A fluid mechanics-based mixing system developed to ensure homogeneous distribution of paraffin at the nano-sized particle level in paraffin emulsions used in wood-based fiberboard production

The fluid mechanics-based mixing system addresses particle agglomeration and non-uniformity in paraffin emulsions by using turbulent flow generators and a dual-cycle process, achieving nano-sized distribution and reducing paraffin usage with continuous operation.

WO2025221217A1PCT designated stage Publication Date: 2025-10-23UNİ MÜHENDİSLİK TEKNOLOJİ & DANIŞMANLIK SANAYİ TİCARET ANONİM ŞİRKETİ
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Patent Information

Application Number
PCT/TR2024/051516
Authority / Receiving Office
WO · WO
Patent Type
Applications
Current Assignee / Owner
Filing Date
2024-12-09
Publication Date
2025-10-23

AI Technical Summary

Technical Problem

Existing paraffin emulsions in wood-based fiberboard production suffer from particle agglomeration and non-homogeneous distribution, which affects adhesive performance and dimensional stability, and there is a need for a system to reduce paraffin usage while ensuring uniform distribution at the nano-particle level.

Method used

A fluid mechanics-based mixing system utilizing turbulent flow generators and a dual-cycle process to micronize and homogeneously distribute paraffin particles at the nano-level within emulsions, incorporating redundant components for uninterrupted operation.

Benefits of technology

The system effectively reduces paraffin particle size to nano-level, enhances distribution uniformity, minimizes adhesive requirements, and ensures continuous operation by integrating backup systems.

✦ Generated by Eureka AI based on patent content.

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Abstract

It is about the system which mixes the pressurised liquid paraffin emulsion by passing it through the turbulent flow generator (14) under high pressure in order to reduce the paraffin in the paraffin emulsions prepared by using water or different liquid chemicals, especially in the production of wood-based fibreboard, to nanoparticle size and to ensure homogeneous distribution in the emulsion, micronises, disperses the paraffin lumps, and is structured with system elements and product cycle line with back-up against any technical staff failure.
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Description

[0001] DESCRIPTION

[0002] A Fluid Mechanics-Based Mixing System Developed to Ensure Homogeneous Distribution of Paraffin at the Nano-Sized Particle Level in Paraffin Emulsions Used in Wood-Based Fiberboard Production

[0003] Field of the Invention

[0004] In paraffin emulsions used in the production of wood-based fibreboard, it is related to the system that enables the paraffin to be reduced to nano-particle level in the emulsion, eliminating clumping and enabling homogeneous distribution. In particular, the invention relates to a fully automatic mixture preparation system developed on the basis of fluid mechanics to ensure homogeneous distribution of paraffin in the emulsion at the nano level.

[0005] Prior Art

[0006] The description regarding the definition, explanation of wood-based panels (MDF, LDF, HDF), and the reasons for using paraffin in their manufacture is referenced from the doctoral dissertation titled "Different Chemical Usage Aimed at Improving the Performance of Medium Density Fiberboard (MDF)" by Assistant Professor Meryem ONDARAL at Karadeniz Technical University, dated 2019.

[0007] According to this thesis:

[0008] With the acceleration of industrial development and population growth, the demand for wood-based materials has increased, leading to issues with raw material supply. To meet industrial needs and ensure production continuity, research has been conducted into alternative products to solid wood, resulting in advancements in the production of wood- based panels (Eroglu and Usta, 2000). Wood-based panels include chipboard, fiberboard, oriented strand board, plywood, and veneer sheets. Among the reasons for choosing these materials are their ease of processing, homogeneous structure, ease of machine cutting, and ability to be manufactured with desired properties depending on their intended use (Ybrur and Birinci, 2018). Fiberboards are produced by refining fibers from lignocellulosic materials such as wood or annual plant stems, followed by shaping and pressing with the addition of adhesives and additives to achieve the desired form (Guller, 2001 ). Wood-based panels, particularly fiberboards, play a significant role, with medium density fiberboards (MDF) being at the forefront of production. Reasons for this include extensive industrial applications, high physical and mechanical resistance properties, and the ability to be manufactured using low- cost wood raw materials. Alongside these positive attributes, fiberboards also exhibit some drawbacks. One primary disadvantage is their hygroscopic nature, which leads to changes in dimensional stability and mechanical resistance due to moisture absorption from hygroscopic fibers (Carll and Wiedenhoeft, 2009). This underscores the importance of tailored fiberboard production based on specific uses. The addition of water-repellent chemicals to make fiberboards resistant to water and moisture has become crucial (Torkaman, 2008). Producing fiberboards with resistance to water and moisture ensures their reliability in usage environments and promotes their long-term economic viability.

[0009] Paraffins are hydrophobic materials used in the production of fiberboards and particleboards to prevent the structure of boards from deteriorating or "working" when in contact with water and moisture. Their non-polar nature prevents them from being chemically active. Their hydrophobic effect involves penetrating the capillary gaps of fibers to prevent water and moisture from entering these areas. Paraffins are typically used in the form of emulsions. Using more than 1 -2% of paraffins relative to the dry weight of fibers can adversely affect adhesive performance. It is known that hydrophobic materials reduce the bonding structure within the boards, thereby deteriorating their resistance properties (Eroglu and Usta, 2000).

[0010] In research conducted on the Turkish Patent and Trademark Office database, Application Number 97 / 00095 dated February 6, 1997 has been found.

[0011] In this application, it is mentioned that before the gluing process in chipboard production, an emulsion of paraffin is sprayed and pulverized onto the chips with compressed air. This emulsion facilitates the application process, enhances the chipboard's resistance to moisture, reduces glue consumption, minimizes contamination during the transport and spreading of glued chips, and improves these processes at the following rates.

[0012] This application represents the finalized and completed version of our minimum requirements application with file number 2024 / 002496 as of March 1 , 2024.

[0013] Accordingly, the purpose of the invention is to reduce paraffin to nano particle size using a fluid mechanics-based system in paraffin emulsions prepared with water or different liquid chemicals, especially in the production of wood-based fiberboard, and to ensure homogeneous distribution within the emulsion.

[0014] Another object of the present invention is to eliminate micro-level particle agglomerations in paraffin emulsions.

[0015] Another object of the present invention is to reduce the amount of paraffin and adhesive used in the emulsion.

[0016] Another object of the present invention is to increase the mixture ratio of paraffin with adhesive.

[0017] Another object of the present invention is to ensure that the paraffin emulsion is prepared to exhibit a balanced distribution on the applied surface.

[0018] Another object of the present invention is to establish a redundant operation system that can bypass malfunctioning components during the emulsion processing process and continue operation.

[0019] Another object of the present invention is to

[0020] Introduce a modular structured system that operates separately from the wood-based fiberboard production system and can be integrated into the wood-based fiberboard production system as desired.

[0021] In the preferred embodiment of the invention, the processing of the system's product is carried out in a dual-cycle manner.

[0022] In the preferred embodiment of the invention,

[0023] In case of any element failure in the system, the system elements are interconnected in parallel to include their backups, ensuring uninterrupted operation until the maintenance team arrives.

[0024] Reference Numbers

[0025] 1 . Circulation pump / pumps 2. Three-way actuated valve / valves

[0026] 3. Piston pump / pumps

[0027] 4. Piston pump motor / motors

[0028] 5. Filter housing and filter / filters

[0029] 6. Pressure sensor / sensors

[0030] 7. Manometer / manometers

[0031] 8. Temperature sensor / sensors

[0032] 9. Fluid pipeline and hose / hoses

[0033] 10. Pressure regulator (accumulator)

[0034] 11 . Conditioner

[0035] 12. HMI screen

[0036] 13. Flow meter

[0037] 14. Turbulent flow generator / generators

[0038] 15. Upper block

[0039] 16. Upper block flow channel

[0040] 17. Upper block flow channel sets

[0041] 18. Upper block mounting element sockets

[0042] 19. Lower block

[0043] 20. Lower block flow channel

[0044] 21 . Lower block flow channel sets

[0045] 22. Lower block mounting element sockets

[0046] 23. Fluid inlet port

[0047] 24. Fluid outlet port

[0048] 25. Mounting element / elements

[0049] 26. Turbulent flow generator heat sensor

[0050] 27. RFID Lock

[0051] 28. Connection bracket

[0052] 29. Enclosure cabinet

[0053] 30. Resistor

[0054] 31. Heat exchanger

[0055] 32. Manual valve

[0056] 33. Tank / tanks 34. Tank mixer and motor

[0057] 35. Level sensor

[0058] 36. Electrical panel

[0059] 37. Chassis

[0060] 38. PLC

[0061] 39. Second cycle circulation pump

[0062] 40. Pump BYPASS

[0063] 41. Product inlet port

[0064] 42. Water inlet port

[0065] 43. Product outlet port

[0066] 44. Heat exchanger water inlet port

[0067] Description of the Figures

[0068] Figure 1 . Top view of the system.

[0069] Figure 2. Front view of the system's product inlet area.

[0070] Figure 3. Front view of the system's product outlet area.

[0071] Figure 4. Comprehensive side view of the operator panel of the system.

[0072] Figure 5. Comprehensive rear view of the system.

[0073] Figure 6. Assembled view of the turbulent flow generator

[0074] Figure 7. Top view of the assembled turbulent flow generator

[0075] Figure 8. Appearance of the assembled turbulent flow generator inside the enclosure.

[0076] Figure 9. Demonstration of the turbulent flow generator's upper block flow mixing channel.

[0077] Figure 10. Demonstration of the turbulent flow generator's lower block flow mixing channel.

[0078] Figure 11 . Isometric view of the heat exchanger system.

[0079] Figure 12. Front view of the heat exchanger system.

[0080] Figure 13. View of Cycle 1 piping diagram.

[0081] Figure 14. View of Cycle 1 piping diagram.

[0082] Figure 15. View of piston pumps and motors.

[0083] Figure 16. Front view of the filter assemblies.

[0084] Figure 17. Front view of the filter assemblies. Detailed Description of the Invention

[0085] The invention relates to the "Fluid Mechanics-Based Mixture Preparation System Developed to Ensure Homogeneous Distribution of Paraffin at the Nano-Particle Level within the Emulsion in Paraffin Emulsions Used in the Production of Wood-Based Fiber Boards," which eliminates all the disadvantages and achieves the intended results mentioned in the related subject above.

[0086] As is known, particularly in systems that use liquid fluids, there are two types of flow patterns in the transmission elements, such as pipes: aerodynamic or laminar (smooth layered flow) and turbulent flow.

[0087] In laminar flow, all particles of the fluid move parallel to each other. In turbulent flow, however, the flow conditions contribute to turbulence formation due to factors such as the very small size of the flow passage relative to the desired fluid speed, the high viscosity of the hydraulic fluid, sudden changes in the diameter of rough, irregularly shaped fluid passages, and abrupt changes in the direction of the fluid.

[0088] The invention employs a turbulent flow generator (14), which can intentionally create turbulent flow, a type of flow pattern in fluid mechanics, to reduce paraffin particles to the nano-particle level within the emulsion and ensure their homogeneous distribution. The system architecture is developed around this turbulent flow and the turbulent flow generator (14) that produces it to achieve its intended purpose.

[0089] Accordingly;

[0090] At least one circulation pump (1 ) to load the paraffin emulsion mixed with liquid into the system, taking it from the preparation tank (30) where it is stored after the first processing cycle to be re-pressurized by the piston pumps (3),

[0091] At least twenty-five three-way actuator valves (2) directing the fluid paraffin emulsion throughout the fluid pipeline and hoses (9) to the necessary system components during the process, including bypassing elements and locally stopping or starting the flow and for opening or closing,

[0092] At least three piston pumps (3) to generate fluid pressure in the system to ensure that the paraffin emulsion passes through the turbulent flow generator (14) at high speed and pressure, At least three piston pump motors (4) to drive the piston pumps (3),

[0093] At least six filter housings and filters (5) to filter the product (paraffin emulsion) processed within the system during the processing stage,

[0094] At least eleven pressure sensors (6) to measure and monitor the system pressure,

[0095] At least three manometers (7) to analogly monitor the system pressure,

[0096] At least four temperature sensors (8) to monitor the system temperature,

[0097] Fluid piping and hoses (9) to transport and process the product throughout the system during the processing stage and deliver it to the necessary system components,

[0098] At least two pressure regulators (accumulators) (10) to balance pressure drops in the system,

[0099] A conditioner (1 1 ) to condition the flow,

[0100] At least one HMI screen (12) to control, program, and make necessary adjustments to the system's process and operations,

[0101] At least two flow meters (13) to measure the quantity of processed product discharged from the system, to ensure that the product processed in the system is reduced to nano particle size through cavitation under high pressure in a turbulent flow environment and achieves homogeneous distribution within the emulsion, an upper block (15) comprising a semi-cylindrical upper block flow channel (16) extending in proportion to its length on the horizontal axis in the central inner region and protruding upper block flow channel sets (17) arranged in a form and arrangement to enable the fluid to impinge and change direction along the said flow channel (16), lower block fastening element slots (22) and upper block fastening element slots (18) on the same axis and in an arrangement to meet each other, and a semi-cylindrical lower block flow channel (20) extending in proportion to its length on the horizontal axis in the central inner region and a lower block (19) comprising protruding lower block flow channel sets (21 ) arranged in a form and arrangement to enable the fluid to impact and change direction along the said flow channel (20), upper block fastening slots (18) and lower block fastening slots (22) on the same axis and in a mutually meeting arrangement, at least two turbulent flow generators (14) having fluid inlet port (23) and fluid outlet port (24) points which are integrated as a result of the upper block flow channel (16) and lower block flow channel (20) regions being joined by means of fastening element(s) (25) through the upper block fastening element slots (18) and lower block fastening element slots (22) so as to meet and overlap each other,

[0102] Fastening elements (25) to connect the upper block (15) and the lower block (16) together,

[0103] A turbulent flow generator temperature sensor (26) to detect the temperature within the turbulent flow generator,

[0104] At least one RFID lock (27) to prevent unauthorized access to the enclosure housing the turbulent flow generator(s),

[0105] The turbulent flow generator(s) housed (29) within at least one enclosure,

[0106] A heat exchanger (31 ) to reduce the temperature of the processed product to a suitable level for storage outside the system,

[0107] Manual valves (32) are used for draining the cleaning fluid or air from the system during the processing phase or at any point in the process, for redirecting the fluid within the system, draining it, or cleaning the system,

[0108] Tank / tanks (33) to store the product during the first cycle of the processing phase,

[0109] Tank mixer and motor (34) when necessary, the product stored in the tank is mixed,

[0110] A level sensor (35) to determine the liquid level of the product in the tank,

[0111] Electrical panel (36) that houses the electronic control and switching elements,

[0112] Chassis (37), which is comprises three separate cube-shaped blocks on which the system elements are mounted,

[0113] PLC (38) to program, manage, regulate, and modify the product processing system,

[0114] To reintroduce the paraffin emulsion stored in the tank(s) (33) after the initial processing phase into the second cycle, secondary circulation (39) pump elements are used for the following processes;

[0115] - Loading the paraffin emulsion prepared outside the system into the system using a circulation pump (1 ),

[0116] - Sending it to the filter (5) unit(s) for filtration (5), - Conveying it to the piston pumps (3) for pressurization,

[0117] - Pressurizing it in the piston pump(s) (3),

[0118] - Transferring it to the turbulent flow generator (14) under high pressure for micronization and mixing,

[0119] - Passing it through the turbulent flow generator (14) under high pressure,

[0120] - Sending and storing it in the preparation tank(s) (33) at the exit of the turbulent flow generator (14) under low pressure for the second process cycle

[0121] - Taking the paraffin emulsion stored in the preparation tank(s) (33) from the preparation tank(s) (33) via the second circulation pump (39) in order to enter it into the second cycle,

[0122] - Sending it to the piston pump(s) (3) via the second circulation pump (38) to be re-pressurized,

[0123] - Repressurization of paraffin emulsion,

[0124] - Sending it to the filter (5) unit(s) for filtration (5),

[0125] - Transferring it to the turbulent flow generator (14) under high pressure for micronization and mixing,

[0126] - Passing it through the turbulent flow generator (14) under high pressure,

[0127] - Reducing the pressure at the outlet of the turbulent flow generator (14),

[0128] - Sending it to the heat exchanger (31 ) unit to reduce the temperature in order to be stored at room temperature,

[0129] - Lowering the temperature in the heat exchanger (31 ),

[0130] - After being passed through the flow meter (13) for storage, being discharged out of the system.

[0131] As detailed above, the invention features a two-cycle process in the product processing procedure.

[0132] During the first cycle:

[0133] - Loading the paraffin emulsion prepared outside the system into the system using a circulation pump (1 ),

[0134] - Sending it to the filter (5) unit(s) for filtration (5),

[0135] - Conveying it to the piston pumps (3) for pressurization,

[0136] - Pressurizing it in the piston pump(s) (3), - Transferring it to the turbulent flow generator (14) under high pressure for micronization and mixing,

[0137] - Passing it through the turbulent flow generator (14) under high pressure,

[0138] - Sending and storing it in the preparation tank(s) (33) at the exit of the turbulent flow generator (14) under low pressure for the second process cycle. In this phase, the paraffin particles in the paraffin emulsion are micronized as much as possible and mixed within the emulsion.

[0139] In the second cycle of the process, it comprises the following process steps:

[0140] - Taking the paraffin emulsion stored in the preparation tank(s) (33) from the preparation tank(s) (33) via the second circulation pump (38) in order to enter it into the second cycle,

[0141] - Sending it to the piston pump(s) (3) via the second circulation pump (38) to be re-pressurized,

[0142] - Repressurization of paraffin emulsion,

[0143] - Sending it to the filter unit(s) (5) for filtration (5),

[0144] - Transferring it to the turbulent flow generator (14) under high pressure for micronization and mixing,

[0145] - Passing it through the turbulent flow generator (14) under high pressure,

[0146] - Reducing the pressure at the outlet of the turbulent flow generator (14),

[0147] - Sending it to the heat exchanger (31 ) unit to reduce the temperature in order to be stored at room temperature,

[0148] - Lowering the temperature in the heat exchanger (31 ),

[0149] - After being passed through the flow meter (13) for storage, being discharged out of the system.

[0150] The aim of the second process is to reduce the size of the paraffin particles in the paraffin emulsion to nano level and make their distribution in the emulsion more homogeneous.

[0151] In the system's first processing cycle, one of the three piston pumps is activated, pressurizing the paraffin emulsion and sending it to the turbulent flow generator section. In the second processing cycle, another of the three piston pump / pumps (3) is activated, pressurizing the paraffin emulsion and sending it to the turbulent flow generator (14) section.

[0152] The system employs two active piston pumps (3) to pressurize the paraffin emulsion. The third piston pump (3) serves as a backup, activated by the system when either of the two active pumps (3) malfunctions.

Claims

CLAIMS1 . A fluid mechanics-based mixing system developed to ensure homogeneous distribution of paraffin at the nano-sized particle level in paraffin emulsions used in wood-based fiberboard production, characterized in that, in order to eliminate paraffin lumps in paraffin emulsions prepared by using water or different liquid chemicals in the production of wood-based fibreboard, to micronise paraffin particle sizes, to distribute as evenly as possible in the emulsion, to mix easily and homogeneously with glue, to spread homogeneously on the application surface, to prevent increases in the amount of use resulting from paraffin lumps, comprising at least one circulation pump(s) (1 ) to load the paraffin emulsion mixed with liquid into the system, to take the product from a preparation tank (30) where it is stored at the end of the first processing cycle and to transmit it to piston pumps (3) to be re-pressurised at least twenty-five three-way actuated valves (2) for directing the fluid paraffin emulsion to the required system elements on the fluid pipework and hoses (9) throughout the process, element bypasses, localised interruption or opening of the flow, at least three piston pumps (3) to generate fluid pressure in the system to ensure that the paraffin emulsion is passed through the turbulent flow generator (14) at high speed and pressure, at least three piston pump motor(s) (4) for the drive of piston pumps (3), at least six filter chambers and filter(s) (5) for filtering the product (paraffin emulsion) processed in the system during the process, at least eleven pressure sensor / sensors (6) for measuring and monitoring the system pressure, at least three manometer(s) (7) for analogue monitoring of system pressure, at least four temperature sensor(s) (8) for monitoring system temperature, fluid pipeline and hose / hoses (9) for conveying the processed product to the necessary system elements in order to transport and process it within the system during the processing process, at least two pressure regulators (accumulators) (10) in order to balance pressure drops in the system, conditioner (1 1 ) for conditioning the flow, at least one Hmi screen (12) for controlling, programming and making necessary adjustments to the process and operations of the system, at least two flow meters (13) to measure the quantity of the processed product during discharge out of thesystem, in order to reduce the product processed in the system to nanoparticle size by cavitation in a turbulent flow environment under high pressure and to ensure homogeneous distribution in the emulsion, at least two turbulent flow generators (14) wherein an upper block (15) comprising a semi-cylindrical upper block flow channel (16) extending in length on the horizontal axis in the centre inner region and protruding upper block flow channel sets (17) arranged in a form and arrangement that will allow the fluid to hit and change direction along the said flow channel (16), lower block fastening element slots (22) and upper block fastening element slots (18) on the same axis and in an arrangement to meet each other and a lower block (19) comprising a semi-cylindrical lower block flow channel (20) extending in the horizontal axis in the centre inner region in proportion to its length, and a lower block (19) comprising protruding lower block flow channel sets (21 ) arranged in a form and arrangement to enable the fluid to strike and change direction along the said flow channel (20), upper block fastening element slots (18) and lower block fastening element slots (22) on the same axis and in a mutually meeting arrangement, are joined by means of fastener(s) (25) through the upper block fastening element slots (18) and the lower block fastening element slots (22) in such a way that the upper block flow channel (16) and the lower block flow channel (20) meet and overlap each other, having a fluid inlet port (23) and a fluid outlet port (24) points, fastening elements (25) for connecting the upper (15) and lower blocks (16) with each other, a turbulent flow generator heat sensor (26) for the detection of heat in the turbulent flow generator, At least one Rfid Lock (27) to prevent unauthorised opening of the enclosure cabinet the turbulent flow generator(s), at least one enclosure cabinet (29) housing the turbulent flow generator(s), a heat exchanger (31 ) to reduce the processed product to the appropriate temperature level when it is discharged out of the system for storage, a manual valve (32) for the diversion and discharge of the fluid in the system during the process phase or at any point in the process, or for the discharge of the fluid used for cleaning during the cleaning phase of the system or for the discharge of the air in the system, preparation tank(s) (33) for the purpose of storing the product during the product processing process of the system, especially during the first cycle phase of the product, a tankmixer and motor (34) for mixing the product stored in the preparation tank(s) when necessary, a level sensor (35) for determining the level of the product liquid in the preparation tank(s) (33), an electrical panel (36) containing electronic control and switchgear elements, a chassis (37) comprises three separate cube-shaped blocks on which the system elements are mounted, a PLC (38) to programme, manage, regulate and modify the product handling process of the system, Second circulation pump (39) elements to ensure that the paraffin emulsion stored in the tank(s) (33) as a result of the first product processing is introduced into the second cycle, comprises the following product processing steps;- Loading the paraffin emulsion prepared outside the system into the system using a circulation pump (1 ),- Sending it to the filter (5) unit(s) for filtration (5),- Conveying it to the piston pumps (3) for pressurization,- Pressurizing it in the piston pump(s) (3),- Transferring it to the turbulent flow generator (14) under high pressure for micronization and mixing,- Passing it through the turbulent flow generator (14) under high pressure,- Sending and storing it in the preparation tank(s) (33) at the exit of the turbulent flow generator (14) under low pressure for the second process cycle- Taking the paraffin emulsion stored in the preparation tank(s) (33) from the preparation tank(s) (33) via a second circulation pump (39) in order to enter it into the second cycle,- Sending it to the piston pump(s) (3) via the second circulation pump (39) to be re-pressurized,- Repressurization of paraffin emulsion,- Sending it to the filter (5) unit(s) for filtration (5) again second time,- Again transferring it to the turbulent flow generator (14) under high pressure for micronization and mixing,- Again passing it through the turbulent flow generator (14) under high pressure,- Reducing the pressure at the outlet of the turbulent flow generator (14),- Sending it to the heat exchanger (31 ) unit to reduce the temperature in order to be stored at room temperature,- Lowering the temperature in the heat exchanger (31 ),- After being passed through the flow meter (13) for storage, being discharged out of the system.

2. A fluid mechanics-based mixing system developed to ensure homogeneous distribution of paraffin at the nano-sized particle level in paraffin emulsions used in wood-based fiberboard production according to claim 1 , characterized in that; the process of processing paraffin emulsion comprises two stages of product processing, namely the 1stcycle and the 2ndcycle stage.

3. A fluid mechanics-based mixing system developed to ensure homogeneous distribution of paraffin at the nano-sized particle level in paraffin emulsions used in wood-based fiberboard production according to claim 1 , characterized in that; the first cycle process comprises of the following process steps; Loading the paraffin emulsion prepared outside the system into the system with the circulation pump (1 ),- Sending it to the filter unit(s) (5) for filtration (5),- Conveying it to the piston pumps (3) for pressurization,- Pressurizing it in the piston pump(s) (3),- Transferring it to the turbulent flow generator (14) under high pressure for micronization and mixing,- Passing it through the turbulent flow generator (14) under high pressure,- Sending and storing it in the preparation tank(s) (33) at the exit of the turbulent flow generator (14) under low pressure for the second process cycle.

4. A fluid mechanics-based mixing system developed to ensure homogeneous distribution of paraffin at the nano-sized particle level in paraffin emulsions used in wood-based fiberboard production according to claim 1 , characterized in that; the second cycle process comprises of the following process steps; Taking the paraffin emulsion stored in thepreparation tank(s) (33) from the preparation tank(s) (33) via the second circulation pump (38) in order to enter it into the second cycle,- Sending it to the piston pump(s) (3) via the second circulation pump (38) to be re-pressurized,- Repressurization of paraffin emulsion,- Sending it to the filter unit(s) (5) for filtration (5),- Transferring it to the turbulent flow generator (14) under high pressure for micronization and mixing,- Passing it through the turbulent flow generator (14) under high pressure,- Reducing the pressure at the outlet of the turbulent flow generator (14),- Sending it to the heat exchanger (31 ) unit to reduce the temperature in order to be stored at room temperature,- Lowering the temperature in the heat exchanger (31 ),- After being passed through the flow meter (13) for storage, being discharged out of the system.

5. A fluid mechanics-based mixing system developed to ensure homogeneous distribution of paraffin at the nano-sized particle level in paraffin emulsions used in wood-based fiberboard production according to claim 1 , characterized in that; the filter (5), piston pump (3), turbulent flow generator (14), and heat exchanger(s) (31 ) are used in such a way that each of them contains a spare part and are connected in parallel with each other in order for the system to continue its operation by bypassing the part that fails during the product processing process.

Citation Information

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