CN106186728A - A kind of wetting agent configuration system producing continuous basalt fiber - Google Patents
A kind of wetting agent configuration system producing continuous basalt fiber Download PDFInfo
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- CN106186728A CN106186728A CN201610773502.7A CN201610773502A CN106186728A CN 106186728 A CN106186728 A CN 106186728A CN 201610773502 A CN201610773502 A CN 201610773502A CN 106186728 A CN106186728 A CN 106186728A
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C25/00—Surface treatment of fibres or filaments made from glass, minerals or slags
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Abstract
A kind of wetting agent configuration system producing continuous basalt fiber, relate to Inorganic Non-metallic Materials manufacture field, it is charging system the most 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 form, part discharge nozzle I converges at retort charging aperture, remaining discharge nozzle I converges 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 is connected with PLC with valve.The present invention is that wetting agent provides optimal dissolving and reaction temperature, is delivered directly in wire-drawing frame by wetting agent, it is achieved that automatic proportioning, improves production efficiency and the quality of basalt fibre.
Description
Technical field
The present invention relates to Inorganic Non-metallic Materials manufacture field, particularly relate to a kind of infiltration producing continuous basalt fiber
Agent configuration system.
Background technology
Continuous basalt fiber is using natural volcano effusive rock as raw material, adds in melting furnaces after being crushed,
After 1450～1500 DEG C are melted, the continuous fiber made by bushing.It is with carbon fiber, aramid fiber, superhigh molecular weight polyethylene
Other tec fibers such as alkene fiber (UHMWPE) are compared, and have a lot of unique advantage, as good in mechanical property, resistance to elevated temperatures
Good, can work continuously in the range of-269～650 DEG C, acid-fast alkali-proof, anti-ultraviolet property is strong, and hygroscopicity is low, has preferably
Environmental resistance, additionally, also good insulation preformance, the advantage such as high temperature filtration is good, radioprotective, good wave transparent performance.With even
Continuous basalt fibre is the composite that reinforcement can be made into various excellent performance, 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 producing continuous basalt fiber, need to smear wetting agent from leakage bushing tow out, existing
Configuration operation complexity, the labor intensive of some wetting agents, reduce the production efficiency of basalt fibre.
Summary of the invention
The shortcoming that the present invention is to solve above-mentioned prior art, it is provided that a kind of wetting agent producing continuous basalt fiber
Configuration system, this system can provide optimal Compounding conditions, it is possible to realizes automatic proportioning such that it is able to improves basalt fine
The production efficiency of dimension and quality.
The present invention is achieved in that a kind of wetting agent configuration system producing continuous basalt fiber, depends on from top to bottom
Secondary is charging system, retort, mixing tank and sub-feed tube, and described charging system is by feed pot, stirring of being arranged in feed pot
The heating mantle I, the liquid level sensor I being arranged in feed pot that mix device I, are arranged on outside feed pot, it is arranged on feed pot band
Being made up of the water inlet pipe I of valve I and the discharge nozzle I being provided with valve II, the discharge nozzle I of n feed pot is in the charging of retort
Converging at Kou, n is the integer more than or equal to 2, and the discharge nozzle I of remaining feed pot and the discharge nozzle II of retort are at mixing tank
Converge at charging aperture, retort be internally provided with agitating device II, air blowing ring and liquid level sensor II, the outside of retort sets
Being equipped with heating mantle II, retort top is provided with the water inlet pipe II with valve III, and the bottom of retort is provided with valve
The discharge nozzle II of IV, mixing tank be internally provided with agitating device III and liquid level sensor III, the outside of mixing tank is provided with and adds
Hot jacket III, the bottom of mixing tank is provided with the discharge nozzle III with valve V, and this discharge nozzle III is connected with sub-feed tube, each sub-material
Valve VI it is both provided with on pipe, wherein, the input phase of liquid level sensor I, liquid level sensor II and liquid level sensor III and PLC
Even, valve I, valve II, valve III, valve IV are connected with the outfan of PLC with valve V.
Described valve I, valve II, valve III, valve IV and valve V are electromagnetic valve.
Being provided with steam inlet I bottom described heating mantle I, heating mantle I top is provided with steam (vapor) outlet I, steam inlet I
On be provided with valve VII, steam (vapor) outlet I is provided with valve VIII.
Being provided with steam inlet II bottom described heating mantle II, heating mantle II top is provided with steam (vapor) outlet II, steam
It is provided with valve Ⅸ in import II, steam (vapor) outlet II is provided with valve Ⅹ.
Being provided with steam inlet III bottom described heating mantle III, heating mantle III top is provided with steam (vapor) outlet III, steam
It is provided with valve Ⅺ in import III, steam (vapor) outlet III is provided with valve Ⅻ.
Described air blowing ring is for carrying leachy looped pipeline, and this 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 part, discharge nozzle II is arranged on the lowest part that retort is tank bottoms, and discharge nozzle III is arranged on the lowest part that mixing tank is tank bottoms.
Relative to prior art, the invention has the beneficial effects as follows:
The invention provides a kind of wetting agent configuration system producing continuous basalt fiber, this system utilizes heating mantle for infiltration
The raw material of agent provides optimal dissolving and reaction temperature, is connected with PLC with valve by liquid level sensor, utilizes sub-feed tube to soak
Profit agent is delivered directly in the baster of wire-drawing frame, it is achieved that automatic proportioning, improves the production efficiency of basalt fibre
And quality.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Detailed description of the invention
Embodiment 1
As it is shown in figure 1, a kind of wetting agent configuration system producing continuous basalt fiber, be the most successively charging system,
Retort 1, mixing tank 2 and sub-feed tube 3, agitating device I 5 that described charging system by feed pot 4, is arranged in feed pot,
The heating mantle I 6, the liquid level sensor I 7 being arranged in feed pot that are arranged on outside feed pot, it is arranged on feed pot with valve I
The water inlet pipe I 9 of 8 and discharge nozzle I 11 composition being provided with valve II 10, discharge nozzle I 11 the entering in retort 1 of n feed pot
Converging at material mouth, n is the integer more than or equal to 2, and the discharge nozzle I 11 of remaining feed pot 4 exists with the discharge nozzle II 12 of retort 1
Converge at the charging aperture of mixing tank, retort 1 be 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, and retort top is provided with the water inlet pipe II 18 with valve III 17, instead
The bottom answering tank 1 is provided with the discharge nozzle II 12 with valve IV 19, mixing tank 2 be internally provided with agitating device III 20 and liquid
Level sensor III 21, the outside of mixing tank 2 is provided with heating mantle III 22, and the bottom of mixing tank is provided with going out with valve V 23
Material pipe III 24, this discharge nozzle III 24 is connected with sub-feed tube 3, and each sub-feed tube is both provided with valve VI 25, wherein, level sensing
Device I 7, liquid level sensor II 15 are connected with the input of PLC with liquid level sensor III 21, valve I 8, valve II 10, valve III
17, valve IV 19 is connected with the outfan of PLC with valve V 23.
Described valve I 8, valve II 10, valve III 17, valve IV 19 and valve V 23 are electromagnetic valve.
Being provided with steam inlet I 26 bottom described heating mantle I 6, heating mantle I 6 top is provided with steam (vapor) outlet I 27, steams
It is provided with valve VII 28 on vapor inlet I, steam (vapor) outlet I is provided with valve VIII 29.Because the material dissolution at configuration wetting agent
Required temperature is different, and the heating mantle I 6 outside the most each feed pot 4 is respectively arranged with steam (vapor) outlet I 27, steam enters
Mouth I 26, valve VII 28 and valve VIII 29, choose whether use steam and select use during using as required
The temperature of steam, thus provide optimal solution temperature for whole raw material.
Being provided with steam inlet II 30 bottom described heating mantle II 16, heating mantle II 16 top is provided with steam (vapor) outlet II
31, steam inlet II is provided with valve Ⅸ 32, steam (vapor) outlet II is provided with valve Ⅹ 33.Because the formula of wetting agent is not
With, some formula need part material chemical reaction first occurs, its product again with other raw material hybrid reaction, and retort 1
It it is exactly the container of part material hybrid reaction.Because the temperature needed for different reactions is different, the therefore heating outside retort 1
Overlap and on II 16, be provided with steam (vapor) outlet II 31, steam inlet II 30, valve Ⅸ 32 and valve Ⅹ 33, can be according to entering into reaction
The reaction temperature needed for raw material in tank 1 chooses whether to need use steam and can select the temperature of the steam used, from
And be that the reaction of raw material provides optimal reaction temperature.
Being provided with steam inlet III 34 bottom described heating mantle III 22, heating mantle III 22 top is provided with steam (vapor) outlet III
35, steam inlet III is provided with valve Ⅺ 36, steam (vapor) outlet III is provided with valve Ⅻ 37.Because joining of different wetting agents
Fang Butong, the temperature that they react required is different, and the heating mantle III 22 therefore arranged outside mixing tank 2 is provided with steam (vapor) outlet
III 35, according to the reaction temperature needed for raw material, steam inlet III 34, valve Ⅺ 36 and valve Ⅻ 37, can choose whether that needs make
With steam and the temperature of steam used can be selected, thus provide optimal reaction temperature for whole reaction.
Described air blowing ring 14 is for carrying leachy looped pipeline, and this pipeline is connected with aerator, the air blowing ring of retort 1
The quantity of 14 is two.Such structure has the advantage that (a) can work in coordination with agitating device II 13, accelerates to need the most instead
The mixing of the raw material answered and reaction；B product in retort 1 can be blown in mixing tank 2 by ()；C () produces when reaction
After thing is flowed in mixing tank 2, the valve III 17 of water inlet pipe II 18 is opened, under the effect of air blowing ring 14, by the tank of retort 1
The product of wall residual purges in mixing tank 2.
The number of described feed pot 4 is the integer more than or equal to 3.During using, according to the formula of wetting agent
Selecting the number of feed pot 4, the number of feed pot can be any value of the integer more than or equal to 3, and will be according to wetting agent
Formula determine the number of feed pot that the charging aperture with retort 1 is connected.
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 part, discharge nozzle II 12 is arranged on the lowest part that retort 1 is tank bottoms, and it is tank bottoms that discharge nozzle III 24 is arranged on mixing tank 2
Lowest part.Such setting is not so that the bottom of feed pot 4, retort 1 and mixing tank 2 has solution residual.
During using, decide whether as required to open the valve VII 28 of heating mantle I 6 and valve VIII 29, heating
Overlap the valve Ⅸ 32 of II 16 and the valve Ⅺ 36 of valve Ⅹ 33 and heating mantle III 22 and valve Ⅻ 37, add in feed pot 4
Initial raw material, opens agitating device I 5, and signal is passed to PLC by the liquid level sensor I 7 of each feed pot, and PLC is according to setting
Value controls the folding of valve I 8 on water inlet pipe I 9, and initial raw material is mix homogeneously, level sensing under the stirring of agitating device I 5
Signal is passed to the discharge nozzle I 11 that PLC, PLC need the feed pot 4 at the raw material place first reacted according to setup control by device I 7
The opening and closing of valve II 10, simultaneously close off all feed pot valve I 8.Open agitating device II 13 and aerator, enter into reaction
The biochemical reaction of raw material hybrid concurrency in tank, signal is passed to PLC, PLC and opens according to the value arranged by liquid level sensor II 15
The discharge nozzle I 11 of the feed pot 4 at the valve IV 19 opening discharge nozzle II 12 and the raw material place that need not hybrid reaction in advance
Valve II 10, opens agitating device III 20, the product of antedating response and remaining raw material and enters 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 all enters into mixing tank 2, liquid level
Signal is passed to PLC, PLC according to setting closedown valve IV 19 and valve II 10 by 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, signal is passed to PLC by liquid level sensor II 15, and PLC is according to setting
Open valve III 17 and the valve IV 19 of discharge nozzle II 12 of water inlet pipe II 18, under the effect blowing water ring 14, by retort 1
The product of tank skin residual purges in mixing tank 2, and after the liquor capacity in mixing tank 2 reaches setting value, liquid level passes
Signal is passed to PLC, PLC and closes valve III 17 valve V 23 of opening on discharge nozzle III 24 according to arranging by sensor III 21,
The raw material prepared enters in sub-feed tube 3.Because sub-feed tube is connected with the baster of wire-drawing frame, workman can determine as required
Fixed the most whether Open valve VI 25, it is possible to control the flow of wetting agent voluntarily.
Embodiment 2
As it is shown in figure 1, a kind of wetting agent configuration system producing continuous basalt fiber, be the most successively charging system,
Retort 1, mixing tank 2 and sub-feed tube 3, agitating device I 5 that described charging system by feed pot 4, is arranged in feed pot,
The heating mantle I 6, the liquid level sensor I 7 being arranged in feed pot that are arranged on outside feed pot, it is arranged on feed pot with valve I
The water inlet pipe I 9 of 8 and discharge nozzle I 11 composition being provided with valve II 10, discharge nozzle I 11 the entering in retort 1 of 3 feed pots
Converging at material mouth, the discharge nozzle I 11 of remaining 1 feed pot 4 and the discharge nozzle II 12 of retort 1 are at the charging aperture of mixing tank
Converge, retort 1 be internally provided with agitating device II 13, air blowing ring 14 and liquid level sensor II 15, the outside of retort 1 sets
Being equipped with heating mantle II 16, retort top is provided with the water inlet pipe II 18 with valve III 17, and the bottom of retort 1 is provided with band
Have the discharge nozzle II 12 of valve IV 19, mixing tank 2 be internally provided with agitating device III 20 and liquid level sensor III 21, mixing tank
The outside of 2 is provided with heating mantle III 22, and the bottom of mixing tank is provided with the discharge nozzle III 24 with valve V 23, this discharge nozzle III
24 are connected with sub-feed tube 3, and each sub-feed tube is both provided with valve VI 25, wherein, liquid level sensor I 7, liquid level sensor II 15
It is connected with the input of PLC with liquid level sensor III 21, valve I 8, valve II 10, valve III 17, valve IV 19 and valve V 23
It is 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.
Being provided with steam inlet I 26 bottom described heating mantle I 6, heating mantle I 6 top is provided with steam (vapor) outlet I 27, steams
It is provided with valve VII 28 on vapor inlet I, steam (vapor) outlet I is provided with valve VIII 29.Because the material dissolution at configuration wetting agent
Required temperature is different, and the heating mantle I 6 outside the most each feed pot 4 is respectively arranged with steam (vapor) outlet I 27, steam enters
Mouth I 26, valve VII 28 and valve VIII 29, choose whether use steam and select use during using as required
The temperature of steam, thus provide optimal solution temperature for whole raw material.
Being provided with steam inlet II 30 bottom described heating mantle II 16, heating mantle II 16 top is provided with steam (vapor) outlet II
31, steam inlet II is provided with valve Ⅸ 32, steam (vapor) outlet II is provided with valve Ⅹ 33.Because the formula of wetting agent is not
With, some formula need part material chemical reaction first occurs, its product again with other raw material hybrid reaction, and retort 1
It it is exactly the container of part material hybrid reaction.Because the temperature needed for different reactions is different, the therefore heating outside retort 1
Overlap and on II 16, be provided with steam (vapor) outlet II 31, steam inlet II 30, valve Ⅸ 32 and valve Ⅹ 33, can be according to entering into reaction
The reaction temperature needed for raw material in tank 1 chooses whether to need use steam and can select the temperature of the steam used, from
And be that the reaction of raw material provides optimal reaction temperature.
Being provided with steam inlet III 34 bottom described heating mantle III 22, heating mantle III 22 top is provided with steam (vapor) outlet III
35, steam inlet III is provided with valve Ⅺ 36, steam (vapor) outlet III is provided with valve Ⅻ 37.Because joining of different wetting agents
Fang Butong, the temperature that they react required is different, and the heating mantle III 22 therefore arranged outside mixing tank 2 is provided with steam (vapor) outlet
III 35, according to the reaction temperature needed for raw material, steam inlet III 34, valve Ⅺ 36 and valve Ⅻ 37, can choose whether that needs make
With steam and the temperature of steam used can be selected, thus provide optimal reaction temperature for whole reaction.
Described air blowing ring 14 is for carrying leachy looped pipeline, and this pipeline is connected with aerator, the air blowing ring of retort 1
The quantity of 14 is two.Such structure has the advantage that (a) can work in coordination with agitating device II 13, accelerates to need the most instead
The mixing of the raw material answered and reaction；B product in retort 1 can be blown in mixing tank 2 by ()；C () produces when reaction
After thing is flowed in mixing tank 2, the valve III 17 of water inlet pipe II 18 is opened, under the effect of air blowing ring 14, by the tank of retort 1
The product of wall residual purges in mixing tank 2.
The number of the formulation selection feed pot 4 according to wetting agent is 4.
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 part, discharge nozzle II 12 is arranged on the lowest part that retort 1 is tank bottoms, and it is tank bottoms that discharge nozzle III 24 is arranged on mixing tank 2
Lowest part.Such setting is not so that the bottom of feed pot 4, retort 1 and mixing tank 2 has solution residual.
During using, decide whether as required to open the valve VII 28 of heating mantle I 6 and valve VIII 29, heating
Overlap the valve Ⅸ 32 of II 16 and the valve Ⅺ 36 of valve Ⅹ 33 and heating mantle III 22 and valve Ⅻ 37, add in feed pot 4
Initial raw material, opens agitating device I 5, and signal is passed to PLC by the liquid level sensor I 7 of each feed pot, and PLC is according to setting
Value controls the folding of valve I 8 on water inlet pipe I 9, and initial raw material is mix homogeneously, level sensing under the stirring of agitating device I 5
Signal is passed to the discharge nozzle I 11 that PLC, PLC need the feed pot 4 at the raw material place first reacted according to setup control by device I 7
The opening and closing of valve II 10, simultaneously close off all feed pot valve I 8.Open agitating device II 13 and aerator, enter into reaction
The biochemical reaction of raw material hybrid concurrency in tank, signal is passed to PLC, PLC and opens according to the value arranged by liquid level sensor II 15
The discharge nozzle I 11 of the feed pot 4 at the valve IV 19 opening discharge nozzle II 12 and the raw material place that need not hybrid reaction in advance
Valve II 10, opens agitating device III 20, the product of antedating response and remaining raw material and enters 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 all enters into mixing tank 2, liquid level
Signal is passed to PLC, PLC according to setting closedown valve IV 19 and valve II 10 by 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, signal is passed to PLC by liquid level sensor II 15, and PLC is according to setting
Open valve III 17 and the valve IV 19 of discharge nozzle II 12 of water inlet pipe II 18, under the effect blowing water ring 14, by retort 1
The product of tank skin residual purges in mixing tank 2, and after the liquor capacity in mixing tank 2 reaches setting value, liquid level passes
Signal is passed to PLC, PLC and closes valve III 17 valve V 23 of opening on discharge nozzle III 24 according to arranging by sensor III 21,
The raw material prepared enters in sub-feed tube 3.Because sub-feed tube is connected with the baster of wire-drawing frame, workman can determine as required
Fixed the most whether Open valve VI 25, it is possible to control the flow of wetting agent voluntarily.
Embodiment 3
As it is shown in figure 1, a kind of wetting agent configuration system producing continuous basalt fiber, be the most successively charging system,
Retort 1, mixing tank 2 and sub-feed tube 3, agitating device I 5 that described charging system by feed pot 4, is arranged in feed pot,
The heating mantle I 6, the liquid level sensor I 7 being arranged in feed pot that are arranged on outside feed pot, it is arranged on feed pot with valve I
The water inlet pipe I 9 of 8 and discharge nozzle I 11 composition being provided with valve II 10, discharge nozzle I 11 the entering in retort 1 of 3 feed pots
Converging at material mouth, the discharge nozzle I 11 of remaining 2 feed pots 4 and the discharge nozzle II 12 of retort 1 are at the charging aperture of mixing tank
Converge, retort 1 be internally provided with agitating device II 13, air blowing ring 14 and liquid level sensor II 15, the outside of retort 1 sets
Being equipped with heating mantle II 16, retort top is provided with the water inlet pipe II 18 with valve III 17, and the bottom of retort 1 is provided with band
Have the discharge nozzle II 12 of valve IV 19, mixing tank 2 be internally provided with agitating device III 20 and liquid level sensor III 21, mixing tank
The outside of 2 is provided with heating mantle III 22, and the bottom of mixing tank is provided with the discharge nozzle III 24 with valve V 23, this discharge nozzle III
24 are connected with sub-feed tube 3, and each sub-feed tube is both provided with valve VI 25, wherein, liquid level sensor I 7, liquid level sensor II 15
It is connected with the input of PLC with liquid level sensor III 21, valve I 8, valve II 10, valve III 17, valve IV 19 and valve V 23
It is 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.
Being provided with steam inlet I 26 bottom described heating mantle I 6, heating mantle I 6 top is provided with steam (vapor) outlet I 27, steams
It is provided with valve VII 28 on vapor inlet I, steam (vapor) outlet I is provided with valve VIII 29.Because the material dissolution at configuration wetting agent
Required temperature is different, and the heating mantle I 6 outside the most each feed pot 4 is respectively arranged with steam (vapor) outlet I 27, steam enters
Mouth I 26, valve VII 28 and valve VIII 29, choose whether use steam and select use during using as required
The temperature of steam, thus provide optimal solution temperature for whole raw material.
Being provided with steam inlet II 30 bottom described heating mantle II 16, heating mantle II 16 top is provided with steam (vapor) outlet II
31, steam inlet II is provided with valve Ⅸ 32, steam (vapor) outlet II is provided with valve Ⅹ 33.Because the formula of wetting agent is not
With, some formula need part material chemical reaction first occurs, its product again with other raw material hybrid reaction, and retort 1
It it is exactly the container of part material hybrid reaction.Because the temperature needed for different reactions is different, the therefore heating outside retort 1
Overlap and on II 16, be provided with steam (vapor) outlet II 31, steam inlet II 30, valve Ⅸ 32 and valve Ⅹ 33, can be according to entering into reaction
The reaction temperature needed for raw material in tank 1 chooses whether to need use steam and can select the temperature of the steam used, from
And be that the reaction of raw material provides optimal reaction temperature.
Being provided with steam inlet III 34 bottom described heating mantle III 22, heating mantle III 22 top is provided with steam (vapor) outlet III
35, steam inlet III is provided with valve Ⅺ 36, steam (vapor) outlet III is provided with valve Ⅻ 37.Because joining of different wetting agents
Fang Butong, the temperature that they react required is different, and the heating mantle III 22 therefore arranged outside mixing tank 2 is provided with steam (vapor) outlet
III 35, according to the reaction temperature needed for raw material, steam inlet III 34, valve Ⅺ 36 and valve Ⅻ 37, can choose whether that needs make
With steam and the temperature of steam used can be selected, thus provide optimal reaction temperature for whole reaction.
Described air blowing ring 14 is for carrying leachy looped pipeline, and this pipeline is connected with aerator, the air blowing ring of retort 1
The quantity of 14 is two.Such structure has the advantage that (a) can work in coordination with agitating device II 13, accelerates to need the most instead
The mixing of the raw material answered and reaction；B product in retort 1 can be blown in mixing tank 2 by ()；C () produces when reaction
After thing is flowed in mixing tank 2, the valve III 17 of water inlet pipe II 18 is opened, under the effect of air blowing ring 14, by the tank of retort 1
The product of wall residual purges in mixing tank 2.
The number of the formulation selection feed pot 4 according to wetting agent is 5.
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 part, discharge nozzle II 12 is arranged on the lowest part that retort 1 is tank bottoms, and it is tank bottoms that discharge nozzle III 24 is arranged on mixing tank 2
Lowest part.Such setting is not so that the bottom of feed pot 4, retort 1 and mixing tank 2 has solution residual.
During using, decide whether as required to open the valve VII 28 of heating mantle I 6 and valve VIII 29, heating
Overlap the valve Ⅸ 32 of II 16 and the valve Ⅺ 36 of valve Ⅹ 33 and heating mantle III 22 and valve Ⅻ 37, add in feed pot 4
Initial raw material, opens agitating device I 5, and signal is passed to PLC by the liquid level sensor I 7 of each feed pot, and PLC is according to setting
Value controls the folding of valve I 8 on water inlet pipe I 9, and initial raw material is mix homogeneously, level sensing under the stirring of agitating device I 5
Signal is passed to the discharge nozzle I 11 that PLC, PLC need the feed pot 4 at the raw material place first reacted according to setup control by device I 7
The opening and closing of valve II 10, simultaneously close off all feed pot valve I 8.Open agitating device II 13 and aerator, enter into reaction
The biochemical reaction of raw material hybrid concurrency in tank, signal is passed to PLC, PLC and opens according to the value arranged by liquid level sensor II 15
The discharge nozzle I 11 of the feed pot 4 at the valve IV 19 opening discharge nozzle II 12 and the raw material place that need not hybrid reaction in advance
Valve II 10, opens agitating device III 20, the product of antedating response and remaining raw material and enters 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 all enters into mixing tank 2, liquid level
Signal is passed to PLC, PLC according to setting closedown valve IV 19 and valve II 10 by 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, signal is passed to PLC by liquid level sensor II 15, and PLC is according to setting
Open valve III 17 and the valve IV 19 of discharge nozzle II 12 of water inlet pipe II 18, under the effect blowing water ring 14, by retort 1
The product of tank skin residual purges in mixing tank 2, and after the liquor capacity in mixing tank 2 reaches setting value, liquid level passes
Signal is passed to PLC, PLC and closes valve III 17 valve V 23 of opening on discharge nozzle III 24 according to arranging by sensor III 21,
The raw material prepared enters in sub-feed tube 3.Because sub-feed tube is connected with the baster of wire-drawing frame, workman can determine as required
Fixed the most whether Open valve VI 25, it is possible to control the flow of wetting agent voluntarily.
Embodiment 4
As it is shown in figure 1, a kind of wetting agent configuration system producing continuous basalt fiber, be the most successively charging system,
Retort 1, mixing tank 2 and sub-feed tube 3, agitating device I 5 that described charging system by feed pot 4, is arranged in feed pot,
The heating mantle I 6, the liquid level sensor I 7 being arranged in feed pot that are arranged on outside feed pot, it is arranged on feed pot with valve I
The water inlet pipe I 9 of 8 and discharge nozzle I 11 composition being provided with valve II 10, discharge nozzle I 11 the entering in retort 1 of 2 feed pots
Converging at material mouth, the discharge nozzle I 11 of remaining 2 feed pots 4 and the discharge nozzle II 12 of retort 1 are at the charging aperture of mixing tank
Converge, retort 1 be internally provided with agitating device II 13, air blowing ring 14 and liquid level sensor II 15, the outside of retort 1 sets
Being equipped with heating mantle II 16, retort top is provided with the water inlet pipe II 18 with valve III 17, and the bottom of retort 1 is provided with band
Have the discharge nozzle II 12 of valve IV 19, mixing tank 2 be internally provided with agitating device III 20 and liquid level sensor III 21, mixing tank
The outside of 2 is provided with heating mantle III 22, and the bottom of mixing tank is provided with the discharge nozzle III 24 with valve V 23, this discharge nozzle III
24 are connected with sub-feed tube 3, and each sub-feed tube is both provided with valve VI 25, wherein, liquid level sensor I 7, liquid level sensor II 15
It is connected with the input of PLC with liquid level sensor III 21, valve I 8, valve II 10, valve III 17, valve IV 19 and valve V 23
It is 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.
Being provided with steam inlet I 26 bottom described heating mantle I 6, heating mantle I 6 top is provided with steam (vapor) outlet I 27, steams
It is provided with valve VII 28 on vapor inlet I, steam (vapor) outlet I is provided with valve VIII 29.Because the material dissolution at configuration wetting agent
Required temperature is different, and the heating mantle I 6 outside the most each feed pot 4 is respectively arranged with steam (vapor) outlet I 27, steam enters
Mouth I 26, valve VII 28 and valve VIII 29, choose whether use steam and select use during using as required
The temperature of steam, thus provide optimal solution temperature for whole raw material.
Being provided with steam inlet II 30 bottom described heating mantle II 16, heating mantle II 16 top is provided with steam (vapor) outlet II
31, steam inlet II is provided with valve Ⅸ 32, steam (vapor) outlet II is provided with valve Ⅹ 33.Because the formula of wetting agent is not
With, some formula need part material chemical reaction first occurs, its product again with other raw material hybrid reaction, and retort 1
It it is exactly the container of part material hybrid reaction.Because the temperature needed for different reactions is different, the therefore heating outside retort 1
Overlap and on II 16, be provided with steam (vapor) outlet II 31, steam inlet II 30, valve Ⅸ 32 and valve Ⅹ 33, can be according to entering into reaction
The reaction temperature needed for raw material in tank 1 chooses whether to need use steam and can select the temperature of the steam used, from
And be that the reaction of raw material provides optimal reaction temperature.
Being provided with steam inlet III 34 bottom described heating mantle III 22, heating mantle III 22 top is provided with steam (vapor) outlet III
35, steam inlet III is provided with valve Ⅺ 36, steam (vapor) outlet III is provided with valve Ⅻ 37.Because joining of different wetting agents
Fang Butong, the temperature that they react required is different, and the heating mantle III 22 therefore arranged outside mixing tank 2 is provided with steam (vapor) outlet
III 35, according to the reaction temperature needed for raw material, steam inlet III 34, valve Ⅺ 36 and valve Ⅻ 37, can choose whether that needs make
With steam and the temperature of steam used can be selected, thus provide optimal reaction temperature for whole reaction.
Described air blowing ring 14 is for carrying leachy looped pipeline, and this pipeline is connected with aerator, the air blowing ring of retort 1
The quantity of 14 is two.Such structure has the advantage that (a) can work in coordination with agitating device II 13, accelerates to need the most instead
The mixing of the raw material answered and reaction；B product in retort 1 can be blown in mixing tank 2 by ()；C () produces when reaction
After thing is flowed in mixing tank 2, the valve III 17 of water inlet pipe II 18 is opened, under the effect of air blowing ring 14, by the tank of retort 1
The product of wall residual purges in mixing tank 2.
The number of the formulation selection feed pot 4 according to wetting agent is 4.
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 part, discharge nozzle II 12 is arranged on the lowest part that retort 1 is tank bottoms, and it is tank bottoms that discharge nozzle III 24 is arranged on mixing tank 2
Lowest part.Such setting is not so that the bottom of feed pot 4, retort 1 and mixing tank 2 has solution residual.
During using, decide whether as required to open the valve VII 28 of heating mantle I 6 and valve VIII 29, heating
Overlap the valve Ⅸ 32 of II 16 and the valve Ⅺ 36 of valve Ⅹ 33 and heating mantle III 22 and valve Ⅻ 37, add in feed pot 4
Initial raw material, opens agitating device I 5, and signal is passed to PLC by the liquid level sensor I 7 of each feed pot, and PLC is according to setting
Value controls the folding of valve I 8 on water inlet pipe I 9, and initial raw material is mix homogeneously, level sensing under the stirring of agitating device I 5
Signal is passed to the discharge nozzle I 11 that PLC, PLC need the feed pot 4 at the raw material place first reacted according to setup control by device I 7
The opening and closing of valve II 10, simultaneously close off all feed pot valve I 8.Open agitating device II 13 and aerator, enter into reaction
The biochemical reaction of raw material hybrid concurrency in tank, signal is passed to PLC, PLC and opens according to the value arranged by liquid level sensor II 15
The discharge nozzle I 11 of the feed pot 4 at the valve IV 19 opening discharge nozzle II 12 and the raw material place that need not hybrid reaction in advance
Valve II 10, opens agitating device III 20, the product of antedating response and remaining raw material and enters 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 all enters into mixing tank 2, liquid level
Signal is passed to PLC, PLC according to setting closedown valve IV 19 and valve II 10 by 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, signal is passed to PLC by liquid level sensor II 15, and PLC is according to setting
Open valve III 17 and the valve IV 19 of discharge nozzle II 12 of water inlet pipe II 18, under the effect blowing water ring 14, by retort 1
The product of tank skin residual purges in mixing tank 2, and after the liquor capacity in mixing tank 2 reaches setting value, liquid level passes
Signal is passed to PLC, PLC and closes valve III 17 valve V 23 of opening on discharge nozzle III 24 according to arranging by sensor III 21,
The raw material prepared enters in sub-feed tube 3.Because sub-feed tube is connected with the baster of wire-drawing frame, workman can determine as required
Fixed the most whether Open valve VI 25, it is possible to control the flow of wetting agent voluntarily.
Embodiment 5
As it is shown in figure 1, a kind of wetting agent configuration system producing continuous basalt fiber, be the most successively charging system,
Retort 1, mixing tank 2 and sub-feed tube 3, agitating device I 5 that described charging system by feed pot 4, is arranged in feed pot,
The heating mantle I 6, the liquid level sensor I 7 being arranged in feed pot that are arranged on outside feed pot, it is arranged on feed pot with valve I
The water inlet pipe I 9 of 8 and discharge nozzle I 11 composition being provided with valve II 10, discharge nozzle I 11 the entering in retort 1 of 3 feed pots
Converging at material mouth, the discharge nozzle I 11 of remaining 2 feed pots 4 and the discharge nozzle II 12 of retort 1 are at the charging aperture of mixing tank
Converge, retort 1 be internally provided with agitating device II 13, air blowing ring 14 and liquid level sensor II 15, the outside of retort 1 sets
Being equipped with heating mantle II 16, retort top is provided with the water inlet pipe II 18 with valve III 17, and the bottom of retort 1 is provided with band
Have the discharge nozzle II 12 of valve IV 19, mixing tank 2 be internally provided with agitating device III 20 and liquid level sensor III 21, mixing tank
The outside of 2 is provided with heating mantle III 22, and the bottom of mixing tank is provided with the discharge nozzle III 24 with valve V 23, this discharge nozzle III
24 are connected with sub-feed tube 3, and each sub-feed tube is both provided with valve VI 25, wherein, liquid level sensor I 7, liquid level sensor II 15
It is connected with the input of PLC with liquid level sensor III 21, valve I 8, valve II 10, valve III 17, valve IV 19 and valve V 23
It is 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.
Being provided with steam inlet I 26 bottom described heating mantle I 6, heating mantle I 6 top is provided with steam (vapor) outlet I 27, steams
It is provided with valve VII 28 on vapor inlet I, steam (vapor) outlet I is provided with valve VIII 29.Because the material dissolution at configuration wetting agent
Required temperature is different, and the heating mantle I 6 outside the most each feed pot 4 is respectively arranged with steam (vapor) outlet I 27, steam enters
Mouth I 26, valve VII 28 and valve VIII 29, choose whether use steam and select use during using as required
The temperature of steam, thus provide optimal solution temperature for whole raw material.
Being provided with steam inlet II 30 bottom described heating mantle II 16, heating mantle II 16 top is provided with steam (vapor) outlet II
31, steam inlet II is provided with valve Ⅸ 32, steam (vapor) outlet II is provided with valve Ⅹ 33.Because the formula of wetting agent is not
With, some formula need part material chemical reaction first occurs, its product again with other raw material hybrid reaction, and retort 1
It it is exactly the container of part material hybrid reaction.Because the temperature needed for different reactions is different, the therefore heating outside retort 1
Overlap and on II 16, be provided with steam (vapor) outlet II 31, steam inlet II 30, valve Ⅸ 32 and valve Ⅹ 33, can be according to entering into reaction
The reaction temperature needed for raw material in tank 1 chooses whether to need use steam and can select the temperature of the steam used, from
And be that the reaction of raw material provides optimal reaction temperature.
Being provided with steam inlet III 34 bottom described heating mantle III 22, heating mantle III 22 top is provided with steam (vapor) outlet III
35, steam inlet III is provided with valve Ⅺ 36, steam (vapor) outlet III is provided with valve Ⅻ 37.Because joining of different wetting agents
Fang Butong, the temperature that they react required is different, and the heating mantle III 22 therefore arranged outside mixing tank 2 is provided with steam (vapor) outlet
III 35, according to the reaction temperature needed for raw material, steam inlet III 34, valve Ⅺ 36 and valve Ⅻ 37, can choose whether that needs make
With steam and the temperature of steam used can be selected, thus provide optimal reaction temperature for whole reaction.
Described air blowing ring 14 is for carrying leachy looped pipeline, and this pipeline is connected with aerator, the air blowing ring of retort 1
The quantity of 14 is two.Such structure has the advantage that (a) can work in coordination with agitating device II 13, accelerates to need the most instead
The mixing of the raw material answered and reaction；B product in retort 1 can be blown in mixing tank 2 by ()；C () produces when reaction
After thing is flowed in mixing tank 2, the valve III 17 of water inlet pipe II 18 is opened, under the effect of air blowing ring 14, by the tank of retort 1
The product of wall residual purges in mixing tank 2.
The number of the formulation selection feed pot 4 according to wetting agent is 5.
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 part, discharge nozzle II 12 is arranged on the lowest part that retort 1 is tank bottoms, and it is tank bottoms that discharge nozzle III 24 is arranged on mixing tank 2
Lowest part.Such setting is not so that the bottom of feed pot 4, retort 1 and mixing tank 2 has solution residual.
During using, decide whether as required to open the valve VII 28 of heating mantle I 6 and valve VIII 29, heating
Overlap the valve Ⅸ 32 of II 16 and the valve Ⅺ 36 of valve Ⅹ 33 and heating mantle III 22 and valve Ⅻ 37, add in feed pot 4
Initial raw material, opens agitating device I 5, and signal is passed to PLC by the liquid level sensor I 7 of each feed pot, and PLC is according to setting
Value controls the folding of valve I 8 on water inlet pipe I 9, and initial raw material is mix homogeneously, level sensing under the stirring of agitating device I 5
Signal is passed to the discharge nozzle I 11 that PLC, PLC need the feed pot 4 at the raw material place first reacted according to setup control by device I 7
The opening and closing of valve II 10, simultaneously close off all feed pot valve I 8.Open agitating device II 13 and aerator, enter into reaction
The biochemical reaction of raw material hybrid concurrency in tank, signal is passed to PLC, PLC and opens according to the value arranged by liquid level sensor II 15
The discharge nozzle I 11 of the feed pot 4 at the valve IV 19 opening discharge nozzle II 12 and the raw material place that need not hybrid reaction in advance
Valve II 10, opens agitating device III 20, the product of antedating response and remaining raw material and enters 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 all enters into mixing tank 2, liquid level
Signal is passed to PLC, PLC according to setting closedown valve IV 19 and valve II 10 by 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, signal is passed to PLC by liquid level sensor II 15, and PLC is according to setting
Open valve III 17 and the valve IV 19 of discharge nozzle II 12 of water inlet pipe II 18, under the effect blowing water ring 14, by retort 1
The product of tank skin residual purges in mixing tank 2, and after the liquor capacity in mixing tank 2 reaches setting value, liquid level passes
Signal is passed to PLC, PLC and closes valve III 17 valve V 23 of opening on discharge nozzle III 24 according to arranging by sensor III 21,
The raw material prepared enters in sub-feed tube 3.Because sub-feed tube is connected with the baster of wire-drawing frame, workman can determine as required
Fixed the most whether Open valve VI 25, it is possible to control the flow of wetting agent voluntarily.
Embodiment 6
As it is shown in figure 1, a kind of wetting agent configuration system producing continuous basalt fiber, be the most successively charging system,
Retort 1, mixing tank 2 and sub-feed tube 3, agitating device I 5 that described charging system by feed pot 4, is arranged in feed pot,
The heating mantle I 6, the liquid level sensor I 7 being arranged in feed pot that are arranged on outside feed pot, it is arranged on feed pot with valve I
The water inlet pipe I 9 of 8 and discharge nozzle I 11 composition being provided with valve II 10, discharge nozzle I 11 the entering in retort 1 of 3 feed pots
Converging at material mouth, the discharge nozzle I 11 of remaining 3 feed pots 4 and the discharge nozzle II 12 of retort 1 are at the charging aperture of mixing tank
Converge, retort 1 be internally provided with agitating device II 13, air blowing ring 14 and liquid level sensor II 15, the outside of retort 1 sets
Being equipped with heating mantle II 16, retort top is provided with the water inlet pipe II 18 with valve III 17, and the bottom of retort 1 is provided with band
Have the discharge nozzle II 12 of valve IV 19, mixing tank 2 be internally provided with agitating device III 20 and liquid level sensor III 21, mixing tank
The outside of 2 is provided with heating mantle III 22, and the bottom of mixing tank is provided with the discharge nozzle III 24 with valve V 23, this discharge nozzle III
24 are connected with sub-feed tube 3, and each sub-feed tube is both provided with valve VI 25, wherein, liquid level sensor I 7, liquid level sensor II 15
It is connected with the input of PLC with liquid level sensor III 21, valve I 8, valve II 10, valve III 17, valve IV 19 and valve V 23
It is 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.
Being provided with steam inlet I 26 bottom described heating mantle I 6, heating mantle I 6 top is provided with steam (vapor) outlet I 27, steams
It is provided with valve VII 28 on vapor inlet I, steam (vapor) outlet I is provided with valve VIII 29.Because the material dissolution at configuration wetting agent
Required temperature is different, and the heating mantle I 6 outside the most each feed pot 4 is respectively arranged with steam (vapor) outlet I 27, steam enters
Mouth I 26, valve VII 28 and valve VIII 29, choose whether use steam and select use during using as required
The temperature of steam, thus provide optimal solution temperature for whole raw material.
Being provided with steam inlet II 30 bottom described heating mantle II 16, heating mantle II 16 top is provided with steam (vapor) outlet II
31, steam inlet II is provided with valve Ⅸ 32, steam (vapor) outlet II is provided with valve Ⅹ 33.Because the formula of wetting agent is not
With, some formula need part material chemical reaction first occurs, its product again with other raw material hybrid reaction, and retort 1
It it is exactly the container of part material hybrid reaction.Because the temperature needed for different reactions is different, the therefore heating outside retort 1
Overlap and on II 16, be provided with steam (vapor) outlet II 31, steam inlet II 30, valve Ⅸ 32 and valve Ⅹ 33, can be according to entering into reaction
The reaction temperature needed for raw material in tank 1 chooses whether to need use steam and can select the temperature of the steam used, from
And be that the reaction of raw material provides optimal reaction temperature.
Being provided with steam inlet III 34 bottom described heating mantle III 22, heating mantle III 22 top is provided with steam (vapor) outlet III
35, steam inlet III is provided with valve Ⅺ 36, steam (vapor) outlet III is provided with valve Ⅻ 37.Because joining of different wetting agents
Fang Butong, the temperature that they react required is different, and the heating mantle III 22 therefore arranged outside mixing tank 2 is provided with steam (vapor) outlet
III 35, according to the reaction temperature needed for raw material, steam inlet III 34, valve Ⅺ 36 and valve Ⅻ 37, can choose whether that needs make
With steam and the temperature of steam used can be selected, thus provide optimal reaction temperature for whole reaction.
Described air blowing ring 14 is for carrying leachy looped pipeline, and this pipeline is connected with aerator, the air blowing ring of retort 1
The quantity of 14 is two.Such structure has the advantage that (a) can work in coordination with agitating device II 13, accelerates to need the most instead
The mixing of the raw material answered and reaction；B product in retort 1 can be blown in mixing tank 2 by ()；C () produces when reaction
After thing is flowed in mixing tank 2, the valve III 17 of water inlet pipe II 18 is opened, under the effect of air blowing ring 14, by the tank of retort 1
The product of wall residual purges in mixing tank 2.
The number of the formulation selection feed pot 4 according to wetting agent is 6.
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 part, discharge nozzle II 12 is arranged on the lowest part that retort 1 is tank bottoms, and it is tank bottoms that discharge nozzle III 24 is arranged on mixing tank 2
Lowest part.Such setting is not so that the bottom of feed pot 4, retort 1 and mixing tank 2 has solution residual.
During using, decide whether as required to open the valve VII 28 of heating mantle I 6 and valve VIII 29, heating
Overlap the valve Ⅸ 32 of II 16 and the valve Ⅺ 36 of valve Ⅹ 33 and heating mantle III 22 and valve Ⅻ 37, add in feed pot 4
Initial raw material, opens agitating device I 5, and signal is passed to PLC by the liquid level sensor I 7 of each feed pot, and PLC is according to setting
Value controls the folding of valve I 8 on water inlet pipe I 9, and initial raw material is mix homogeneously, level sensing under the stirring of agitating device I 5
Signal is passed to the discharge nozzle I 11 that PLC, PLC need the feed pot 4 at the raw material place first reacted according to setup control by device I 7
The opening and closing of valve II 10, simultaneously close off all feed pot valve I 8.Open agitating device II 13 and aerator, enter into reaction
The biochemical reaction of raw material hybrid concurrency in tank, signal is passed to PLC, PLC and opens according to the value arranged by liquid level sensor II 15
The discharge nozzle I 11 of the feed pot 4 at the valve IV 19 opening discharge nozzle II 12 and the raw material place that need not hybrid reaction in advance
Valve II 10, opens agitating device III 20, the product of antedating response and remaining raw material and enters 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 all enters into mixing tank 2, liquid level
Signal is passed to PLC, PLC according to setting closedown valve IV 19 and valve II 10 by 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, signal is passed to PLC by liquid level sensor II 15, and PLC is according to setting
Open valve III 17 and the valve IV 19 of discharge nozzle II 12 of water inlet pipe II 18, under the effect blowing water ring 14, by retort 1
The product of tank skin residual purges in mixing tank 2, and after the liquor capacity in mixing tank 2 reaches setting value, liquid level passes
Signal is passed to PLC, PLC and closes valve III 17 valve V 23 of opening on discharge nozzle III 24 according to arranging by sensor III 21,
The raw material prepared enters in sub-feed tube 3.Because sub-feed tube is connected with the baster of wire-drawing frame, workman can determine as required
Fixed the most whether Open valve VI 25, it is possible to control the flow of wetting agent voluntarily.
Embodiment described above, the simply one of the present invention more preferably detailed description of the invention, those skilled in the art
The usual variations and alternatives that member is carried out in the range of technical solution of the present invention are intended to be included in protection scope of the present invention.
Claims (8)
1. produce a wetting agent configuration system for continuous basalt fiber, be charging system, retort the most successively
(1), mixing tank (2) and sub-feed tube (3), it is characterised in that: described charging system by feed pot (4), be arranged in feed pot
Agitating device I (5), the heating mantle I (6) being arranged on outside feed pot, the liquid level sensor I (7) being arranged in feed pot, arrange
On feed pot with valve I (8) water inlet pipe I (9) and be provided with valve II (10) discharge nozzle I (11) composition, n charging
The discharge nozzle I (11) of tank converges at the charging aperture of retort (1), and n is the integer more than or equal to 2, remaining feed pot (4)
Discharge nozzle I (11) converges at the charging aperture of mixing tank with the discharge nozzle II (12) of retort (1), and the inside of retort (1) sets
Being equipped 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), retort top is provided with the water inlet pipe II (18) with valve III (17), and the bottom of retort (1) is provided with valve
Door IV (19) discharge nozzle II (12), mixing tank (2) be internally provided with agitating device III (20) and liquid level sensor III (21),
The outside of mixing tank (2) is provided with heating mantle III (22), and the bottom of mixing tank is provided with the discharge nozzle III with valve V (23)
(24), this discharge nozzle III (24) is connected with sub-feed tube (3), and each sub-feed tube is both provided with valve VI (25), and wherein, liquid level passes
Sensor I (7), liquid level sensor II (15) are connected with the input of PLC with liquid level sensor III (21), valve I (8), valve II
(10), valve III (17), valve IV (19) are connected with the outfan of PLC with valve V (23).
The wetting agent configuration system of production continuous basalt fiber the most according to claim 1, it is characterised in that: described
Valve I (8), valve II (10), valve III (17), valve IV (19) and valve V (23) are electromagnetic valve.
The wetting agent configuration system of production continuous basalt fiber the most according to claim 1, it is characterised in that: described
Heating mantle I (6) bottom is provided with steam inlet I (26), and heating mantle I (6) top is provided with steam (vapor) outlet I (27), steam inlet I
On be provided with valve VII (28), steam (vapor) outlet I is provided with valve VIII (29).
The wetting agent configuration system of production continuous basalt fiber the most according to claim 1, it is characterised in that: described
Heating mantle II (16) bottom is provided with steam inlet II (30), and heating mantle II (16) top is provided with steam (vapor) outlet II (31), steams
It is provided with valve Ⅸ (32) on vapor inlet II, steam (vapor) outlet II is provided with valve Ⅹ (33).
The wetting agent configuration system of production continuous basalt fiber the most according to claim 1, it is characterised in that: described
Heating mantle III (22) bottom is provided with steam inlet III (34), and heating mantle III (22) top is provided with steam (vapor) outlet III (35), steams
It is provided with valve Ⅺ (36) on vapor inlet III, steam (vapor) outlet III is provided with valve Ⅻ (37).
The wetting agent configuration system of production continuous basalt fiber the most according to claim 1, it is characterised in that: described
Air blowing ring (14) is for carrying leachy looped pipeline, and this pipeline is connected with aerator, the quantity of the air blowing ring (14) of retort (1)
It it is two.
The wetting agent configuration system of production continuous basalt fiber the most according to claim 1, it is characterised in that: described
The number of feed pot (4) is the integer more than or equal to 3.
The wetting agent configuration system of production continuous basalt fiber the most according to claim 1, it is characterised in that: described
The bottom of feed pot (4), retort (1) and mixing tank (2) is inverted cone, and it is tank bottoms that discharge nozzle I (11) is arranged on feed pot (4)
Lowest part, discharge nozzle II (12) is arranged on the lowest part that retort (1) is tank bottoms, and discharge nozzle III (24) is arranged on mixing tank (2)
Tank bottoms lowest part.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610773502.7A CN106186728B (en) | 2016-08-31 | 2016-08-31 | A kind of size compounding system producing continuous basalt fiber |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610773502.7A CN106186728B (en) | 2016-08-31 | 2016-08-31 | A kind of size compounding system producing continuous basalt fiber |
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| CN106186728B CN106186728B (en) | 2018-11-16 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN114953199A (en) * | 2022-06-29 | 2022-08-30 | 泉州坚石混凝土建材有限公司 | Full-automatic batching conveying equipment for concrete production |
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|---|---|
| CN106186728B (en) | 2018-11-16 |
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Address after: 452477 Yangcheng Industrial Zone, Dengfeng City, Zhengzhou City, Henan Province Patentee after: Zhengzhou electric Basalt Fiber Co. Ltd Address before: 452483 Sanlizhuang High-tech Park, Dengfeng City, Zhengzhou City, Henan Province Patentee before: Zhengzhou electric Basalt Fiber Co. Ltd |