruder (33) is a single screw extruder.

The single screw extruder is provided with 5-7 sections of independent barrels to form a modularized barrel, 5-7 temperature areas are corresponding, and the temperature setting range of each temperature area is as follows: the modularized machine barrel is provided with a single screw hole at the temperature of 40-230 ℃ and is matched with a single modularized screw, and the length-diameter ratio of the screw is 26:1-40:1.

The multi-shaft screw extruder is provided with 7-9 sections of independent barrels to form a modularized barrel, 7-9 temperature areas are corresponding, and the temperature setting range of each temperature area is as follows: the temperature of 40-230 ℃ and the modularized machine barrel is a multi-screw hole. And a plurality of modularized screws are matched, and the length-diameter ratio of the screws is 30:1-62:1.

The independent machine barrel is provided with an independent temperature control channel, is connected with a mold temperature machine (316) and is an independent temperature zone.

The die temperature machine (316) is composed of a water tank, a heating and cooling system, a power transmission system, a liquid level control system and a temperature sensor.

The modularized screw (314) is composed of a screw mandrel (3141) and a screw element (3142), wherein a spline is machined on the shaft body of the screw mandrel (3141), spline grooves are machined in the inner holes of the screw element (3142), screw elements (3142) are provided with thread sections with different pitches and different lengths and matched elements, the screw mandrel (3141) is matched with the screw elements (3142), and the screw elements (3142) are installed on the screw mandrel according to the machining process of materials and in sequence to form the modularized screw (314).

As shown in fig. 11, the multicolor mixing system 4 includes a diversion system (41), an color injection barrel (42), a mixing barrel (43), and a diversion system (44).

The flow distribution system 41 comprises 2-16 flow distribution channels, each flow distribution channel is connected with the color injection machine barrel (42), and materials enter the 2-16 color injection machine barrels (42) through the flow distribution channels.

The color injection machine is characterized in that 2-16 material channels are formed in the color injection machine barrel (42), the mixing machine barrel (43) and the diversion system (44), color injection ports (421) are formed in each material channel of the color injection machine barrel (42), multicolor materials enter the material channels of the color injection machine barrel (42) through the color injection ports (421), and enter the tubular object system (5) through the diversion system (44) after the mixing machine barrel (43) and main materials are fully mixed. The process comprises the following steps: main material, a flow distribution channel of a flow distribution system (41), a color injection machine barrel (42), multi-color material mixture entering a material channel through a color injection port (421), a mixing machine barrel (43), a material cavity of a flow guide system (44), and a first mixed material, a second mixed material and a third mixed material.

As shown in fig. 11-12, the tube system 5 includes a die mandrel plate (51), a first take-off plate (52), a second take-off plate (53), a third take-off plate (54), a first take-off die (55), and an antistatic annular cooling collar combination one 56.

The die core shaft plate (51) is uniformly fixed with 1 to 500 die core shafts in the vertical direction of the plate surface, a first discharging plate (52),

The second discharging plate (53), the third discharging plate (54) and the first discharging die (55) are respectively provided with 1-500 discharging holes.

The first discharging plate (52), the second discharging plate (53) and the third discharging plate (54) are respectively used for processing a first material groove, a second material groove and a third material groove, and are communicated with one side of each die hole, and the three material grooves are mutually independent and do not interfere with each other.

The first discharging die (55) is provided with a temperature control channel which is connected with a die temperature machine (316) to control the temperature of the first discharging die (55) and set the temperature within the range of 40-80 ℃. The die temperature machine (316) adopts a die temperature machine.

The first anti-static annular cooling ring sleeve assembly (56) comprises a first anti-static annular cooling ring head die sleeve (561) and a first anti-static annular cooling ring shaping sleeve (562), the first anti-static annular cooling ring head die sleeve (561) is arranged on the discharging die and used for controlling the extremely rapid cooling of the discharging die, and the first anti-static annular cooling ring shaping sleeve (562) is arranged between the first discharging die (55) and the traction system and used for controlling the extremely rapid cooling of the produced tubular object.

The process comprises the following steps: the method comprises the steps of mixing a first mixed material, a second mixed material, a third mixed material, a first material tank, a second material tank and a third material tank, a tubular material channel, cross fusion reaction, extrusion of a tubular material, traction, shaping of an antistatic annular cooling ring, rotary cutting, sterilization, packaging and obtaining of a multicolor tubular material.

The granulating system comprises a discharging die II (61) and an antistatic annular cooling ring sleeve II (62).

And the second discharging die (61) is used for processing 1-500 discharging holes and is uniformly arranged on the second discharging die (61). The diameter size range of the discharging hole is as follows: 1-10 mm.

The anti-static annular cooling ring sleeve combination II (62) comprises an anti-static annular cooling ring machine head die sleeve II (621) and an anti-static annular cooling ring shaping sleeve II (622), the anti-static annular cooling ring machine head die sleeve II (621) is arranged on the discharging die, the discharging die is controlled to be cooled very fast, the anti-static annular cooling ring shaping sleeve II (622) is arranged between the discharging die II (61) and the traction system, and produced modified material particles are controlled to be cooled very fast.

The process comprises the following steps: melting materials, vacuumizing, granulating and extruding, drawing, rotary cutting, fine granulating, sterilizing, and packaging to obtain modified material particles.

The antistatic annular cooling ring is in a circular ring structure and comprises an air inlet, an air exchange main body, a rotating body and an air outlet. The air inlets are even in number and uniformly distributed at the lower part or the side surface and are connected with the fan wind distributing bags through air pipes. The wind exchange main body is a hollow shell, the cross section is a labyrinth, high-speed flowing air is generated by utilizing a high-pressure fan, and the produced tubular product and the produced granular product are cooled immediately and efficiently. The device has frequency conversion automatic regulating system, ensures that wind pressure and flow are stable controllable, and the annular sleeve body adopts binary channels double-circuit circulating water cooling, sets for cooling temperature according to the product requirement, ensures that the product is extremely fast cooled, and the high-efficient design guarantees product quality.

A mechanical apparatus for simultaneous production of a plurality of single multi-colored tubes and modified material particles using a plurality of feed ports is described in detail below by way of specific embodiments, which are provided to illustrate the invention and not to limit the scope of the invention.

The following are specific three embodiments:

example 1. A mechanical device for simultaneous production of a plurality of single multi-colour tubes and modified material particles using a plurality of feed openings, the process is:

modified starch is subjected to screw pushing reaction through a screw forced feeding device I (12) of a buffer bin I (11), drying at 60 ℃ for 5min in a vacuum drying chamber, stirring and conveying (14), is subjected to screw pushing reaction through a screw forced feeding device II (212) of a first feeding hole (21) of a feeding hole module 2, is subjected to mixing with modified materials injected through a plunger type high-precision metering pump I (221) of a second feeding hole (22) of the feeding hole module 2, is subjected to mixing with compatible materials injected through a plunger type high-precision metering pump II (231) of a third feeding hole (23) of the feeding hole module 2, is subjected to compatible modification at 70-100 ℃, is subjected to air discharge, is subjected to mixing with polybutylene succinate PBS materials through a screw forced feeding device III (242) of a fourth feeding hole (24) of the feeding hole module 2, is cured at 130-195 ℃ under high-temperature high-pressure metering conditions, is extruded through the first screw extruder (31) to a two synchronously operated second screw extruder (32) and a third extruder (33), and multi-single multi-color granular materials are produced. Wherein:

1. The two-stage screw extruder (32) is provided with a multicolor mixing system 4 and a tube system 5, and the flow is as follows: the curing material is vacuumized in a molten state, flows into a diversion system (41) of a multicolor mixing system 4, a color injecting machine barrel (42), a mixing machine barrel (43), a flow guiding system (44), and is formed into a first mixed material, a second mixed material and a third mixed material, enters into a first material groove, a second material groove and a third material groove, passes through a tubular material channel, is subjected to cross fusion reaction, is subjected to antistatic annular cooling ring machine head die sleeve (561), is subjected to tubular material extrusion, is subjected to antistatic annular cooling ring shaping sleeve (562), is subjected to traction, is subjected to rotary cutting, is subjected to sterilization and is subjected to packaging, and 100 medical catheters with the outer diameter of 10mm, the wall thickness of 1mm and the length of 300mm are obtained.

The three-stage screw extruder (33) is provided with a granulating system 6, and the flow is as follows: the cured material is vacuumized, an antistatic annular cooling ring machine head die sleeve II (621), granulating and extruding, an antistatic annular cooling ring shaping sleeve II (622), traction, rotary cutting, fine particles, sterilization and packaging in a molten state to obtain the PBS modified material particles with the diameter of 3mm and the length of 3 mm.

The primary screw extruder (31) adopts a double screw extruder, the secondary screw extruder (32) adopts a single screw extruder, and the tertiary screw extruder (33) adopts a single screw extruder.

The double-screw extruder adopted by the primary screw extruder (31) is characterized in that a modularized machine barrel is provided with 9 independent machine barrels, 9 independent temperature areas are set, and the temperature settings of the temperature areas are respectively as follows: 60 ℃, 65 ℃, 70 ℃, 75 ℃, 90 ℃, 195 ℃, 170 ℃, 150 ℃, 130 ℃. Wherein the first temperature zone to the ninth temperature zone are temperature controlled by a mold temperature machine 316.

The single screw extruder for producing the tubular objects by the secondary screw extruder (32) is characterized in that a modularized machine barrel is provided with 5 independent machine barrels, 5 independent temperature areas are set, and the temperature settings of the temperature areas are respectively as follows: 160 ℃, 140 ℃, 120 ℃, 100 ℃, 80 ℃, and the temperature of the first discharging mold (55) is set to 60 ℃. Wherein the first to fifth temperature zones and the first discharge mold (55) are controlled in temperature by a mold temperature machine 316.

The single screw extruder adopted by the three-stage screw extruder (33) for producing particles is characterized in that a modularized machine barrel is provided with 5 independent machine barrels, 5 independent temperature areas are set, and the temperature settings of the temperature areas are respectively as follows: 160 ℃, 140 ℃, 100 ℃, 80 ℃, 60 ℃, and the temperature of the second discharging mould (61) is set to 40 ℃. Wherein the first to fifth temperature areas and the second discharging mold (61) are controlled by a mold temperature machine 316.

The die mandrel plate (51) and the discharge die one (55) of the tube system 5 are sized: diameter size of the die mandrel:

Phi 8mm, diameter size of discharge hole: phi 10mm, number of die core shafts and discharge holes: 100.

The second discharging die (61) of the granulating system 6 is used for processing the size: diameter size of discharge hole: phi 3mm, number of discharge holes: 259.

The secondary screw extruder (32) and the tertiary screw extruder (33) synchronously work to synchronously produce 100 medical catheters with the outer diameter of 10mm, the wall thickness of 1mm and the length of 300mm and PBS modified material particles with the diameter of 3mm and the length of 3 mm.

The discharging dies of the tube system 5 and the granulating system 6 are replaced according to the requirement, and various tubes such as various plastic tubes, medical catheters, disposable straws, stirring bars and the like are produced in a large scale.

Example 2. A mechanical device for simultaneous production of a plurality of single multi-colour tubes and modified material particles using a plurality of feed openings, the process is:

modified starch is dried in a vacuum drying chamber at 60 ℃ for 5min through a first spiral forced feeding device (12) of a first buffering bin (11), stirred and conveyed for 14 min, pushed by a screw through a second spiral forced feeding device (212) of a first feeding hole (21) of a feeding hole module (2), pushed by a screw through a first-stage screw extruder (31), then mixed with modified material injected by a second feeding hole (22) of the feeding hole module (2) through a first plunger type high-precision metering pump (221), then mixed with compatible material injected by a third feeding hole (23) of the feeding hole module (2) through a second plunger type high-precision metering pump (231), compatible modified at 70-100 ℃, exhausted, mixed with polylactic acid PLA through a third spiral forced feeding device (242) of a fourth feeding hole (24) of the feeding hole module (2), cured under the conditions of high temperature and high pressure and high shear of 130-185 ℃, extruded to a second-stage screw extruder (32) and a third-stage screw extruder (31) which work synchronously, and a multi-color tubular extruder and a multi-color granular material are produced. Wherein:

1. The secondary screw extruder (32) is provided with a multicolor mixing system (4) and a tube system (5), and the flow is as follows: the curing material is vacuumized in a molten state, flows through a diversion system (41) of a multicolor mixing system (4), flows through a color injecting machine barrel (42), flows through a mixing machine barrel (43), flows through a flow guiding system (44), becomes a first mixed material, a second mixed material and a third mixed material, enters a first material groove, a second material groove and a third material groove, passes through a tubular material passage, is subjected to cross fusion reaction, is subjected to an antistatic annular cooling ring machine head die sleeve (561), is extruded through a tubular material, is subjected to antistatic annular cooling ring shaping sleeve (562), is subjected to traction, is subjected to rotary cutting, is subjected to sterilization, and is packaged to obtain the product

144 three-color disposable straws with the outer diameter of 8mm, the wall thickness of 0.7mm and the length of 300mm are produced.

The three-stage screw extruder (33) is provided with a granulating system (6), and the flow is as follows: the curing material is vacuumized, an antistatic annular cooling ring machine head die sleeve II (621), granulating and extruding, an antistatic annular cooling ring shaping sleeve II (622), traction, rotary cutting, fine particles, sterilization, packaging and obtaining polylactic acid PLA modified material particles with the diameter of 2mm and the length of 2 mm.

The primary screw extruder (31) adopts a double screw extruder, the secondary screw extruder (32) adopts a double screw extruder, and the tertiary screw extruder (33) adopts a double screw extruder.

The double-screw extruder adopted by the primary screw extruder (31) is characterized in that a modularized machine barrel is provided with 9 independent machine barrels, 9 independent temperature areas are set, and the temperature settings of the temperature areas are respectively as follows: 60 ℃, 65 ℃, 70 ℃, 75 ℃, 90 ℃, 120 ℃, 185 ℃, 170 ℃, 150 ℃. Wherein the temperature of the first temperature zone to the ninth temperature zone is controlled by a mold temperature machine (316).

The double-screw extruder for producing the tubular objects by the secondary screw extruder (32) is characterized in that 7 independent barrels are configured in a modularized barrel, 7 independent temperature areas are set, and the temperature settings of the temperature areas are respectively as follows: the temperature of the first discharging mold (55) is set at 40 ℃ at 120 ℃, 110 ℃, 100 ℃, 90 ℃, 80 ℃, 70 ℃, 60 ℃. Wherein the first to seventh temperature areas and the first discharging mold (55) are controlled by a mold temperature machine (316).

The double-screw extruder adopted by the three-stage screw extruder (33) for producing particles is characterized in that 7 independent barrels are configured in a modularized barrel, 7 independent temperature areas are set, and the temperature settings of the temperature areas are respectively as follows: 130 ℃, 120 ℃, 100 ℃, 90 ℃, 80 ℃, 70 ℃, 60 ℃, and the temperature of the second discharging die (61) is set to 40 ℃. Wherein the first to seventh temperature areas and the second discharging mold (61) are controlled by a mold temperature machine (316).

The die mandrel plate (51) and the discharge die I (55) of the tube system (5) are machined in size: diameter size of the die mandrel: phi 6.6mm, diameter size of the discharging hole: phi 8mm, die mandrel and number of discharge holes: 144.

And a second discharging die (61) of the granulating system (6) is used for processing the size: diameter size of discharge hole: phi 2mm, number of discharge holes: 259.

The secondary screw extruder (32) and the tertiary screw extruder (33) synchronously work to synchronously produce 144 three-color disposable straws with the outer diameter of 8mm, the wall thickness of 0.7mm and the length of 300mm and polylactic acid modified material particles with the diameter of 2mm and the length of 2 mm.

And (3) replacing discharge dies of the tube system (5) and the granulating system (6) according to the requirements, and producing various tubes such as various plastic tubes, medical catheters, disposable straws, stirring rods and the like in a large scale.

Example 3. A mechanical device for simultaneous production of a plurality of single multi-colored tubes and modified material particles using a plurality of feed ports, the process comprising:

Drying modified starch in vacuum drying chamber at 60deg.C for 5min by screw forced feeding device (12) of buffer bin (11)

Stirring and conveying (14), pushing by a screw forced feeding device II (221) of a first feeding hole (21) of a feeding hole module (2), mixing with a modified material injected by a plunger type high-precision metering pump I (221) of a second feeding hole (22) of the feeding hole module (2) under high pressure metering, mixing with a compatible material injected by a plunger type high-precision metering pump II (231) of a third feeding hole (23) of the feeding hole module (2), compatible modification under the condition of 70-100 ℃, exhausting, mixing with polyhydroxyalkanoate of a screw forced feeding device III (242) of a fourth feeding hole 24 of the feeding hole module 2, curing under the condition of high temperature and high pressure and high shearing at 130-160 ℃, extruding to two synchronously working secondary screw extruders (32) and three-stage screw extruders (33) by the primary screw extruder (31), and synchronously producing a plurality of single multi-color objects and modified material particles. Wherein:

1. the secondary screw extruder (32) is provided with a multicolor mixing system (4) and a tube system (5), and the flow is as follows: the cured materials are vacuumized in a molten state, flow distribution system (41) of a multicolor mixing system (4), color injecting machine barrel (42), mixing machine barrel (43), flow guiding system (44), first mixed materials, second mixed materials and third mixed materials, enter into a first material groove, a second material groove and a third material groove, pass through a tubular material channel, cross fusion reaction, an antistatic annular cooling ring machine head die sleeve (561), extrusion of a tubular material, an antistatic annular cooling ring shaping sleeve (562), traction, rotary cutting, sterilization and packaging, and 200 six-color stirring rods with the outer diameter of 6mm, the wall thickness of 2.5mm and the length of 200mm are obtained.

The three-stage screw extruder (33) is provided with a granulating system (6), and the flow is as follows: the cured material is vacuumized, subjected to granulation extrusion, subjected to traction, subjected to rotary cutting, subjected to fine particle sterilization and packaged in a molten state, and subjected to granulation extrusion, subjected to antistatic annular cooling ring shaping sleeve II (622), subjected to sterilization, and subjected to packaging, so that polyhydroxyalkanoate PHA modified material particles with the diameter of 4mm and the length of 3mm are obtained.

The primary screw extruder (31) adopts a multi-shaft screw extruder, the secondary screw extruder (32) adopts a single screw extruder, and the tertiary screw extruder (33) adopts a double screw extruder.

The multi-shaft screw extruder adopted by the primary screw extruder (31) is characterized in that a modularized machine barrel is provided with 9 independent machine barrels, 9 independent temperature areas are set, and the temperature areas are respectively set as follows: 60 ℃, 65 ℃, 70 ℃, 75 ℃, 90 ℃, 120 ℃, 160 ℃, 150 ℃, 140 ℃. Wherein the temperature of the first temperature zone to the ninth temperature zone is controlled by a mold temperature machine (316).

The single screw extruder for producing the tubular objects by the secondary screw extruder (32) is characterized in that a modularized machine barrel is provided with (5) independent machine barrels, and (5) independent temperature areas are set, wherein the temperature areas are respectively: 130 ℃, 120 ℃, 100 ℃, 80 ℃, 60 ℃, and the temperature of the first discharging mold (55) is set to 40 ℃. Wherein the first to fifth temperature areas and the first discharging mold (55) are controlled by a mold temperature machine (316).

The three-stage screw extruder (33) is used for producing particles, a double screw extruder is adopted, 7 independent barrels are configured in a modularized barrel, 7 independent temperature areas are set, and the temperature settings of the temperature areas are respectively as follows: 130 ℃, 120 ℃, 110 ℃, 100 ℃, 80 ℃, 60 ℃, 50 ℃ and the temperature of the second discharging die (61) is set to 40 ℃. Wherein the first to seventh temperature areas and the second discharge mold (61) are controlled by a mold temperature machine 316.

The die mandrel plate (51) and the discharge die I (55) of the tube system (5) are machined in size: diameter size of the die mandrel: phi 1mm, diameter tu of discharge hole: phi 6mm, number of die core shafts and discharge holes: 200.

And a second discharging die (61) of the granulating system (6) is used for processing the size: diameter size of discharge hole: phi 4mm, number of discharge holes: 180.

The secondary screw extruder (32) and the tertiary screw extruder (33) synchronously work to synchronously produce 200 six-color stirring rods with the outer diameter of 6mm, the wall thickness of 2.5mm and the length of 200mm and PHA modified material particles with the diameter of 4mm and the length of 3 mm.

It should be noted that, in view of the above 3 embodiments, the foregoing is a further detailed description of the present invention with reference to specific embodiments, and it should not be construed that the specific embodiments of the present invention are limited thereto, and those skilled in the art, under the above guidance of the present invention, may change the type or model of the apparatus by expanding the combination of the combination modules of the screw extruder, increase or decrease the number of related designs or make various improvements and modifications, and these combinations, changes in type or model, increase or decrease the number, various improvements or modifications fall within the scope of the present invention.

Claims

1. A mechanical device for synchronously producing a plurality of single multicolor tubular objects and modified material particles by adopting a plurality of feed inlets is characterized in that: comprises a drying module (1), a feed inlet module (2), a screw extruder combined module (3), a multicolor mixing system (4), a tube system (5) and a granulating system (6);

The drying module (1) comprises a first buffering bin (11), a first spiral forced feeding device (12), a vacuum drying chamber (13), a stirring and conveying device (14) and a mold temperature machine (316); the first buffer bin (11) is connected with a first spiral forced feeding device (12), the first spiral forced feeding device (12) is connected with a vacuum drying chamber (13), and the vacuum drying chamber (13) is connected with a stirring conveying device (14); the vacuum drying chamber (13) is provided with a temperature control channel connected with a mold temperature machine (316);

the feed port module (2) comprises a first feed port (21), a second feed port (22), a third feed port (23), a fourth feed port (24) and an exhaust device (25); the first feed inlet (21) is connected with a first machine barrel (3131) of the primary screw extruder (31), and is suitable for powder materials, granular materials or mixed materials of powder and granules; the second feed inlet (22) is connected with a second machine barrel (3132) of the primary screw extruder (31), and is suitable for liquid or semisolid flowing materials; the third feed inlet (23) is connected with a fourth machine barrel (3134) of the primary screw extruder (31), and is suitable for liquid or semisolid flowing materials; the fourth feed inlet (24) is connected with a sixth machine barrel (3136) of the primary screw extruder (31), and is suitable for powder materials, granular materials or mixed materials of powder and granules; the exhaust device (25) is connected with a fifth machine barrel (3135) of the primary screw extruder (31), and the useless gas in the materials is discharged through the exhaust device (25);

The first feeding port (21) and the fourth feeding port (24) comprise a second buffer bin (211), a third buffer bin (241) and a second spiral forced feeding device (212), a third spiral forced feeding device (242), and the second feeding port (22) and the third feeding port (23) comprise a first plunger type high-precision metering pump (221), a second plunger type high-precision metering pump (231) and a first feeding device (222), and a second feeding device (232);

the multicolor mixing system (4) comprises a diversion system (41), an color injection machine barrel (42), a mixing machine barrel (43) and a diversion system (44);

the distribution system (41) comprises 2-16 distribution channels, each distribution channel is connected with the color injection machine barrel (42), and materials enter the 2-16 color injection machine barrels (42) through the distribution channels;

2-16 material channels are arranged in the color injection machine barrel (42), the mixing machine barrel (43) and the diversion system (44), a color injection port (421) is arranged in each material channel of the color injection machine barrel (42), multicolor materials enter the material channel of the color injection machine barrel (42) through the color injection port (421), and enter the tubular object system (5) through the diversion system (44) after the mixing machine barrel (43) and main materials are fully mixed;

The granulating system comprises a second discharging mould (61) and a second antistatic annular cooling ring sleeve combination (62);

1-500 discharge holes are processed in the second discharge die (61), and the discharge holes are uniformly arranged on the second discharge die (61); the diameter size range of the discharging hole is as follows: 1-10 mm;

the second anti-static annular cooling ring sleeve combination (62) comprises a second anti-static annular cooling ring head die sleeve (621) and a second anti-static annular cooling ring shaping sleeve (622), the second anti-static annular cooling ring head die sleeve (621) is arranged on the discharging die, the discharging die is controlled to be cooled very fast, the second anti-static annular cooling ring shaping sleeve (622) is arranged between the second discharging die (61) and the traction system, and produced modified material particles are controlled to be cooled very fast;

2. The mechanical device for simultaneous production of a plurality of single multi-colored tubulars and modified material particles using a plurality of feed ports of claim 1, wherein: the screw extruder combination module (3) is divided into three stages, namely a first-stage screw extruder (31), a second-stage screw extruder (32) and a third-stage screw extruder (33);

The screw extruder comprises a single screw extruder, a double screw extruder and a multi-shaft screw extruder; according to the preparation requirements of different products, the screw extruder combination module (3) is provided with the following combination modes:

combining: the primary screw extruder (31) is a double screw extruder, the secondary screw extruder (32) is a single screw extruder, and the tertiary screw extruder (33) is a single screw extruder;

and (2) combining two: the primary screw extruder (31) is a double screw extruder, the secondary screw extruder (32) is a double screw extruder, and the tertiary screw extruder (33) is a double screw extruder;

and (3) combining three: the primary screw extruder (31) is a double screw extruder, the secondary screw extruder (32) is a single screw extruder, and the tertiary screw extruder (33) is a double screw extruder;

combination four: the primary screw extruder (31) is a multi-shaft screw extruder, the secondary screw extruder (32) is a double-screw extruder, and the tertiary screw extruder (33) is a double-screw extruder;

and (5) combining: the primary screw extruder (31) is a multi-shaft screw extruder, the secondary screw extruder (32) is a single screw extruder, and the tertiary screw extruder (33) is a double screw extruder;

And (3) combining six: the primary screw extruder (31) is a multi-shaft screw extruder, the secondary screw extruder (32) is a single screw extruder, and the tertiary screw extruder (33) is a single screw extruder;

the single-screw extruder is provided with 5-7 sections of independent barrels to form a modularized barrel, the modularized barrel corresponds to 5-7 temperature areas, the modularized barrel is provided with single-screw holes and is provided with a single modularized screw, and the length-diameter ratio of the screw is 26:1-40:1;

the double-screw extruder is provided with 7-9 sections of independent barrels to form a modularized barrel, 7-9 temperature areas are correspondingly formed, the modularized barrel is provided with double-screw holes and two modularized screws, and the length-diameter ratio of the screws is 30:1-62:1;

the multi-shaft screw extruder is provided with 7-9 sections of independent barrels to form a modularized barrel, wherein 7-9 temperature areas correspond to the modularized barrel, and the modularized barrel is provided with a plurality of screw holes; a plurality of modularized screws are matched, and the length-diameter ratio of the screws is 30:1-62:1;

the independent machine barrel is provided with an independent temperature control channel, is connected with a mold temperature machine (316) and is an independent temperature zone;

the mold temperature machine (316) consists of a water tank, a heating and cooling system, a power transmission system, a liquid level control system and a temperature sensor;

the modularized screw (314) consists of a screw mandrel (3141) and a screw element (3142), wherein the screw element (3142) is provided with thread sections with different pitches and different lengths and matched elements, the screw mandrel (3141) and the screw element (3142) are connected through a spline, and the screw element (3142) is arranged on the screw mandrel according to the processing technology of materials and the arrangement sequence to form the modularized screw (314).

3. The mechanical device for simultaneous production of a plurality of single multi-colored tubulars and modified material particles using a plurality of feed ports of claim 1, wherein: the tubular object system (5) comprises a die mandrel plate (51), a first discharging plate (52), a second discharging plate (53), a third discharging plate (54), a first discharging die (55) and an antistatic annular cooling ring sleeve combination (56);

the die core shaft plate (51) is characterized in that 1-500 die core shafts (511) are uniformly fixed in the vertical direction of the plate surface, and the first discharging plate (52), the second discharging plate (53), the third discharging plate (54) and the first discharging die (55) are respectively correspondingly provided with 1-500 discharging holes;

the diameter size range of the die mandrel is as follows: 1-8 mm, and the diameter size range of the discharge hole: 6-12 mm;

the first discharging plate (52), the second discharging plate (53) and the third discharging plate (54) are respectively provided with a first material groove, a second material groove and a third material groove which are communicated with one side of each die hole, and the three material grooves are mutually independent and do not interfere with each other;

the first discharging die (55) is provided with a temperature control channel, is connected with a die temperature machine (316), and is used for controlling the temperature of the first discharging die (55) to be 40-80 ℃;

4. The mechanical device for simultaneous production of a plurality of single multi-colored tubulars and modified material particles using a plurality of feed ports of claim 1, wherein: the drying module (1) and the screw extruder combined module (3) are arranged in an up-down multilayer mode, the drying module (1) is located at the uppermost position, the first-stage screw extruder (31) is located at the center, and the second-stage screw extruder (32) and the third-stage screw extruder (33) are located at the lowermost position.

5. The mechanical device for simultaneous production of a plurality of single multi-colored tubulars and modified material particles using a plurality of feed ports of claim 1, wherein: the tube system (5) and the granulating system (6) are replaced according to the requirement, the discharging dies of the tube system (5) and the granulating system (6) are replaced, and the tubes are produced in a large scale, and the particles of biodegradable modified materials including polylactic acid PLA, polycaprolactone PCL, polybutylene succinate-adipate copolymer PBSA, polybutylene adipate/terephthalate PBAT, polyhydroxyalkanoate PHA, polybutylene succinate PBS, polydioxanone PPDO, polyglycolide PGA, polypropylene carbonate or carbon dioxide/propylene oxide copolymer PPC, carbon dioxide ethylene oxide copolymer PEC, cellulose acetate CA, starch St, bio-based polyethylene Bio-PE, bio-based polypropylene Bio-PP, bio-based nylon Bio-PA, bio-based polyurethane Bio-PUR and Bio-based poly furan dimethyl ester PEF are produced.

6. The mechanical device for simultaneous production of a plurality of single multi-colored tubulars and modified material particles using a plurality of feed ports of claim 1, wherein: is applied to the fields of industrial, medical, catering and daily plastics and degradation materials.