Processing device for sheet by rolling method
By using cold plasma technology to process roll-pressed sheets, the problems of long drying time and severe loss of flavorings and fragrances have been solved, achieving efficient drying and low-cost production. This has improved the production cost and quality of heated non-combustible cigarette sheets.
Patent Information
- Application Number
- CN202423289395.X
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-30
- Publication Date
- 2026-01-23
- Estimated Expiration
- 2034-12-30
AI Technical Summary
In the current production of heated tobacco products, the drying time of the roll-pressed sheets is long, the energy consumption is high, and the flavoring and fragrance are severely lost.
Cold plasma technology is used to process roll-pressed sheets. The surface of the sheets is etched by a cold plasma reaction device to improve the moisture diffusion rate, shorten the drying time, and reduce the loss of fragrances and flavorings.
It improves the drying rate of sheet products, shortens drying time, reduces energy consumption, reduces the loss of fragrances and flavors, improves product quality, and reduces production costs.
Smart Images
Figure CN223816956U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of heated non-combustible cigarette manufacturing technology, and more specifically, to a processing device for thin sheets produced by roller pressing. Background Technology
[0002] As a new type of tobacco product, heated tobacco products have a focus of industry attention regarding the production method of their dedicated tobacco sheets. Roll pressing is currently the mainstream method for manufacturing tobacco sheets specifically for heated tobacco cigarettes. This involves mixing tobacco powder and fiber, then uniformly mixing them with atomizing agents, flavorings, water, and other additives. The mixture is then subjected to multi-stage rolling and oven drying to obtain rolled sheets. However, the oven drying process requires a long drying time to achieve the desired moisture content, resulting in high energy consumption. Furthermore, a large amount of flavorings evaporates due to heat, leading to economic waste. Therefore, increasing the hot air drying rate of the sheets and reducing drying time are essential for lowering production costs and improving product quality.
[0003] Cold plasma technology is an emerging non-thermal food processing technology characterized by its adaptability, high efficiency, and environmental friendliness. It has attracted widespread attention due to its outstanding applications in food processing, environmental hygiene, and medical and health fields. Research shows that cold plasma treatment can etch the surface of the treated material, increasing the rate of moisture diffusion and drying speed. Utility Model Content
[0004] In view of this, the purpose of this utility model is to provide a processing device for roll-pressed sheets, which uses cold plasma technology to process roll-pressed sheets and improve the hot air drying rate, so as to solve the problems of long drying time, high energy consumption and serious loss of fragrance and flavor in the prior art.
[0005] This utility model provides a processing device for roll-pressed thin sheets, comprising:
[0006] Cold plasma reactor; the cold plasma reactor is provided with an inlet end and an outlet end;
[0007] A filtration system connected to the inlet end;
[0008] An air pump connected to the filtration system;
[0009] The fan frequency conversion control system is connected to the outlet end;
[0010] A conveying system connected to the frequency conversion control system of the fan; the conveying system is provided with an input end and an output end; the output end outputs a cold plasma gas flow.
[0011] A pipe connected to the input terminal; the pipe is connected to the fan frequency conversion control system.
[0012] Preferably, the cold plasma reaction device is a compact atmospheric pressure cold plasma jet generator.
[0013] Preferably, the cold plasma reaction device is also equipped with a high-voltage power supply and is fixed by a base.
[0014] Preferably, the conveying system is a double-sided conveying system, which is connected to the fan frequency conversion control system via pipelines.
[0015] Preferably, the distance between the upper and lower surfaces of the double-sided conveying system is adjusted by a height adjustment valve on the support.
[0016] Preferably, the rolling sheet processing apparatus further includes:
[0017] Roller pressing device, conveyor belt and drying device.
[0018] Preferably, the rolling device is a multi-stage rolling mill unit, wherein the sheet pressed out by the last stage rolling mill enters the conveying system.
[0019] Preferably, the drying device is a mesh belt oven; the sheet output from the conveying system enters the drying device via a conveyor belt.
[0020] This utility model provides a processing device for roll-pressed thin sheets, comprising: a cold plasma reaction device; the cold plasma reaction device having an inlet end and an outlet end; a filtration system connected to the inlet end; an air pump connected to the filtration system; a fan frequency conversion control system connected to the outlet end; a conveying system connected to the fan frequency conversion control system; the conveying system having an input end and an output end; the output end outputting cold plasma airflow; a pipe connected to the input end; and the pipe being connected to the fan frequency conversion control system. Compared with existing technologies, the processing device provided by this utility model adopts a specific structure and connection relationship to achieve better overall interaction. It can process the upper and lower surfaces of the roll-pressed sheet using green, safe, and environmentally friendly cold plasma technology, followed by hot air drying. This process etches both surfaces of the sheet, accelerates surface moisture evaporation, reduces surface moisture content, increases the moisture content gradient, and accelerates moisture diffusion, thereby improving the drying rate and shortening the drying time. At the same time, the shortened drying time reduces energy consumption and lowers production costs. Furthermore, this processing device can reduce the loss of additives such as fragrances and flavorings during the drying process, improving product quality and reducing raw material costs. Attached Figure Description
[0021] Figure 1 A schematic diagram of the roll forming sheet processing device provided by this utility model;
[0022] Figure 2A schematic diagram (front view) of the operation of the roll forming sheet processing device provided by this utility model. Detailed Implementation
[0023] The technical solution of this utility model will be clearly and completely described below with reference to its embodiments. Obviously, the described embodiments are only some embodiments of this utility model, and not all embodiments. Based on the embodiments of this utility model, all other embodiments obtained by those skilled in the art without creative effort are within the protection scope of this utility model.
[0024] This utility model provides a processing device for roll-pressed thin sheets, comprising:
[0025] Cold plasma reactor; the cold plasma reactor is provided with an inlet end and an outlet end;
[0026] A filtration system connected to the inlet end;
[0027] An air pump connected to the filtration system;
[0028] The fan frequency conversion control system is connected to the outlet end;
[0029] A conveying system connected to the frequency conversion control system of the fan; the conveying system is provided with an input end and an output end; the output end outputs a cold plasma gas flow.
[0030] A pipe connected to the input terminal; the pipe is connected to the fan frequency conversion control system.
[0031] This invention provides a processing device for roll-pressed sheets, specifically a device that utilizes cold plasma (plasma is considered the fourth state of matter besides solid, liquid, and gas; it is an ionized gaseous substance produced after atoms or molecules are ionized, and can be divided into high-temperature plasma and low-temperature plasma; when the electron temperature is much higher than the ion temperature and the system is in a non-thermal equilibrium state, the gas in the system is slightly ionized, and the discharge temperature is close to room temperature, at which point it is called cold plasma) technology to process roll-pressed sheets and increase their hot air drying rate. This device can solve the problems of long drying time, high energy consumption, and serious loss of fragrances and flavors in existing technologies.
[0032] In this invention, the processing device for the roll-pressed sheet includes a cold plasma reaction device, a filtration system, an air pump, a fan frequency conversion control system, a conveying system, and pipelines.
[0033] In this invention, the cold plasma reaction device is preferably a compact atmospheric pressure cold plasma jet (APPJ) generator for generating cold plasma; the cold plasma reaction device is provided with an inlet end and an outlet end, and preferably also with a high-voltage power supply, which is fixed by a base.
[0034] In this invention, the filtration system is used to filter the gas pumped in by the air pump; the filtration system is connected to the inlet end; the other end is connected to the air pump.
[0035] In this invention, the air pump is used to pump in gas; air is preferably used as the working gas, which is low in cost and easy to obtain, and can generate effective plasma.
[0036] In this invention, the fan frequency conversion control system is used to control the flow rate of the cold plasma gas output by the cold plasma reactor; the fan frequency conversion control system is connected to the outlet end.
[0037] In this invention, the conveying system is used to perform cold plasma treatment on the sheet during the conveying process; the conveying system is connected to the frequency conversion control system of the fan; the conveying system is provided with an input end and an output end; the output end outputs a cold plasma airflow.
[0038] In this invention, the conveying system is preferably a double-sided conveying system, which is connected to the frequency conversion control system of the fan via pipelines; the distance between the upper and lower surfaces of the double-sided conveying system is preferably adjusted by a height adjustment valve on the support.
[0039] In this invention, the pipe is connected to the input end; the other end of the pipe is connected to the fan frequency conversion control system.
[0040] In this invention, the processing apparatus for the roll-pressed sheet preferably further includes:
[0041] Roller pressing device, conveyor belt and drying device.
[0042] In this invention, the roller pressing device is preferably a multi-stage roller pressing unit, more preferably a five-stage roller pressing unit; wherein, the sheet pressed out by the last stage roller pressing unit enters the conveying system.
[0043] In this invention, the drying device is preferably a mesh belt oven; the sheet output from the conveying system enters the drying device via a conveyor belt.
[0044] This utility model also provides a method for processing thin sheets by roll forming, including the following steps:
[0045] a) After premixing the powdered raw materials with the fiber, mix them evenly with the liquid raw materials to obtain a mixture;
[0046] b) After the mixture obtained in step a) is rolled into shape, it is subjected to cold plasma treatment and drying in sequence to obtain the treated rolled sheet.
[0047] The present invention first prepares the raw materials: after premixing the powdered raw materials with the fiber, it is mixed evenly with the liquid raw materials to obtain a mixture.
[0048] In this invention, the powdered raw material is preferably composed of a matrix powder and sodium carboxymethyl cellulose in a mass ratio of 100:(1-5), more preferably 100:3.
[0049] In this invention, the matrix powder is preferably selected from one or more of tobacco powder or other non-tobacco plant-based powders such as vine tea powder, black tea powder, lotus leaf powder, and corn cob powder, and more preferably from tobacco powder, vine tea powder, or lotus leaf powder. This invention does not impose any special restrictions on the source of the matrix powder; commercially available tobacco powder or non-tobacco matrix powders such as vine tea powder and lotus leaf powder, which are well-known to those skilled in the art, can be used.
[0050] In this invention, the adhesive is preferably selected from one or more of sodium carboxymethyl cellulose, hydroxypropyl methyl cellulose, guar gum, xanthan gum, locust bean gum, and tamarind polysaccharide, and more preferably sodium carboxymethyl cellulose. This invention does not impose any special restrictions on the source of the adhesive; commercially available products well-known to those skilled in the art can be used.
[0051] In this invention, the mass ratio of the powdered raw material to the fiber is preferably 103:(1-5), more preferably 103:(2-4).
[0052] In this invention, the liquid raw material is preferably a mixed solution of water, atomizing agent, flavoring and nicotine salt; the atomizing agent is preferably selected from one or more of propylene glycol, glycerol, and polyethylene glycol, more preferably propylene glycol and glycerol; the flavoring is preferably selected from one of blueberry flavoring, sweet orange flavoring, peppermint flavoring, coffee flavoring, green tea flavoring, pineapple flavoring, and grape flavoring, more preferably blueberry flavoring.
[0053] In this invention, the mass ratio of water to atomizing agent in the mixed solution of water, atomizing agent, flavoring and nicotine salt is preferably (25-35):(25-35), the content of flavoring is preferably 1‰-5‰, and the content of nicotine salt is preferably 0‰-5‰.
[0054] In a preferred embodiment of this invention, the mass ratio of water, propylene glycol, glycerol, and blueberry flavoring in the mixed solution is preferably (25-35):10:(15-25), more preferably 30:10:20, and the content of blueberry flavoring is preferably 1‰-5‰, more preferably 3‰; the mass ratio of water, propylene glycol, glycerol, nicotine salt, and blueberry flavoring in the mixed solution is preferably (25-30):(15-20):(5-20), more preferably 28:(15-20):(10-15), the content of nicotine salt is preferably 1‰-5‰, more preferably 3‰, and the content of blueberry flavoring is preferably 1‰-5‰, more preferably 3‰.
[0055] This invention does not impose any special restrictions on the source of the raw materials such as propylene glycol, glycerol, nicotine salt, and blueberry flavoring; commercially available products well known to those skilled in the art can be used. The water is preferably deionized water.
[0056] In this invention, the preferred mass ratio of the liquid raw material to the powdered raw material is (50-70):103, and more preferably (58-60):103.
[0057] After obtaining the mixture, the present invention roll-presses the mixture into shape, and then subjectes it to cold plasma treatment and drying to obtain the treated roll-pressed sheet.
[0058] In this invention, the roll forming process preferably employs a multi-stage roll forming unit to form a sheet with a certain thickness and density. In a preferred embodiment of this invention, the multi-stage roll forming unit is a five-stage roll forming unit.
[0059] In this invention, the cold plasma treatment preferably employs the processing device described in the above technical solution, which uses cold plasma to etch the surface of the thin sheet to increase the moisture diffusion rate on the surface of the thin sheet; the working gas for the cold plasma treatment is preferably air; and the object of the cold plasma treatment is preferably the upper and lower surfaces of the thin sheet.
[0060] In this invention, the output power of the cold plasma treatment is preferably 500W to 1000W, more preferably 800W to 1000W; the flow rate of the cold plasma gas flow is preferably 100L / min to 500L / min, more preferably 300L / min to 400L / min, and is controlled by the aforementioned fan frequency conversion control system; the jet distance of the cold plasma treatment is preferably 10cm to 30cm, more preferably 20cm to 30cm; this invention adopts a method of simultaneously spraying cold plasma from above and below, and the jet distance is the distance between the cold plasma and the thin sheet.
[0061] In this invention, the cold plasma treatment time (the treatment time refers to the time from when the sheet begins to enter the conveying system and is subjected to the cold plasma jet until the sheet leaves the conveying system) is preferably not less than 30s, and more preferably 30s to 40s; the time the sheet is subjected to the cold plasma can be adjusted by controlling the speed of the roller press, the speed of the conveyor belt, and the distance between the roller press and the conveyor belt.
[0062] In this invention, the drying method is preferably hot air drying, which can be achieved using an oven, preferably a mesh belt oven; after drying, a roll-pressed sheet with a suitable moisture content is obtained; the drying temperature is preferably 70℃~100℃, more preferably 80℃~90℃, and the moisture content after drying is preferably not higher than 10% (calculated by oven method).
[0063] Finally, the finished products are collected: after drying, the thin sheets undergo cooling, cutting and other subsequent processing to obtain the final roll-pressed tobacco sheets for heat-not-burn cigarettes.
[0064] This utility model provides a processing device for roll-pressed thin sheets, comprising: a cold plasma reaction device; the cold plasma reaction device having an inlet end and an outlet end; a filtration system connected to the inlet end; an air pump connected to the filtration system; a fan frequency conversion control system connected to the outlet end; a conveying system connected to the fan frequency conversion control system; the conveying system having an input end and an output end; the output end outputting cold plasma airflow; a pipe connected to the input end; and the pipe being connected to the fan frequency conversion control system. Compared with existing technologies, the processing device provided by this utility model adopts a specific structure and connection relationship to achieve better overall interaction. It can process the upper and lower surfaces of the roll-pressed sheet using green, safe, and environmentally friendly cold plasma technology, followed by hot air drying. This process etches both surfaces of the sheet, accelerates surface moisture evaporation, reduces surface moisture content, increases the moisture content gradient, and accelerates moisture diffusion, thereby improving the drying rate and shortening the drying time. At the same time, the shortened drying time reduces energy consumption and lowers production costs. Furthermore, this processing device can reduce the loss of additives such as fragrances and flavorings during the drying process, improving product quality and reducing raw material costs.
[0065] To further illustrate this utility model, the following embodiments will be described in detail.
[0066] Example 1
[0067] See Figures 1-2 As shown, Figure 1A schematic diagram of the structure of the roller pressing sheet processing device provided by this utility model, wherein, 2: roller pressing sheet, 31: air pump, 32: filtration system, 33: high voltage power supply, 34: cold plasma reaction chamber, 35: fan frequency conversion control system, 36: pipeline, 37: conveying system, 38: cold plasma airflow, 39: base; Figure 2 A schematic diagram (front view) of the roller pressing sheet processing device provided by this utility model, wherein 1: roller press, 11: pressure roller, 2: roller pressing sheet, 36: pipe, 37: conveying system, 38: cold plasma airflow, 4: conveyor belt.
[0068] The working process of the roll forming sheet processing device provided by this utility model is as follows:
[0069] After the sheet (2) is pressed out by the last stage roller press (1), the upper and lower surfaces are treated by cold plasma spraying from the cold plasma device (3), and then conveyed to the mesh belt oven for hot air drying via the conveyor belt (4). Among them, the gas is pumped into the filtration system (32) by the air pump (31), and after filtration, it enters the reaction chamber (34) and generates cold plasma after being excited by the electric field or electromagnetic field. The cold plasma is then conveyed to the surface of the sheet via the fan frequency conversion control system (35), pipeline (36) and conveying system (37). The distance between the upper and lower double-sided conveying systems (37) can be adjusted by the height adjustment valve (41) on the support (40) to adjust the jet distance of the cold plasma on the sheet.
[0070] In Embodiment 1 of this utility model, the sheet material is prepared according to the following proportions:
[0071] Powdered ingredients: 100 parts by weight of tobacco powder, 3 parts by weight of sodium carboxymethyl cellulose, and 2 parts by weight of added fiber; Liquid ingredients: 30 parts by weight of water, 10 parts by weight of propylene glycol, 20 parts by weight of glycerol, and 3‰ of blueberry flavoring.
[0072] Process flow, specific conditions and parameters:
[0073] After the powdered raw materials are premixed with the fibers, they are mixed evenly with a solution containing atomizing agents, adhesives, water and other additives, and then fed into a roller press to begin five-stage roller pressing.
[0074] After five stages of rolling, the sheet is pulled onto a conveyor belt and laid flat, and then cold plasma treatment begins.
[0075] The cold plasma device was set to have an output power of 800W, a cold plasma gas flow rate of 300L / min, a jet distance of 20cm, and a cold plasma treatment time of 30s.
[0076] The thin sheets are placed in an oven for hot air drying at a temperature of 90°C.
[0077] Finally, the finished products are collected: after drying, the thin sheets undergo cooling, cutting and other subsequent processing to obtain the final roll-pressed tobacco sheets for heat-not-burn cigarettes.
[0078] Example 2
[0079] The device and working process provided in Example 1 are used, with the following differences:
[0080] Example 2: The sheet material was prepared according to the following proportions:
[0081] Powdered ingredients: 100 parts by weight of vine tea powder, 3 parts by weight of sodium carboxymethyl cellulose, and 4 parts by weight of added fiber; Liquid ingredients: 28 parts by weight of water, 15 parts by weight of propylene glycol, 15 parts by weight of glycerol, 3‰ of nicotine salt, and 3‰ of blueberry flavoring.
[0082] Process flow, specific conditions and parameters:
[0083] After the powdered raw materials are premixed with the fibers, they are mixed evenly with a solution containing atomizing agents, adhesives, water and other additives, and then fed into a roller press to begin five-stage roller pressing.
[0084] After five stages of rolling, the sheet is pulled onto a conveyor belt and laid flat, and then cold plasma treatment begins.
[0085] The cold plasma device was set to have an output power of 900W, a cold plasma gas flow rate of 300L / min, a jet distance of 30cm, and a cold plasma treatment time of 40s.
[0086] The thin sheets are placed in an oven for hot air drying at a temperature of 90°C.
[0087] Finally, the finished products are collected: after drying, the thin sheets undergo cooling, cutting and other subsequent processing to obtain the final roll-pressed tobacco sheets for heat-not-burn cigarettes.
[0088] Example 3
[0089] The device and working process provided in Example 1 are used, with the following differences:
[0090] Example 3: The sheet material was prepared according to the following proportions:
[0091] Powdered ingredients: 100 parts by weight of lotus leaf powder, 3 parts by weight of sodium carboxymethyl cellulose, and 4 parts by weight of added fiber; Liquid ingredients: 28 parts by weight of water, 20 parts by weight of propylene glycol, 10 parts by weight of glycerol, 3‰ of nicotine salt, and 3‰ of blueberry flavoring.
[0092] Process flow, specific conditions and parameters:
[0093] After the powdered raw materials are premixed with the fibers, they are mixed evenly with a solution containing atomizing agents, adhesives, water and other additives, and then fed into a roller press to begin five-stage roller pressing.
[0094] After five stages of rolling, the sheet is pulled onto a conveyor belt and laid flat, and then cold plasma treatment begins.
[0095] The cold plasma device was set to have an output power of 1000W, a cold plasma gas flow rate of 400L / min, a jet distance of 30cm, and a cold plasma treatment time of 40s.
[0096] The thin sheets are placed in an oven for hot air drying at a temperature of 80°C.
[0097] Finally, the finished products are collected: after drying, the thin sheets undergo cooling, cutting and other subsequent processing to obtain the final roll-pressed tobacco sheets for heat-not-burn cigarettes.
[0098] Comparative Example
[0099] Prepare the sheet material according to the following proportions:
[0100] Powdered raw materials: 100 parts by weight of tobacco powder, 3 parts by weight of sodium carboxymethyl cellulose; 2 parts by weight of added fiber; Liquid raw materials: 30 parts by weight of water, 10 parts by weight of propylene glycol, 20 parts by weight of glycerol, and 3‰ of blueberry flavoring. After the powdered raw materials and fiber are premixed, they are mixed evenly with a solution containing atomizing agent, adhesive, water and other additives, and then fed into a roller press for five-stage roller pressing.
[0101] The thin sheets, without being treated by the cold plasma device, are placed in an oven for hot air drying at a temperature of 90°C.
[0102] Finally, the finished products are collected: after drying, the thin sheets undergo cooling, cutting and other subsequent processing to obtain the final roll-pressed tobacco sheets for heat-not-burn cigarettes.
[0103] The moisture content was measured using the oven drying method. The length of the mesh belt oven was fixed, and the drying time of the sheet was controlled by adjusting the speed of the conveyor belt. The drying time was defined as the time from the start of drying until the sheet reached the target moisture content (not exceeding 10%). The drying times of the comparative example and the three embodiments are shown in Table 1 below.
[0104] Table 1
[0105]
[0106]
[0107] The comparison shows that cold plasma treatment can significantly reduce the drying time of the roll forming sheet, and the improvement in the drying rate of the sheet is more significant as the power of the cold plasma device increases, the flow rate increases, and the processing time increases.
[0108] The tobacco sheets prepared in Examples 1-3 and the tobacco sheets prepared under conventional techniques in the comparative example were compared by gas chromatography-mass spectrometry to determine the retention of aroma components. Vanillin was used as the characteristic marker of the added blueberry flavor. The comparison results are shown in Table 2 below.
[0109] Table 2
[0110]
[0111] Although the amount of flavorings and fragrances added to cigarette sheets is relatively low, their cost accounts for a significant proportion of the production cost. Furthermore, flavorings and fragrances are highly volatile when heated. In traditional cigarette sheet production processes, to ensure that the amount of flavorings and fragrances retained in the finished sheets meets the sensory requirements for heated cigarettes, the amount added is often increased, thus increasing production costs. A comparison shows that, in different embodiments, after cold plasma treatment, as the hot air drying time in the oven is reduced, the amount of flavorings added to the sheets decreases, the retention rate increases, and the flavoring efficiency is improved.
[0112] The above description of the disclosed embodiments enables those skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the present invention. Therefore, the present invention is not 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
1. A processing apparatus for roll-pressed thin sheets, characterized in that, include: Cold plasma reactor; the cold plasma reactor is provided with an inlet end and an outlet end; A filtration system connected to the inlet end; An air pump connected to the filtration system; The fan frequency conversion control system is connected to the outlet end; A conveying system connected to the frequency conversion control system of the fan; the conveying system is provided with an input end and an output end; the output end outputs a cold plasma gas flow. A pipe connected to the input terminal; the pipe is connected to the fan frequency conversion control system.
2. The processing apparatus for roll-pressed thin sheets according to claim 1, characterized in that, The cold plasma reaction device is a compact atmospheric pressure cold plasma jet generator.
3. The processing apparatus for roll-pressed thin sheets according to claim 1, characterized in that, The cold plasma reactor is also equipped with a high-voltage power supply and is fixed by a base.
4. The processing apparatus for roll-pressed thin sheets according to claim 1, characterized in that, The conveying system is a double-sided conveying system, which is connected to the fan frequency conversion control system via pipelines.
5. The processing apparatus for roll-pressed thin sheets according to claim 4, characterized in that, The upper and lower double-sided conveying system adjusts the distance between the upper and lower surfaces using a height adjustment valve on the support frame.
6. The processing apparatus for roll-pressed thin sheets according to claim 1, characterized in that, The rolling sheet processing apparatus further includes: Roller pressing device, conveyor belt and drying device.
7. The rolling sheet processing apparatus according to claim 6, characterized in that, The roller pressing device is a multi-stage roller pressing unit, wherein the sheet pressed out by the last stage roller pressing enters the conveying system.
8. The rolling sheet processing apparatus according to claim 7, characterized in that, The drying device is a mesh belt oven; the sheets output from the conveyor system enter the drying device via a conveyor belt.