CN102160980A - High viscosity liquid resin discharging process and dedicated equipment thereof - Google Patents
High viscosity liquid resin discharging process and dedicated equipment thereof Download PDFInfo
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- CN102160980A CN102160980A CN2011100575575A CN201110057557A CN102160980A CN 102160980 A CN102160980 A CN 102160980A CN 2011100575575 A CN2011100575575 A CN 2011100575575A CN 201110057557 A CN201110057557 A CN 201110057557A CN 102160980 A CN102160980 A CN 102160980A
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Abstract
The invention discloses high viscosity liquid resin discharging equipment and a discharging process thereof. The equipment comprises a discharging head at the opening of a reacting kettle and a collecting tank under the discharging head, and is characterized in that: a heating device is arranged on the discharging head, and a screen is arranged at the bottom of the discharging head; a cutting blade and a coolant generator are arranged under the screen. The process is characterized in that: the discharging equipment is adopted for discharging materials; and the process comprises the steps of discharging through an insulating screen, granulating, cooling, collecting material granules and the like. Compared with the prior art, the equipment and the process have the advantages of simple and scientific equipment structure, reasonable process design, quick material cooling, high discharging efficiency and industrial large-scale production requirement fulfillment.
Description
Technical field
The present invention relates to the discharging technology of reactor, especially relate to a kind of discharging technology and special equipment thereof of high viscosity liquid resin.
Background technology
The high viscosity liquid resin, for example polyether-ether-ketone, polyether sulfone are the very high special engineering plastics of temperature classification, have been widely used in special industry, as the Aero-Space parts, special machine parts, military project structural member, electronic component, high-tech sectors such as nuclear power.Generally need carry out purifying to polyether-ether-ketone in the post-processing stages of producing polyether-ether-ketone, as Chinese patent 200910009128.3,200410081436.4, patents such as 99110082.4 have been introduced different purification treating methods.In patent 99110082.4, disclosed a kind of hot dispersing technology of PAEK resin, be with the direct aqueous precipitation of high temperature mucus after the polymerization, pulverize.Yet along with the continuous amplification of reaction unit equipment, polymeric kettle is amplified to 2000m3 by 300m3, because material increases, the drain hole opening is big, can cause following problem 1) the material chap, cooling effectiveness is slack-off.2) discharging 3-4 consuming time hour; 3) water loss increases, and has increased the difficulty of post processing.Material increases, and it is long to pulverize discharging time by a pulverizer, causes the interior material of polymeric kettle reaction time lengthening at high temperature, has influenced the quality of product.Therefore how to improve discharging efficient and become the bottleneck that polymerization is produced, bite problem to be solved.
Summary of the invention
For overcoming above technical problem, the invention provides a kind of discharging equipment and discharging technology thereof that is applicable to the high viscosity liquid resin, have the advantages that discharging is fast, cooling is fit to the large-scale production needs soon.
Discharging equipment of the present invention comprises is located at going out stub bar and being located at out the material collecting tank of stub bar below of reactor exit, it is characterized in that this discharging special equipment also comprises:
Be located at out the heater on the stub bar, the temperature when keeping the material discharging is suddenly lowered the temperature when preventing discharging, and material is blocked in the blanking process.
Be located at out the screen cloth of stub bar bottom, be separated into slice after making material by screen cloth, cool off sooner, also be beneficial to pulverizing.For make after the separation the slice adhesion together, the hole of screen cloth can not be too close, according to screen area, the about 0.5-1 of spacing centimetre, the about 0.5-2cm in aperture.
Be located at the grain-cutter of screen cloth below, this grain-cutter at high temperature tentatively is cut into particle with the mucus that flows out, and is convenient to pulverize.Suggestion adopts the fusion grain-cutter of rotation at a high speed further to raise the efficiency.
Be located at the cooling fluid generator of screen cloth below, cooling fluid results from from the below of the mucus of screen cloth outflow, makes high temperature mucus cool off fast in the process that flows downward.This cooling fluid generator can be distilled water or deionized water, also can be the water smoke that is produced by the steam generator, is distributed in the grain-cutter below.
As another kind of technical scheme, described heater is located at out the stub bar inwall, and inwall is provided with the cavity that is full of thermal medium and has the connector that forms the peripheral passage with extraneous thermal medium.
The described thermal medium cavity that goes out the stub bar inwall can be connected to form the peripheral passage with the heating temperature-control system of reactor.
Its process characteristic is, the above-mentioned discharging special equipment of this process using, and comprise the steps:
A, insulation screen cloth discharging step, promptly material is extruded strip-shaped materials by the stub bar that goes out that is provided with heater from the screen cloth that goes out the stub bar lower end;
B, pelletizing step, material is extruded the back by the grain-cutter of being located at described screen cloth lower end from screen cloth, will be cut into grain from the mucus that screen cloth flows out;
C, cooling step, material is extruded the back by the cooling fluid cooling that is distributed in described screen cloth below from screen cloth;
D, material grain are collected step, are collected by the material collecting tank of being located at the grain-cutter below, and this material collecting tank is connected with pulverizer.
Slower as the polymer discharging speed, can exert pressure to the polymer liquid level by the upper end of polymeric kettle.For example, the inert gas pressurization, pressurized with compressed air or mechanical piston pressing mode are pressurizeed.
With respect to prior art, advantage applies of the present invention exists:
1. the science simple in structure of special equipment, technological design is reasonable.
2. adopt this process stream cooling fast, discharging efficient height is when preventing that polymerization product from high temperature reacting
Between long, guarantee product quality.
3. satisfy the needs that large-scale industrialization is produced, enhance productivity energy-saving low-carbon.
Description of drawings
Accompanying drawing is the preferred embodiment structure principle chart of special equipment of the present invention.
The specific embodiment
As shown in drawings, present embodiment comprises that one cylindrically goes out stub bar 1, can nestedly be fixed on the outlet of reactor, is provided with cavity 10 and can leads to the circulating hot oil heating going out stub bar 1 inwall, cavity 10 is provided with oil-in 11 and is connected with the circulating hot oil of reactor with oil-out 12, forms the peripheral passage.Going out stub bar 1 bottom is screen cloth 2, about 1 centimetre of the spacing of sieve screen apertures, the about 1cm in aperture.Below going out stub bar 1, adopt a fusion grain-cutter 3 of rotation at a high speed, the mucus that flows out at high temperature tentatively is cut into particle 6.Particle 6 is collected by the material collecting tank 5 of being located at out stub bar 1 below, imports to pulverizer and pulverizes.Going out stub bar positioned beneath cooling fluid generator 4, producing condensation water smoke, the material that flows out is being sprayed cold mist cool off.
Its working method comprises the steps:
A, insulation screen cloth discharging step, promptly material is extruded strip-shaped materials by the stub bar 1 that goes out that is provided with heater from the screen cloth 2 that goes out stub bar 1 lower end;
B, pelletizing step, material is extruded the back from screen cloth 2 will be cut into grain from the mucus that screen cloth 2 flows out by the grain-cutter 3 of being located at described screen cloth 2 lower ends;
C, cooling step, material is extruded the back by the cooling fluid generator 4 ejection condensed water fog coolings that are distributed in described screen cloth 2 belows from screen cloth 2;
D, material grain are collected step, are collected by the material collecting tank 5 of being located at grain-cutter 3 belows, and this material collecting tank 5 is connected with pulverizer.
Claims (5)
1. the discharging special equipment of a high viscosity liquid resin comprises and is located at going out stub bar and being located at out the material collecting tank of stub bar below of reactor exit, it is characterized in that this discharging special equipment also comprises:
-be located at out the heater on the stub bar;
-be located at out the screen cloth of stub bar lower end, the gap is 0.5-1cm between the hole of this screen cloth, the pore diameter range of screen cloth is 0.5-2cm;
Be located at the grain-cutter of screen cloth below, will be cut into particle from the mucus that screen cloth flows out;
Be located at the cooling fluid generator of screen cloth below, the coolant distribution of described cooling fluid generator in the below of the mucus that flows out from screen cloth, make cooling fast the process that high temperature mucus flowing downward.
2. discharging special equipment as claimed in claim 1 is characterized in that described heater is located at out the stub bar inwall, and inwall is provided with the cavity of filling thermal medium and has the connector that forms the peripheral passage with extraneous thermal medium.
3. discharging special equipment as claimed in claim 2 is characterized in that, the described heating control apparatus that goes out stub bar inner surface heat dielectric cavity and reactor joins, and forms the thermal medium peripheral passage.
4. discharging special equipment as claimed in claim 1 is characterized in that the cooling fluid of described cooling fluid generator is the water smoke shape, is distributed in the grain-cutter below.
5. the discharging technology of a high viscosity liquid resin is characterized in that, this process using such as right
Require 1 or 2 or 3 or 4 described discharging special equipments, comprise the steps:
A, insulation screen cloth discharging step, promptly material is extruded strip-shaped materials by the stub bar that goes out that is provided with heater from the screen cloth that goes out the stub bar lower end;
B, pelletizing step, material is extruded the back by the grain-cutter of being located at described screen cloth lower end from screen cloth, will be cut into grain from the mucus that screen cloth flows out;
C, cooling step, material is extruded the back by the cooling fluid cooling that is distributed in described screen cloth below from screen cloth;
D, material grain are collected step, are collected by the material collecting tank of being located at the grain-cutter below, and this material collecting tank is connected with pulverizer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100575575A CN102160980A (en) | 2011-03-10 | 2011-03-10 | High viscosity liquid resin discharging process and dedicated equipment thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100575575A CN102160980A (en) | 2011-03-10 | 2011-03-10 | High viscosity liquid resin discharging process and dedicated equipment thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102160980A true CN102160980A (en) | 2011-08-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011100575575A Pending CN102160980A (en) | 2011-03-10 | 2011-03-10 | High viscosity liquid resin discharging process and dedicated equipment thereof |
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| CN (1) | CN102160980A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102672842A (en) * | 2012-05-20 | 2012-09-19 | 湖州展望药业有限公司 | Manufacturing device and preparation method for resin grains |
| TWI837856B (en) * | 2022-10-03 | 2024-04-01 | 品元實業股份有限公司 | Jelly bobas and apparatus and method for forming same |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2247086Y (en) * | 1996-02-13 | 1997-02-12 | 王慧宁 | Horizontal water circular heating granule cutting machine |
| CN1417015A (en) * | 2001-11-08 | 2003-05-14 | 上海欧亚合成材料有限公司 | Thermosetting plastic extruding and pelletizing process |
| CN1558818A (en) * | 2001-09-25 | 2004-12-29 | Granulating mill and process for the production of cut pieces | |
| JP2006257117A (en) * | 2005-03-15 | 2006-09-28 | Trial Corp | Granulation apparatus and granulation method |
-
2011
- 2011-03-10 CN CN2011100575575A patent/CN102160980A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2247086Y (en) * | 1996-02-13 | 1997-02-12 | 王慧宁 | Horizontal water circular heating granule cutting machine |
| CN1558818A (en) * | 2001-09-25 | 2004-12-29 | Granulating mill and process for the production of cut pieces | |
| CN1417015A (en) * | 2001-11-08 | 2003-05-14 | 上海欧亚合成材料有限公司 | Thermosetting plastic extruding and pelletizing process |
| JP2006257117A (en) * | 2005-03-15 | 2006-09-28 | Trial Corp | Granulation apparatus and granulation method |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102672842A (en) * | 2012-05-20 | 2012-09-19 | 湖州展望药业有限公司 | Manufacturing device and preparation method for resin grains |
| CN102672842B (en) * | 2012-05-20 | 2014-07-02 | 湖州展望药业有限公司 | Manufacturing device and preparation method for resin grains |
| TWI837856B (en) * | 2022-10-03 | 2024-04-01 | 品元實業股份有限公司 | Jelly bobas and apparatus and method for forming same |
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Application publication date: 20110824 |