CN101578173B

CN101578173B - Mixture of synthetic material with wood particles

Info

Publication number: CN101578173B
Application number: CN2007800426106A
Authority: CN
Inventors: H·鲁斯特; H·萨斯
Original assignee: Novo Technology & Co KG GmbH; Rust & Mitschke Entex LLC
Current assignee: Novo Technology & Co KG GmbH; Rust & Mitschke Entex LLC; Entex Rust and Mitschke GmbH; Novo Tech GmbH and Co KG
Priority date: 2006-11-15
Filing date: 2007-10-22
Publication date: 2013-09-18
Anticipated expiration: 2027-10-22
Also published as: DE102006054204A1; CN101578173A

Abstract

According to the invention, mixtures of wood particles, plant particles and synthetic material are produced in an extruder such that the synthetic material is separately transformed into a hot melt form before introduction takes place.

Description

Synthetic material mixes with wood particles

Technical field

The present invention relates to mixing of synthetic material and wood particles or other plant particle or similar particle.In addition as long as only refer to timber or only refer to wood particles, in that just is included in other plant and plant particle.

Background technology

Synthetic material of many uses:

Drip molding, workpiece, ingot blank, panel, film, track, cover layer, pipe, flexible pipe, rod, bar, section bar, band, rope, wire rod, bristle, net;

Adhesive, lacquer, sizing material, paste, putty, binding agent;

Pigment, mortar, spatula, cast and encapsulant, fusion and coating material, gel;

Line, fiber, yarn, silk, hank knotting, mat, toison, fabric.

Synthetic material can be made by monomer and/or polymer.It often is mixture, wherein also mixes as synthetic material with other material.This is particularly useful for the manufacturing of synthetic material foam.

For synthetic material is handled, preferably use squeezer.The material fusing that utilizes squeezer to make to pack into, mix homogenising and disperse in other words highly beneficially.

In addition, can simultaneously charging (Einsatzgut) be heated or cool off.For heating or cool off, in the squeezer overcoat and also in main shaft, use cooling line heating pipe line in other words in case of necessity.In addition, the distortion that is applied to described charging by described squeezer main shaft causes and adds thermal effect significantly.

In squeezer, very difficult material is mixed mutually.Timber and synthetic material belong to the material that is difficult to mix.Timber is sent in the squeezer with comminutions and is synthesized material there at this and wrapped up.In order to cause parcel, synthetic material is plastified strongly.This carries out under corresponding heating and pressure.But, the poor effect that heat is passed from timber.In addition, timber contains hole degree height.According to suggestion early, find a kind of danger, namely synthetic material is pressed in the pore by hypergeometric routinely and distributes unevenly and do not wrap up wood particles all sidedly.

Timber-synthetic material mixture is also referred to as substitute for wood.

Timber is applied in various fields.Furniture, inside fitting, exhibition apparatus even automobile-plaque all belong to such field.

Aspect furniture, can be divided into timber and only also be used to form positive furniture as furniture or the timber of structural material.In upholstered furniture, the timber majority is only as structural material.Usually all upholstered furnitures all have solid substructure, for example have framework, are called carriage again.Take a seat face, backrest and handrail and base of optional installation in described carriage or on the carriage.Optional described carriage also directly forms the described face of taking a seat, backrest and handrail or opposite.Making the employed material of described framework is described structural material.

Traditionally, the framework that is used for upholstered furniture is made by timber.Use plank and wooden stick at this.The advantage of timber is, each parts can strike that hobnail (Tackern) is connected to each other and are connected with liner and liner bag decorations by so-called.The clip of U-shaped is used for striking hobnail.Clip has replaced early stage bullen-nail.

Other furniture shows that timber is as positive and trim decorative cover in other words.A consequent requirement part is only satisfied by specific rare wood seed collecting class.Rare timber is relatively more expensive.Therefore cutting plaque by the rare timber that forms the front for a long time belongs to prior art.Plaque comprises wood chip thin, the film shape.At this, if process plaque as wooden growth, a large amount of waste materials appears then.

Mixing by timber and synthetic material produces favourable substitute for wood.Replacing wood also can use other comminuted plants.Can select for use synthetic material and timber and other additives to make extrudate foaming or that do not foam.When the timber share in extrudate is hanged down, relate to arrangement of reinforcement (Armierung) or timber is used as filler.In the U.S., if the timber share in the mixture reaches 50% weight quota, then relate to substitute for wood.Very general in the U.S. such as the plank of being made by the mixture of timber and synthetic material that has illustrated mixing share.American market is accepted this point.WO02/103113A shows a kind of for the embodiment at the common mixture of the U.S..

The European market is only just accepted substitute for wood during basically close to timber in the outward appearance of material in visibility region.Need 70% to reach higher timber share at this.Certainly so far also can't with a kind of such material realization lasting with flawless applications.

Use other plant part such as the situation of straw for replacing wood, similar with the situation of using timber.Plant part partly has the intensity less than timber.As long as strength problem is very important, that just should come by the variation of mixture this is taken in.As other plant part, also can use the hay of whole wheat granular and pulverizing.

Suggestion according to early should reduce the synthetic material share in the extrudate as far as possible.At this, be devoted to the timber share of 60 to 95 weight percent points in the extrudate about mixture.The performance number that should depend on the regulation of mixture share, processing situation and mixture adds best synthetic material share.

According to this suggestion early, the size of plant particle depends on the trafficability characteristic of the particle in the squeezer when using common squeezer Determine.Depend in the squeezer gap of movable squeezer parts and the opening degree in nozzle slit is determined described trafficability characteristic at this.Described trafficability characteristic can be determined by means of known machine data.Then can determine the size that concerning corresponding squeezer, allows of plant particle.For security reasons, can select the size of described plant particle less than above-mentioned trafficability characteristic.

According to this suggestion early, scheme also can make the trafficability characteristic of squeezer and desired particle size be complementary as an alternative.This carries out in the process such as the axle sleeve in replacing squeezer worm screw, nozzle or the squeezer shell at coming of new squeezer or replacing parts.The squeezer that conforms with the epoch has axle sleeve in the squeezer shell, worm screw is just rotated in this axle sleeve.

As synthetic material, consider the synthetic material that all can push, especially polyethylene (PE), polystyrene (PS), polyurethane (PU) and polypropylene (PP).Especially preferably use PE.

Increase the adhesive force agent can to synthetic material and plant particle in other words and the adhesive force that lacks between the timber compensate.

Material to be connected is arranged is that interface between the synthetic material forms the molecule bridge here being in to increase the adhesive force agent.

As long as also use other filler or arrangement of reinforcement/reinforcement such as glass fibre, so described increase the adhesive force agent can also bear improve and these other material between the task of adhesive force.Increase the adhesive force agent and can be VC (vinyl chloride)-copolymer, can polymerization polyester or the rare nitrile-methacrylic acid of ethene-third-copolymer

Phenolic resins, rubber derivative or do not contain or contain PF (phenol-formaldehyde) resin or the acrylic resin of EP (epoxy) resin.

As increasing adhesive force agent also known EVA (ethene-vinyl acetate-copolymer) usually; Make described plant particle have hydrophobicity and that is to say that this way of reduction surface tension also may be enough.

Traditionally synthetic material is added in the squeezer with plant particle and additives as pellet.Optional described pellet has comprised synthetic material and accrete mixture.

Can humidity be reduced to every kind of yardstick desired concerning extrusion process by drying.Always do not expect minimum water capacity at this, but the specific water capacity of optional expectation utilizes this water capacity can influence the characteristic of extrusion process and/or extrudate.

For extruding, the twin worm squeezer is considered to advantageous particularly so far, because these squeezers have:

The very high effect of sending into

Extraordinary pressure forms effect.

Advantageously, squeezer can by different elements in other words the section of different structure form.Therefore, for plasticizing zone, can use there favourable twin worm squeezer version element and can this element is combined with other the version that has advantage there in other squeezer district.Such as can use single worm screw squeezer section in the injection region, utilize this list worm screw squeezer section can advantageously produce pressure and form effect.Other section is then more suitable for mixing and homogenising.

Synthetic material fusing under pressure and temperature.In other process that the charging of being undertaken by squeezer mixes, mixture obtains uniform treatment.For homogenising district and dispersive region, advantageously, use the squeezer element that has big combined power there.This is such as being the element with version of planetary roll pressed device.This element has high cooling effect simultaneously, utilizes this cooling effect can very accurately control processing temperature.By floristics timber kind and obtain the optimal process temperature that other is used for liquation by synthetic material in other words.This temperature can be such as until 200 degrees centigrade when being 15 minutes in maximum residence time (thermic load duration).The duration more in short-term maximum temperature be higher than when longer in the duration.

When further extruding, can be divided into the extruding of the synthetic material of the extruding of the synthetic material of foaming not and foaming.

In these two kinds of extrusion processes, can expect specific water capacity.Residual moisture can be used as lubricant.Residual moisture also can enter in the chemical reaction.Such as moisture can enter and the lignin of plant particle between reaction in.Surprisingly, can cause better adhesion effect between timber and synthetic material thus.Suitable moisture content/content of lignin can be checked by the variation of moisture and the variation of content of lignin.The commercial lignin that liquid form also is provided usually.

If when extruding, do not expect to have water, can before extruding, deal with by the drying of plant particle so on the one hand.Scheme or replacement are dry as a supplement, can remove moisture after the evaporation process in squeezer in degassing procedure.Can be right after and after evaporation process, carry out degasification.This is exactly this situation at plasticizing zone usually.Carry out necessary heating there.This heating produces from deformation operation when plasticizing and is undertaken by the input of heat in case of necessity.Such as importing heat by the adjustment in the squeezer shell.

As long as expectation so, degassing procedure is carried out near before the extruding jet nozzle at the latest.

The prerequisite of degasification is to reduce melting pressure.

Also known, the transitional region between two squeezers is carried out degasification under the situation of two squeezers of use in tandem arrangement.

Also can in squeezer, carry out degasification.The step-down of necessity of liquation can be carried out with different measures, carries out such as the variation of the pitch by worm screw in the squeezer.

For carrying out degasification, also can be with liquation sucking-off and come delivery and send back to once again in the described squeezer by depassing unit from described squeezer.Connect the liquation pump at this by the centre and can simplify pressure control greatly.This also is applicable to and abuts against extruding jet nozzle (instrument) pressure before.Here can carry out uniform treatment by the liquation pump to pressure extraly and improve the quality of extrudate thus.

Timber share in the mixture is more high, and the danger that material no longer is suitable for applications is just more big.Material known through after some times owing to continuous frost/dew alternation decomposes.Other shortcoming of material known is superproportional expansion, and this causes too big damage easily or must take in superproportional expansion slit.

In addition, the wearing and tearing of extrusion equipment have been improved along with the increase of timber share.Wearing and tearing have then reduced the economy of equipment.

Summary of the invention

Therefore, task of the present invention is to improve by the mixture of wood particles or other plant particle and make substitute for wood.Especially should make the material with better timber outward appearance, the economy that should use material in the open air and should improve equipment by the reduction of wearing and tearing.As long as refer to timber in addition, in the plant particle of the scheme as an alternative that just will be referred to above is included in.The better timber outward appearance desired with respect to Unite States Standard causes that at least 60 weight percent put preferred 65 weight percent points or higher timber share plant share in other words.

In by the method for in extrusion equipment, making the mixture that is constituted by wood particles and/or other plant particle and synthetic material of the present invention; a) described extrusion equipment has the charging part; be arranged in the squeezer and the parts that are configured to planetary roll pressed device or planetary roll pressed device section of side; b) wherein; described wood particles and/or other plant particle are added in the described charging part; c) add to and with the synthetic material particle and describedly describedly to be arranged in the squeezer of side and not rely on described wood particles subsequently and/or the liquefaction of other plant particle is the synthetic material liquation for synthetic material is not relied on; d) wherein; described synthetic material liquation is packed in the described parts that are configured to planetary roll pressed device or planetary roll pressed device section; the described parts that are configured to planetary roll pressed device or planetary roll pressed device section have wood particles and/or other plant particle that is in its inside; e) wherein; described wood particles plant particle in other words accounts for 60 weight percent points at least in mixture; f) and with described synthetic material liquation and described wood particles and/or other plant particle in the described parts that are configured to planetary roll pressed device or planetary roll pressed device section, mix mutually and uniform treatment; g) and subsequently mixture is sent from the described parts that are configured to planetary roll pressed device or planetary roll pressed device section; h) wherein, described mixture is compressed.

According to the present invention, by in planetary roll pressed device or planetary roll pressed device section, synthetic material being mixed to realize significant method improvement with wood particles mutually with other plant particle.

Simultaneously following understanding is opposed with described application, namely high timber share in other words high plant share in the planetary roll pressed device that for this reason arranges or planetary roll pressed device section, cause heavy wear.

Preferably reduce wear in the following manner, be synthetic material at least under the situation of separating with timber and optionally also plastify causing under the situation that the additives of wearing and tearing separates with other of mixture, and be ejected into subsequently in the wood particles stream and to mixture and carry out uniform treatment and extruding.

Belonging to described in addition accretely has: pigment, be used for improving the adhesive force between synthetic material and timber couplant (Koppler), be used for reducing lubricant, water-repelling agent, the stabilizing agent of the friction of squeezer.

In addition, in US6479002B1, also mention, under the situation of separating with wood particles and other plant particle, make the synthetic material fusing and flow to described wood particles or other plant particle subsequently.But this is not for the wear problem that solves on the planetary roll pressed device, but the solution relevant with the special drying of timber or other plant particle.Make the unnecessary water content evaporation of described wood particles or other plant particle by compression at this.Subsequently should the sucking-off water vapour.Sucking-off is reduced to prerequisite with pressure.

In this regulation, repeatedly repeat the compression process with pressure leak process, until reaching desired degree of drying.

Such drying is improper for purposes of the invention.

FR-A-2564374 demonstrates the situation of using auxiliary squeezer except main squeezer.The task of described auxiliary squeezer is, in the described main squeezer of regenerant feed-in.At this, those skilled in the art will appreciate that the regenerant that always allows small percentage with respect to the amount of the new synthetic material in the main squeezer.By means of described auxiliary squeezer weight feed well.But the synthetic material fusing that is used in timber-synthetic material mixture individually is used for the wear problem this point of the planetary roll pressed device of solution then not to be illustrated.

EP1262294A1 does not provide solution for wear problem yet.In the disclosure document, illustrated by timber-synthetic material mixture and made foam.

Therefore do not provide the method for the independent fusing synthetic material that will mention in the document for the enlightenment that solves the wear problem on the planetary roll pressed device by above-mentioned open source literature yet.

Synthetic material is mixed mutually with additives and melt and make liquation mixture homogenising.Next mix with timber.

By uniform treatment, synthetic material is distributed on the wood particles equably.Advantageously, liquation is liquid for said process.Every kind of thermoplastic synthetic material has a fusing point and a point is arranged on this fusing point, and synthetic material is gaseous state and/or carry out chemical reaction in this point.Synthetic material gradates the state into gaseous state on a point, and this point depends on environmental pressure.Therefore fusion temperature (is in concerning PE-LD between 105-118 degree centigrade such as be in 100 to 135 concerning polyethylene (PE) between by the characteristic of synthetic material, concerning PE-MD, be between the 120-125 degree, concerning PE-HD, be between the 126-130 degree, being in concerning PE-UHMW between the 10-135 degree, is 126 degree concerning PE-LLD).Under corresponding pressure, fusion temperature (Massetemperatur) possibility much higher (concerning PE-LD, be between the 160-260 degree, concerning PE-HD, be between the 260-300 degree, concerning PE-HD-UHMW, be between the 240-300 degree).

By the extruding of wood particles, reduce its cavity at least significantly.Preferably cavity/the pore in the timber is reduced at least 10% of its initial volume, preferably reduced at least 20% of its initial volume.Also optional described wood particles is further compressed, such as reducing at least 40% of its initial volume.This is undertaken by the compression of plant particle in other words of described wood particles.At least from the teeth outwards compress.By compression minimizing synthetic material consumption from the teeth outwards, need described synthetic material consumption between particle, setting up enough connections and being used for moisture absorption and the expansion of particle are reduced to the yardstick that allows concerning corresponding application at this.

Observe this way of specific granular size and have similar effect.

The preferred chip that has less than 1 millimeter particle size that uses further preferably is less than or equal to 0.8 millimeter particle size.Employed chip has diversified particle.The great majority of preferred chip are in 0.3 to 0.4 millimeter particle size.Described great majority refer at least 50% of chip, preferably at least 60%.

Timber is compressed with for the manufacture of the mixture that is made of timber and synthetic material, and this would have been the theme of suggestion early.In described suggestion early, before converging with synthetic material, make wood particles carry out granulation (pelletieren).The use of pellet is preferred for enlarging the timber share in mixture, such as expand the share that surpasses 80 weight percent points in mixture.At this, pellet has been simplified wood particles has been pulled in the squeezer.That is to say that described pellet enters into the charging hopper of squeezer easily.Described pellet also can easily measure.But pellet does not stand severe tests in practice, because exist such danger, i.e. and pellet not fully division in squeezer, if but after being shaped, mixture make its tide saturating afterwards, then decompose.Described danger is much bigger when externally described material is used in the zone, if always stood frost/dew alternation again and again by the saturating pellet of tide in mixture.

When granulation, also pushing timber and reducing cavity in the timber, but this with carry out before the synthetic material liquation contacts.

In by method of the present invention, demonstrate good resistivity at frost/dew alternation surprisingly and demonstrate much smaller expansion character, use with the liquation contact before produced pellet the time opposite situation then appears.

According to the present invention, according to handling with modes different in the suggestion of the described pulverizing that does not have big pellet and necessity thereof early, but breaking through the scope of its upper limit by the adding of littler particle, this upper limit makes to be crushed into and unnecessaryly becomes littler by the compression in the squeezer in other words.Have such danger for pellet, namely described pellet does not have again the nubbin of pulverizing fully and not pulverizing to enter into product, and synthetic material does not then enter between the particle that presses together each other.The moisture absorption of described pellet then causes expansion and causes the loss of particle key (Partikelbindung) in the pellet residue.

Preferably under the situation of timber being carried out preheating, synthetic material liquation and timber are converged by the present invention, make the flowability of described liquation not reduce because heat is transmitted on the timber significantly.

Preferably in planetary roll pressed device, in the planetary roll section of squeezer, timber and synthetic material liquation are converged in other words.Central principal axis, the planet main shaft of rotation and the shell of inner tooth punching in the middle of described planetary roll comprises.Described planet main shaft is meshed with the shell of described central principal axis and described inner tooth punching in rotation.Arriving wood particles and described synthetic material liquation between the tooth of described planet main shaft at this carries out exceptionally closely mixing and being extruded simultaneously.

In principle, only in squeezer, just wood particles is carried out preheating.Advantageously, before being added to wood particles in the squeezer, it is carried out preheating, because traditional device that is used for preheating only causes the fraction cost of squeezer.

The described mixture of preferred so selection leaves the outlet temperature of described squeezer, make the forming belt (Profilstrang) send have enough rigidity, be used for such as can the roller-way of the roller of close arrangement cools off having each other under the situation that disadvantageous distortion do not occur.But also can control higher outlet temperature, method is directly in the extruding jet nozzle back calibrator to be set.This calibrator is at the desired cross section that is equivalent to compressive zone (Extrusionsstrang) aspect the size of its reach through hole.But the contact-making surface of described calibrator and compressive zone obtains cooling, makes externally sclerosis and being fixed on the roller-way thus on the edge of compressive zone.

Described calibrator and described extruding jet nozzle are very similar.Described extruding jet nozzle also has opening, and the cross section of this opening is equivalent to the cross section of desired compressive zone.Described nozzle also preferably has cooler.As long as this cooler is enough to make the compressive zone of output to be fixed on the roller-way, so the calibrator on above-mentioned meaning just become unnecessary.On the contrary, the use of calibrator can be than the extruding jet nozzle economy with long especially cooling circuit of special form.

The preferred section bar that especially is forced out has extra high intensity and king-sized at the resistivity of moisture absorption and the stability of extra high anti-frost/dew alternation, mixes mutually with the synthetic material liquation immediately after wood particles is entering in the planetary roll section of described squeezer in described section bar and compressed between the parts of described planetary roll pressed device section subsequently.

Utilize following situation to explain the present invention, namely described liquation entered in the cavity/pore of timber before it is compressed in by method of the present invention at least in part described.In this case, described by method of the present invention in the compression advantageously cause described cavity/pore further to be filled up and seal.In known method, the compression of timber only causes narrowing down of described cavity/pore, though make the liquation of viscous no longer can or almost can not infiltrate in the cavity, water and especially steam also might infiltrate in the cavity very much.The moisture that infiltrates is the reason that causes expansion.The extreme loads that mixture when frost/dew alternation, can occur.Danger in this existence is that described mixture breaks when melting ice in other words because freezing.

With regard to method of the present invention, each feature itself is known with regard to described.But not with by combination of the present invention.

On this meaning, the manufacturing of mixture is disclosed from EP1297933A1, at first make synthetic material fusing during fabrication and it is mixed mutually with wood particles and stir.Subsequently mixture is flowed to squeezer and be pressed into plate.Relate to typical particieboard manufacturing at this.In particieboard is made, should carry out wetting to wood particles and compress subsequently with bonding agent.In the manufacturing of particieboard, chip is not pushed.Be typically, chip is stirred mutually with bonding agent in mixer.

On the contrary, extruding then is set described in by method of the present invention.Do not need extra mixer at this.Timber and the direct delivery of synthetic material quilt are in squeezer.Timber/synthetic material mixture is then sent from squeezer with the form of " unlimited " band.In addition, in known method, not only will consider more expense, and the stirring of liquid liquation also causes higher synthetic material share.

EP1262293A1 also comprises for the suggestion that mixes wood chip and synthetic material.Chip should have 0.5 to 20 millimeter width, 0.5 to 2.5 millimeter thickness and 1 to 50 millimeter length.Wetting for wood chip is carried out, produce the beam of liquid synthetic material and be distributed to wood chip in this beam and arranging that conveyer belt in its lower section produces material layer, carries out jam-packed to this material layer subsequently.Do not load wood chip to squeezer.Just to making synthetic material liquefaction squeezer is set.The suggestion of the disclosure does not surmount the known suggestion of explaining before this.This point is suitable equally, carries out wetting with synthetic material to fiber as long as refer in suggestion.

US-PS5653534 demonstrates a kind of for the method for synthetic material being strengthened with fiber.Synthetic material is placed the form of liquation.Then quantitatively import fiber.The product that produces have basically with not with the identical outward appearance of the synthetic material of strengthening lining.But, by in the method for the present invention, should produce the substitute for wood of the outward appearance with wood surface described.

In addition, have 60% and the processing of the timber/synthetic material mixture of the timber share of higher percentage compare with the processing of the fiber/synthetic material mixture with fiber share of 30% and propose much higher requirement.

Before extruding/compression by the present invention with timber when liquid liquation mixes, the temperature of mixing share is significant.The high temperature of liquation advantageously.Melt temperature is more high, the flowability of liquation with regard to more high and before timber is compressed liquation infiltrate better in its cavity/pore.Maximum melt temperature depends on material.Preferably keep safe spacing for this melt temperature and a specific temperature, liquation is converted into the state of gaseous state or produces chemical reaction when this specific temperature.Described safe spacing be chosen as described specific temperature at least 5%, be more preferably at least 10% and the most at least 15%, liquation is converted into the state of gaseous state or chemical reaction takes place when described specific temperature.

In addition, described melt temperature is subjected to the restriction of the characteristic of timber.By characteristic, the timber variable color that easy appearance is not expected when temperature is higher.

Press material and pressure, obtain the different processing temperature of liquation.Whether machining area completely or partially is fully used, and this depends on the temperature of employed timber and timber.When temperature is higher, produce the synthetic material of high fluidity.This means, describedly comprise strong liquefaction by plasticizing of the present invention.

The preferred the highest recovery synthetic material once that uses.The frequency of material recovery is more high, and is mobile just more poor for some synthetic material.The synthetic material that perhaps uses the mixture that constituted by new material and recycled materials to make, and it has at least and reclaims the identical flowability of material that is no more than once altogether.

In a word, further preferably use new synthetic material, rather than recycled materials.

Optional synthetic material is plastified with additives or after synthetic material plasticizing with additives is mixed mutually before wood particles mixes with synthetic material.Preferred pigments and increase the adhesive force agent and water-repelling agent belongs to these additives.

Wood particles is preferably used such as the form with sawdust with the form of chip.When converted timber, produce sawdust in large quantities.The size of sawdust is in the specific boundary simultaneously.Usually carry sawdust with compressed air.Utilize compressed air, can go up at an arbitrary position such as in charging hopper, carrying the wood particles that is in the wideer boundary.Usually produce compressed air under the situation of using air blast, described air blast is pressed into air in the transfer pipeline at side suction air and at opposite side.

At the destination county that wood particles is carried, compressed air must separate with wood particles once again.This is undertaken by suitable filter.But filter can not be separated every dust from compressed air in practice.Thin dust can enter in the environment more or less.

In other structure of the present invention, should reduce thin dust and overflow.Therefore be preferably and carry wood particles to use the suction air.Sucking the destination county that air is carried, as in the compressed air delivery, making wood particles and suck air separation with filter.

Optional timber is used with the form of preheating.Can be conducive to liquation through the timber of preheating and infiltrate in described cavity/pore because liquation when contacting with timber with respect to when timber is normal temperature in littler scope release heat.In addition, the preheating of timber causes drying effect.

The plasticizing of synthetic material can be carried out in different devices.It is contemplated that by batch ground and liquefy.The liquefaction that is preferably synthetic material arranges the pressure vessel through heating.By batch the method for operation allow when using a unique pressure vessel with a unique cavity, only to carry out desultory liquefaction process.But, utilize two pressure vessels then can carry out continuous liquefaction process.This is equally applicable to a unique pressure vessel with two liquation chambeies, can alternately fill and empty described two liquation chambeies at this.Preferably empty described pressure vessel by pump.Described pump not only is used for emptying fast.This pump also can form high pressure in liquation.

Preferably in squeezer, carry out the plasticizing of liquation.In squeezer, can control/regulate melt temperature easily.

As long as expectation is carried out preheating to timber, that just heats timber on another position concurrently.After heating, wood particles is mixed mutually with synthetic material, carry out above illustrated all even compressions and handle.

The heating of wood particles can single phase or the multistage carry out.With heat before synthetic material contacts.By temperature and the further processing situation of described mixture and the temperature control situation that causes thus of the liquation of carrying, the liquation that timber can pass through to carry and further processing are further heated or are obtained cooling off.The preheating of timber preferably is at least 50 degrees centigrade, further preferably is at least 100 degrees centigrade and most preferably at least 150 degrees centigrade.

Can select for use different heaters to come timber is carried out the multistage preheating.Every firing equipment can be continuously or is carried out work discontinuously.The firing equipment of continuous operation is such as being heating tape and/or tunnel heating.

Described heating tape is the ribbon conveyer that obtains heating, and wood particles obtains heating at this ribbon conveyer.Wood particles also can be carried in described heating tape under suitable heat radiation.At this advantageously, add shroud for described heating tape, be used for avoiding temperature loss.The difference of tunnel heating and heating tape is, be not conveyer belt is set but be provided with heater shroud and/or described shroud is passed in the heated air delivery.So select heating-up temperature, thereby concerning timber, avoid every kind of fire hazard/fire hazard.

Can in a container, carry out discontinuous heating, reach desired temperature until wood particles.The optional heat medium of gaseous state that makes flows through from described container.The heated air of inertia advantageously.The heated air of inertia can be such as importing in the described container with the temperature more much higher than air under not having the situation of fire hazard.

After wood particles is carried out desired heating, can open described container and wood particles can be discharged in order to mix with synthetic material from described container.

For mixing and the uniform treatment of timber and liquation, can use different blenders.Agitator also belongs to blender.Preferred described blender is worked under pressure, needs described pressure to be used for entering under the inlet temperature of described blender at this and keeps the liquation state to be used for being higher than the operating temperature of melt temperature in other words under blender/agitator remains on normal pressure.

If described preheating fully or is partly carried out in the squeezer section (module) in other words at squeezer, the mixing of synthetic material and timber then preferably is connected the squeezer of back or is connected in the squeezer section of back at another and carries out so.Each squeezer/squeezer section is provided with the material charge door and is used for the outlet of treated material.Described material charge door is on the end of described squeezer.Material is therefrom at the material outlet that is transported under the situation that stands desired processing on another extrusion head.

Preferably described wood particles is added in the charge door of described squeezer, wood particles mixes with synthetic material in described squeezer.Described synthetic material preferably plastifies in independent squeezer, and the pressure that in a single day formation is enough in the timber of packing into just is ejected into for the squeezer that mixes as liquation.When described squeezer being used for simultaneously timber heated, so select eject position, make bringing-up section be long enough to the temperature that reaches desired.

Different structural styles is disclosed for squeezer.

At this single worm screw squeezer, twin worm squeezer and planetary roll pressed device are arranged.Described single worm screw squeezer only has the worm screw that a velamen shell surrounds.Described twin worm squeezer has two parallel worm screws that are engaged with each other that are arranged side by side.Described worm screw can be rotated or reverse rotation in the same way.

Not only described single worm screw squeezer but also described twin worm squeezer all have multipart worm screw usually.In axial direction successively arrange that a large amount of axle sleeves, described axle sleeve have tooth portion outside and be provided with clear opening inside, make it to clamp mutually with pull bar at this.This structural style allows the twin worm squeezer is configured to mixer in desired length range.

Described planetary roll pressed device has the driven central principal axis in the middle of being arranged in.Arranging the planet main shaft round described central principal axis.Described planet main shaft is meshed with described central principal axis.

Described planet main shaft is surrounded by the shell of tooth punching inside.Described planet main shaft is meshed with the internal tooth portion of described shell.Each rotation of described central principal axis causes the rotation of described planet main shaft.Said planet main shaft rotates round described central principal axis just as planet.

Different structural styles also can make up.Elementary squeezer such as series devices can be made of single worm screw squeezer or twin worm squeezer, and secondary squeezer then is planetary roll pressed device.Described elementary squeezer and secondary squeezer can turn round with different rotating speeds.This has huge advantage.

Also can in a unique squeezer, carry out the combination of different squeezer systems.At this, the squeezer system of combination with one another forms the squeezer section in described squeezer.These sections can be consistent with the process section of described squeezer, but be not must be so.

When described process section is handled separately synthetic material in independent squeezer such as be the drawing in of synthetic material, melt, the homogenising/disperse of independent liquation.

Described process section in squeezer to timber/wood particles add man-hour such as be draw in, the injection of liquation, with the mixing of liquation, mixture homogenising, degasification and mixture is cooled to extrusion temperature.

The above-mentioned procedure of processing of timber/wood particles also can be carried out in the squeezers of two or more priority layouts.Arrange successively/connect that two squeezers refer to have the series devices of elementary squeezer and secondary squeezer.When successively arranging more squeezers, then relate to cascade device.

Described series devices and described cascade device are particularly suitable for to described mixture degasification.Said mixture sending into the mouth below the described discharge end of being arranged in of described secondary squeezer portion is entered by the discharge end clan of described elementary squeezer.

Between described elementary squeezer and secondary squeezer, also can arrange conveyer, such as ribbon conveyer.When using conveyer, described mixture can be fallen on the conveyer and with described conveyer level or inclination and down or in the ramp upwards carry.

From described elementary squeezer to the approach of secondary squeezer, can carry out degasification.Can under environmental pressure, carry out degasification.If should strengthen degasification, so can by low pressure should be used for carry out.Add shroud for the transport way from described elementary squeezer to secondary squeezer for this reason.

Not only in series devices but also at mixture described in the cascade device, in high temperature, be converted to especially extrudate of extruded product.Described high temperature will cool off the cooling that especially is cooled to environment temperature significantly and foreclose.According to the present invention, the mixture part as water-repelling agent may as described in produce before reacting in the mixture as described in extruded product.In addition, described mixture did not obtain the sclerosis of synthetic material before entering into the last squeezer of processing sections (such as the secondary squeezer of described series devices).Otherwise the mixture particle of sclerosis can break in secondary squeezer once again, and does not guarantee that the timber of described particle is enough to resist moisture absorption once again at rent.

As long as use the squeezer that is made of shell section/module during fabrication, that is just together fixed to one another with shell with flange in known manner, preferably is tightened on together each other.

Usually use simultaneously a common main shaft in this regard.Be extended to the zone that is configured to planetary roll pressed device/section such as described worm screw from the zone " processing of synthetic material " that is configured to single worm screw squeezer/section and " liquation be cooled to extrusion temperature ".Form described central principal axis common worm screw described in described planetary roll pressed device/section.

For different squeezer sections uses a common worm screw fairly simple concerning popular squeezer, because these worm screws are made up of axle sleeve, described axle sleeve is then passed by a common bar and clamps each other.This structural style also has other advantage.

Described squeezer section also often is configured in the squeezer shell.

Said shell section clamps each other with flange on the end.

Only refer to squeezer below, this not only comprises and identical or other the combination of squeezer, and is included in the combination by section of squeezer systems different in the squeezer.Comprise the combination of the squeezer section of identical system equally.

All popular squeezers all are provided with temperature-adjusting device (Temperierung).

For this reason, described squeezer is provided with axle sleeve inside.Described axle sleeve has passage outside, and described passage is as groove or as threaded line or be worked into as the worm screw line in the outer surface of described axle sleeve.Can process the described passage that is arranged in the outside by turning and milling with the machining form with comparalive ease at this.

The passage of so processing is enclosed in the smooth shell aperture in the inside.By described passage, optional along the liquation flow direction or be in reverse to liquation flow direction extruding cooling agent or thermophore.Optionally can produce bringing-up section and cooling section arbitrarily at this.Spiralization by described passage is over long distances and come the described thermophore of delivery cooling agent in other words along the outer wall of described axle sleeve in other words along the shell wall body controllably especially.This has guaranteed extreme cooling or heating.

Relate to bringing-up section or cooling section, this produces from corresponding method.Must or therefrom take heat away to the medium transport heat of percolation at this.

In theory, described passage also can be arranged on the inner surface of outer cover and described axle sleeve sidelight is sliding outside extends.

Described passage is worked into the shell inboard to bother than the way in the foregoing outer surface that is worked into axle sleeve.

In addition, advantageously, by shrinking described axle sleeve is installed in the squeezer shell.This heating by the squeezer shell is carried out.By heating, described squeezer shell obtains expanding.In this state, cold axle sleeve is pushed in the dead eye of described squeezer shell.In cooling subsequently, described squeezer shell shrinks and firmly and described axle sleeve is surrounded with sealing, if described axle sleeve has corresponding external dimensions and described shell aperture has corresponding inside dimension.When using so-called interference fit, produce a kind of such situation.In interference fit, described axle sleeve has and squeezer enclosure identical diameter or have than its slightly bigger diameter just outside at least.

So described known interference fit of design, thus the corresponding heating by described shell can separate described axle sleeve and described squeezer shell once again after shrinking, and can not damage associated components.Described separately is important, thereby where necessary the tooth portion in the described axle sleeve is reprocessed or change old axle sleeve with new axle sleeve.

What be preferably synthetic material/timber-mixture arranges squeezer by processing of the present invention, and this squeezer comprises the different sections of different structure pattern, that is to say to preferably include a single worm screw module/section and one or more planetary roll module.

At this advantageously, get described single worm screw modular design so long and it is heated, make the timber that loads on call when leaving described single worm screw module, reach desired temperature.Advantageously, described single worm screw module forms pressure simultaneously in timber, and described pressure forms and prevents that the synthetic material liquation court of spraying is used for the direction outflow of the charge door of timber.

Also advantageously, add the synthetic material of plasticizing to described single worm screw module and between other squeezer module that arranges synthetic material and mixing of timber by thrust ring or by spacer ring.

The common tubular shell that plays encapsulation belongs to each module section in other words.This module that is applicable to every kind of structure is section in other words.Described shell is provided with flange (flange) in each end.The shell of section and the shell that will be arranged on the transmission mechanism on the squeezer in case of necessity usually are fixed on the described flange in other words with adjacent modules.Described transmission mechanism belongs to the drive unit of squeezer.

The spacer ring of liquid synthetic material liquation of being provided for packing into can have different shapes.

This can be pipe fitting, and the shell of section is similar in other words with described single worm screw module except little axial length for this pipe fitting.Then this pipe fitting has flange equally on the end, utilizes described flange that described spacer ring is fixed on adjacent squeezer module in other words on the shell of section.Described spacer ring is extruded device worm screw/main shaft and therefrom passes.Described squeezer worm screw/main shaft is single worm screw in the zone of single worm screw section in described single worm screw module in other words, is central principal axis in the zone of described planetary roll module.

Described squeezer worm screw/main shaft is configured to many element structures usually.All parts have the axle sleeve shape, and the axle sleeve shape has tooth portion in the outside.Pass middle hole with tie-rod, the task of this tie-rod is that all axle sleeves are clamped together each other.In single worm screw module, described squeezer worm screw/main shaft majority is made up of a large amount of parts/axle sleeves, and described parts/axle sleeve has different tooth portions in the outside, and the compression that influences the charging of single worm screw module for the structure by the worm screw line is handled in other words.In described planetary roll module, the axle sleeve of single member is set usually, this axle sleeve forms described central principal axis and fixes with the identical tie-rod of the axle sleeve of fixing described single worm screw module.

Described tie-rod also extends through recited above for the spacer ring that sprays (Bed ü sung).In described spacer ring, on described tie-rod, be provided with axle sleeve equally.This axle sleeve can have in its end and the same or different tooth of single worm screw portion outside.Optional described spacer ring is to be provided with temperature-adjusting device with the identical mode of described squeezer module/section, and this temperature-adjusting device allows to cool off or heat as required.

Described spacer ring also can be installed under non-lipped situation.Then described spacer ring is placed between the flange of adjacent shell, just is placed between the shell of the shell of described single worm screw module and described planetary roll module.Subsequently, the flange under two clamps mutually by fishbolt or other clamping element.

Advantageously, spacer ring embeds adjacent shell in other words in the internal point of flange, and perhaps opposite, adjacent shell embeds in the internal point of described spacer ring.Described internal point can by spacer ring in other words the bore hole on the end face of adjacent shell constitute.At this, little bore hole can be enough.The projection that is located at accordingly on the corresponding opposed end face is corresponding with described bore hole.

For importing liquid liquation, in described spacer ring, preferably be provided with a plurality of charging apertures that distribute at circumference equably.Each pipeline can lead to different charging apertures.But also can connect described charging aperture by the cannelure in the spacer ring, described cannelure is sealed by cover plate and comes liquation to its feed-in liquid state by common transfer pipeline.

Described transfer pipeline will be connected with described spacer ring for the set squeezer of the liquefaction of synthetic material.Advantageously, described transfer pipeline is isolated and heated, in order to not desired temperatures decline or liquation in liquation, do not occur even solidify.

Can be selected in different leading in the transfer pipeline of described spacer ring valve or baffle plate are set, be used for regulating liquation stream.The optional permission of described valve is adjusted in running influences described liquation stream in other words.This can be used for difference is carried out that homogenising is handled or for generation of difference.As additional aspects or replace described valve, also can be by being positioned at the inserts in the described transfer pipeline

Realize the variation of liquation stream.Described inserts also can be arranged in the described spacer ring.

In addition, liquation is carried and is determined by the rotating speed of the squeezer that is provided for synthetic material is plastified.

In the optional described single worm screw module/section of also on the end of bringing-up section, the liquation of liquid state being packed into.Then the described squeezer that is provided for making liquid liquation is directly connected on single worm screw module/section that the heating for timber arranges.

Optionally connect in the following manner, just the squeezer that will be provided for liquefying directly is connected on the shell of described single worm screw module/section with flange, and transfer pipeline perhaps is set, and this transfer pipeline leads to the shell of described single worm screw module/section.

Directly with flange be connected on described single worm screw module and can be called the side arm squeezer for the manufacture of the squeezer of the liquation of liquid state.This squeezer can have and the identical structural style of single worm screw module.But also can use the squeezer of other structural style.

In described single worm screw module/section that the liquation of liquid state is packed into, must bore a hole to the shell of described single worm screw module/section.At this shell that is configured to double-walled construction in order to carry out adjustment is packed into eleven punch 11.In order on the one hand to make described liquation not flow in the hollow sleeve and to make the temperature regulato described liquation of not making dirty on the other hand, can mounting flange, this flange stretches in the described hole with a flange and again with described hollow sleeve sealing.

Be the liquation of the described liquid state of packing into, also can bore a hole to adjacent planetary roll module.

Also there are the two covers of shell there, open the two covers of described shell and necessary closed again by described hole.

According to DE10356423, this realizes in the following manner with axle sleeve, namely

Make described hole pass described shell and stretch in the axle sleeve that is in the shell,

Wherein the material input unit stretches in the described hole with the input shell, and

Aa) wherein said hole has the those widened sections of annular in the zone that is used for thermoregulator passage, thus round described input shell produce the interface channel that is used for described annular for thermoregulator passage or

Bb) wherein said hole is stretched in the groove always, on the whole circumference of the axle sleeve of this groove in being in described shell or the part of its circumference extend and the width of this groove greater than the diameter of described input shell, be used for described interface channel for thermoregulator passage thereby produce round described input shell

Perhaps

Cc) wherein use the input shell that stretches in the described axle sleeve, wherein said input shell is provided with at least one interface channel for these passages in described zone for thermoregulator passage.

Preferred described according to cc) interface channel can be worked into outside in the described input shell by milling or the turning mode with machining.

Preferred input shell is provided with many interface channels, makes each fracture that produces because of described hole of passage be connected passage and eliminates in other words and overlap.

The input shell that also further preferably has many interface channels of placing up and down.Each interface channel can be used as groove placed side by side and is worked in the described input shell.Described passage can be in the outside of described input shell.

At this advantageously, the described interface channel of placing up and down has the height less than width.So select the size of width simultaneously, make described interface channel have enough cross sections equally, be used for interference-free and continue the delivery temperature regulato, preferred described cross section is identical.Advantageously, so select the height of described interface channel, the height that makes described that place up and down and total height by the spaced interface channel of dividing plate be not more than to be used for thermoregulator passage in the axle sleeve is the degree of depth in other words.The preferred described passage of placing up and down can be used in the pipe box that outside described input shell is surrounded in this zone and seal.Then, the described pipe box that is in the outside is provided with hand-hole and portals.So arrange each hand-hole, make on the channel end that its fracture because of illustrated under being in produces.

The pipe box that the inboard and described interface channel that optional described interface channel also has been machined into described input shell is in the inside seals.By being worked into the hand-hole in the described input shell outside and portalling the same interface channel that produces.

Perhaps

Dd) wherein said hole is enlarged with respect to described input shell and wherein is provided with in described shell and has opening or have inserts for the joint of admitting described input shell.This inserts has the one or more of interface channels that are in the outside or are in the inside, and described interface channel is as at cc) described in interface channel constitute in other words and make.

Ee) wherein in described hole, place an inserts, described input shell is fixed on this inserts and this inserts has one or more and is in the outside or is in the interface channel of the inside, and described interface channel is as at cc) described in interface channel constitute in other words and make.

Above illustrated input shell can so run through the axle sleeve that is in the described squeezer shell, make that it is termination with the inner surface of described axle sleeve completely or partially.If the inner surface of described input shell and described axle sleeve is complementary, then can be fully be termination with the inner surface of described axle sleeve.This also can be applied on the axle sleeve of the inside tooth punching of squeezer shell.By turning or milling or grinding or when the shell axle sleeve with tooth punching inside is complementary, mate in the following manner, just in the shell wall body, to process tooth portion with the identical mode of internal tooth portion of axle sleeve in being in the squeezer shell.Advantageously use electron discharge to carry out tooth punching at this.

In addition, identical with the situation that is used for being connected on single worm screw module for the situation on the shell that will be connected to described planetary roll module for the manufacture of the squeezer of the liquation of liquid state.

Described side arm squeezer can have different structures.

At this single worm screw squeezer, twin worm squeezer and planetary roll pressed device are arranged.

Described single worm screw squeezer is the inexpensive structure form of squeezer, but also is the squeezer with minimum version.

When using single worm screw squeezer, the pitch of worm screw should cause desired conveying effect.

Described twin worm squeezer has two parallel be arranged side by side and worm screws of being engaged with each other.Though described twin worm squeezer is than single worm screw squeezer costliness.But described twin worm squeezer has the conveying effect more much bigger than single worm screw squeezer.Equally, described twin worm squeezer is also more favourable.In addition, the structure of described twin worm squeezer is also very little.Because high conveying effect can guarantee easily with described twin worm squeezer, is ejected in the described planetary roll module with the liquation of correct pressure with liquid state.

Also be chosen as this side arm squeezer and use planetary roll spare.In application, also can make this planetary roll spare so mobile, be used for spraying liquid liquation thereby produce essential pressure.

Description of drawings

In the accompanying drawings, Fig. 1 shows different embodiment of the present invention respectively to Figure 11.

The specific embodiment

Fig. 1 is the squeezer for the manufacture of the mixture that is made of synthetic material and wood particles.This squeezer has four sections.Three squeezer sections are configured to planetary roll pressed device section, and the 4th squeezer section is configured to single worm screw squeezer and is used for sending into material.

At this with 5 shells of representing described planetary roll pressed device section, and with 1 shell of representing single worm screw squeezer section.Each shell 5 has the flange 6 and 7 of welding, and described flange 6 and 7 is tightened on together each other with unshowned form.Described shell 1 is provided with flange 3 and 4, described flange 3 with 4 as described flange 6 and 7 usefulness that fix.Each shell 1 and 5 is lined with axle sleeve inside.

In addition, show passage inside the shell, load thermophore or cooling agent to described passage on demand at this.

The shown end of described shell 5 is bore hole in the back, and is respectively equipped with centering ring 11 and thrust ring and wear ring 8.

Described thrust ring and wear ring 8 are formed for the sliding surface of planet main shaft 10.Described thrust ring and wear ring 8 have the internal diameter littler than the rolling radius of indicating of described planet main shaft 10.

All squeezer sections have a common main shaft.The common main shaft of this root is represented with 9 in the zone of described planetary roll pressed device section and is represented with 19 in the zone of described single worm screw squeezer section as feeder.

Charging is made of wood chip in the present embodiment.Described wood chip quantitatively adds by opening 2 via funnel.Described wood chip in a not shown manner by means of suck that air feeder is extracted out from bunker and the filter of delivery above being arranged in described funnel in and separate with described suction air.By means of unshowned obstruction worm screw (Stopfschnecke) wood chip is drawn in the described funnel from filter.Amount to sawdust in funnel is carried out cubing.In other embodiments, extra weight measurement or weight measurement only is set is set.Regulate described suction air feeder by means of measurement result.

The described first squeezer section is formed for the feeder of the second squeezer section.In the described second squeezer section, carry out weight feed and mix with the synthetic material liquation of liquid state, and compress; In described the 3rd squeezer section, mixture is carried out uniform treatment.In last squeezer section, described mixture is cooled to outlet temperature.Timber has 70 weight percent points and synthetic material has 30 weight percent points in mixture in this embodiment.In other embodiments, the timber share is such as account for 65% or 75% in mixture.Additives such as pigment and water-repelling agent are added in the synthetic material share by calculating at this.

The mixture that produces enters in the unshowned extruding jet nozzle at most advanced and sophisticated 12 places of squeezer, and the opening of this extruding jet nozzle imitates the cross section on floor, thereby produces the unlimited compressive zone (Endlosstrang) of the cross section with floor by the extruding of mixture.Unshowned sizing by described compressive zone is sheared, and produces the floor of the outward appearance with wood floors.

Contoured is carried out at downside in described floor.So select described profile, thereby produce 10 millimeters wall thickness.Select 8 to 12 millimeters wall thickness in other embodiments.

Described contoured comprises cavity chamber formation in other words.

In Fig. 2, liquid liquation is provided with side arm squeezer 20 at planetary roll spare 5 in order to pack into.

Described side arm squeezer is configured to the twin worm squeezer.Described twin worm squeezer comprises the worm screw of two reverse work.In described side arm squeezer 20, add the synthetic material pellet with unshowned form, add polyethylene pellet in this embodiment, it is compressed and heat, and in this process, be deformed into the liquation of liquid state.Add additives such as pigment and water-repelling agent simultaneously with described PE pellet.In liquation, described additives obtains favourable distribution.

Utilize described twin worm squeezer, can be ejected in the described planetary roll spare 5 with the liquation of huge pressure with described liquid state.The liquation of described liquid state carries out wetting to the surface of wood particles, and infiltrates in cavity/pore.When subsequently wood particles being compressed, the cavity/pore that still keeps opening wide when spraying liquation reduces and is sealed by described liquation.Add described liquation with certain temperature, under this temperature, if described liquation by with the evolution of heat that contacts of described wood particles, then this liquation also still keeps liquid.

Between different wood particles, described liquation works as bonding agent.

The shell of described side arm squeezer 20 is manifold.Head part 21 is in the hole of shell of described planetary roll spare 5 as the input shell.Described hole under passing simultaneously axle sleeve 22 and be termination with the inner surface of described axle sleeve 22.

In this embodiment, described side arm squeezer is suitable for producing very high feed pressure.

In the embodiment in figure 1, be right after and after the material feeder, be right after in other words at charging part (F ü llteil) the planetary roll spare 5 shown in Figure 4 of packing into afterwards.In another kind of embodiment, described planetary roll spare 5 with side arm squeezer is used as the third line star formula roll spare after the second planetary roll spare.

In other embodiments, each planetary roll spare is provided be used to the side arm squeezer of sending into liquid liquation.

In a kind of additional embodiments of pressing Fig. 3, the squeezer shell that the usefulness 30 of described side arm squeezer is represented is stretched over shell 30 places of described planetary roll spare 5 always.Described squeezer shell 30 is connected with inserts (Einsatz) 31, and this inserts 31 is in the hole of described shell 5.Described inserts 31 has the

groove

32 and 34 that twice are placed up and down in its outside.Between described twice groove 32 and 34, dividing plate 33 is arranged.These grooves form interface channel.Be provided with two interface channels, because described shell is lined with axle sleeve 22 and is provided with tooth portion because of described axle sleeve 22 in the outside and inboard.Unshowned internal tooth portion is used for being meshed with the planet main shaft of rotation shown in Figure 1.Outer toothed portion is formed for the passage of temperature regulato, and described temperature regulato then is used for the heating/cooling of described planetary roll spare.The outer toothed portion of described axle sleeve 22 is interrupted by the affiliated hole that is used for described inserts 31 on two positions.Every interface channel is used for a fracture, and one of them fracture end is connected with affiliated another fracture end.

The pipe box 35 that described

groove

32 and 34 is in the outside seals, and does not flow into mistakenly or flows out thereby do not have any thermophore or cooling agent.

What show described groove 34 in this embodiment enters hole 37.The Kong Ze that advances of described groove 32 is on another unshowned position.The portal unshowned side of the diametrically contraposition that is in described inserts 31 in this embodiment.

Embodiment by Fig. 4 shows squeezer for the foam manufacturing.The working media of liquid state is pumped in the described synthetic material liquation by the inserts 40 that is in the described squeezer shell 5 at this.

Be provided with unshowned inserts in the zone of described axle sleeve 41, this inserts is with difference by the inserts of Fig. 3, only is provided with an interface channel.

Fig. 5 to 7 shows other squeezer, and this squeezer has the planetary roll module that has shell 101 and the side arm squeezer that connects with flange.

Described planetary roll module has the squeezer shell, and this squeezer shell has the axle sleeve that is arranged in its inside.Described shell hot pressing is sleeved on the described axle sleeve.

Described axle sleeve has the passage that is used for temperature regulato of milling in the outside, described temperature regulato then is used for cooling or heating.

Described passage helically produces in the outer surface extension of described axle sleeve and by milling.Two different temperature regulated zone are set in this embodiment.One of them zone represents that with inflow entrance and flow export 120,121 another zone is then represented with inflow entrance and flow export 122,123.

Described side arm squeezer is the twin worm squeezer and is made up of different parts.Two worm screws that are arranged side by side 116 belong to this side arm squeezer, and described worm screw 116 is engaged with each other and drives by motor.Between motor and worm screw 116, be provided with transmission mechanism and the clutch 111 with shell 115.In addition, described side arm squeezer is made up of charging part 109 and extrusion 102.Described charging part 109 has the opening for unshowned material input.

Described side arm squeezer has thermoregulator shell in extrusion 102.This shell has the end 104 of classification, and described shell is placed in the hole 103 with this end, and described hole 103 is passed the shell of described planetary roll spare 101 and passed affiliated axle sleeve and extends in the inner chamber of described planetary roll module always.Described hole causes the special guide effect of the passage that arranges for described temperature regulato in the outside of described axle sleeve in inflow entrance and flow export 122,123 zone.Described passage extends round the zone in described hole there, make described hole around also obtain adjustment.Extra is used for thermoregulator scheme in the acquisition on every side of the thermoregulator leading section of described side arm squeezer.

Top illustrated step is passed in described hole, the bearing-surface 102 on shell.

Fig. 8 to 10 has illustrated the complete device for the manufacture of the mixture that is made of wood particles and synthetic material in a kind of additional embodiments.

The squeezer that has charging part 201 and two planetary roll spares 202 and 203 in this use.Described charging part 201 has the structure of single worm screw and at single worm screw part that principle is equivalent to Fig. 1 part of feeding in other words.Described two planetary roll spares 202 and 203 are equivalent to the planetary roll spare 5 and 10 of Fig. 1 in principle.

From funnel 205 to described charging part 201 feed-in sawdust.Described wood particles is drawn in the described charging part and obtains preheating a little.

In addition, the squeezer 204 that is arranged in the side belongs to described equipment.The described squeezer 204 that is arranged in the side is single worm screw squeezers and is used for making the synthetic material fusing.The described squeezer that is arranged in the side is ejected into the liquation of liquid state in the described squeezer between described charging part 201 and planetary roll spare 202.

Between described charging part 201 and planetary roll spare 202, be provided with spacer ring.This spacer ring is shown in Figure 11.In Figure 11, with 211 represent the to feed shells of part 201 and with 210 shells of representing planetary roll spare 202.Two outer casing ends opposite each other are provided with flange 214 and 213.Between these two flanges, put into spacer ring 212.Described spacer ring 212 is placed in the internal point on the end face that is located at described flange.Described spacer ring 212 has a plurality of openings that are evenly distributed on the circumference, and liquation pipeline 216 leads to described opening from described squeezer 204.Described spacer ring 212 is clamped between described flange 211 and 213.Clamp by fishbolt, only show a center line 215 for these fishbolts.Described fishbolt run through two flanges and with the nut acting in conjunction.

After the liquation of liquid state and wood particles converge, in described planetary roll spare 202, mix with uniform treatment and compress.With planetary roll spare that this planetary roll spare is connected in be cooled to desired outlet temperature.In this embodiment, the temperature of described mixture is also so high, makes described mixture evaporation and lose the moisture of not expecting in this process.

Flow out and evaporation after, described mixture is distributed on a plurality of other squeezers in this embodiment.Be provided with distributor 220 for this reason.Described distributor 220 is arranged in the delivery to three of described mixture in single worm screw squeezer 221,222 and 223 of back.Can individually or a plurality ofly or all evenly or differently load mixture to these single worm screw squeezers together.Target is to push different or identical profile specification with described single worm screw squeezer 221,222 and 223 as required.

In this embodiment, described distributor constitutes by being located at the preselector (Weiche) that mixture leaves in the delivery stroke after the squeezer.Utilize this preselector can make desired mixture amount turn to or also can be divided into two strands or three bursts of tributaries towards specific single worm screw squeezer, relevant single worm screw squeezer is then given by delivery in described tributary.

Claims

1. in extrusion equipment, make the method for the mixture that is constituted by wood particles and/or other plant particle and synthetic material,

A) described extrusion equipment has charging part (201), is arranged in the squeezer (204) of side and is configured to planetary roll pressed device or the parts of planetary roll pressed device section (202,203),

B) wherein, described wood particles and/or other plant particle are added in the described charging part,

C) and add to the synthetic material particle in the described squeezer (204) that is arranged in the side and do not rely on described wood particles subsequently and/or the liquefaction of other plant particle is the synthetic material liquation,

D) wherein, described synthetic material liquation is packed in the described parts (202,203) that are configured to planetary roll pressed device or planetary roll pressed device section, the described parts (202,203) that are configured to planetary roll pressed device or planetary roll pressed device section have wood particles and/or other plant particle that is in its inside

E) wherein, described wood particles plant particle in other words accounts for 60 weight percent points at least in mixture,

F) and with described synthetic material liquation and described wood particles and/or other plant particle in the described parts (202,203) that are configured to planetary roll pressed device or planetary roll pressed device section, mix mutually and uniform treatment,

G) and subsequently mixture is sent from the described parts (202,203) that are configured to planetary roll pressed device or planetary roll pressed device section,

H) wherein, described mixture is compressed.

2. by the described method of claim 1, it is characterized in that using the wood particles plant particle in other words with the highest 1 millimeter particle size.

3. by claim 1 or 2 described methods; it is characterized in that; before described wood particles and/or other plant particle are compressed, mix the synthetic material liquation and/or additives was mixed with described synthetic material liquation before the plant particle mixes in other words with described wood particles, and/or by using through the wood particles of preheating plant particle in other words.

4. by the described method of claim 3, it is characterized in that described wood particles at least 50 degrees centigrade preheat temperature of plant particle in other words.

5. by the described method of claim 3, it is characterized in that at the described wood particles of outside preheating of described squeezer plant particle in other words.

6. by the described method of claim 1, it is characterized in that the cavity volume of described wood particles and/or other plant particle is reduced by at least 10% by compression with respect to initial volume.

7. by the described method of claim 1, it is characterized in that described synthetic material liquation mixes at the place that begins of planetary roll pressed device section in other words at described planetary roll pressed device.

8. by the described method of claim 1, it is characterized in that the synthetic material of liquefaction converges with described wood particles and/or other plant particle separately under pressure.

9. by the described method of claim 8, it is characterized in that, the synthetic material of described liquefaction is sprayed towards described wood particles and/or other plant particle.

10. by the described method of claim 1, it is characterized in that described mixture machine-shaping or mixture of being extruded out in high temperature are made into particle.

11. by the described method of claim 1, it is characterized in that, carry out the liquefaction of synthetic material continuously and for liquefaction, will assist squeezer or side arm squeezer as the described squeezer (204) that is arranged in the side

Perhaps

Synthetic material by batch be liquefied and by means of being pumped in the parts (202,203) that are configured to planetary roll pressed device or planetary roll pressed device section that arrange for mixing

And/or

Described for the shell of the squeezer that mix to arrange on and/or between the section of the described squeezer that arranges for mixing, pack into the synthetic material of described liquefaction.

12. by the described method of claim 1, it is characterized in that, add additives except timber and other plant and synthetic material with synthetic material.

13. by the described method of claim 1, it is characterized in that, single worm screw squeezer or single worm screw squeezer section usefulness acted on the charging part (201) of sending into described wood particles and/or other plant particle.

14. by the described method of claim 1, it is characterized in that using the squeezer that has the charging part that is configured to single worm screw and be arranged in the planetary roll spare of back, wherein, the synthetic material liquation of described liquid state in being arranged in the independent squeezer of side, make and described liquation at least in part

A) between described single worm screw part and planetary roll spare, install in the described squeezer,

B) install in the described planetary roll spare at the described place that begins that is arranged in the planetary roll spare of single worm screw part back.

15. by the described method of claim 14, it is characterized in that using spacer ring (212),

A) this spacer ring (212) imitates described charging part shell (201) and/or planetary roll spare and has flange, utilize described flange described spacer ring (212) to be fixed on the adjacent flange of described charging part (201) and on the adjacent flange of described planetary roll spare

Perhaps

B) described spacer ring is held individually between described planetary roll spare and the charging part (201), makes the adjacent flange of described planetary roll spare and the adjacent flange of described charging part (201) be clamped together.

16. by the described method of claim 14, it is characterized in that using spacer ring (212), described spacer ring (212) embeds in the internal point in the adjacent end face of described charging part (201) or opposite described planetary roll spare and charging part (201) embed in the internal point on the end face of described spacer ring (212).

17. by the described method of claim 11, it is characterized in that,

A) will assist squeezer or side arm squeezer to be used for the fusing synthetic material, described auxiliary squeezer or side arm squeezer are connected on the end of described charging part (201) or the beginning on place or the described spacer ring (212) of described planetary roll spare with flange

Perhaps

B) will assist squeezer or side arm squeezer to be used for the fusing synthetic material, described synthetic material is connected with the end of described charging part (201) by the liquation pipeline or is connected or is connected with described spacer ring (212) by described liquation pipeline with the place that begins of described planetary roll spare by described liquation pipeline.

18. by the described method of claim 17, it is characterized in that, with twin worm squeezer or twin worm squeezer section or single worm screw squeezer or single worm screw squeezer section with acting on auxiliary squeezer or the side arm squeezer that involutory one-tenth material melts.

19. by the described method of claim 1, it is characterized in that, after making mixture, make its evaporation and/or it is assigned on a plurality of single worm screw squeezers (221,222,223), wherein distribute on demand.

20. by the described method of claim 17, it is characterized in that in planetary roll pressed device or have in the squeezer of planetary roll spare making mixture,

Wherein, in the side arm squeezer, make the synthetic material liquation,

Wherein, concerning described side arm squeezer, hole is passed described squeezer shell (101) and is stretched in the axle sleeve in the described squeezer shell of being in of described planetary roll spare (101),

Wherein, input shell or pipe or inserts stretch in the described hole and

Wherein, have those widened sections in the zone of the passage of described Kong Zaiwei temperature regulato setting, thus between the described inwall that stretches into input shell in the hole or pipe or inserts and described hole, exist a spacing that forms cavity and described cavity will be in the past by described hole import in other words coolant channel that shell or pipe or inserts interrupt in other words the thermophore passage couple together.

21. by the described method of claim 20, it is characterized in that using squeezer shell (101), have groove in the zone of the passage that is used for temperature regulato on described squeezer shell (101) axle sleeve in being in this squeezer shell (101), inner tooth punching, this groove round the circumference of described axle sleeve on whole circumference or the part of circumference extend and its width greater than the diameter of described input shell or be used for the pipe of material input or the diameter of inserts.

22. by the described method of claim 21, it is characterized in that using squeezer shell (101), described squeezer shell (101) has and is in being provided with outside for the axle sleeve of the passage of temperature regulato and the hole of running through from the shell that is used for the input liquation of the inside, be provided with inserts in pass-through zone, this inserts has at least one interface channel that is used for the passage of delivery temperature regulato.

23. by the described method of claim 22, it is characterized in that using the squeezer shell (101) with the axle sleeve that is in the inside, described axle sleeve is provided with the passage for temperature regulato outside, and have the connecting hole for the side arm squeezer, wherein said passage for temperature regulato distributes round described connecting hole.

24. by the described method of claim 1, it is characterized in that using the spacer ring (212) that is positioned between charging part (201) and the planetary roll spare, wherein locate the liquid liquation of packing at spacer ring (212).

25. by the described method of claim 1, it is characterized in that described wood particles plant particle in other words accounts for 65 weight percent points at least in mixture.

26. by the described method of claim 2, it is characterized in that, use the wood particles plant particle in other words with the highest 0.8 millimeter particle size.

27. by the described method of claim 26; it is characterized in that; the wood particles plant particle in other words that uses major part to have 0.3 to 0.4 millimeter particle size, wherein, described major part accounts for described wood particles at least 50% share of plant particle amount in other words.

28., it is characterized in that described major part accounts for described wood particles at least 60% share of plant particle amount in other words by the described method of claim 27.

29. by the described method of claim 3, it is characterized in that described additives is pigment, couplant and increases adhesive force agent, stabilizing agent, lubricant and water-repelling agent.

30. by the described method of claim 4, it is characterized in that described preheat temperature is at least 100 degrees centigrade.

31. by the described method of claim 30, it is characterized in that described preheat temperature is at least 150 degrees centigrade.

32., it is characterized in that the cavity volume of described wood particles and/or other plant particle is reduced by at least 20% by compression with respect to initial volume by the described method of claim 6.