CN113996195A - Sizing method for slashing - Google Patents
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Abstract
The application relates to a slashing size mixing method, relating to the technical field of size mixing technology, and the slashing size mixing method comprises the following steps: acquiring a plurality of different slurry mixing configuration parameter sets; weighing the solid material by adopting a weight loss method based on the slurry mixing configuration parameter set; based on the size mixing configuration parameter set, quantitatively distributing the liquid material by using a preset first flow metering device; based on the slurry mixing configuration parameter set, quantitatively distributing water by using a preset second flow metering device; performing size mixing operation on the quantified solid material, the quantified liquid material and the water based on the size mixing configuration parameter set; and recording the corresponding size mixing effect of different size mixing configuration parameter sets. The slurry mixing operation is carried out based on different slurry mixing configuration parameter sets, effective slurry mixing effect guarantee measures are combined, the slurry mixing operation is effectively guaranteed, the corresponding slurry mixing effect is recorded, and data basis is provided for later-stage data analysis.
Description
Technical Field
The application relates to the technical field of size mixing processes, in particular to a slashing size mixing method.
Background
At the present stage, the sizing process research has the defects of complex model, imperfect constructed mathematical model, large influence of human factors, poor control effect, delayed diagnosis and the like.
The automation development of the textile industry is so far, the monitoring of the operation process of the sizing slurry preparation equipment is common, a large amount of data are accumulated, the historically accumulated large amount of data contribute to improving the product quality, reducing the production energy consumption and providing the traceability of products at the stage for users, and the method is also the inevitable requirement of intelligent transformation and upgrading of the textile industry.
How to effectively count the historical accumulated data and provide data basis for later effect analysis is a problem which is urgently needed to be solved at present.
Disclosure of Invention
The application provides a sizing mixing method, carries out size mixing operation based on the configuration parameter set of size mixing of difference, combines effectual size mixing effect safeguard measure, records the size mixing effect that corresponds when carrying out effective guarantee to the size mixing operation, provides the data basis for later stage data analysis to make contributions for promoting product quality, reducing production energy consumption, providing the traceability of product.
In a first aspect, the present application provides a slashing size mixing method, comprising the steps of:
acquiring a plurality of different slurry mixing configuration parameter sets;
weighing the solid material by adopting a weight loss method based on the slurry mixing configuration parameter set;
based on the size mixing configuration parameter set, quantitatively distributing the liquid material by using a preset first flow metering device;
based on the slurry mixing configuration parameter set, quantitatively distributing water by using a preset second flow metering device;
performing size mixing operation on the quantified solid material, the quantified liquid material and the water based on the size mixing configuration parameter set;
and recording the corresponding size mixing effect of different size mixing configuration parameter sets.
The embodiment of the application carries out size mixing operation based on different size mixing configuration parameter sets, combines effectual size mixing effect safeguard measure, and the size mixing effect that the record corresponds when carrying out effective guarantee to the size mixing operation provides the data foundation for later stage data analysis to make contributions for promoting product quality, reducing production energy consumption, providing the traceability of product.
Specifically, the slurry mixing configuration data comprises a solid-liquid weight ratio, a water distribution amount, a stirring temperature, a stirring rotation speed and a cleaning frequency.
Specifically, the method for weighing the solid material by adopting a weight loss method based on the slurry mixing configuration parameter set comprises the following steps:
and based on the slurry mixing configuration parameter set, acquiring the sum of the weight of the solid hopper body and the solid material by using a weighing sensor preset on the solid hopper, and weighing the solid material by adopting a weight loss method.
Specifically, the slurry mixing operation of the quantified solid material, the quantified liquid material and the quantified water based on the slurry mixing configuration parameter set includes the following steps:
mixing the solid material, the liquid material and the water directly.
Specifically, the water is at normal temperature.
Further, after recording the corresponding slurry mixing effects of the different slurry mixing configuration parameter sets, the method further includes the following steps:
obtaining a size mixing performance curve corresponding to the size mixing configuration parameter set by adopting a multiple regression method;
and comparing the slurry mixing performance curves to obtain an optimal slurry mixing curve.
Further, after comparing the slurry mixing performance curves to obtain an optimal slurry mixing curve, the method further comprises the following steps:
recording the slurry mixing configuration parameter set corresponding to the optimal slurry mixing curve
Specifically, the first flow metering device is a metering pump.
Specifically, the second flow measuring device is an electromagnetic flow meter.
Specifically, the solid material is PVA.
It should be noted that one of the advantages of the present application is the treatment of PVA;
for the PVA treatment mode, the PVA is usually thermally dissolved in water, and then is fully mixed with other ingredients and water distribution and enters the next procedure;
in the embodiment of the application, the optimization is carried out, the solid PVA is directly and fully mixed with other ingredients and normal temperature water distribution and then enters the next procedure,
the treatment ensures the water-based gel property of the product, and saves the water distribution amount and the material preparation time.
In addition, in the method, a multiple discriminant vector method (Fisher) is used, non-main factors in the process are reduced, the object space is subjected to dimension reduction through effective linear transformation, the point set of the object sample is displayed in a graphic mode, the optimization of the process is displayed according to a target value, low-dimensional variables correspond to original variables, and therefore an optimized working area of the original variables is selected, and error points are removed. And obtaining a corresponding curve of the weight ratio of the solid to the liquid, the water distribution amount, the stirring temperature, the stirring rotating speed and the cleaning times by adopting a multiple regression method, and seeking the process condition with the optimal size mixing effect.
The beneficial effect that technical scheme that this application provided brought includes:
the slurry mixing operation is carried out based on different slurry mixing configuration parameter sets, an effective slurry mixing effect guarantee measure is combined, the slurry mixing effect corresponding to the slurry mixing operation is effectively guaranteed, a data basis is provided for later data analysis, and contribution is made to improving product quality, reducing production energy consumption and providing traceability of products.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present application, the drawings needed to be used in the description of the embodiments are briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present application, and it is obvious for those skilled in the art to obtain other drawings based on these drawings without creative efforts.
Fig. 1 is a flow chart of the steps of a slashing size mixing method provided in an embodiment of the present application.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present application clearer, the technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application, and it is obvious that the described embodiments are some embodiments of the present application, but not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present application.
Embodiments of the present application will be described in further detail below with reference to the accompanying drawings.
The embodiment of the application provides a sizing mixing method, carries out size mixing operation based on different size mixing configuration parameter sets, combines effectual size mixing effect safeguard measure, records the corresponding size mixing effect when carrying out effective guarantee to the size mixing operation, provides the data basis for later data analysis to make contributions for promoting product quality, reducing production energy consumption, providing the traceability of product.
In order to achieve the technical effects, the general idea of the application is as follows:
a slashing size mixing method, comprising the following steps:
s1, acquiring a plurality of different slurry mixing configuration parameter sets;
s2, weighing the solid material by adopting a weight loss method based on the size mixing configuration parameter set;
s3, quantitatively distributing the liquid material by using a preset first flow metering device based on the size mixing configuration parameter set;
s4, quantitatively distributing water by using a preset second flow metering device based on the size mixing configuration parameter set;
s5, carrying out size mixing operation on the quantified solid material, the quantified liquid material and the water based on the size mixing configuration parameter set;
and S6, recording the corresponding size mixing effect of different size mixing configuration parameter sets.
Embodiments of the present application will be described in further detail below with reference to the accompanying drawings.
In a first aspect, referring to fig. 1, an embodiment of the present application provides a slashing size mixing method, including the following steps:
s1, acquiring a plurality of different slurry mixing configuration parameter sets;
s2, weighing the solid material by adopting a weight loss method based on the size mixing configuration parameter set;
s3, quantitatively distributing the liquid material by using a preset first flow metering device based on the size mixing configuration parameter set;
s4, quantitatively distributing water by using a preset second flow metering device based on the size mixing configuration parameter set;
s5, carrying out size mixing operation on the quantified solid material, the quantified liquid material and the water based on the size mixing configuration parameter set;
and S6, recording the corresponding size mixing effect of different size mixing configuration parameter sets.
The embodiment of the application carries out size mixing operation based on different size mixing configuration parameter sets, combines effectual size mixing effect safeguard measure, and the size mixing effect that the record corresponds when carrying out effective guarantee to the size mixing operation provides the data foundation for later stage data analysis to make contributions for promoting product quality, reducing production energy consumption, providing the traceability of product.
Specifically, the slurry mixing configuration data comprises a solid-liquid weight ratio, a water distribution amount, a stirring temperature, a stirring rotation speed and a cleaning frequency.
Specifically, the first flow metering device is a metering pump.
Specifically, the second flow measuring device is an electromagnetic flow meter.
Specifically, the solid material is PVA;
PVA, i.e. Polyvinyl Alcohol, is an organic compound of the formula [ C2H4O]n, the appearance is white flaky, flocculent or powdery solid and is tasteless. Soluble in water (above 95 deg.C), slightly soluble in dimethyl sulfoxide, insoluble in gasoline, kerosene, gasoline, water, etc,Vegetable oil, benzene, toluene, dichloroethane, carbon tetrachloride, acetone, ethyl acetate, methanol, ethylene glycol, and the like. Polyvinyl alcohol is an important chemical raw material, and is used for manufacturing polyvinyl acetal, gasoline-resistant pipelines, vinylon, fabric treating agents, emulsifiers, paper coatings, adhesives, glue and the like;
the physical properties of polyvinyl alcohol are influenced by chemical structure, alcoholysis degree and polymerization degree. The main structure in the polyvinyl alcohol molecule is 1, 3-propanediol, i.e. "head-tail" structure. The polymerization degree of polyvinyl alcohol is classified into ultra-high polymerization degree (molecular weight 25-30 ten thousand), high polymerization degree (molecular weight 17-22 ten thousand), medium polymerization degree (molecular weight 12-15 ten thousand) and low polymerization degree (2.5-3.5 ten thousand). The alcoholysis degree is generally 78%, 88% and 98%. The alcoholysis degree of partial alcoholysis is generally 87-89%, and the alcoholysis degree of complete alcoholysis is 98-100%. Often, the thousand or hundred digits of the average degree of polymerization are placed in front of the polymerization, and the percentage of alcoholysis is placed in the back, e.g., 17-88, i.e., the apparent degree of polymerization is 1700 and the alcoholysis is 88%. In general, the polymerization degree increases, the viscosity of an aqueous solution increases, and the strength and solvent resistance after film formation are improved, but the solubility in water and the elongation after film formation decrease. The relative density (25 ℃/4 ℃) of the polyvinyl alcohol is 1.27-1.31 (solid) and 1.02 (10% solution), the melting point is 230 ℃, the glass transition temperature is 75-85 ℃, and the polyvinyl alcohol is heated to more than 100 ℃ in the air to slowly change color and embrittle. Heating to 160-170 ℃ for dehydration and etherification, losing solubility, and heating to 200 ℃ for decomposition. And becomes a polymer containing conjugated double bonds at more than 250 ℃. The refractive index is 1.49-1.52, the thermal conductivity is 0.2W/(m.K), the specific heat capacity is 1-5J/(kg.K), and the resistivity is (3.1-3.8). times.10 omega.cm. Dissolving in water, and heating to 65-75 ℃ for complete dissolution. The oil-soluble gel is insoluble in gasoline, kerosene, vegetable oil, benzene, toluene, dichloroethane, carbon tetrachloride, acetone, ethyl acetate, methanol, ethylene glycol and the like, is slightly soluble in dimethyl sulfoxide, can be dissolved in glycerol at 120-150 ℃, and becomes a jelly when cooled to room temperature. The polyvinyl alcohol is dissolved by adding the materials into room temperature water under stirring, uniformly dispersing, and then heating to accelerate dissolution, so as to prevent agglomeration and influence the dissolution speed;
the aqueous solution (5%) of polyvinyl alcohol is sensitive to borax and boric acid, and is easy to cause gelation, and when the mass of borax reaches 1% of the solution, irreversible gelation is generated. Chromates, dichromates, permanganates can also gel polyvinyl alcohols. The aqueous solution of PVA 17-88 showed a gradual increase in viscosity at room temperature over time, but the viscosity at a concentration of 8% was absolutely stable regardless of time. Polyvinyl alcohol has good film forming properties and is highly uncomfortable with many gases other than water vapor and ammonia. The light resistance is good and is not influenced by illumination. When open fire is applied, the material can burn and has special smell. Aqueous solutions sometimes exhibit toxic effects when stored. It is non-toxic and non-irritating to human skin.
Specifically, the method for weighing the solid material by adopting a weight loss method based on the slurry mixing configuration parameter set comprises the following steps:
and based on the slurry mixing configuration parameter set, acquiring the sum of the weight of the solid hopper body and the solid material by using a weighing sensor preset on the solid hopper, and weighing the solid material by adopting a weight loss method.
Specifically, the slurry mixing operation of the quantified solid material, the quantified liquid material and the quantified water based on the slurry mixing configuration parameter set includes the following steps:
mixing the solid material, the liquid material and the water directly.
It should be noted that one of the advantages of the embodiments of the present application is the treatment of PVA;
for the PVA treatment mode, the PVA is usually thermally dissolved in water, and then is fully mixed with other ingredients and water distribution and enters the next procedure;
in the embodiment of the application, the optimization is carried out, the solid PVA is directly and fully mixed with other ingredients and normal temperature water distribution and then enters the next procedure,
the treatment ensures the water-based gel property of the product, and saves the water distribution amount and the material preparation time.
Specifically, the water is at normal temperature.
Further, after recording the corresponding slurry mixing effects of the different slurry mixing configuration parameter sets, the method further includes the following steps:
obtaining a size mixing performance curve corresponding to the size mixing configuration parameter set by adopting a multiple regression method;
and comparing the slurry mixing performance curves to obtain an optimal slurry mixing curve.
Further, after comparing the slurry mixing performance curves to obtain an optimal slurry mixing curve, the method further comprises the following steps:
and recording the slurry mixing configuration parameter set corresponding to the optimal slurry mixing curve.
It should be noted that, in the embodiment of the present application, a multiple discriminant vector method (Fisher) is used to reduce non-main factors in a process, reduce dimensions of an object space through effective linear transformation, display a point set of an object sample in a graphical manner, display optimization of the process according to a target value, and correspond a low-dimensional variable to an original variable, thereby selecting an optimized working area of the original variable and removing error points. A multivariate regression method is adopted to obtain corresponding curves of the weight ratio of solid and liquid, the water distribution amount, the stirring temperature, the stirring rotating speed and the cleaning times, and the process conditions of the optimal size mixing effect are searched, as shown in the following table 1:
TABLE 1
The optimum process conditions were calculated as shown in table 2 below:
TABLE 2
The parameters are corrected according to the optimization method, and the optimal process conditions are finally obtained, as shown in the following table 3:
TABLE 3
Through production verification, the process formula shortens the production time and reduces the energy consumption.
It is noted that, in the present application, relational terms such as "first" and "second", and the like, are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
The foregoing are merely exemplary embodiments of the present application and are presented to enable those skilled in the art to understand and practice the present application. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the application. Thus, the present application is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (10)
1. A slashing size mixing method, characterized in that the method comprises the following steps:
acquiring a plurality of different slurry mixing configuration parameter sets;
weighing the solid material by adopting a weight loss method based on the slurry mixing configuration parameter set;
based on the size mixing configuration parameter set, quantitatively distributing the liquid material by using a preset first flow metering device;
based on the slurry mixing configuration parameter set, quantitatively distributing water by using a preset second flow metering device;
performing size mixing operation on the quantified solid material, the quantified liquid material and the water based on the size mixing configuration parameter set;
and recording the corresponding size mixing effect of different size mixing configuration parameter sets.
2. The sizing process according to claim 1, characterized in that:
the slurry mixing configuration data comprises solid-liquid weight ratio, water distribution amount, stirring temperature, stirring rotating speed and cleaning times.
3. The sizing process of claim 1, wherein the weighing of the solid material by weight loss based on the set of sizing configuration parameters comprises the steps of:
and based on the slurry mixing configuration parameter set, acquiring the sum of the weight of the solid hopper body and the solid material by using a weighing sensor preset on the solid hopper, and weighing the solid material by adopting a weight loss method.
4. The sizing process according to claim 1, wherein the sizing operation of the dosed solid material, liquid material and water based on the set of sizing configuration parameters comprises the following steps:
mixing the solid material, the liquid material and the water directly.
5. The sizing process according to claim 4, characterized in that:
the water is at normal temperature.
6. The slashing sizing method according to claim 1, wherein after recording the corresponding sizing effects of different sets of sizing configuration parameters, the method further comprises the following steps:
obtaining a size mixing performance curve corresponding to the size mixing configuration parameter set by adopting a multiple regression method;
and comparing the slurry mixing performance curves to obtain an optimal slurry mixing curve.
7. The slashing sizing method according to claim 6, wherein after comparing the sizing performance curves to obtain an optimal sizing curve, the method further comprises the following steps:
and recording the slurry mixing configuration parameter set corresponding to the optimal slurry mixing curve.
8. The sizing process according to claim 1, characterized in that:
the first flow metering device is a metering pump.
9. The sizing process according to claim 1, characterized in that:
the second flow metering device is an electromagnetic flow meter.
10. The sizing process according to claim 1, characterized in that:
the solid material is PVA.
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Citations (7)
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| US20010049397A1 (en) * | 1998-08-19 | 2001-12-06 | Norchem Industries, Inc. | Means for and methods of using a selected energy factor to apply a paper coating |
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| CN105442317A (en) * | 2015-12-18 | 2016-03-30 | 西安工程大学 | Formula of slurry capable of being applied to weaving under low sizing rate and sizing method thereof |
| CN206199188U (en) * | 2016-10-18 | 2017-05-31 | 中原工学院 | The automatic blended size system of warp sizing machine |
| CN206935294U (en) * | 2017-07-27 | 2018-01-30 | 北京广盛源生物科技有限公司 | A kind of intelligent starch is sized mixing tank |
| CN108067106A (en) * | 2016-11-16 | 2018-05-25 | 深圳格林德能源有限公司 | Pulp of lithium ion battery is pre-mixed dispersing technology for glue |
| CN108499406A (en) * | 2017-02-28 | 2018-09-07 | 无锡灵鸽机械科技股份有限公司 | A kind of continuous process system of lithium battery slurry |
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2021
- 2021-10-29 CN CN202111280577.9A patent/CN113996195A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20010049397A1 (en) * | 1998-08-19 | 2001-12-06 | Norchem Industries, Inc. | Means for and methods of using a selected energy factor to apply a paper coating |
| CN204933372U (en) * | 2015-08-19 | 2016-01-06 | 广东江门生物技术开发中心有限公司 | A kind of powder mix and blended size system |
| CN105442317A (en) * | 2015-12-18 | 2016-03-30 | 西安工程大学 | Formula of slurry capable of being applied to weaving under low sizing rate and sizing method thereof |
| CN206199188U (en) * | 2016-10-18 | 2017-05-31 | 中原工学院 | The automatic blended size system of warp sizing machine |
| CN108067106A (en) * | 2016-11-16 | 2018-05-25 | 深圳格林德能源有限公司 | Pulp of lithium ion battery is pre-mixed dispersing technology for glue |
| CN108499406A (en) * | 2017-02-28 | 2018-09-07 | 无锡灵鸽机械科技股份有限公司 | A kind of continuous process system of lithium battery slurry |
| CN206935294U (en) * | 2017-07-27 | 2018-01-30 | 北京广盛源生物科技有限公司 | A kind of intelligent starch is sized mixing tank |
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