CN109763976A - A kind of gear pump - Google Patents
A kind of gear pump Download PDFInfo
- Publication number
- CN109763976A CN109763976A CN201711096862.9A CN201711096862A CN109763976A CN 109763976 A CN109763976 A CN 109763976A CN 201711096862 A CN201711096862 A CN 201711096862A CN 109763976 A CN109763976 A CN 109763976A
- Authority
- CN
- China
- Prior art keywords
- gear
- melt
- pump housing
- pump
- face
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Rotary Pumps (AREA)
Abstract
The present invention relates to a kind of gear pumps, including end plate, driven gear, the pump housing, gear shaft and front end-plate, it is both provided with concave-convex anti-adhesion structure on the wall with the component of molten polymer joint in gear pump, anti-adhesive attraction of the polymer melt in filament spinning component may be implemented;The bumps prevent adhesion the mechanism of action of mechanism are as follows: include depressed section and convex portion in concave-convex anti-adhesion structure, convex portion is higher by the setting of member internal walls surface, directly contacting between highly viscous polymer melt and member internal walls is reduced using supporting role between points, and gas suspension effect is formed under the action of high temperature and pressure melt, plays and prevents adhesion from separate type.
Description
Technical field
The present invention relates to textile technology fields, and in particular to a kind of gear pump for melt spinning.
Background technique
British patent in 1845 is come from the earliest record of melt spinning process.Nineteen thirty-nine melt spinning is as manufacture nylon
The production technology of 66 fibers obtains industrial applications.As Figure 1-1, melt spinning basic process includes material melts, from spinneret
It is squeezed out in plate micropore, melt stream cooling and solidifying forming.Manufactured long filament can be used bobbin coiling and molding or carry out other processing.
During melt spinning, polymer feeds extruder, and it is tired to be sent to metering further along after screw rod transmission, plasticizing, melting:
Metering is poly- to ensure that the melt of polymer can be flowed into critical component filament spinning component to stable and uniform by accurate measurement, is spinning
Melt passes through the filtering of filter medium in silk component, is provided in porous spinneret after eliminating impurity and bubble by high pressure indentation
As thread;Thread is drawn while being quickly cooled down (quenching) by horizontal blowing since the effect of following wireline reel also generates high power
It stretches, so that diameter attenuates;As-spun fibre is wound into certain package.
Under normal conditions filament spinning component be mainly the filter layer being made of upper layer overcurrent lid, metal mesh and filter sand, distribution plate and
Porous spinneret is constituted.After spinning melt flows into filament spinning component from top-level entries, lie prone the mistake of type via the back taper minister in ancient times in sand chamber
Stream lid diffusely enters in the inner cavity of component, and filtration combination layer is ingeniously entered under the action of upper stressor layer.Filter layer usually has multilayer
Filter screen and METALLIC FILTRATION SAND composition.The a piece of coarse net for not luring steel wire to weave into often is placed in the top layer of filter layer, becomes cover net
Or cover net, it is therefore an objective to stop the sundries of bulk and prevent the layer of sand of lower part mobile.When filtering using filter sand, sand grains is pressed in principle
Granularity is carefully sequentially arranged by thick.When placing multistorey strainer mesh, and the principle descending by mesh size.In filtration combination layer
The bottom placed one layer of supporting network, it be usually be made of a piece of or two panels coarse net, it is therefore an objective to support upper level filter layer,
Increase longitudinal rigidity, has the function that not to be depressed, it can also prevent the effect for draining to spinneret orifice under broken filter sand sometimes.By
Melt after fine filtering flows into the hole of distribution plate.On the one hand the effect of distribution plate is to play support upper level filter layer, another
Aspect is before polymer melt is assigned to spinneret plate as homogeneously as possible, so that the uniform flow in every hole, also tubing flow displacement filament plate
The melt pressure of part is shared, so that spinning plate surface is unlikely to superpressure and deforms.Polymer melt is squeezed into spinneret
Guide hole after, micropore gives the certain shape of melt and is extruded as strand, finishes to dazzle body like this inside filament spinning component
The design of the filament spinning component of flowing need to mainly determine its structure snd size.Wherein component external structure snd size mainly need to examine
The problems such as considering the intensity and corrosion resistance of itself, the problem of also relating to installing and dismounting and leakproofness.The inside member of filament spinning component
Part just really carries main spinning function, it should how to select filtration combination element, hybrid element, distribution member and spinneret
Panel element etc., it is necessary to comprehensive to go sufficiently to be calculated and considered from multi-angles such as hydrodynamics, melt rheology and heat conductions.
Certainly it can not ignore the inner sealing of each element while design and the problem of strong rigidity.Melt spinning is to carry out at high temperature
, if polymer melt is chronically at high humidity state, it may occur that degradation influences the quality of precursor, and institute W is inside design component
When channel, melt should be made to be uniformly distributed in each micropore of spinneret as far as possible, channel resistance is answered equal, cannot be existed in component
Dead angle, in case melt residence time is too long and decomposes.It should process smooth with king's part surface of melt contacts, object cannot be made
Material is detained due to wall surface resistance.Fluid motion uniformity mainly includes fluid motion speed, pressure, stop in filament spinning component
The contents such as time, discharging distribution.Ideal filament spinning component should be able to guarantee that simultaneously above-mentioned parameter is all identical, and sample presentation just can ensure that
Polymer melt is evenly distributed in each spinneret orifice of spinneret with identical matter, and it is uniformly high-quality finally to spin out structural behaviour
Measure fiber.However, the factor for influencing flow field uniformity in filament spinning component is numerous, wherein mainly having material properties, process conditions, setting
Standby structural parameters etc..When the above two control identical, device structure is its most important influence factor again.
The flow behavior of polymer melt is more complex compared with for small molecule solution.Under external force, melt is not only
Irreversible viscous yielding is shown, but also shows reversible flexible deformation.This is because the flowing of polymer is not
Simple Relative sliding between macromolecular chain, but the overall result of moving cell successively transition.Under external force, macromolecular chain
It is inevitably stretched along external force direction, removes external force, macromolecular chain will be spontaneously rolled up again.This conformation change
Caused elastically-deformable development and Recovery Process are relaxation, which depends on polymer molecular weight, external force
Time, temperature etc..It is the appearance of flexible deformation and its subsequent lax pair fiber, dimensional stability, interior in molding process
Stress etc. has substantial connection.
High polymer molten viscosity cuts flowing and is mainly characterized in that: that cut viscosity very high;Viscosity strong depend-ence trimming rate is cut, absolutely
Most of high polymer moltens belong to pseudoplastic fluid;Velocity flow profile of the pseudoplastic behavior high polymer molten in round tube is not parabolically
It is linear, and it is close to plunger flow, velocity gradient concentrates on near-wall, and there may be tube wall sliding to move in some cases,
It there may also be molecular-weight gradation effect in flowing, make low molecular weight fraction in near-wall more than pipe axis.
It is not constant temperature process in actual production process, and is unstable state, but above-mentioned " spinnability " is theoretical, it is right
The forming process of chemical fibre still has preferable reference and directive significance, and the principal element obtained from " spinnability " theory is all
It is the factor for controlling spinning and going on smoothly.Such as be viscosity and surface tension to capillary mechanism major influence factors, to cohesive energy
The principal element that failure mechanism influences is deformation speed and viscoplasticity size etc..The spinnability principle for understanding melt facilitates us
When adjusting spinning technique, optimal conditions are targetedly selected, to avoid occurring wild effect in spinning.Change and spins
The rheological property of silk Wang Yi parameter and raw material may make the variable element range for stablizing spinning sufficiently increase, convenient and technique
Adjustment.
Since the high temperature polymer melt of melting needs to shift and flow in filament spinning component, high-temperature fusant and spinning group
Inevitably there are contacts for part quality inspection, also just inevitably there is adherency on the inner wall of filament spinning component, although
At present when preparing filament spinning component can by the smooth enough of its inwall processing, largely reduced due to
Inner wall surface problem and caused by attachment of polymers still due to the limitation of machining accuracy and processing technology, be difficult to accomplish inner wall
It is completely smooth, still can generate the adherency of polymer in this way;There are also during the spinning process in polymer and spinning in the prior art
The scheme that lubricant is added between the inner wall of component, can play certain anti-adhesiving effect in this way, but what these were added
Lubricant will certainly enter in polymer, and then the property of polymer and the property of subsequent spinning generate unpredictable shadow
It is loud and worthless.Due to the adherency of polymer during the spinning process, all needed after the production plan for not completing a batch
Filament spinning component is thoroughly cleaned, time and cost will lead to the cleaning of filament spinning component and greatly consume, but also
There are some dead angles to be difficult to be cleaned for meeting, and can adversely affect to subsequent production.Therefore, exploitation one is needed
Kind new anti-adherency of filament spinning component or anti-blocking techniques, the shortcomings that overcome in the prior art.
Summary of the invention
For the prior art there are above-mentioned technical problem, the present invention provide it is a kind of reduction polymer melt adherency it is novel
Gear pump.
To achieve the above object, the present invention the following technical schemes are provided:
A kind of gear pump, including end plate, driven gear, the pump housing, gear shaft and front end-plate, further include two high-pressure seal rings,
Four sliding bearings, stuffing-box and flange gland;Gear and driven gear on the gear shaft are setting up and down and mounted in pump
In the gear cavity of body, the gear cavity of the pump housing is respectively and on the melt inlet and pump housing left side wall that are arranged on pump housing right side wall
Melt outlet connection, the gear on gear shaft engages with driven gear, the both ends of the outer circumferential end face of the gear on gear shaft
It is respectively provided with a shoulder end face, the both ends of the outer circumferential end face of the driven gear are respectively provided with a shoulder end face, the gear
One sliding bearing, gear shaft are respectively housed on two shoulder end faces of the gear on axis and two shoulder end faces of driven gear
On gear and end plate between and driven gear and end plate between respectively be equipped with a high-pressure seal ring, the rear end of the pump housing
Face is detachably connected with end plate, and the front end-plate is detachably connected on gear shaft and with the front end face of the pump housing;In gear
Chamber, gear, driven gear, melt inlet and melt outlet the surface being in contact with polymer melt on be provided with bumps
Prevent adhesion mechanism;The bumps anti-adhesion structure is equally distributed recess and protrusion.
Preferably, the recess in the concave-convex anti-adhesion structure and protrusion are spaced apart from each other and are uniformly distributed;The surface area of protrusion
It is 0.5-2 square millimeters, the surface area of recess is 1-3 square millimeters.Further, raised surface area is 1 square millimeter,
The surface area of recess is 2 square millimeters
Preferably, the gear shaft is process with gear thereon using integrated.
Compared with prior art, the invention has the following advantages that due to being in contact in gear pump with molten polymer
Component surface on be both provided with concave-convex anti-adhesion structure, anti-adherency of the polymer melt in filament spinning component may be implemented and make
With;The bumps prevent adhesion the mechanism of action of mechanism are as follows: include depressed section and convex portion, lug boss in concave-convex anti-adhesion structure
Divide and be higher by the setting of parts surface surface, supporting role between points is utilized to reduce highly viscous polymer melt and component table
Direct contact between face, and gas suspension effect is formed under the action of high temperature and pressure melt, it plays anti-sticking from separate type
Even;Sunk structure plays the role of accommodating levitation gas, cooperates with convex portion;The surface area of protrusion is 0.5-2 squares
Millimeter, the surface area of recess are 1-3 square millimeters, it is preferable that raised surface area is 1 square millimeter, and the surface area of recess is 2
Square millimeter, depressed section and lug boss branch point are connected to form accurate honeycomb protection grid, by parts surface with polymerize
Object melt separation is opened, and the effect to prevent adhesion is increased.The area of convex portion and depressed section should not be too large, if area is excessive,
Good preventing adhesiving effect can not be then played, and without two the case where polymer melt is directly in contact with parts surface;Its
The area of the two is also unsuitable too small, if area is too small, can not play estimated preventing adhesiving effect, and difficulty of processing
It can be very big.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of gear pump of the present invention.
Fig. 2 is another angled arrangement schematic diagram of gear pump of the present invention.
Appended drawing reference:
1 --- end plate;
2 --- driven gear;
3 --- high-pressure seal ring;
4 --- sliding bearing;
5 --- gear shaft;
6 --- the pump housing;
7 --- front end-plate;
8 --- stuffing-box;
9 --- flange gland;
10 --- gear;
11 --- melt inlet;
12 --- melt outlet.
Specific embodiment
Below in conjunction with specific embodiments and drawings, the present invention is described in detail.
Illustrate present embodiment in conjunction with FIG. 1 to FIG. 2, present embodiment includes end plate 1, driven gear 2, the pump housing 6, tooth
Wheel shaft 5 and front end-plate 7 further include two high-pressure seal rings, 3, four sliding bearings 4, stuffing-box 8 and flange gland 9;Gear shaft
Gear 10 and driven gear 2 on 5 are setting up and down and in the gear cavity of the pump housing 6, the gear cavity of the pump housing 6 respectively with set
It sets and is connected in the melt inlet 11 on 6 right side wall of the pump housing with the melt outlet 12 on 6 left side wall of the pump housing, the gear on gear shaft 5
10 engage with driven gear 2, and the both ends of the outer circumferential end face of the gear 10 on gear shaft 5 are respectively provided with a shoulder end face, driven
The both ends of the outer circumferential end face of gear 2 are respectively provided with a shoulder end face, on two shoulder end faces of the gear 10 on gear shaft 5 and
One sliding bearing 4 is respectively housed, between the gear 10 and end plate 1 on gear shaft 5 on two shoulder end faces of driven gear 2
And a high-pressure seal ring 3 is respectively housed between driven gear 2 and end plate 1, rear end face and the end plate 1 of the pump housing 6 detachably connect
It connects, front end-plate 7 is detachably connected on gear shaft 5 and with the front end face of the pump housing 6, is filled on the gear shaft 5 of 7 front end of front end-plate
There is flange gland 9, stuffing-box 8 is housed, stuffing-box 8 and flange gland 9 can on the gear shaft 5 between flange gland 9 and front end-plate 7
Dismantling connection, each sliding bearing 4 are respectively provided with a guide groove on the inner wall close to 12 side of melt outlet, and the pump housing 6 is located at
Guiding groove is provided on the inner wall of melt inlet 11, on the end face that end plate 1 is in contact with the pump housing 6 and front end-plate 7 and the pump housing 6
Guiding lubrication groove is respectively provided on the end face being in contact.Guide groove, guiding groove and guiding lubrication groove are set, and the pump housing is in lubricating system
On, self-lubricating is carried out using the melt of itself conveying.
Preferably, in the molten with polymer of gear cavity, gear 10, driven gear 2, melt inlet 11 and melt outlet 12
Bumps are provided on the surface that body is in contact to prevent adhesion mechanism;The bumps anti-adhesion structure be it is equally distributed recess and it is convex
It rises.Recess and protrusion in concave-convex anti-adhesion structure, which are spaced apart from each other, to be uniformly distributed;The surface area of protrusion is 0.5-2 square millimeters,
The surface area of recess is 1-3 square millimeters, and further, raised surface area is 1 square millimeter, and the surface area of recess is 2
Square millimeter.
It is both provided with concave-convex anti-adhesion structure on the surface of the component being in contact with molten polymer in gear pump, it can
To realize anti-adhesive attraction of the polymer melt in filament spinning component;The bumps prevent adhesion the mechanism of action of mechanism are as follows: bumps are anti-
It include depressed section and convex portion in adhesion structure, convex portion is higher by the setting of parts surface surface, using between points
Supporting role reduce directly contacting between highly viscous polymer melt and parts surface, and in high temperature and pressure melt
Gas suspension effect is formed under effect, is played and is prevented adhesion from separate type;Sunk structure plays the role of accommodating levitation gas, and convex
Part is played to cooperate;The surface area of protrusion is 0.5-2 square millimeters, and the surface area of recess is 1-3 square millimeters, it is preferable that
The surface area of protrusion is 1 square millimeter, and the surface area of recess is 2 square millimeters, and depressed section is connected shape with lug boss branch point
Grid is protected at accurate honeycomb, parts surface and polymer melt are separated, the effect to prevent adhesion is increased.Convex portion
It should not be too large with the area of depressed section, if area is excessive, good preventing adhesiving effect, and polymer can not be played
The case where melt is directly in contact with parts surface is without two;The area of the two is also unsuitable too small, if area is too small, also not
Estimated preventing adhesiving effect can be played, and difficulty of processing also can be very big.Concave-convex anti-adhesion structure can prepare filament spinning component
Various pieces when apply on these parts respectively, can be using will have the sark of the concave-convex mechanism that prevents adhesion directly docile and obedient
Form on the surface of component carries out, and can also be carried out in the form of precision lathe processing, specific processing method is existing
There are the common parts machining means in technology.
One is made with gear 10 thereon in gear shaft 5, easy to process, and can guarantee concentricity.Other compositions and connection
Relationship is same as the specific embodiment one.
Working principle is: the space that gear on the pump housing, gear shaft and driven gear are formed constitutes melt inlet area, defeated
Send area and outlet area.In melt inlet area, the tooth of two gears is in the state for continuously separating, disengaging, melt inlet area with slot
Space constantly increase, polymer melt is sent into melt inlet area with lower pressure and filled by its upper end equipment extruder
Full tooth socket.With the rotation of gear, the melt in tooth socket constantly shifts to melt outlet area through melt delivery area, goes out in melt
Mouth region, two gears and slot enter closure or meshing state, and the space in melt inlet area is constantly reduced, and the melt in each tooth socket is forced
It squeezes out, to realize the function of increasing pressure of Melt Pump.Gear often rotates a circle, discharge capacity be it is constant, gear continuously rotates
Realize the continuous dispatch and metering of melt.Meanwhile gear be equivalent to one rotation barrier, can effectively obstruct melt into
Mouth region melt pressure fluctuation and influence of the flowed fluctuation to melt outlet area melt, when pump melt inlet pressure because it is various because
The fluctuation of element and when changing in a very big range, the melt outlet pressure oscillation of pump can control the change in very little completely
Change in range, to realize the voltage stabilizing function of pump.
Finally it should be noted that the above embodiments are merely illustrative of the technical solutions of the present invention, rather than the present invention is protected
The limitation of range is protected, although explaining in detail referring to preferred embodiment to the present invention, those skilled in the art are answered
Work as understanding, it can be with modification or equivalent replacement of the technical solution of the present invention are made, without departing from the reality of technical solution of the present invention
Matter and range.
Claims (4)
1. a kind of gear pump, including end plate, driven gear, the pump housing, gear shaft and front end-plate further include two high pressure sealings
Circle, four sliding bearings, stuffing-box and flange gland, gear and driven gear on the gear shaft are setting up and down and are mounted in
In the gear cavity of the pump housing, the gear cavity of the pump housing respectively with the melt inlet and pump housing left side wall that are arranged on pump housing right side wall
On melt outlet connection, the gear on gear shaft engages with driven gear, the two of the outer circumferential end face of the gear on gear shaft
End is respectively provided with a shoulder end face, and the both ends of the outer circumferential end face of the driven gear are respectively provided with a shoulder end face, the tooth
One sliding bearing, gear are respectively housed on two shoulder end faces of the gear on wheel shaft and two shoulder end faces of driven gear
One high-pressure seal ring is respectively housed, after the pump housing between the gear and end plate on axis and between driven gear and end plate
End face is detachably connected with end plate, and the front end-plate is detachably connected on gear shaft and with the front end face of the pump housing, special
Sign is: on the surface of gear cavity, gear, driven gear, melt inlet and melt outlet being in contact with polymer melt
On be provided with bumps and prevent adhesion mechanism, which is equally distributed recess and protrusion.
2. gear pump as described in claim 1, it is characterised in that: the recess and protrusion in the bumps anti-adhesion structure are mutual
Interval is uniformly distributed;The surface area of protrusion is 0.5-2 square millimeters, and the surface area of recess is 1-3 square millimeters.
3. gear pump as claimed in claim 2, it is characterised in that: raised surface area is 1 square millimeter, the surface area of recess
It is 2 square millimeters.
4. gear pump according to claim 3, it is characterised in that: the gear shaft is added with gear thereon using integrated
Work forms.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711096862.9A CN109763976A (en) | 2017-11-09 | 2017-11-09 | A kind of gear pump |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711096862.9A CN109763976A (en) | 2017-11-09 | 2017-11-09 | A kind of gear pump |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109763976A true CN109763976A (en) | 2019-05-17 |
Family
ID=66449231
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711096862.9A Pending CN109763976A (en) | 2017-11-09 | 2017-11-09 | A kind of gear pump |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109763976A (en) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2128472Y (en) * | 1992-07-17 | 1993-03-24 | 刘木竹 | Thin plastic gloves |
CN2423840Y (en) * | 2000-04-25 | 2001-03-21 | 黄胜雄 | Ladle |
CN201022638Y (en) * | 2007-02-12 | 2008-02-20 | 田海金 | Strong flame cooking health fume-free frying pan |
CN201212474Y (en) * | 2008-07-31 | 2009-03-25 | 哈尔滨理工大学 | High viscosity polymer melt pump |
CN201249454Y (en) * | 2008-08-21 | 2009-06-03 | 缪家栋 | Antisticking cutter |
CN201825985U (en) * | 2010-09-26 | 2011-05-11 | 舟山市7412工厂 | Thermal treatment anti-adhesion device |
-
2017
- 2017-11-09 CN CN201711096862.9A patent/CN109763976A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2128472Y (en) * | 1992-07-17 | 1993-03-24 | 刘木竹 | Thin plastic gloves |
CN2423840Y (en) * | 2000-04-25 | 2001-03-21 | 黄胜雄 | Ladle |
CN201022638Y (en) * | 2007-02-12 | 2008-02-20 | 田海金 | Strong flame cooking health fume-free frying pan |
CN201212474Y (en) * | 2008-07-31 | 2009-03-25 | 哈尔滨理工大学 | High viscosity polymer melt pump |
CN201249454Y (en) * | 2008-08-21 | 2009-06-03 | 缪家栋 | Antisticking cutter |
CN201825985U (en) * | 2010-09-26 | 2011-05-11 | 舟山市7412工厂 | Thermal treatment anti-adhesion device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107604450A (en) | A kind of melting electrostatic device for spinning | |
US2278875A (en) | Method and apparatus for the production of artificial structures | |
CN110917663A (en) | Continuous defoaming device and method for solvent spinning cellulose spinning solution | |
AU773690B2 (en) | High speed melt spinning of fluoropolymer fibers | |
CN109763976A (en) | A kind of gear pump | |
CN104278337B (en) | PLA Masterbatch filament spinning component | |
CN107829155A (en) | A kind of Mixing of Polymer Melt device | |
CN107419344A (en) | One kind prevents adhesion filament spinning component | |
CN101988217A (en) | Vertical atomized chemical fiber molding method | |
KR102105865B1 (en) | Spin bath and method for consolidation of a shaped article | |
CN207845836U (en) | A kind of polymer melt metering pump | |
CN114318557A (en) | Spinning assembly for polyester industrial yarns and processing method | |
CN207845835U (en) | One kind prevents adhesion screw extruder | |
CN105420824A (en) | Spinning assembly and spinning method thereof | |
CN107829156A (en) | A kind of spinneret | |
CN107829154A (en) | A kind of Mixing of Polymer Melt tower | |
CN207845838U (en) | One kind prevents adhesion two-chamber filament spinning component | |
CN109281028A (en) | The equipment and preparation method thereof of the different combined yarn of One-step production POY/FDY tri- | |
CN207512324U (en) | A kind of low adherency spinning melt pipeline | |
CN107574483A (en) | A kind of melt electrostatic spinning device | |
CN108411384A (en) | A kind of suitable gravity cylindrical static electric spinning device and method | |
CN107824084A (en) | One kind melting dynamic mixer | |
CN207845837U (en) | One kind prevents adhesion filament spinning component | |
CN102677194B (en) | Polyphenylene sulfide spinning technology | |
CN107447261A (en) | A kind of polymer melt measuring pump |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190517 |