CN206752113U - A kind of post processing sizing quetsch of temperature concentration double control - Google Patents
A kind of post processing sizing quetsch of temperature concentration double control Download PDFInfo
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- CN206752113U CN206752113U CN201720499098.9U CN201720499098U CN206752113U CN 206752113 U CN206752113 U CN 206752113U CN 201720499098 U CN201720499098 U CN 201720499098U CN 206752113 U CN206752113 U CN 206752113U
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- slurry
- stock tank
- concentration
- control device
- temperature
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- 238000004513 sizing Methods 0.000 title claims abstract description 26
- 238000012805 post-processing Methods 0.000 title claims abstract description 18
- 239000002002 slurry Substances 0.000 claims abstract description 164
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims description 31
- 239000011440 grout Substances 0.000 claims description 12
- 238000009955 starching Methods 0.000 claims description 12
- 230000008901 benefit Effects 0.000 claims description 10
- 230000007246 mechanism Effects 0.000 claims description 4
- 238000012544 monitoring process Methods 0.000 abstract description 3
- 229920002472 Starch Polymers 0.000 abstract 1
- 238000010276 construction Methods 0.000 abstract 1
- 235000019698 starch Nutrition 0.000 abstract 1
- 239000008107 starch Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 4
- 230000007812 deficiency Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000007792 addition Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006255 coating slurry Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000003618 dip coating Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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- Paper (AREA)
Abstract
It the utility model is related to a kind of post processing sizing quetsch of temperature concentration double control, including for stock tank (1), starch box (4), Rinsing Area (2), mend stock tank (3) and control device, control device includes concentration of slurry control device (5) and slurry temperature control device (6), concentration of slurry control device (5) passes through concentration of slurry detector (7), clear water supply valve (13) and slurry supply valve (14) control the concentration for stock tank (1) interior slurries, slurry temperature control device (6) controls the temperature for stock tank (1) interior slurries by electric heater (10) and slurry temperature detector (8).The utility model is simple in construction, easy to operate, can automatically control the temperature and concentration of slurries, ensure that yarn sizing quality, it is not necessary to artificial monitoring and regulation, it is time saving and energy saving, and labour cost is reduced, improves operating efficiency.
Description
Technical field
It the utility model is related to glass fibre device for sizing technical field, more particularly to a kind of temperature concentration double control
Post processing sizing quetsch.
Background technology
Because glass fabric has the superior functions such as good insulating, heat resistance are strong, corrosion resistance is good, composite wood is commonly used for
In material.In glass fabric production process, sizing technique is essential.Starching is fabric dip-coating slurries and dried to obtain feel
The arrangement process of abundant and stiffening effect, the purpose of starching is intended to prevent or reduces yarn, line produces broken end in weaving, to improve
The strength of yarn, Yarn filoplume is reduced, reduce the frictional force of yarn and loom, improve operating efficiency；And sizing technique is to slurries
Temperature and concentration also there are certain requirements, to reach the purpose that yarn sizing works well, at present used in quetsch, and
The control device to slurry temperature and concentration is not provided with, the regulation of temperature is heated merely using electric heater to slurries, is needed
Artificial monitoring slurry temperature, the regulation of concentration need to add after manually the concentration of slurries is regulated in advance, wasted time and energy, to upper
Sizing process causes difficulty, increases the activity duration.
Utility model content
The utility model is directed to the deficiency of above-mentioned technology, there is provided a kind of post processing sizing starching of temperature concentration double control
Device, apparatus structure of the present utility model is simple, easy to operate, can be controlled by concentration of slurry control device and slurry temperature
Device automatically controls the temperature and concentration for being delivered to slurries in slurry box, so as to ensure that yarn sizing quality, it is not necessary to artificial prison
Control and regulation, it is time saving and energy saving, labour cost is reduced, improves operating efficiency.
The utility model is achieved by the following technical solution, and the utility model provides a kind of temperature concentration double control
Post processing sizing quetsch, including for stock tank, slurry box, the starching mechanism being arranged in slurry box and be arranged on slurry cassette bottom portion
Pulp-inlet pipe, grout outlet and return pipe, the pulp-inlet pipe, grout outlet and return pipe are connected with for stock tank by pipeline, also wrapped respectively
Include Rinsing Area, mend stock tank and control device, the Rinsing Area and benefit stock tank are connected by pipeline with for stock tank respectively, clear in connection
Tank is with for setting clear water supply valve on the pipeline of stock tank, stock tank is mended with setting slurry to supply on the pipeline for stock tank in connection
Valve, electric heater is set in the bottom for stock tank, embedded concentration of slurry detector and the slurry temperature inspection in the side wall for stock tank
Device is surveyed, the control device includes concentration of slurry control device and slurry temperature control device, the concentration of slurry control device
Electrically connected respectively with concentration of slurry detector, clear water supply valve and slurry supply valve, the slurry temperature control device respectively with
Electric heater and the electrical connection of slurry temperature detector.
Rinsing Area and benefit stock tank are respectively to for providing clear water and slurry, the concentration and temperature of clear water and slurry after mixing in stock tank
Degree is controlled by control device；The control of slurry concentration is specially：Set required slurry in advance in concentration of slurry control device
Liquid concentration value, concentration of slurry detector will detect is conveyed to concentration of slurry control dress for the concentration of slurry data in stock tank
Put, after concentration of slurry control device is contrasted detected value and setting value, control clear water supply valve and slurry supply valve respectively
Keying, when detected value is more than setting value, close slurry supply valve, open clear water supply valve, when detected value is less than setting value
When, clear water supply valve is closed, starts slurry supply valve；The temperature control of slurry is specially：Carried in slurry temperature control device
Before set required slurry temperature value, slurry temperature control device starts electric heater, and slurry temperature detector is in real time to slurry
The Temperature numerical that the conveying of liquid temperature control equipment detects, when detected value reaches setting value, the control of slurry temperature control device
Electric heater is closed, and when detected value deteriorates to less than setting value, is again started up electric heater, until detected value is equal to setting value
When close electric heater.
Preferably, for also setting up liquid level of slurry detector, the liquid level of slurry detector and concentration of slurry in stock tank
Control device electrically connects.Set and be delivered to for the minimum liquid level in stock tank and highest liquid level in concentration of slurry control device,
The liquid level data detected is conveyed to concentration of slurry control device by liquid level of slurry detector, when detected value is less than minimum liquid level value
When, concentration of slurry control device control Rinsing Area and benefit stock tank continue to stock tank feed flow is supplied, when detected value reaches highest level value
When, concentration of slurry control device control Rinsing Area and benefit stock tank stop, to stock tank feed flow is supplied, setting the mesh of liquid level of slurry detector
Be：1. preventing feed tank to be delivered to the slurries deficiency of slurry box from pulp-inlet pipe, cause starching unsuccessful；2. prevent in feed tank
Slurries overfill and overflow feed tank.
Preferably, slurry circulating pump is set on the pipeline that pulp-inlet pipe is connected with for stock tank.Slurry circulating pump is used for will
It is delivered to for the slurries in stock tank in slurry box.
Preferably, inlet valve is set on the pipeline that pulp-inlet pipe is connected with for stock tank.Inlet valve is used to control slurries certainly
Feed tank enters slurry box through pulp-inlet pipe.
Preferably, outlet valve is set on the pipeline that grout outlet is connected with for stock tank.Outlet valve is used to control slurries certainly
Slurry box enters feed tank through grout outlet.
Preferably, screen pack is provided with the pulp-inlet pipe.Screen pack can filter out the magazine in slurries, ensure yarn
The quality of beam starching.
Preferably, the overfall mouth of return pipe is concordant with the slurries liquid level of setting in slurry box.When the liquid level of slurries in slurry box
During more than setting liquid level, unnecessary slurries can flow into secondary use in feed tank, will not so cause the waste of slurries.
The beneficial effects of the utility model are：
The structure of the post processing sizing quetsch of the utility model temperature concentration double control is simple, easy to operate, energy
The temperature and concentration for being delivered to slurries in slurry box are enough automatically controlled by concentration of slurry control device and slurry temperature control device,
So as to ensure that yarn sizing quality, it is not necessary to artificial monitoring and regulation, it is time saving and energy saving, labour cost is reduced, improves work
Make efficiency.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model post processing sizing quetsch；
Fig. 2 is the electric control schematic diagram of the utility model post processing sizing quetsch concentration；
Fig. 3 is the electric control schematic diagram of the utility model post processing sizing quetsch temperature；
In figure：1st, for stock tank, 2, Rinsing Area, 3, mend stock tank, 4, slurry box, 5, concentration of slurry control device, 6, slurry temperature
Control device, 7, concentration of slurry detector, 8, slurry temperature detector, 9, liquid level of slurry detector, 10, electric heater, 11, slurry
Liquid circulating pump, 12, outlet valve, 13, clear water supply valve, 14, slurry supply valve, 15, pulp-inlet pipe, 16, grout outlet, 17, return pipe,
18th, starching mechanism, 19, inlet valve.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, with reference to embodiments, to this
Utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining this practicality
It is new, it is not used to limit the utility model.
Application principle of the present utility model is further described with reference to specific embodiment.
Embodiment 1, as shown in Figures 1 to 3, a kind of post processing sizing quetsch of temperature concentration double control, including supply
Stock tank 1, slurry box 4, it is arranged at the starching mechanism 18 starched in box 4 and is arranged on the pulp-inlet pipe 15 for starching the bottom of box 4, grout outlet 16 and returns
Pipe 17 is starched, the pulp-inlet pipe 15, grout outlet 16 and return pipe 17 are connected by pipeline with for stock tank 1 respectively, in addition to Rinsing Area
2nd, stock tank 3 and control device are mended, the Rinsing Area 2 and benefit stock tank 3 are connected by pipeline with for stock tank 1 respectively, in connection clear water
Groove 2 is with for setting clear water supply valve 13 on the pipeline of stock tank 1, stock tank 3 is mended with setting slurry to supply on the pipeline for stock tank 1 in connection
To valve 14, electric heater 10 is set in the bottom for stock tank 1, embedded concentration of slurry detector 7 and slurry in the side wall for stock tank 1
Liquid temperature detector 8, the control device include concentration of slurry control device 5 and slurry temperature control device 6, and the slurries are dense
Degree control device 5 electrically connects with concentration of slurry detector 7, clear water supply valve 13 and slurry supply valve 14 respectively, the slurries temperature
Degree control device 6 electrically connects with electric heater 10 and slurry temperature detector 8 respectively.
Rinsing Area 2 and benefit stock tank 3 are respectively to for providing clear water and slurry, the concentration of clear water and slurry after mixing in stock tank 1
Controlled with temperature by control device；The control of slurry concentration is specially：Set in advance in concentration of slurry control device 5
Required concentration of slurry value, concentration of slurry detector 7 are conveyed to concentration of slurry by what is detected for the concentration of slurry data in stock tank 1
Control device 5, after concentration of slurry control device 5 is contrasted detected value and setting value, the He of clear water supply valve 13 is controlled respectively
The keying of slurry supply valve 14, when detected value is more than setting value, slurry supply valve 14 is closed, opens clear water supply valve 13, when
When detected value is less than setting value, clear water supply valve 13 is closed, starts slurry supply valve 14；The temperature control of slurry is specially：
Required slurry temperature value is set in slurry temperature control device 6 in advance, slurry temperature control device 6 starts electric heater
10, slurry temperature detector 8 conveys the Temperature numerical detected to slurry temperature control device 6 in real time, is set when detected value reaches
During definite value, slurry temperature control device 6 controls electric heater 10 to close, and when detected value deteriorates to less than setting value, opens again
Dynamic electric heater 10, until detected value closes electric heater 10 when being equal to setting value.
Slurry circulating pump 11 is set on the pipeline that pulp-inlet pipe 15 is connected with for stock tank 1.Slurry circulating pump 11 is used for will be for
Slurries in stock tank 1 are delivered in slurry box 4.Inlet valve 19 is set on the pipeline that pulp-inlet pipe 15 is connected with for stock tank 1.Inlet valve
19 are used to control slurries confession liquid bath 1 to enter slurry box 4 through pulp-inlet pipe 15.Set on the pipeline that grout outlet 16 is connected with for stock tank 1
Put outlet valve 12.Outlet valve 12 is used to control slurries to enter feed tank 1 through grout outlet 16 from box 4 is starched.In the pulp-inlet pipe 15
Provided with screen pack.Screen pack can filter out the magazine in slurries, ensure the quality of yarn beam starching.
The overfall mouth of return pipe 17 is concordant with the slurries liquid level of setting in slurry box 4.Set when the liquid level of slurries in slurry box 4 exceedes
When determining liquid level, unnecessary slurries can flow into secondary use in feed tank 1, will not so cause the waste of slurries.
Embodiment 2, as shown in Figures 1 to 3, the present embodiment and the difference of embodiment 1 are, for also being set in stock tank 1
Liquid level of slurry detector 9 is put, the liquid level of slurry detector 9 electrically connects with concentration of slurry control device 5.Controlled in concentration of slurry
The liquid that is delivered to and will be detected for the minimum liquid level in stock tank 1 and highest liquid level, liquid level of slurry detector 9 is set in device 5
Position data are conveyed to concentration of slurry control device 5, and when detected value is less than minimum liquid level value, concentration of slurry control device 5 controls
Rinsing Area 2 and benefit stock tank 3 continue to for the feed flow of stock tank 1, when detected value reaches highest level value, concentration of slurry control device 5
Control Rinsing Area 2 and benefit stock tank 3 stop：1. prevent feed flow
Groove 1 is delivered to the slurries deficiency of slurry box 4 from pulp-inlet pipe 15, causes starching unsuccessful；2. prevent the slurries overfill in feed tank 1 and
Overflow feed tank 1.
Certainly, described above is also not limited to the example above, and technical characteristic of the utility model without description can lead to
Cross or realized using prior art, be will not be repeated here；Above example and accompanying drawing are merely to illustrate technology of the present utility model
It is to limitation of the present utility model that scheme, which is not, and the utility model is described in detail with reference to preferred embodiment, this
Field it is to be appreciated by one skilled in the art that those skilled in the art institute in essential scope of the present utility model
For the variations, modifications, additions or substitutions made without departure from objective of the present utility model, should also belong to right of the present utility model will
Seek protection domain.
Claims (7)
1. a kind of post processing sizing quetsch of temperature concentration double control, including supply stock tank (1), slurry box (4), be arranged at slurry
Starching mechanism (18) in box (4) and pulp-inlet pipe (15), grout outlet (16) and the return pipe (17) for being arranged on slurry box (4) bottom,
The pulp-inlet pipe (15), grout outlet (16) and return pipe (17) are connected by pipeline with for stock tank (1) respectively, it is characterised in that：
Also include Rinsing Area (2), mend stock tank (3) and control device, the Rinsing Area (2) and benefit stock tank (3) are respectively by pipeline with supplying
Stock tank (1) is connected, and in connection Rinsing Area (2) with setting clear water supply valve (13) on the pipeline for stock tank (1), stock tank is mended in connection
(3) with setting slurry supply valve (14) on the pipeline for stock tank (1), electric heater (10) is set in the bottom for stock tank (1),
Include slurry for embedded concentration of slurry detector (7) and slurry temperature detector (8), the control device in the side wall of stock tank (1)
Liquid concentration control apparatus (5) and slurry temperature control device (6), the concentration of slurry control device (5) respectively with concentration of slurry
Detector (7), clear water supply valve (13) and slurry supply valve (14) electrical connection, the slurry temperature control device (6) respectively with
Electric heater (10) and slurry temperature detector (8) electrical connection.
A kind of 2. post processing sizing quetsch of temperature concentration double control according to claim 1, it is characterised in that
Liquid level of slurry detector (9), the liquid level of slurry detector (9) and concentration of slurry control device are also set up in for stock tank (1)
(5) electrically connect.
A kind of 3. post processing sizing quetsch of temperature concentration double control according to claim 1, it is characterised in that
Slurry circulating pump (11) is set on the pipeline that pulp-inlet pipe (15) is connected with for stock tank (1).
A kind of 4. post processing sizing quetsch of temperature concentration double control according to claim 1, it is characterised in that
Inlet valve (19) is set on the pipeline that pulp-inlet pipe (15) is connected with for stock tank (1).
A kind of 5. post processing sizing quetsch of temperature concentration double control according to claim 1, it is characterised in that
Outlet valve (12) is set on the pipeline that grout outlet (16) is connected with for stock tank (1).
6. a kind of post processing sizing quetsch of temperature concentration double control according to claim 1, its feature exist
In being provided with screen pack in the pulp-inlet pipe (15).
A kind of 7. post processing sizing quetsch of temperature concentration double control according to claim 1, it is characterised in that
The overfall mouth of return pipe (17) is concordant with the slurries liquid level of setting in slurry box (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720499098.9U CN206752113U (en) | 2017-05-08 | 2017-05-08 | A kind of post processing sizing quetsch of temperature concentration double control |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720499098.9U CN206752113U (en) | 2017-05-08 | 2017-05-08 | A kind of post processing sizing quetsch of temperature concentration double control |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206752113U true CN206752113U (en) | 2017-12-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720499098.9U Expired - Fee Related CN206752113U (en) | 2017-05-08 | 2017-05-08 | A kind of post processing sizing quetsch of temperature concentration double control |
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| CN (1) | CN206752113U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116695356A (en) * | 2023-06-08 | 2023-09-05 | 新创碳谷集团有限公司 | Sizing system of fiber production line and control method thereof |
-
2017
- 2017-05-08 CN CN201720499098.9U patent/CN206752113U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116695356A (en) * | 2023-06-08 | 2023-09-05 | 新创碳谷集团有限公司 | Sizing system of fiber production line and control method thereof |
| CN116695356B (en) * | 2023-06-08 | 2023-11-03 | 新创碳谷集团有限公司 | Sizing system of fiber production line and control method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171215 |
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| CF01 | Termination of patent right due to non-payment of annual fee |