CN204017525U - The liquid-circulating treatment system of fiber dispersion, expansion or broadening, thin layer device - Google Patents
The liquid-circulating treatment system of fiber dispersion, expansion or broadening, thin layer device Download PDFInfo
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- CN204017525U CN204017525U CN201420487877.3U CN201420487877U CN204017525U CN 204017525 U CN204017525 U CN 204017525U CN 201420487877 U CN201420487877 U CN 201420487877U CN 204017525 U CN204017525 U CN 204017525U
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Abstract
The utility model relates to the auxiliary device of fiber dispersion, expansion or broadening, thin layer production and processing.Be characterised in that, comprise Self-flow filtering groove group and cooling bath, Self-flow filtering groove group utilizes liquid level difference by several reservoirs, and by height, low sequentially laying forms, and reception comes from the liquid of described fiber treatment groove and filters it; Cooling bath is built-in with cooling coil, receives the liquid after via Self-flow filtering groove group filtration treatment also where necessary to its process that cools, and its outlet end is connected with described fiber treatment groove by returning liquid mozzle.The utility model improves fiber dispersion, expansion or broadening, thin layer validity, uniformity and reliability, by the filtering function of Self-flow filtering groove group, improve or purify the fiber suede amount in working environment air, thus ensure that operating personnel are healthy, the normal work of support equipment electric control system.
Description
Technical field
The utility model relates to the auxiliary device of a kind of liquid-circulating treatment system, particularly a kind of fiber dispersion, expansion or broadening, thin layer production and processing.
background technology
The liquid of initial fiber dispersion, expansion or broadening, thin layer device is (as shown in Figure 2) that be left intact, and liquid uses for a long time in dispersion, expansion or broadening, thin layer groove.Shortcoming is: ul-trasonic irradiation is in liquid, and the conversion of ultrasonic wave and liquid energy, makes fluid temperature constantly raise, and the dispersion of fiber, expansion or broadening, thin layer performance, effect change with temperature, and the dispersion of long-term fiber, expansion or broadening, thin layer, the fiber suede amount come off in a liquid constantly increases, one is the mechanical performance of the running roller affected in groove, two is dispersions, expansion or broadening, thin layer good fiber is easy to the fiber suede be scattered in a liquid to take out of, in dispersion, expansion or broadening, in the process of thin layer good fiber drying, fiber suede can float in air, one is can be sucked by the operating personnel at scene, affect personnel healthy, two is can be sucked by on-site electrical equipment radiator fan, cause electrical equipment electrical equipment or element open circuit, damage electrical control equipment.
First time improve be by the liquid of dispersion, expansion or broadening, thin layer groove through piping filter, fan-cooled radiator, reservoir, after fan-cooled radiator, be transmitted back to dispersion again, expand or broadening, in thin layer groove (as shown in Figure 3).Advantage: improve dispersion, expansion or broadening, liquid temperature rise and fiber dispersion, expansion or broadening, thin layer performance and effect make moderate progress in thin layer groove; Shortcoming is: piping filter is easy to often be blocked by fiber suede, and the radiating efficiency of fan-cooled radiator is low, and cooling-down effect is undesirable, noise is large.
Summary of the invention
The utility model be intended to the fiber dispersion after improving for first time, expansion or broadening, thin layer device liquid handling device carry out secondary improvement, and then provide that a kind of efficiency of lowering the temperature is high, the fiber dispersion of improving fiber dispersion, expansion or broadening, thin layer validity, uniformity and the reliability fiber suede amount simultaneously in cleaning ambient air, expansion or broadening, thin layer device liquid-circulating treatment system.
For achieving the above object, the utility model have employed following technical scheme:
The liquid-circulating treatment system of fiber dispersion, expansion or broadening, thin layer device, be communicated with to form closed loop by the fiber treatment groove 1 of pipeline and fiber dispersion, expansion or broadening, thin layer device, special character is, it comprises:
Self-flow filtering groove group, low sequentially laying forms by height to utilize liquid level difference by several reservoirs, and reception comes from the liquid of described fiber treatment groove 1 and carries out filtration treatment to it; Comprise the liquid feeding end be connected with the fluid mozzle 5 of described fiber treatment groove 1, and be communicated to the outlet end of cooling bath 24 by middle diversion pipeline;
Cooling bath 24, is built-in with cooling coil 25, and receive the liquid after via Self-flow filtering groove group filtration treatment also where necessary to its process that cools, its outlet end passes through back liquid mozzle 10 and is connected with described fiber treatment groove 1.
Described Self-flow filtering groove group is that according to liquid level difference, by height, low laying forms by 2-8 the reservoir with screen pack; The reservoir that wherein liquid level is relatively low is positioned at the bottom of the overfall of the relatively high reservoir of liquid level, and the reservoir that liquid level is minimum is connected with cooling bath 24 by middle diversion pipeline;
Described Self-flow filtering groove group is that according to liquid level difference, by height, low arrangement forms by three reservoirs, comprise the one-level reservoir 15 with single filter net 14 and one-level overfall 16, the secondary reservoir 18 with cascade filtration net 17 and secondary overfall 19, and there are three grades of reservoirs 21 of three-stage filtration net 20; Described secondary reservoir 18 is positioned at the bottom of described one-level overfall 16, described three grades of reservoirs 21 are positioned at the bottom of described secondary overfall 19, and the liquid after one-level, secondary, three grades of reservoirs filter finally is discharged by three grades of reservoirs 21 and pumps in described cooling bath 24;
The described fluid mozzle 5 be communicated between fiber treatment groove 1 and described Self-flow filtering groove group is provided with first-class gauge 12 and the first ball valve 13;
The described middle diversion pipeline be communicated between Self-flow filtering groove group and cooling bath 24 is provided with the first circulating pump 28, second gauge 22 and the second ball valve 23;
The described time liquid mozzle 10 be communicated between cooling bath 24 and fiber treatment groove 1 is provided with the second circulating pump 29, the 3rd flowmeter 26 and the 3rd ball valve 27.
Described cooling coil 25 connects and is controlled by outside cooling-water machine 30, the inner liquid temperature of described fiber treatment groove 1 is detected by described cooling-water machine 30, when liquid temperature is higher than preset temperature, cooling-water machine 30 starts, and the liquid of controlled cooling model coil pipe 25 to described cooling bath 24 inside cools.
The utility model is a kind of to fiber dispersion, expansion or broadening, liquid required in thin layer process does the circulating treating system of closed-loop control, utilize the Self-flow filtering groove group of liquid level difference simultaneously, cooling coil in cooling bath and there is the cooling-water machine of temperature control system of closed loop, its advantage is the efficiency that can improve liquid cooling, fiber dispersion can be ensured by the temperature setting of cooling-water machine, expansion or broadening, work in suitable temperature range time thin layer, temperature is regulated and controled by cooling-water machine start and stop when producing deviation in time, improve fiber dispersion, expansion or broadening, thin layer validity, uniformity and reliability, by the filtering function of Self-flow filtering groove group, improve or purify the fiber suede amount in working environment air, thus ensure that operating personnel are healthy, the normal work of support equipment electric control system.
Accompanying drawing explanation
Fig. 1: the utility model is connected with the liquid-circulating treatment system structural representation of the fiber dispersion of fiber treatment groove, expansion or broadening, thin layer device;
Figure 1A: the liquid-circulating treatment system structural representation of the utility model fiber dispersion, expansion or broadening, thin layer device;
Figure 1B: the liquid-circulating treatment system operation principle block diagram of the utility model fiber dispersion, expansion or broadening, thin layer device;
Fig. 2: the fiber dispersion of the first generation, expansion or broadening, thin layer device, be left intact to liquid, not yet has and carries out for liquid the device that processes;
Fig. 3: the fiber dispersion of the second generation, expansion or broadening, thin layer device, be provided with treating apparatus liquid being carried out to air-cooled process, but effect is unsatisfactory;
Fig. 3 A: the operation principle block diagram of the liquid handling device of the second generation.
In Fig. 1,1, fiber treatment groove, 5, fluid mozzle, 10, liquid mozzle is returned, 12, first-class gauge, the 13, first ball valve, 14, single filter net, 15, one-level reservoir, 16, one-level overfall, 17, cascade filtration net, 18, secondary reservoir, 19, secondary overfall, 20, three-stage filtration net, 21, three grades of reservoirs, 22, second gauge, the 23, second ball valve, 24, cooling bath, 25, cooling coil, 26, the 3rd flowmeter, the 27, the 3rd ball valve, the 28, first circulating pump, 29, the second circulating pump, 30, cooling-water machine.
Detailed description of the invention
Referring to accompanying drawing, provide detailed description of the invention of the present utility model, be used for being further described structure of the present utility model.
Embodiment 1
The liquid-circulating treatment system of the fiber dispersion of the present embodiment, expansion or broadening, thin layer device is with reference to figure 1-Figure 1B, it is the liquid-circulating treatment system being matched in fiber dispersion, expansion or broadening, thin layer device, the fiber treatment groove 1 of itself and fiber dispersion, expansion or broadening, thin layer device designs existence liquid level difference, the liquid level of fiber treatment groove 1 higher than the highest liquid level of native system, and then enables the liquid in fiber treatment groove 1 inner from flowing into native system.
The liquid-circulating treatment system of fiber dispersion, expansion or broadening, thin layer device comprises two parts, and a part is Self-flow filtering groove group, and one other component is cooling bath.
Described Self-flow filtering groove group is by the relatively high one-level reservoir 15 of liquid level, liquid level relatively slightly low secondary reservoir 18 and the relatively low three grades of reservoirs 21 of liquid level arranges from high to low according to liquid level and forms, the liquid of described fiber treatment groove 1 is inner from flowing into one-level reservoir 15 by fluid mozzle 5, and carry out single filter by the single filter net 14 set by its inside, then flow into via one-level overfall 16 the secondary reservoir 18 being positioned at its underpart inner, cascade filtration is carried out by the cascade filtration net 17 of secondary reservoir 18 inside, then flow into via secondary overfall 19 the three grades of reservoirs 21 being positioned at its underpart inner, and after carrying out three-stage filtration by the three-stage filtration net 20 of three grades of reservoir 21 inside, finally to be flowed out by the liquid outlet of three grades of reservoirs 21 and via middle diversion pipeline, and the first circulating pump 28 on pipeline and the second ball valve 23 to pump into cooling bath 24 inner, cooling bath 24 is controlled by and is communicated with outside cooling-water machine 30, liquid temperature in cooling-water machine 30 pairs of fiber treatment grooves 1 is set with a temperature-control range and monitors its variations in temperature at any time, when liquid temperature is higher than the temperature-control range value preset, now cooling-water machine 30 self-starting, and carry out cooling down by the cooling coil 25 pairs of liquid being positioned at cooling bath 24 inside, when liquid temperature is in the temperature-control range interval of presetting, now cooling-water machine 30 does not work.In cooling bath 24 inside through cooling down or do not need the liquid of cooling down via the inside returning liquid mozzle 10 and the second circulating pump 29 and the 3rd ball valve 27 and again pump into fiber treatment groove 1, so far, system completes the course of work of a closed loop.
First-class gauge 12 and the first ball valve 13 be equipped with fluid mozzle 5 between fiber treatment groove 1 and gravity flow reservoir 15, to adjust the flow of flow and metering importing gravity flow reservoir 15; The first circulating pump 28, second gauge 22, second ball valve 23 is provided with, to adjust the flow of flow and metering inflow cooling bath 24 between described three grades of reservoirs 21 and cooling bath 24;
Described one-level reservoir 15, secondary reservoir 18, three grades of reservoirs 21 can be rectangle or other any shapes, and material can be the material of stainless steel or other not easily corrosions;
Described one-level reservoir 15 is higher than secondary reservoir 18, and secondary reservoir 18 exists liquid level difference successively higher than between three grades of reservoirs, 21, three cell bodies, flows automatically to realize liquid and filters between these three cell bodies;
It is inner that described single filter net 14, cascade filtration net 17, three-stage filtration net 20 are detachably installed on one-level reservoir 15, secondary reservoir 18 and three grades of reservoirs 21 respectively, can take out cleaning filter screen at any time, described filter screen shape can be rectangle or other any shapes; Material can be the material of stainless steel or other not easily corrosions;
Described cooling coil 25 is placed in cooling bath 24; Its material is stainless steel or other materials that not easily corrosion heat conduction is good;
First-class gauge 12, first ball valve 13 and second gauge 22, second ball valve 23 and the 3rd flowmeter 26, the 3rd ball valve 27 ensure the flow equilibrium of the whole circulatory system.
The course of work of the present utility model and operation principle as follows:
The liquid of fiber treatment groove 1 is imported to single filter net 14 and one-level reservoir 15 by first-class gauge 12, first ball valve 13 by fluid mozzle 5;
One-level reservoir 15 liquid overflows to cascade filtration net 17 and secondary reservoir 18 by one-level overfall 16;
Secondary reservoir 18 liquid overflows to three-stage filtration net 20 and three grades of reservoirs 21 by secondary overfall 19;
Liquid in three grades of reservoirs 21 pumps in cooling bath 24 by second gauge 22, second ball valve 23 by the first circulating pump 28;
Liquid in cooling bath 24 pumps in fiber treatment groove 1 by the 3rd flowmeter 26, the 3rd ball valve 27, return flow guide pipe 10 by the second circulating pump 29 again;
First-class gauge 12, first ball valve 13 and second gauge 22, second ball valve 23 and the 3rd flowmeter 26, the 3rd ball valve 27 are for controlling the flow equilibrium of whole system liquid-circulating.
Whole fluid circulation system is not by the impact of cooling-water machine start and stop, and the work of the utility model system works with fiber treatment groove 1;
The fluid temperature of fiber treatment groove 1 is depended in the work of described cooling-water machine 30, when the temperature of fiber treatment groove 1 is higher than the temperature window set, cooling-water machine works, reduce the temperature of liquid in cooling bath 24, the liquid of reduction is sent back to fiber treatment groove 1 and make the temperature of fiber treatment groove 1 drop to (see Figure 1B Suo Shi) in required temperature range.
Claims (9)
1. the liquid-circulating treatment system of fiber dispersion, expansion or broadening, thin layer device, be communicated with by the fiber treatment groove (1) of pipeline and fiber dispersion, expansion or broadening, thin layer device to form closed loop, be characterised in that, it comprises:
Self-flow filtering groove group, low sequentially laying forms by height to utilize liquid level difference by several reservoirs, and reception comes from the liquid of described fiber treatment groove (1) and carries out filtration treatment to it; Comprise the liquid feeding end be connected with the fluid mozzle (5) of described fiber treatment groove (1), and be communicated to the outlet end of cooling bath (24) by middle diversion pipeline;
Cooling bath (24), is built-in with cooling coil (25), and receive the liquid after via Self-flow filtering groove group filtration treatment also where necessary to its process that cools, its outlet end passes through back liquid mozzle (10) and is connected with described fiber treatment groove (1).
2. the liquid-circulating treatment system of fiber dispersion as claimed in claim 1, expansion or broadening, thin layer device, is characterized in that,
The liquid level of described fiber treatment groove (1) is higher than the highest liquid level of Self-flow filtering groove group.
3. the liquid-circulating treatment system of fiber dispersion as claimed in claim 1 or 2, expansion or broadening, thin layer device, is characterized in that,
Described Self-flow filtering groove group is that according to liquid level difference, by height, low laying forms by 2-8 the reservoir with screen pack; The reservoir that wherein liquid level is relatively low is positioned at the bottom of the overfall of the relatively high reservoir of liquid level, and the reservoir that liquid level is minimum is connected with cooling bath (24) by middle diversion pipeline.
4. the liquid-circulating treatment system of fiber dispersion as claimed in claim 3, expansion or broadening, thin layer device, is characterized in that,
Described Self-flow filtering groove group is that according to liquid level difference, by height, low arrangement forms by three reservoirs, comprise the one-level reservoir (15) with single filter net (14) and one-level overfall (16), the secondary reservoir (18) with cascade filtration net (17) and secondary overfall (19), and there are three grades of reservoirs (21) of three-stage filtration net (20); Described secondary reservoir (18) is positioned at the bottom of described one-level overfall (16), described three grades of reservoirs (21) are positioned at the bottom of described secondary overfall (19), and the liquid after one-level, secondary, three grades of reservoirs filter finally is discharged by three grades of reservoirs (21) and pumps in described cooling bath (24).
5. the liquid-circulating treatment system of the fiber dispersion as described in claim 1 or 2 or 4, expansion or broadening, thin layer device, is characterized in that,
Described cooling coil (25) connects and is controlled by outside cooling-water machine (30).
6. the liquid-circulating treatment system of the fiber dispersion as described in claim 1 or 2 or 4, expansion or broadening, thin layer device, is characterized in that,
The described fluid mozzle (5) be communicated between fiber treatment groove (1) and described Self-flow filtering groove group is provided with first-class gauge (12) and the first ball valve (13).
7. the liquid-circulating treatment system of the fiber dispersion as described in claim 1 or 2 or 4, expansion or broadening, thin layer device, is characterized in that,
The described middle diversion pipeline be communicated between Self-flow filtering groove group and cooling bath (24) is provided with the first circulating pump (28), second gauge (22) and the second ball valve (23);
The described time liquid mozzle (10) be communicated between cooling bath (24) and fiber treatment groove (1) is provided with the second circulating pump (29), the 3rd flowmeter (26) and the 3rd ball valve (27).
8. the liquid-circulating treatment system of fiber dispersion as claimed in claim 3, expansion or broadening, thin layer device, is characterized in that,
The described fluid mozzle (5) be communicated between fiber treatment groove (1) and described Self-flow filtering groove group is provided with first-class gauge (12) and the first ball valve (13).
9. the liquid-circulating treatment system of the fiber dispersion as described in claim 1 or 2 or 4, expansion or broadening, thin layer device, is characterized in that,
The described middle diversion pipeline be communicated between Self-flow filtering groove group and cooling bath (24) is provided with the first circulating pump (28), second gauge (22) and the second ball valve (23);
The described time liquid mozzle (10) be communicated between cooling bath (24) and fiber treatment groove (1) is provided with the second circulating pump (29), the 3rd flowmeter (26) and the 3rd ball valve (27).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420487877.3U CN204017525U (en) | 2014-08-28 | 2014-08-28 | The liquid-circulating treatment system of fiber dispersion, expansion or broadening, thin layer device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420487877.3U CN204017525U (en) | 2014-08-28 | 2014-08-28 | The liquid-circulating treatment system of fiber dispersion, expansion or broadening, thin layer device |
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| CN204017525U true CN204017525U (en) | 2014-12-17 |
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| CN201420487877.3U Expired - Fee Related CN204017525U (en) | 2014-08-28 | 2014-08-28 | The liquid-circulating treatment system of fiber dispersion, expansion or broadening, thin layer device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106744008A (en) * | 2017-03-07 | 2017-05-31 | 天津昂林贸烽高新材料有限公司 | A kind of fiber merges expansion equipment |
| CN108525394A (en) * | 2018-05-03 | 2018-09-14 | 齐艳华 | One kind watching water-based no dirt-discharging purifying method |
| CN109370209A (en) * | 2018-11-19 | 2019-02-22 | 中山大学 | A kind of liquid phase preparation process and preparation facilities of ultra-thin prepreg tape |
-
2014
- 2014-08-28 CN CN201420487877.3U patent/CN204017525U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106744008A (en) * | 2017-03-07 | 2017-05-31 | 天津昂林贸烽高新材料有限公司 | A kind of fiber merges expansion equipment |
| CN106744008B (en) * | 2017-03-07 | 2023-09-15 | 天津昂林贸烽高新材料有限公司 | Fiber merging and expanding equipment |
| CN108525394A (en) * | 2018-05-03 | 2018-09-14 | 齐艳华 | One kind watching water-based no dirt-discharging purifying method |
| CN109370209A (en) * | 2018-11-19 | 2019-02-22 | 中山大学 | A kind of liquid phase preparation process and preparation facilities of ultra-thin prepreg tape |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20141217 Termination date: 20160828 |