CN206069707U - A kind of wetting agent configuration system for producing continuous basalt fiber - Google Patents
A kind of wetting agent configuration system for producing continuous basalt fiber Download PDFInfo
- Publication number
- CN206069707U CN206069707U CN201621002985.2U CN201621002985U CN206069707U CN 206069707 U CN206069707 U CN 206069707U CN 201621002985 U CN201621002985 U CN 201621002985U CN 206069707 U CN206069707 U CN 206069707U
- Authority
- CN
- China
- Prior art keywords
- valve
- iii
- discharge nozzle
- retort
- steam
- 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.)
- Expired - Fee Related
Links
Landscapes
- Cookers (AREA)
Abstract
A kind of wetting agent configuration system for producing continuous basalt fiber, it is related to Inorganic Non-metallic Materials manufacture field, it is charging system from top to bottom successively, retort, mixing tank and sub-feed tube, described charging system is by feed pot, agitating device I, heating mantle I, liquid level sensor I, water inlet pipe I and discharge nozzle I are constituted, part discharge nozzle I converges at retort charging aperture, remaining discharge nozzle I is converged at mixing tank charging aperture with discharge nozzle II, retort is provided with agitating device II, air blowing ring, liquid level sensor II, heating mantle II, water inlet pipe II and discharge nozzle II, mixing tank is provided with agitating device III, liquid level sensor III, heating mantle III and discharge nozzle III, liquid level sensor and valve are connected with PLC.This utility model provides optimal dissolving and reaction temperature for wetting agent, and wetting agent is delivered directly in wire-drawing frame, automatic proportioning is realized, and improves the production efficiency and quality of basalt fibre.
Description
Technical field
This utility model is related to Inorganic Non-metallic Materials manufacture field, more particularly to a kind of continuous basalt fiber that produces
Wetting agent configures system.
Background technology
Continuous basalt fiber be using natural volcano effusive rock as raw material, after being crushed add melting furnaces in,
After 1450～1500 DEG C of meltings, by continuous fiber made by bushing.It is with carbon fiber, aramid fiber, superhigh molecular weight polyethylene
Alkene fiber（UHMWPE）Compare Deng other tec fibers, there are many uniquenesses, such as mechanical property is good, resistance to elevated temperatures
It is good, can continuously work in the range of -269～650 DEG C, acid-fast alkali-proof, anti-ultraviolet property are strong, and hygroscopicity is low, have preferably
Environmental resistance, additionally, also good insulation preformance, high temperature filtration is good, radioprotective, good wave transparent performance the advantages of.With even
Continuous basalt fibre can be made into the composite of various excellent performances for reinforcement, can be widely applied to fire-fighting, environmental protection, aviation boat
My god, chemical industry, wind-powered electricity generation, military project, automobile shipbuilding, engineering plastics, the field such as building, military project, civil area.
During production continuous basalt fiber, need to smear wetting agent from leakage bushing tow out, it is existing
The configuration complex operation of some wetting agents, labor intensive, the production efficiency for reducing basalt fibre.
Utility model content
This utility model is in order to solve the shortcoming of above-mentioned prior art, there is provided a kind of leaching for producing continuous basalt fiber
Profit agent configuration system, the system can provide optimal Compounding conditions, can realize automatic proportioning such that it is able to improve the Black Warrior
The production efficiency and quality of rock fiber.
What this utility model was realized in：It is a kind of produce continuous basalt fiber wetting agent configuration system, on to
Under be charging system, retort, mixing tank and sub-feed tube successively, described charging system by feed pot, be arranged in feed pot
Agitating device I, the heating mantle I being arranged on outside feed pot, the liquid level sensor I being arranged in feed pot, be arranged on feed pot
The upper water inlet pipe I with valve I and I composition of discharge nozzle for being provided with valve II, the discharge nozzle I of n feed pot is in retort
Converge at charging aperture, n is the integer more than or equal to 2, and the discharge nozzle I of remaining feed pot is with the discharge nozzle II of retort in batch mixing
Converge at the charging aperture of tank, retort is internally provided with agitating device II, air blowing ring and liquid level sensor II, retort it is outer
Portion is provided with heating mantle II, and the water inlet pipe II with valve III is provided with the top of retort, and the bottom of retort is provided with and carries
The discharge nozzle II of valve IV, mixing tank are internally provided with agitating device III and liquid level sensor III, the outside setting of mixing tank
The bottom for having heating mantle III, mixing tank is provided with the discharge nozzle III with valve V, and the discharge nozzle III is connected with sub-feed tube, each
Valve VI is both provided with sub-feed tube, wherein, the input of liquid level sensor I, liquid level sensor II and liquid level sensor III and PLC
End is connected, and valve I, valve II, valve III, valve IV and valve V are connected with the outfan of PLC.
Described valve I, valve II, valve III, valve IV and valve V are electromagnetic valve.
Described I bottom of heating mantle is provided with steam inlet I, and I top of heating mantle is provided with steam (vapor) outlet I, steam inlet I
On be provided with valve VII, valve VIII is provided with steam (vapor) outlet I.
Described II bottom of heating mantle is provided with steam inlet II, and II top of heating mantle is provided with steam (vapor) outlet II, steam
Valve Ⅸ is provided with import II, valve Ⅹ on steam (vapor) outlet II, is provided with.
Described III bottom of heating mantle is provided with steam inlet III, and III top of heating mantle is provided with steam (vapor) outlet III, steam
Valve Ⅺ is provided with import III, valve Ⅻ on steam (vapor) outlet III, is provided with.
Described air blowing ring is that, with leachy looped pipeline, the pipeline is connected with aerator, the air blowing ring of retort
Quantity is two.
The number of described feed pot is the integer more than or equal to 3.
The bottom of described feed pot, retort and mixing tank is inverted cone, and it is tank bottoms that discharge nozzle I is arranged on feed pot
Lowest point, discharge nozzle II are arranged on the tank bottoms lowest point of retort, and discharge nozzle III is arranged on the tank bottoms lowest point of mixing tank.
Relative to prior art, the beneficial effects of the utility model are：
This utility model provides a kind of wetting agent configuration system for producing continuous basalt fiber, and the system is using heating
Cover the raw material for wetting agent and provide optimal dissolving and reaction temperature, liquid level sensor and valve are connected with PLC, using point
Expects pipe is delivered directly to wetting agent in the baster of wire-drawing frame, realizes automatic proportioning, improves basalt fibre
Production efficiency and quality.
Description of the drawings
Fig. 1 is structural representation of the present utility model.
Specific embodiment
As shown in figure 1, a kind of wetting agent configuration system for producing continuous basalt fiber, is charging system from top to bottom successively
System, retort 1, mixing tank 2 and sub-feed tube 3, described charging system is by feed pot 4, the agitating device being arranged in feed pot I
5th, the heating mantle I 6 being arranged on outside feed pot, the liquid level sensor I 7 being arranged in feed pot, be arranged on feed pot carry valve
The water inlet pipe I 9 of door I 8 is constituted with the discharge nozzle I 11 for being provided with valve II 10, and the discharge nozzle I 11 of n feed pot is in retort 1
Converge at charging aperture, n is the integer more than or equal to 2, the discharge nozzle I 11 of remaining feed pot 4 and the discharge nozzle II 12 of retort 1
Converge at the charging aperture of mixing tank, retort 1 is internally provided with agitating device II 13, air blowing ring 14 and liquid level sensor II
15, the outside of retort 1 is provided with heating mantle II 16, is provided with the water inlet pipe II 18 with valve III 17, instead at the top of retort
The bottom of tank 1 is answered to be provided with the discharge nozzle II 12 with valve IV 19, mixing tank 2 is internally provided with agitating device III 20 and liquid
Level sensor III 21, the outside of mixing tank 2 are provided with heating mantle III 22, and the bottom of mixing tank is provided with going out with valve V 23
Expects pipe III 24, the discharge nozzle III 24 are connected with sub-feed tube 3, and valve VI 25 is both provided with each sub-feed tube, wherein, level sensing
Device I 7, liquid level sensor II 15 and liquid level sensor III 21 are connected with the input of PLC, valve I 8, valve II 10, valve III
17th, valve IV 19 and valve V 23 are connected with the outfan of PLC.
Described valve I 8, valve II 10, valve III 17, valve IV 19 and valve V 23 are electromagnetic valve.
Described I 6 bottom of heating mantle is provided with steam inlet I 26, and I 6 top of heating mantle is provided with steam (vapor) outlet I 27, steams
Valve VII 28 is provided with vapor inlet I, valve VIII 29 on steam (vapor) outlet I, is provided with.Because in the material dissolution of configuration wetting agent
Required temperature is different, therefore the heating mantle I 6 outside each feed pot 4 is respectively arranged with steam (vapor) outlet I 27, steam and enters
Mouth I 26, valve VII 28 and valve VIII 29, choose whether what is used using steam and selection during use as needed
The temperature of steam, so as to provide optimal solution temperature for whole raw material.
Described II 16 bottom of heating mantle is provided with steam inlet II 30, and II 16 top of heating mantle is provided with steam (vapor) outlet II
31, valve Ⅸ 32 is provided with steam inlet II, valve Ⅹ 33 on steam (vapor) outlet II, is provided with.Because the formula of wetting agent is not
Together, need part material that chemical reaction first occurs in some formula, its product again with other raw material hybrid reactions, and retort 1
It is exactly the container of part material hybrid reaction.Because the temperature needed for different reactions is different, therefore the heating outside retort 1
Cover, can be according to entering into reaction
The reaction temperature needed for raw material in tank 1 chooses whether to need the temperature using steam and the steam that can select to use, from
And the reaction for raw material provides optimal reaction temperature.
Described III 22 bottom of heating mantle is provided with steam inlet III 34, and III 22 top of heating mantle is provided with steam (vapor) outlet III
35, valve Ⅺ 36 is provided with steam inlet III, valve Ⅻ 37 on steam (vapor) outlet III, is provided with.Because different wetting agent is matched somebody with somebody
Fang Butong, the temperature required for they react are different, therefore the heating mantle III 22 arranged outside mixing tank 2 is provided with steam (vapor) outlet
III 35, steam inlet III 34, valve Ⅺ 36 and valve Ⅻ 37, reaction temperature that can be according to needed for raw material choose whether that needs make
With steam and the temperature of the steam that can select to use, so as to provide optimal reaction temperature for whole reaction.
Described air blowing ring 14 is that, with leachy looped pipeline, the pipeline is connected with aerator, the air blowing ring of retort 1
14 quantity is two.Such structure has the following advantages that：（a）Agitating device II 13 can be cooperateed with, accelerates to need first instead
The mixing and reaction of the raw material answered；（b）Product in retort 1 can be blown in mixing tank 2；（c）When reaction is produced
After thing is flowed in mixing tank 2, the valve III 17 of water inlet pipe II 18 is opened, in the presence of air blowing ring 14, by the tank of retort 1
The product of wall residual is purged in mixing tank 2.
The number of described feed pot 4 is the integer more than or equal to 3.During use, according to the formula of wetting agent
The number of feed pot 4 is selected, the number of feed pot can be 3,4,5,6,7,8,9,10 etc. any value, and will be according to infiltration
The formula of agent determines the number of the feed pot being connected with the charging aperture of retort 1.
The bottom of described feed pot 4, retort 1 and mixing tank 2 is inverted cone, and discharge nozzle I 11 is arranged on feed pot 4
Tank bottoms lowest point, discharge nozzle II 12 are arranged on the tank bottoms lowest point of retort 1, and it is tank bottoms that discharge nozzle III 24 is arranged on mixing tank 2
Lowest point.Such setting can cause the bottom of feed pot 4, retort 1 and mixing tank 2 not have solution residual.
During use, decide whether as needed to open the valve VII 28 and valve VIII 29 of heating mantle I 6, heating
II 16 valve Ⅸ 32 and the valve Ⅺ 36 of valve Ⅹ 33 and heating mantle III 22 and valve Ⅻ 37 are covered, is added in feed pot 4
Initial raw material, opens agitating device I 5, and, by signal transmission to PLC, PLC is according to setting for the liquid level sensor I 7 of each feed pot
The folding of valve I 8, initial raw material mix homogeneously, level sensing under the stirring of agitating device I 5 on value control water inlet pipe I 9
By signal transmission to PLC, PLC needs the discharge nozzle I 11 of the feed pot 4 at the raw material place reacted first to device I 7 according to setting control
Valve II 10 opening and closing, simultaneously close off all feed pot valve Is 8.Agitating device II 13 and aerator are opened, reaction is entered into
The biochemical reaction of raw material hybrid concurrency in tank, by signal transmission to PLC, PLC is opened liquid level sensor II 15 according to the value for arranging
The discharge nozzle I 11 of the feed pot 4 that the valve IV 19 for opening discharge nozzle II 12 and the raw material that need not shift to an earlier date hybrid reaction are located
Valve II 10, opens agitating device III 20, and the product of antedating response and remaining raw material are entered in mixing tank 2, and
Hybrid reaction under the stirring of agitating device III 20, after the solution in retort 1 and feed pot 4 enters into mixing tank 2, liquid level
, by signal transmission to PLC, PLC closes valve IV 19 and valve II 10 according to setting for sensor I 7 and liquid level sensor II 15.Instead
After answering the solution in tank 1 to be all introduced in mixing tank 2, by signal transmission to PLC, PLC is according to setting for liquid level sensor II 15
The valve IV 19 of the valve III 17 and discharge nozzle II 12 of water inlet pipe II 18 is opened, in the presence of water ring 14 is blown, by retort 1
The product of tank skin residual is purged in mixing tank 2, after the liquor capacity in mixing tank 2 reaches setting value, and liquid level is passed
By signal transmission to PLC, PLC closes valve III 17 according to setting and opens the valve V 23 on discharge nozzle III 24 sensor III 21,
The raw material for preparing is entered in sub-feed tube 3.Because sub-feed tube is connected with the baster of wire-drawing frame, workman can determine as needed
Fixed whether Open valve VI 25, it is possible to voluntarily control the flow of wetting agent.
Embodiment described above, simply one kind of this utility model more preferably specific embodiment, the skill of this area
The usual variations and alternatives that art personnel are carried out in the range of technical solutions of the utility model are intended to be included in guarantor of the present utility model
In the range of shield.
Claims (8)
1. a kind of wetting agent configuration system for producing continuous basalt fiber, is charging system, retort from top to bottom successively
（1）, mixing tank（2）And sub-feed tube（3）, it is characterised in that：Described charging system is by feed pot（4）, be arranged in feed pot
Agitating device I（5）, the heating mantle I that is arranged on outside feed pot（6）, the liquid level sensor I that is arranged in feed pot（7）, arrange
Valve I is carried on feed pot（8）Water inlet pipe I（9）Be provided with valve II（10）Discharge nozzle I（11）Composition, n charging
The discharge nozzle I of tank（11）In retort（1）Charging aperture at converge, n is the integer more than or equal to 2, remaining feed pot（4）'s
Discharge nozzle I（11）With retort（1）Discharge nozzle II（12）Converge at the charging aperture of mixing tank, retort（1）Inside set
It is equipped with agitating device II（13）, air blowing ring（14）With liquid level sensor II（15）, retort（1）Outside be provided with heating mantle II
（16）, it is provided with the top of retort with valve III（17）Water inlet pipe II（18）, retort（1）Bottom be provided with valve
Door IV（19）Discharge nozzle II（12）, mixing tank（2）Be internally provided with agitating device III（20）With liquid level sensor III（21）,
Mixing tank（2）Outside be provided with heating mantle III（22）, the bottom of mixing tank is provided with valve V（23）Discharge nozzle III
（24）, the discharge nozzle III（24）With sub-feed tube（3）It is connected, on each sub-feed tube, is both provided with valve VI（25）, wherein, liquid level is passed
Sensor I（7）, liquid level sensor II（15）With liquid level sensor III（21）It is connected with the input of PLC, valve I（8）, valve II
（10）, valve III（17）, valve IV（19）With valve V（23）It is connected with the outfan of PLC.
2. the wetting agent of production continuous basalt fiber according to claim 1 configures system, it is characterised in that：Described
Valve I（8）, valve II（10）, valve III（17）, valve IV（19）With valve V（23）For electromagnetic valve.
3. the wetting agent of production continuous basalt fiber according to claim 1 configures system, it is characterised in that：Described
Heating mantle I（6）Bottom is provided with steam inlet I（26）, heating mantle I（6）Top is provided with steam (vapor) outlet I（27）, steam inlet I
On be provided with valve VII（28）, on steam (vapor) outlet I, it is provided with valve VIII（29）.
4. the wetting agent of production continuous basalt fiber according to claim 1 configures system, it is characterised in that：Described
Heating mantle II（16）Bottom is provided with steam inlet II（30）, heating mantle II（16）Top is provided with steam (vapor) outlet II（31）, steam
Valve Ⅸ is provided with vapor inlet II（32）, on steam (vapor) outlet II, it is provided with valve Ⅹ（33）.
5. the wetting agent of production continuous basalt fiber according to claim 1 configures system, it is characterised in that：Described
Heating mantle III（22）Bottom is provided with steam inlet III（34）, heating mantle III（22）Top is provided with steam (vapor) outlet III（35）, steam
Valve Ⅺ is provided with vapor inlet III（36）, on steam (vapor) outlet III, it is provided with valve Ⅻ（37）.
6. the wetting agent of production continuous basalt fiber according to claim 1 configures system, it is characterised in that：Described
Air blowing ring（14）It is that, with leachy looped pipeline, the pipeline is connected with aerator, retort（1）Air blowing ring（14）Quantity
For two.
7. the wetting agent of production continuous basalt fiber according to claim 1 configures system, it is characterised in that：Described
Feed pot（4）Number be integer more than or equal to 3.
8. the wetting agent of production continuous basalt fiber according to claim 1 configures system, it is characterised in that：Described
Feed pot（4）, retort（1）And mixing tank（2）Bottom be inverted cone, discharge nozzle I（11）It is arranged on feed pot（4）It is tank bottoms
Lowest point, discharge nozzle II（12）It is arranged on retort（1）Tank bottoms lowest point, discharge nozzle III（24）It is arranged on mixing tank（2）
Tank bottoms lowest point.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621002985.2U CN206069707U (en) | 2016-08-31 | 2016-08-31 | A kind of wetting agent configuration system for producing continuous basalt fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621002985.2U CN206069707U (en) | 2016-08-31 | 2016-08-31 | A kind of wetting agent configuration system for producing continuous basalt fiber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206069707U true CN206069707U (en) | 2017-04-05 |
Family
ID=58434220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621002985.2U Expired - Fee Related CN206069707U (en) | 2016-08-31 | 2016-08-31 | A kind of wetting agent configuration system for producing continuous basalt fiber |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206069707U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106186728A (en) * | 2016-08-31 | 2016-12-07 | 郑州登电玄武石纤有限公司 | A kind of wetting agent configuration system producing continuous basalt fiber |
| CN108103590A (en) * | 2018-01-26 | 2018-06-01 | 江苏南方光纤科技有限公司 | The offline feeding system of coating |
-
2016
- 2016-08-31 CN CN201621002985.2U patent/CN206069707U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106186728A (en) * | 2016-08-31 | 2016-12-07 | 郑州登电玄武石纤有限公司 | A kind of wetting agent configuration system producing continuous basalt fiber |
| CN106186728B (en) * | 2016-08-31 | 2018-11-16 | 郑州登电玄武石纤有限公司 | A kind of size compounding system producing continuous basalt fiber |
| CN108103590A (en) * | 2018-01-26 | 2018-06-01 | 江苏南方光纤科技有限公司 | The offline feeding system of coating |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206069707U (en) | A kind of wetting agent configuration system for producing continuous basalt fiber | |
| CN106186728B (en) | A kind of size compounding system producing continuous basalt fiber | |
| CN108057412A (en) | It is a kind of to be sufficiently stirred the dilution kettle being heated evenly | |
| CN100404415C (en) | Preparation method for carbon bisulfide | |
| CN207655111U (en) | A kind of pressure-resistant reaction kettle in hydrogenation reduction | |
| CN105435684B (en) | A kind of melt mixer of the high viscous material of processing | |
| CN104147952B (en) | A kind of for aramid II prepolymerized material static mixer | |
| CN206688691U (en) | Prepare the reactor and system of sulfamic acid | |
| CN108325492A (en) | A kind of nitration processes and device preparing H acid | |
| CN205550247U (en) | Annular spraying fog formula ethoxylation ware follows outward | |
| CN209423594U (en) | It is a kind of for synthesizing the reaction kettle of Du Lutewei intermediate | |
| CN100582070C (en) | Preparation method of tetrabromobisphenol A | |
| CN206069687U (en) | A kind of kiln feeding device for producing continuous basalt fiber | |
| CN205672901U (en) | A kind of stirring reaction unit producing fast red KD base | |
| CN213253867U (en) | Preparation facilities of covalence organic frame complex film | |
| CN205550245U (en) | Production surface -activeagent's ethoxylation ware | |
| CN209631002U (en) | A kind of industrial chemicals pretreatment unit | |
| CN207913774U (en) | It is a kind of to be sufficiently stirred the dilution kettle being heated evenly | |
| CN104211628A (en) | Production equipment for reduction reaction for producing dicumyl peroxide and production method | |
| CN205392413U (en) | A hydrogenation cauldron for ethylene glycol preparation | |
| CN205340646U (en) | Handle high melting blender that glues material | |
| CN219879914U (en) | Intermediate material feeding device for continuous production of chloramine | |
| CN102030769A (en) | Equipment system for industrially producing Grignard reagent by using gaseous halogenated hydrocarbon | |
| CN105218577B (en) | A kind of method that use double solvents, three component catalysts synthesize γ mercaptopropyltriethoxysilanes | |
| CN216786308U (en) | CaSO4 whisker reactor using desulfurized gypsum as raw material |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: 452483 Yangcheng Industrial Zone, Dengfeng City, Henan Province Patentee after: ZHENGZHOU DENGDIAN CBF CO.,LTD. Address before: 452483 Sanlizhuang High-tech Park, Dengfeng City, Zhengzhou City, Henan Province Patentee before: ZHENGZHOU DENGDIAN CBF CO.,LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170405 Termination date: 20210831 |