CN1096244A - The heating means and the device of the partly crystalline synthetic resins preform blanks made from injection moulding - Google Patents
The heating means and the device of the partly crystalline synthetic resins preform blanks made from injection moulding Download PDFInfo
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- CN1096244A CN1096244A CN 93106966 CN93106966A CN1096244A CN 1096244 A CN1096244 A CN 1096244A CN 93106966 CN93106966 CN 93106966 CN 93106966 A CN93106966 A CN 93106966A CN 1096244 A CN1096244 A CN 1096244A
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Abstract
A kind of heating means and heater that is used for the cold preform blanks of partly crystalline synthetic resins that injection moulding processes.Preform blanks is positioned in the clamper that is located on the conveyer belt, on conveyer belt move on one side around self longitudinal axis rotation on one side; By being heated to blow temperatures behind a plurality of stations, these stations comprise that several are located at the heating and cooling station of transmitting the both sides, road respectively, and blank in the mobile also rotary course, heats from conveyer belt one side on conveyer belt, from the opposite side cooling, thereby make the about evenly heating of preform blanks.Carry out temper at last, thereby make preform blanks before delivering to blowing device, form protective surface.Heating process only needs several minutes.
Description
The present invention relates to heating means and device with the partly crystalline synthetic resins preform blanks of injection moulding manufacturing.The preform blanks that the present invention makes for synthetic resin, partly crystalline synthetic resins or other multilayer material specially carries out while heating and cooling processing, constant temperature processing and temper making the blowing first being processed.
Synthetic resin is used for making diversified product now, comprises bottle, jar, bucket, cabinet and toy.
A kind of method of synthetic resin of processing is arranged " squeezing blow moulding ".When adopting this method, workpiece is to process under heated condition.Usually, a pipe is forced out or extrudes a blow head, is divided into several preform blanks then, and these blanks that are in plastic state are admitted to blowing mould, blows out the body of required hollow in mould.
Also can be processed into finished product to preform blanks with " heating again ".When adopting this method, the blank cooling of making in advance with direct injection moulding is also deposited.Then, take out blank from the storeroom, blowing processing is done in heating more at last.The present invention is exactly the heating means again that propose a kind of uniqueness.
Compare with the extrusion blow method, heating has many advantages again.Promptly cool off fast after the injection moulding processing in that raw material is done, the architectural characteristic of the preform blanks that injects is kept.And these good architectural characteristics can further be improved by heating again, machining and blowing.Formed architectural characteristic has improved anti-damaged performance and the cold damaged performance of tolerance and the transparency fallen of finished product.
Use again heating to also have following advantage, if on the hollow utensil (for example bottle, arrow-necked bottle, container, jar etc.) of processing inlet and floss hole are arranged, then can retrofit in first time injection moulding processing go out to seal the position of usefulness, and these positions needn't remake correction in the blowing processing afterwards.If for utensil processes flank, this advantage is particularly valuable.Because heating has this advantage again, blowing just can be shortened process time, and the neck of hollow utensil is generally thicker, if process neck in the blowing processing unit (plant), then neck required cool time is just than the length of hollow utensil remainder.
Adopting under the heating situation, the preform blanks that is processed into by injection moulding takes out from the storeroom again, and then is heated to required blow temperatures.Usually adopt following heating means: blank is slowly moved through the infra-red radiation system, and this system is heated to a certain uniform temperature to whole blank (comprising the inside and outside).
To be not easy to accomplish very much to the about evenly heating of preform blanks.Simultaneously moving one side at preform blanks is subjected to heating continuously or is interrupted heating in its longitudinal axis rotary course.But, be subjected to the photothermal just outer surface of preform blanks, thereby form the temperature difference in the wall thickness direction.When preform blanks adds man-hour do blowing, generation is axially stretched out usually.If blank temperature everywhere is also incomplete same, the hollow utensil that then processes just has some defect.Because outer surface temperature is higher than the temperature of the inside, the blank inner surface structurally will be different with outer surface.Because the blank temperature inside is lower, blank inside produces distortion in the blowing process, usually stress deformation can take place, and this intensity and profile to the hollow utensil that processes causes harmful effect.
According to European patent 387737A1, can in the short period, carry out the even heating of success to preform blanks.Make in this way, heat the preform blanks that and be lower than blow temperatures, thereby can avoid crystallization again.Allow these blanks cool off, and then be heated to a little higher than blow temperatures.After this, the temperature maintenance of preform blanks is constant, or descend slightly, do blowing processing at last.
But this method also is not suitable for the polymer-based material of partially crystallizable.Main mainstream product as partially crystalline polymer is a polypropylene.Polypropylene has many advantages, and for example breaking strength is excellent, the impact value height, and excellent transparency, proportion is planted synthetic resin (as the polyethylene terephthalate ester) low 30% than it.In addition, polyacrylic price only is equivalent to about half of other synthetic resin.Another advantage is the thing that polypropylene articles is suitable for irritating heat release.The polypropylene utensil also has an advantage, and irritating thing exactly later on can be the thing sterilization of polypropylene utensil together with the inside.This point is crucial to putting medicine and blood plasma product.
Because " the suitable processing district " of polypropylene and so on partly crystalline synthetic resins is very little, so they are difficult to process.Only in the suitable temperature scope, could be processed into above-mentioned each good performance to partly crystalline synthetic resins, and this temperature range is very little, thereby " suitable processing district " is subjected to the strict restriction of this temperature range.For example polyacrylic optimal process temperature range is very little, does not allow above ± 1 ℃.
The Another reason that is difficult to processing polypropylene is because its composition does not promptly have the free hydrogen molecule in the polypropylene.If the material of free hydrogen molecule is arranged, the just vibration of heating back free hydrogen molecule, this helps the uniformity of temperature profile of each one of material.On the contrary, when processing polypropylene, owing to there is not the effect of free hydrogen molecule, be fully make preform blanks high and low and temperature inside and outside even by conduction of heat.
Up to now, used a kind of " divine law energetically " to come the polypropylene preform blanks is done evenly heating.When making in this way, the polypropylene preform blanks is done on conveyer belt than long apart from the heating of accepting for a long time at a slow speed in the moving process, strictness is controlled.This method mainly is that heating makes the about temperature of preform blanks even by doing continuously to blank for a long time.Usually with " divine law energetically ", to be thirty minutes long to the heating of preform blanks.In most of the time during this period, keep the temperature-resistant of preform blanks inside and outside.
This divine law energetically has some critical defects.In blank heating or forming process, unavoidably to there be the shut-in time, the appearance of this shut-in time perhaps is that operating personnel have a mind to, and perhaps is unintentionally.When occurring closing when using energetically the divine law heating, the preform blanks that is placed in the stove usually can be by superheated, thereby becomes useless substandard products.
In view of above-mentioned various reasons, be necessary to invent a kind of heating means again, this method can successfully be used for processing synthetic resin, particularly can be used for processing polypropylene and so on partly crystalline synthetic resins.But, this method can also be used to processing the preform blanks (having partially crystallizable material and amorphous material in the multilayer material) that multilayer material is done.In addition, another advantage of heating is that required time shortens greatly again, preferably only needs a few minutes, and is as being total process time 5 minutes, just the most desirable.
Main purpose of the present invention is to propose a kind of heating means again that go for synthetic resin and comprise the polyacrylic partly crystalline synthetic resins of various forms.Another main purpose is the preform blanks (the existing partially crystallizable material of multilayer material has amorphous material again) that is used for the multilayer material system of processing.
The 3rd purpose of the present invention is when synthetic resin and partly crystalline synthetic resins are heated again, about altogether 5 minutes of required heat treatment time.
According to the present invention, each preform blanks is positioned on the clamping roller, and each roller is connected on the chain conveyor.The preform blanks one side is transmitted by chain conveyor, the one side rotation, and by the flat-temperature zone, the temperature of each one of preform blanks keeps evenly constant in this flat-temperature zone.Preform blanks moves through a heating/cooling stations (alternately doing heating, cooling herein) and several constant temperature zones then.When preform blanks moved through heating/cooling stations, the temperature of blank rose to blow temperatures.At this station destination county, no matter at the length direction of preform blanks or at thickness direction, the temperature of blank is even distribution.Preform blanks moves into surface treatment and tempering station then, and is in stable condition down the blank that forms in heating/cooling stations here, thereby the temperature that guarantees the sotck thinkness direction is balanced fully.
The present invention can take many processing lines, and such two tight adjacent preform blanks conveyer lines can be handled blank equally, by blowing device, is processed into required hollow physique then.The shape and the size of the preform blanks of processing on each bar processing line can be identical, also can be different.
According to the present invention, be provided with initial constant temperature station at the processing line section start.Preform blanks is done to transmit in this constant temperature station when mobile, around longitudinal axis rotation separately, sends into heating/cooling stations then.
Preform blanks is around the longitudinal axis rotation of self in whole process.So just guarantee that preform blanks temperature everywhere is identical, thereby any temperature differences can not occur.According to the size and dimension of preform blanks, can adjust the automatic rotation of preform blanks, angular speed is changed in a big way.
If there are not many processing lines, then every processing line has the whirligig of oneself.In addition, the direction of rotation of preform blanks should match with the direction of motion of chain conveyor.
So far the existing various mechanisms that can be used to rotate preform blanks, but also can adopt other kindred organization.For example, following United States Patent (USP) merits attention: patent No. No.2, and 519,177, patentee Chenault authorizes a day August 15 nineteen fifty; Patent No. No.2,508,259, patentee Helme authorizes a day May 16 nineteen fifty; Patent No. No.4,171,041, patentee Lowe authorizes day on October 16th, 1979; Patent No. No.4,832,173, patentee Hattori etc. authorize day on May 23rd, 1989.
Heater is housed in heating/cooling stations, in the heater in the horizontal direction or vertical direction the quartzy radiating bars of infrared ray is housed selectively.The quantity of the quartzy radiating bars of infrared ray can be according to the size and dimension increase and decrease of the preform blanks of being processed.In addition, in each heater, the direction of the quartzy radiating bars of infrared ray can be different, and promptly the quartzy radiating bars of infrared ray both can have been dressed up vertically, also can dress up level.
Can export and excellent layout by the temperature that the quantity and the direction of variation heating rod are regulated in each heater significantly.
According to the present invention, the preform blanks of rotation one then one the one side of preform blanks (being the lateral surface of chain conveyor) is heated when moving past heater, and another side (being the medial surface of chain conveyor) is cooled simultaneously.Medial surface (relative with heater) at chain conveyor is equipped with reflector.Reflector is connected with the adjustable air of a temperature source, and several cooling air outlet slits are arranged on the reflector, and when preform blanks moved past each reflector, the cooling air blew on the preform blanks, can be cooled to what degree to preform blanks and regulate.The cooling air both had been used for cooling off reflector, was used for preventing the outer surface over-heating of preform blanks again.Air cooling is by opening the aperture on reflector, and groove and other suitable eyelet are realized.
Characteristics of the present invention are: the preform blanks of rotation is by being located at the radiant heat source heating that transmits road one side, simultaneously by the air cooling of emitting from transmission road opposite side.In this way can be successfully accurately bring up to predetermined blow temperatures to the temperature of the preform blanks inside and outside of rotation, can over-heating, and polypropylene is extremely responsive for over-heating.Each section layer as preform blanks is heated in blank rotates a circle process, and at the beginning of first week of rotation, the facing layer of preform blanks at first is subjected to the heat radiation that the heating rod of heater sends.Along with preform blanks continues rotation, because the air cooling effect, the blank temperature that the heat radiation of being sent by heating rod causes raises and constantly reduces in the stairstepping mode.Thereby the intensification of preform blanks is actually and is subjected to the air cooled adjustment that takes place in the preform blanks rotary course.In continuing rotary course, same section layer is owing to alternately be subjected to cooling and thermal-radiating effect, and the temperature rising that produces that whenever rotates a circle is very little.This heating means improve the temperature of preform blanks integral body little by little, equably.The intensification of Xing Chenging can light concentrate on the outer surface of preform blanks like this, is slowly because temperature rises, and enters the section layer of blank effectively, so along with heating process continues, the temperature of whole preform blanks material is uniform basically.
Heat energy by heater input preform blanks is on each parts of the system of being distributed in, and act on the preform blanks in the following manner: do not influence blank surface and enter the transfer function of the heat energy of blank, heat energy enters the absorption of blank inside, is radiated the conduction of the heat energy on the blank surface.When coming partially crystallizable material such as processing polypropylene and polyethylene by the present invention, the transmission of heat energy as many as zero.And blank since the heat energy that obtains of conduction greater than because the heat energy that absorption obtains.In other words, the major part of the heat energy that obtains of preform blanks is because heat radiation effect and conduction of heat.Therefore, make the internal temperature of synthetic resin bring up to the temperature required certain hour that needs.According to the present invention, it is too fast that the cooling air can prevent that the preform blanks surface temperature from raising, thereby can avoid the too high and hot conduction of preform blanks surface temperature to improve the temperature of material.
According to the present invention, at final place one surface treatment and reversing chamber are arranged, in this sealing chamber, the hot air circulate of adding is arranged.This chamber is sealed, and air can only be overflowed from import and outlet for the preform blanks turnover.Have one to add the hot-air source and provide circulating air to surface treatment and reversing chamber, the outer surface of air flow preform blanks.The amount of circulating air and other relevant physical parameters can be regulated as required.As needs, also can be by amount that changes circulating air and the temperature that temperature is regulated this chamber.Owing to can be used for discharged air for the import of preform blanks turnover and outlet, so do not need to consider in addition the air discharging.
According to the present invention, keep at a certain distance away with infrared heating device heating preform blanks, meanwhile, be subjected to the air cooling when adding the opposite side of infrared source when blank rotates to, between each thermal treatment zone, the flat-temperature zone is arranged, be provided with surface treatment and reversing chamber in addition; Thereby make preform blanks reach in advance the accurately blow temperatures of appointment in the short time at the utmost point.For example, generally can in 5 minutes, accurately reach required blow temperatures.In addition, required blow temperatures can (just up to blank inside) be equally distributed in whole preform blanks scope.
Owing to comprehensive implement infrared ray heating, constant temperature and surface treatment and tempering, both can prevent that preform blanks from avoiding the hostile environment influence, can guarantee temperature equalization in the preform blanks again.Use totally enclosed surface treatment chamber and further help the even distribution of heat in the preform blanks, can not make that heat energy spills in the surrounding environment in the blank.
Use the device of chain conveyor always might to be not intended to or to shut down wittingly.In the case, even throw off heater immediately, it is overheated that preform blanks still might be caused by long-pending surplus heat in the heater.But using under the situation of the present invention, the rotary speed that can regulate preform blanks independently regardless of the chain conveyor pace is added preform blanks is done the air cooling, just can not damage preform blanks.
Can use a kind of suitable cooling system to come the portion that returns of cooling chain conveyer belt in the present invention, this cooling system also not exclusively belongs to prior art.
A United States Patent (USP) relevant with the present invention is noted in suggestion, 5,066, No. 222 patents that Here it is, and authorizing day is on November 19th, 1991.
For better understanding the present invention and knowing and how to use, consult accompanying drawing below.This accompanying drawing is the plane that heats blowing device again that the present invention proposes, and two chain conveyors are wherein arranged, two heating stations, two flat-temperature zones and surface treatment and tempering case.
Introduce recommendation instantiation of the present invention now.
Represented method and apparatus of the present invention in the drawings, two processing line I and II are wherein arranged, preform blanks 1 is heating in succession on two adjacent processing lines, and is processed into ducted body subsequently.
Usually the preform blanks 1 that processes with injection moulding is transferred upward processing line I and II by sending into conveyer belt 2 from the storeroom.By sending into preform blanks that conveyer belt the sends into clamping roller 3 of packing into.Leave identical distance between each clamping roller, clamping roller 3 is installed on the chain conveyor 4 (to be represented with chain-dotted line among the figure).Chain conveyor 4 moves by the arrow A direction, after the preform blanks heat treated, preform blanks 1 be transported to ligulate prodger 5 and 5 ', ligulate prodger 5 and 5 ' accept blank; And blank further sent into blowing device (not drawing the figure) from processing line I and II.The clamping roller 3 of clamping preform blanks 1 constantly rotates, thereby makes preform blanks along chain conveyor 4 when moving, around self longitudinal axis rotation.
Preform blanks 1 moves through preparation station 7 earlier, and blank is around the longitudinal axis rotation of self in this station, and it is constant that blank temperature keeps.
After preform blanks 1 moved through preparation station 7, blank just entered heating and cooling station 24.Heating and cooling station 24 generally includes several heating/cooling and constant temperature zones.In illustrated example, on each bar processing line I and II, these sections comprise 3 heaters and two flat-temperature zones.On the processing line I, heater is represented with code name 6,10,13 respectively, and the flat-temperature zone is represented with code name 9 and 12 respectively.On the processing line II, heater use respectively code name 6 ', 10 ' and 13 ' expression, and the flat-temperature zone respectively with 9 ' with 12 ' represent.
Each heating rod was both vertical with respect to the orientation of heater and chain conveyor, also (or or its socket can adorn two kinds of rods) of level.In addition, the quantity of the heating rod of installing in each heater can increase and decrease selectively, so that accurately adjust output temperature.
Can use various well-known existing mechanisms to adjust the height and the spacing of the used heater of the present invention selectively.
Although by heater 10 and 10 ', heating rod in the central station 14 formed of heating rod 15a, 16a be drawn as level orientation with vertical orientations, the orientation among the figure is just schematically.In fact the orientation of heating rod is adjusted by institute's calorific requirement on the size and dimension basis of considering institute's processing work.
Separate with dividing plate between each reflector 8,18,11,19 and 14.The dividing plate 17 that drawn in the drawings, this dividing plate 17 is separated reflector 8 and reflector 18.
Dividing plate can be separated into chamber one by one effectively, is mapped on the corresponding heater thereby can directly blow from the cooling air that reflector flows out.From heater 6,6 ', 10,10 issue, 13, the 13 ' heat energy that gives off only inwardly those preform blanks 1(reflectors that are between heater and the reflector of directive be installed in a side relative on the processing line with heater).Dividing plate can limit heat energy and be lost to constant temperature zone 9,12 from bringing-up section.Like this, constant temperature zone 9,12 just can more effectively cool off, thereby also just more effectively cools off preform blanks 1.
By after the heating/cooling stations 24, blank 1 just enters surface treatment and tempering station 25 at preform blanks 1.Fiery once chamber 20 in surface treatment and the tempering station 25, this is an almost completely space of sealing.Preform blanks 1 carries out tempering here, improves surface strength.By appendix 21 air of heating is blown into surface treatment and reversing chamber 20.Inlet chamber 20 add quantity of hot air and temperature can be regulated, thereby can control this indoor air themperature.The cover plate of chain conveyor plays reversing chamber base plate (not drawing among the figure).Base plate, protection top cover, both sides panel and two ends panel form the almost completely reversing chamber 20 of sealing.On each chain conveyor 4, (close last group heater 13,13 ' locate) has import 22 on the end plates of chamber 20; (close ligulate prodger 5,5 ' locate) has outlet 23 on other end panel.The size of opening 22 and outlet 23 is selected to such an extent that should make preform blanks 1 can pass in and out chamber 20.Because air can be overflowed from import 22 and outlet 23, so there is no need to consider the air discharging usually.
The working order of device is as follows.By sending into conveyer belt 2 preform blanks 1 is sent into from the storeroom, blank is loaded onto controllable rotation clamping roller 3, and is constantly moved by chain conveyor 4, and preform blanks 1 is by roller 3 rotations in moving process.Preform blanks 1 on the top chain conveyor shown in the figure, preferably clockwise direction rotation, and the preform blanks on bottom chain conveyor 4 is rotation counterclockwise.The direction of rotation and the angular speed that are preform blanks 1 all are to control independently on request.Preform blanks 1 at first move into bringing-up section 6,6 ', on one side here blank heats, Yi Bian be subjected to coming from reflector 8 again and the cooling of the air that outwards blows.Like this, the preform blanks in constantly rotating, a side is heated, and opposite side is cooled.The degree of heating and cooling can be controlled, and the temperature of preform blanks 1 is little by little slowly to rise like this, and its surface temperature will never surpass predetermined temperature.
Preform blanks 1 is continued to move by chain conveyor 4 on one side, on one side by 3 rotations of clamping roller, enter flat-temperature zone 9,9 ', here blank 1 continues to be subjected to air to blow, air is that the notch from the reflector 18 blows out, air themperature can be controlled.
Preform blanks 1 continues to be transmitted by chain conveyor 4 left side in figure, at blank by heater 10,10 ' and during reflector 11, its temperature slowly rises again; Wherein air outwards blows out from reflector 11, and the temperature of air can be controlled, to 1 cooling effect of preform blanks.Preform blanks continues by constant temperature zone 12,12 ' (reflector 19 is housed) while rotating then.The function of these flat-temperature zones and constant temperature zone 9,9 ' cardinal principle identical, just temperature is higher.Preform blanks is then by heating/cooling zone, is provided with heater 13,13 ' and reflector 14 here, and the temperature of blank improves once more, the ideal temperature that arrives or process near blowing; If in the end ideal temperature is failed to be warmed up in a heating/cooling zone, then can in reversing chamber 20, reach this temperature, circulate in this chamber from the hot-air that adds that adds hot-air source 21, further heat blank.
At last, when preform blanks 1 by ligulate prodger 5,5 ' when sending into blowing device, blank integral body is in temperature required uniformly, can be blow molded into final products.As long as adjust the device shown in the accompanying drawing rightly, just can realize this temperature; Comprise the quantity of adjusting heating rod and they orientation, the temperature in heater and the characteristic of the cooling air sent into, the temperature of preform blanks 1 just can slowly rise by a small margin like this, and in the process that so heats up in whole preform blanks scope heat be even diffusion.After adjusting, can be by the device that institute's introduction method is made the temperature increase of preform blanks 1 to the required predetermined temperature of blowing processing, whole process is no more than 5 minutes.Roller 3 can be rotated independently, just in case when processing line stops for a certain reason,, make preform blanks 1 keep original temperature, it is slowly descended like this by blowing air to the preform blanks of rotation from reflector.
Can know that according to existing knowledge the temperature increment that preform blanks can bear depends on its physics and chemical property.So the operator of device should suitably adjust this device, make in the rotation of the maximum temperature that reaches on the preform blanks one vertical section laminar surface and preform blanks the temperature difference between the minimum temperature that reaches on should the surface less than a certain temperature difference; This temperature difference, and the thermograde between each section of blank can influence the physics and the chemical property of preform blanks conversely.
Though we have introduced our invention, it may be noted that in following claim scope can be to the present invention's variation that makes an amendment.
Claims (14)
1, a kind of controlled heat method of the cold preform blanks that is used for partly crystalline synthetic resins that injection moulding is produced, wherein preform blanks moves through each heating/cooling stations, send into blowing device then, preform blanks is blown out the hollow utensil, whole controlled heat method comprises following each step:
A. preform blanks moves through projected route on one side, on one side rotation;
B. continuing when above-mentioned projected route moves, in a side of route preform blanks is being heated, the opposite side at route cools off preform blanks simultaneously;
C. continuing when above-mentioned projected route moves, preform blanks enters heated air heating in the almost completely airtight empty chamber.
2, the heating means of the cold preform blanks of partly crystalline synthetic resins as claimed in claim 1, wherein the rotary speed of preform blanks and preform blanks are irrelevant along the linear velocity that projected route moves.
3, the heating means of the cold preform blanks of partly crystalline synthetic resins as claimed in claim 1, wherein blank whenever rotates a circle and produces the little temperature amount of having a net increase of, the temperature of so coming progressively to improve blank during the b step.
4, a kind of device that is used for heating part crystalline resins preform blanks, this device comprises as the lower part;
A. one or several conveyor-belt apparatus is used for making preform blanks to move along an almost straight route;
B. clamping device is used for installing preform blanks and it is independently rotated around self vertical axis;
C. move on one side preform blanks rotates the above-mentioned route in an edge at a constant temperature station that is located on the above-mentioned route, arrives a heating cooling stations, and several heaters spaced a certain distance are housed in this heating cooling stations, in each heater heating element heater is arranged;
D. tempering station that is located on the above-mentioned route and has import and outlet, this tempering station have the space of sealing substantially, add hot-air and circulate around preform blanks in this space;
E. one kind preform blanks delivered to the clamping device of blowing device from transmitting the road.
5, device as claimed in claim 4, wherein the heating element heater in the heater can vertically be provided with or be horizontally disposed with.
6, device as claimed in claim 4, wherein heating element heater can produce infrared heat energy.
7, device as claimed in claim 4, wherein the heating element heater in the heater can increase and decrease on demand.
8, device as claimed in claim 4 wherein is provided with and a kind ofly can regulates the adjusting device of heater with respect to the height of above-mentioned route on demand.
9, device as claimed in claim 4 wherein is provided with and a kind ofly can regulates the roll-setting gear of heater spacing on demand.
10, device as claimed in claim 4 wherein is provided with a kind of keeper in the heater, be used for installing heating element heater to such an extent that become vertical orientations with above-mentioned route.
11, device as claimed in claim 4 wherein is provided with a kind of keeper in the heater, be used for installing heating element heater to such an extent that become level orientation with above-mentioned route.
12, device as claimed in claim 4, wherein an opposite side with heater place side is equipped with cooling air outlet slit over against heater on above-mentioned route.
13, device as claimed in claim 4, wherein on above-mentioned route, the flat-temperature zone arranged between heater.
14, device as claimed in claim 4 wherein heats cooling stations and occupies 70～80% of above-mentioned route total length, and tempering station occupies 20～30% of above-mentioned route total length.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN93106966A CN1058218C (en) | 1993-06-09 | 1993-06-09 | Method and apparatus for heating preform blanks composed of partly crystalline synthetic resins produced by injection molding |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN93106966A CN1058218C (en) | 1993-06-09 | 1993-06-09 | Method and apparatus for heating preform blanks composed of partly crystalline synthetic resins produced by injection molding |
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| Publication Number | Publication Date |
|---|---|
| CN1096244A true CN1096244A (en) | 1994-12-14 |
| CN1058218C CN1058218C (en) | 2000-11-08 |
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| CN93106966A Expired - Fee Related CN1058218C (en) | 1993-06-09 | 1993-06-09 | Method and apparatus for heating preform blanks composed of partly crystalline synthetic resins produced by injection molding |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102922733A (en) * | 2011-08-11 | 2013-02-13 | 克朗斯股份公司 | Method and device for blow moulding containers |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2304501A1 (en) * | 2000-04-10 | 2001-10-10 | Bayer Inc. | Process for hydrogenating carboxylated nitrile rubber, the hydrogenated rubber and its uses |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3101282A1 (en) * | 1981-01-16 | 1982-08-26 | Krupp Corpoplast Maschinenbau GmbH, 2000 Hamburg | Process and device for blow moulding hollow articles, in particular bottles |
| EP0387737B1 (en) * | 1989-03-14 | 1993-08-11 | BEKUM Maschinenfabriken GmbH | Method for heating injection-moulded preforms taken from a magazine for blowing them up to hollow parts in a blow mould and device for blow moulding prefabricated preforms |
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1993
- 1993-06-09 CN CN93106966A patent/CN1058218C/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102922733A (en) * | 2011-08-11 | 2013-02-13 | 克朗斯股份公司 | Method and device for blow moulding containers |
| US9266275B2 (en) | 2011-08-11 | 2016-02-23 | Krones Ag | Device and method for blow moulding containers |
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| Publication number | Publication date |
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| CN1058218C (en) | 2000-11-08 |
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