In general, people need to be careful when processing coated paperboard on a corrugating Machine. Since the surface of the coated paperboard is subjected to a polishing treatment, it has a certain moisture resistance, that is, moisture permeability of the coated paperboard as compared with kraft paper. Performance is worse. Corrugated paper from the center to the local area strictly requires the use of coated paperboard. The quality of the paperboard will have an impact on the subsequent printing and processing of paper products. Rolling, corrugating, and grooving are all potential problems. Therefore, these problems should be emphasized in the production of corrugating machines, rather than waiting for and paying attention to when the printing and processing processes take a break. The following suggestions are made for this particular situation.
A, starch
Increasing the starch content on the applicator to at least 29% will help improve the problems that occur when gluing and rolling. There is no need to change the formula if S/F is bonded, but if the temperature or process changes, the temperature of the gel needs to be adjusted.
Second, single-sided roll material
The preheating and deformation pretreatment of the single-sided web material is controlled to a minimum so that the single-side web material is kept as high as possible and the water content is maintained. The cardboard is pretreated with moist gas (above the drying gas). Correspondingly, the starch content is increased and the material channels are sufficiently cooled.
Third, rubber roller and preheater
An iodine test can be performed to obtain information on the type of glue, and an iodine test should be performed regularly. Check the amount of glue applied by the gluing roller, and set an appropriate interval value (0.001-0.008 inch) to adjust the amount of glue applied. The larger the interval, the greater the amount of glue applied, and vice versa. The adhesive roller, the reel tension roller and the pressure roller must be equal. Adjust the rotation speed of the coating roller to find the "best point" for the strongest adhesion. After gluing off the contradiction device, the humidity of the paperboard should be controlled within 180 degrees and the temperature difference should be kept within ±5 degrees. Temperature control and tension control are all very important factors.
Four, pressure roller
Conveyor belts and heat transfer plates must ensure that the clean, clean, flat, heavier rollers remain level. The temperature at the beginning of entering the hot sheet is low, and heat is gradually increased later. The spray water system is beneficial to any reverse-shaped control. If the corrugator is equipped with a steam device, it can increase the moisture content of the roll material and increase its humidity, thus contributing to wind-up control. After leaving the hot plate, the bottom board temperature should be less than 200 degrees.
5. Sectional, Crimping, and Cutting Quality
Sharp cutting knives, neatly aligned creases, and proper spacing settings prevent powder breaks and breaks, ensuring segmentation, creasing and breaking quality.
Sixth, the conclusion
It turns out that the above mentioned suggestions are very useful in the operation of many corrugated paper machines. However, different corrugating machines have their own characteristics and external conditions. In addition, mere adjustment on the one hand often does not solve the problem. Therefore, the operation must determine what is appropriate for the situation of your company. In order to optimize the performance of the corrugating machine, routine maintenance and training should be carried out to ensure that the corrugating machine maintains a good operating condition. This must be observed and imperative.
Pulp moulding product drying method
Pulp mouldings are a new type of packaging material produced from pulp as a raw material and are widely used for the inner packaging of various products. The production process of pulp molding products is divided into three processes: slurry processing, vacuum forming and thermal energy drying. The energy consumption of the drying process occupies a large proportion in the entire production cost. How to reasonably determine the drying process conditions and reduce energy consumption is a key issue for improving the economic efficiency of enterprises. This article will introduce the following issues related to the drying of pulp molded products.
1 Drying Method and Drying Mechanism of Pulp Moulding Products At present, the vast majority of domestic pulp molded products use the hot air drying method. In a specific drying device, the hot air as a drying medium is used to dry the pulp molded products. Hot air is mainly obtained by two methods. One is to directly generate hot air by burning in a hot air oven; the other is to use hot air to exchange hot air through heat exchanger and air. The equipment used for the drying of pulp mouldings includes drying ovens, tunnel dryers and chain dryers. No matter which type of drying equipment is used, the drying mechanism is basically the same.
The wet paper mold blank consisting mainly of pulp is a porous body having a capillary structure inside. Moisture exists between the surface of the fiber and the pores of the fiber capillary. Pulp mouldings used for internal packaging of products generally require good dynamic buffering properties, in which the moisture cannot be removed by means of mechanical squeezing, and all of them need to be removed in a dry manner first. Therefore, the pulp molded article has a great drying strength as compared with the conventional sheet drying process. Hot air, on the one hand, acts as a heat source to provide energy for removing moisture; on the other hand, it acts as a water carrier and takes away the water that has been continuously evaporated. The moisture in the wet paper mold blank depends on the internal diffusion and the external diffusion of water. The so-called internal diffusion refers to the migration of water from the interior to the surface in the wet paper mold blank; the external diffusion refers to the moisture being evaporated after evaporating from the surface thereof. The process of walking. The degree of drying efficiency of pulp moulding products depends on the speed of internal and external diffusion of moisture and the balance and coordination between the two, and reasonable process conditions are formulated around these two aspects and the drying properties of pulp mouldings.
2 Ways to Improve the Drying Efficiency of Pulp Molded Products In the drying process of pulp molded products, it is necessary to increase the drying efficiency, reduce the humidity of the drying medium (hot air), and increase the temperature and air flow rate. However, it is necessary to increase the moisture content at the same time. Outward diffusion rate. In production practice, it can be achieved through the following ways.
2.1 Appropriately reduce the thickness of pulp mouldings The greater the thickness of pulp mouldings, the more difficult it is to dry. Therefore, when designing the thickness dimension of pulp molded products, the thickness of pulp molded products should be reduced as much as possible while ensuring its overall strength and packaging performance, which is not only beneficial to the improvement of the drying efficiency, but also reducing the consumption of fiber raw materials. The difference in thickness of each part should not be too large, so as to avoid the difficulty of out-diffusion of its local moisture and affect the overall drying speed.
2.2 Appropriately increase the water gradient on the surface and internal of the wet paper mold blank. During the drying process, the moisture concentration on the surface and internal of the wet paper mold blank is the main driving force for water diffusion. Increasing the moisture gradient by adjusting the temperature, humidity, wind speed, and air volume of the hot air is advantageous for increasing the internal diffusion of moisture. However, if the out-diffusion rate of water is too high, the shrinkage of the surface of the wet paper mold is too fast and the internal diffusion rate of moisture is affected, which will have a negative effect on the drying of the pulp molded product.
2.3 Properly increase the drying temperature The increase of the drying temperature facilitates the migration of moisture from the inside of the wet paper mold blank to the surface. However, in the production practice, the increase in temperature has to be limited in many aspects, so it can only be properly improved.
3 Drying process conditions 3.1 Drying temperature Increasing the temperature can speed up drying. However, the high temperature will reduce the overall strength and other performance indicators of the pulp molded products. Each part of the wet paper mold blank will form a large temperature gradient, which will cause greater thermal stress and cause defects in the pulp molded products. In addition, an excessively high hot air temperature also increases the energy consumption, and the thermal efficiency of drying is severely reduced. Therefore, when the wet paper mold blank is dried, the temperature of the hot air is generally controlled at about 110° C. It is absolutely not allowed to exceed 120° C., and it is required that the temperature in various parts of the drying equipment should be consistent.
3.2 Control of hot air humidity during drying Hot air humidity control is very important. The moisture that evaporates out of the wet paper mold blank at the initial stage of drying, if not eliminated, will cause the humidity in the drying equipment to increase continuously, thereby prolonging the drying time of the pulp molding product and reducing the drying efficiency. For some hot air circulation drying equipment, the proportion of circulating hot air and fresh hot air must be adjusted at any time, so as not to make the drying efficiency of drying equipment colorful due to excessive humidity.
3.3 Speed ​​and flow rate of hot air The speed and flow rate of hot air entering the drying equipment is also an effective way to increase the drying speed. The speed of out-diffusion of moisture in wet paper mold blanks depends to a large extent on the speed and flow rate of hot air in the drying equipment, and it requires that high-speed hot air can be evenly blown onto the surface of the wet paper mold blank and ensure sufficient hot air flow. , It is made to be evenly dried. Generally, the pulp molding can be dried faster when the hot air speed reaches 5 m/s or more.
4 Conclusions The drying process of pulp molding products directly affects the product quality and production costs. Therefore, it is very important to understand its drying mechanism, characteristics, and determine a reasonable drying condition. At present, in the domestic production enterprises, the drying process of pulp molding products generally has the problems of high energy consumption and low drying efficiency. Some of them are defects in the drying equipment itself, but most of them are not controlled in the production of hot air temperature. The three major process elements, humidity and flow rate (flow rate), reasonably determine these three major process elements in order to obtain a better drying effect of pulp molded products.
A, starch
Increasing the starch content on the applicator to at least 29% will help improve the problems that occur when gluing and rolling. There is no need to change the formula if S/F is bonded, but if the temperature or process changes, the temperature of the gel needs to be adjusted.
Second, single-sided roll material
The preheating and deformation pretreatment of the single-sided web material is controlled to a minimum so that the single-side web material is kept as high as possible and the water content is maintained. The cardboard is pretreated with moist gas (above the drying gas). Correspondingly, the starch content is increased and the material channels are sufficiently cooled.
Third, rubber roller and preheater
An iodine test can be performed to obtain information on the type of glue, and an iodine test should be performed regularly. Check the amount of glue applied by the gluing roller, and set an appropriate interval value (0.001-0.008 inch) to adjust the amount of glue applied. The larger the interval, the greater the amount of glue applied, and vice versa. The adhesive roller, the reel tension roller and the pressure roller must be equal. Adjust the rotation speed of the coating roller to find the "best point" for the strongest adhesion. After gluing off the contradiction device, the humidity of the paperboard should be controlled within 180 degrees and the temperature difference should be kept within ±5 degrees. Temperature control and tension control are all very important factors.
Four, pressure roller
Conveyor belts and heat transfer plates must ensure that the clean, clean, flat, heavier rollers remain level. The temperature at the beginning of entering the hot sheet is low, and heat is gradually increased later. The spray water system is beneficial to any reverse-shaped control. If the corrugator is equipped with a steam device, it can increase the moisture content of the roll material and increase its humidity, thus contributing to wind-up control. After leaving the hot plate, the bottom board temperature should be less than 200 degrees.
5. Sectional, Crimping, and Cutting Quality
Sharp cutting knives, neatly aligned creases, and proper spacing settings prevent powder breaks and breaks, ensuring segmentation, creasing and breaking quality.
Sixth, the conclusion
It turns out that the above mentioned suggestions are very useful in the operation of many corrugated paper machines. However, different corrugating machines have their own characteristics and external conditions. In addition, mere adjustment on the one hand often does not solve the problem. Therefore, the operation must determine what is appropriate for the situation of your company. In order to optimize the performance of the corrugating machine, routine maintenance and training should be carried out to ensure that the corrugating machine maintains a good operating condition. This must be observed and imperative.
Pulp moulding product drying method
Pulp mouldings are a new type of packaging material produced from pulp as a raw material and are widely used for the inner packaging of various products. The production process of pulp molding products is divided into three processes: slurry processing, vacuum forming and thermal energy drying. The energy consumption of the drying process occupies a large proportion in the entire production cost. How to reasonably determine the drying process conditions and reduce energy consumption is a key issue for improving the economic efficiency of enterprises. This article will introduce the following issues related to the drying of pulp molded products.
1 Drying Method and Drying Mechanism of Pulp Moulding Products At present, the vast majority of domestic pulp molded products use the hot air drying method. In a specific drying device, the hot air as a drying medium is used to dry the pulp molded products. Hot air is mainly obtained by two methods. One is to directly generate hot air by burning in a hot air oven; the other is to use hot air to exchange hot air through heat exchanger and air. The equipment used for the drying of pulp mouldings includes drying ovens, tunnel dryers and chain dryers. No matter which type of drying equipment is used, the drying mechanism is basically the same.
The wet paper mold blank consisting mainly of pulp is a porous body having a capillary structure inside. Moisture exists between the surface of the fiber and the pores of the fiber capillary. Pulp mouldings used for internal packaging of products generally require good dynamic buffering properties, in which the moisture cannot be removed by means of mechanical squeezing, and all of them need to be removed in a dry manner first. Therefore, the pulp molded article has a great drying strength as compared with the conventional sheet drying process. Hot air, on the one hand, acts as a heat source to provide energy for removing moisture; on the other hand, it acts as a water carrier and takes away the water that has been continuously evaporated. The moisture in the wet paper mold blank depends on the internal diffusion and the external diffusion of water. The so-called internal diffusion refers to the migration of water from the interior to the surface in the wet paper mold blank; the external diffusion refers to the moisture being evaporated after evaporating from the surface thereof. The process of walking. The degree of drying efficiency of pulp moulding products depends on the speed of internal and external diffusion of moisture and the balance and coordination between the two, and reasonable process conditions are formulated around these two aspects and the drying properties of pulp mouldings.
2 Ways to Improve the Drying Efficiency of Pulp Molded Products In the drying process of pulp molded products, it is necessary to increase the drying efficiency, reduce the humidity of the drying medium (hot air), and increase the temperature and air flow rate. However, it is necessary to increase the moisture content at the same time. Outward diffusion rate. In production practice, it can be achieved through the following ways.
2.1 Appropriately reduce the thickness of pulp mouldings The greater the thickness of pulp mouldings, the more difficult it is to dry. Therefore, when designing the thickness dimension of pulp molded products, the thickness of pulp molded products should be reduced as much as possible while ensuring its overall strength and packaging performance, which is not only beneficial to the improvement of the drying efficiency, but also reducing the consumption of fiber raw materials. The difference in thickness of each part should not be too large, so as to avoid the difficulty of out-diffusion of its local moisture and affect the overall drying speed.
2.2 Appropriately increase the water gradient on the surface and internal of the wet paper mold blank. During the drying process, the moisture concentration on the surface and internal of the wet paper mold blank is the main driving force for water diffusion. Increasing the moisture gradient by adjusting the temperature, humidity, wind speed, and air volume of the hot air is advantageous for increasing the internal diffusion of moisture. However, if the out-diffusion rate of water is too high, the shrinkage of the surface of the wet paper mold is too fast and the internal diffusion rate of moisture is affected, which will have a negative effect on the drying of the pulp molded product.
2.3 Properly increase the drying temperature The increase of the drying temperature facilitates the migration of moisture from the inside of the wet paper mold blank to the surface. However, in the production practice, the increase in temperature has to be limited in many aspects, so it can only be properly improved.
3 Drying process conditions 3.1 Drying temperature Increasing the temperature can speed up drying. However, the high temperature will reduce the overall strength and other performance indicators of the pulp molded products. Each part of the wet paper mold blank will form a large temperature gradient, which will cause greater thermal stress and cause defects in the pulp molded products. In addition, an excessively high hot air temperature also increases the energy consumption, and the thermal efficiency of drying is severely reduced. Therefore, when the wet paper mold blank is dried, the temperature of the hot air is generally controlled at about 110° C. It is absolutely not allowed to exceed 120° C., and it is required that the temperature in various parts of the drying equipment should be consistent.
3.2 Control of hot air humidity during drying Hot air humidity control is very important. The moisture that evaporates out of the wet paper mold blank at the initial stage of drying, if not eliminated, will cause the humidity in the drying equipment to increase continuously, thereby prolonging the drying time of the pulp molding product and reducing the drying efficiency. For some hot air circulation drying equipment, the proportion of circulating hot air and fresh hot air must be adjusted at any time, so as not to make the drying efficiency of drying equipment colorful due to excessive humidity.
3.3 Speed ​​and flow rate of hot air The speed and flow rate of hot air entering the drying equipment is also an effective way to increase the drying speed. The speed of out-diffusion of moisture in wet paper mold blanks depends to a large extent on the speed and flow rate of hot air in the drying equipment, and it requires that high-speed hot air can be evenly blown onto the surface of the wet paper mold blank and ensure sufficient hot air flow. , It is made to be evenly dried. Generally, the pulp molding can be dried faster when the hot air speed reaches 5 m/s or more.
4 Conclusions The drying process of pulp molding products directly affects the product quality and production costs. Therefore, it is very important to understand its drying mechanism, characteristics, and determine a reasonable drying condition. At present, in the domestic production enterprises, the drying process of pulp molding products generally has the problems of high energy consumption and low drying efficiency. Some of them are defects in the drying equipment itself, but most of them are not controlled in the production of hot air temperature. The three major process elements, humidity and flow rate (flow rate), reasonably determine these three major process elements in order to obtain a better drying effect of pulp molded products.
Futsal PVC Flooring,PVC Soccer Flooring,Sport Flooring
Landscape Grass Co., Ltd. , http://www.nsbcflooring.com