TWI439595B - Impulsive Detonation Wave Fast Dyeing Machine - Google Patents

Description

Impulse detonation wave fast dyeing machine

The invention relates to an impulse detonation wave fast dyeing machine, which is simply a detonation wave dyeing machine, which is improved by a spray type openable pneumatic vibration accelerating dyeing machine, and belongs to a high efficiency, multifunctional, multi-purpose and environment-friendly type. Dyeing and processing machine.

In the energy-saving and carbon-reduction call, in order to reduce the impact of global warming and change, many special processing technologies are applied to the processing of fiber fabrics, including detonation wave, electrochemical, low-temperature plasma technology, carbon dioxide supercritical fluid technology, and biology. Enzyme processing technology, ultrasonic, radiant energy, microwave, etc. clean dyeing and finishing technology for its convenience, rapid, effective, safe and wide applicability, saving dyes, reducing environmental pollution, saving energy and facilitating automation of electronic computer control And so on, it is currently actively developing in all parts of the world. However, most of the technical development directions are mainly for the development of single-purpose and special-purpose models. The high-efficiency and environmentally-friendly models for multi-functional and multi-purpose use have not been heard so far. Therefore, it has further motivated the "Injection-type pneumatic open-end vibration accelerating dyeing machine" of the previous invention [Note: The case has obtained invention patents of more than 20 countries, including the Republic of China (application date: 1997/2/25, application number: 86102237), Mainland China (application date: 1997/04/29, application number: ZL97 1 82145.3), United States (application date: 1997/03/31, application number: 828,884) Canada (application date: 1997/04/29, Application No.: 2,288,214), EU (application date: 1997/4/29, application number: 97917988.4), India (application date: 1997/5/28, application number: 1126/MAS/97), Japan (application date: 1997) /4/29, application number: 10546452), Korea (application date: 1999/10/28, application number: 997009996), etc., once again, there is a clearer, more specific and firmer direction for improvement and innovation. The source of power is to look forward to participating in a new and better thinking and concept Energy conservation and carbon reduction to help the dyeing and finishing industry to achieve clean production goals in an urgent moment.

As we all know, textile dyeing and finishing production has been carried out with water as a medium for various wet processing. It has always been one of the major polluters in industrial production. Under the pressure of global warming warnings, it has also forced the international textile market to rise. The green whirlwind means that environmentally friendly textiles will become the main appeal of future products. On the contrary, it is undoubtedly a severe challenge for the dyeing and finishing industry that is not easy to reach the level of environmental protection technology. In order to ensure sustainable development of the dyeing and finishing industry, in the long run, the adoption of clean production techniques or facilities has been considered the only way.

In fact, the problem of climate warming and change has reached an urgent point. For the dyeing and finishing industry, it is necessary to speed up the pace of clarifying new ideas and viewpoints, re-changing new facilities or establishing new processes and new methods.

Therefore, in order to achieve better energy-saving, water-saving, and clean production facilities, the present invention particularly concentrates the fiber fabric with the dye or the treatment agent in a high-energy wave field to promote all the participating reactants in a very short time. In the limited resources, the high-energy wave field acts to bring about faster and more efficient processing, and also the low-temperature plasma processing technology is also involved in the invention to promote the fiber fabric. In some processing operations, in addition to achieving the goal of waterless processing, a better and wider process creation space can be obtained and the best product processing effect can be obtained.

At present, most of the dyeing and finishing facilities are still unidirectional (Note: it refers to the simultaneous processing of other processes at the same time), which is not only consumes a lot of water, but also wastes a lot of energy, and Serious pollution of the environment, its processing costs are too high, but also cause unnecessary economic losses, but also bring great harm to the ecology.

At present, the textile market tends to appeal to small, diverse, multi-functional, and delicate clean production. Direction, therefore, batch (intermittent) environmentally friendly dyeing facilities will become the mainstream of production, for general-purpose facilities, whether it is a wide-width, beam-type airflow dyeing machine or a more traditional jet flow dyeing machine There are still some problems in the dyeing or other processing of fabrics, such as reproducibility, left and right color, front and back color and other line marks, etc., unevenness, power belt wheel and actuating nozzle The speed between the speed is not synchronized, the speed of the cloth is not fast enough, the scratch or collision and the hooking, the jetting force of the nozzle is too large, the yarn of the fabric is broken, the nozzle and the filter are easily blocked during the process, or The body does not reach a rich sense, the efficiency of biological enzyme treatment is not good, the treatment time is too slow, the function of the facility is insufficient to limit the processing process, the problem of excessive energy use and the excessive waste of water resources, resulting in a large amount of sewage treatment costs. , because of the setting of the power belt cloth wheel, it may cause work safety problems or problems of poor hand feeling, but the above mentioned various In addition to man-made negligence, most of them are caused by poor design and manufacturing of the facilities. The main reason is that the fiber fabric and the dye liquor or the treatment fluid and the air stream work and the heat distribution is uneven. For example, the tube difference color is generated in the multi-tube processing tank facility, because the conventional dyeing machine is composed of a multi-groove type, and therefore, the dyeing liquid or air flow distribution method also adopts a split. Second, subdivided into four, and then divided into eight ways to complete the branch-type distribution operation, the biggest disadvantage is that the segmentation causes too many T-joints. According to the fluid dynamics discussion, the fluid is difficult to accurately divide into two equal halves. In the introduction of the pipeline there will be any sideways situation, the error will be more and more divided, and the original set flow changes, as well as the uneven dyeing caused by uneven distribution, still can not be resolved. Therefore, in order to achieve the goal of ideal cleaning and dyeing, it is necessary to solve these problems at the same time, because the process of rebuilding and re-dying caused by the problem will bring more energy and water resources, and also Increase the load of production costs.

Tracing the development of dyeing theory So far, most dyeing theories have been considered that the dye-to-fiber dyeing process can be divided into the following four stages:

1. The dye gradually moves closer to the fiber interface with the dye solution in the dye solution. The nature and state of the dye at this stage are basically independent of the dyeing performance. The dye molecules in the dissolved state or the dye particles in the suspended state flow with the dye solution, and the migration speed is determined by the flow rate of the dye solution.

2. Due to the existence of a difficult dynamic boundary layer (stagnation layer) at the interface between the liquid and the fiber, the dye enters the kinetic boundary layer and approaches the fiber surface to a certain distance, and mainly approaches the fiber by its own diffusion. The migration speed of the dye at this stage is not only related to the flow rate of the dye solution, but also related to the diffusion speed of the dye. The dye molecules in the dissolved state diffuse much faster than the dyes in the suspended state and the aggregated state. Therefore, the solubility and dispersion state of the dye are at this stage. The migration speed of the dye has a large influence.

3. After the dye has diffused to a certain distance from the surface of the fiber, there is a large enough molecular force between the dye and the fiber, and the dye is quickly adsorbed to the surface of the fiber. The migration speed of the dye at this stage depends mainly on the structure and properties of the dye molecules and the fiber molecules, that is, the interaction between the dye and the fiber, and also on the properties of the interface solution, wherein the solubility and dispersion state of the dye have a great influence. Therefore, the greater the force between the dye and the fiber at this stage, the better the dye is dissolved and the faster the adsorption speed.

4. After the dye is adsorbed to the surface of the fiber, a dye concentration difference or an internal and external dye chemical difference is generated inside and outside the fiber. According to Fick's law, the dye will diffuse from the fiber surface to the inside of the fiber. The rate of migration at this time depends mainly on the chemical and physical microstructure of the fiber and also on the molecular structure and concentration of the dye. The proportion of the amorphous region of the fiber is large, the pores are large or the free volume is large, the dye concentration on the fiber surface is high, and the dye migrates into the fiber. soon. Therefore, the rate of migration of the dye at this stage is directly related to the degree to which the fiber is swollen or plasticized and the concentration of the dye on the surface of the fiber.

It can be seen from the above that the dyeing speed is determined not only by the molecular structure of the dye and the fiber, but also by the solubility of the dye in the solution and the degree of swelling or plasticization of the fiber. In fact, the interaction between the dye and the fiber does not require a large amount of working fluid to obtain dissolution or rapid dyeing. If the dye is dissolved in an excess of working fluid during dyeing, it will be subjected to excessive working fluid resistance. Breaking dye or treatment agent and fiber in a short distance contact opportunity, making the effective contact probability less, also lost the purpose of rapid dyeing or treatment, it will also convert most of the input energy into the rotational kinetic energy of the working fluid molecule, And the energy from the vibration of each atom in the working fluid molecule, in addition, there are various interaction forces between the working fluid molecules that are not related to the dyeing or processing.

In order to make the dye have a certain solubility in dyeing, when synthesizing the dye, a certain amount of polar groups are always introduced into the dye molecule to increase the solubility of the dye. However, the introduction of water-soluble ionic groups, in addition to a few cases can improve the combination of dyes and fibers, but after the completion of the dyeing process, it will bring many problems, such as reducing the wet fastness of textile dyeing by hydration dissolution on the fibers. The water-soluble dye remaining in the dyeing solution is difficult to decolorize and purify, and it is difficult to treat sewage.

For the poorly soluble disperse dye, it does not have an ionic group in the molecule, and at a normal pressure of 100 ° C, since the solubility is low, the degree of swelling or plasticization of the fiber is low, the dyeing speed is very slow, and it is difficult to perform dyeing. The dye in the working fluid must rely on a large amount of dispersing agent to be dispersed in the working fluid in a suspended form. This requires not only a large amount of dispersing agent, but also the stability of the suspension is not easy to maintain, and it will stain and stain. Water treatment brings problems. Therefore, appropriately increasing the solubility of the disperse dye not only reduces the dispersant or dispersant, but also maintains the dye dispersion stability, and is also advantageous for dyeing.

For hydrophobic synthetic fibers, it is difficult to swell in water, so it is difficult to diffuse the dye in the fiber. Generally, dyeing requires a high temperature. For example, polyester fiber must be dyed at a temperature of 130 ° C at high temperature and high pressure. Increasing the degree of swelling or plasticization of these fibers can accelerate the diffusion rate of the dye in the fiber or lower the dyeing temperature.

In addition, as for the natural cellulose fiber, since the microscopic structure is complicated, it is easy to form a large number of cavities and is filled with air. Therefore, when the solution penetrates, the relative movement is less likely to occur, that is, the retention phenomenon occurs, and the dye is not easily infiltrated, so it usually takes a long time. In order to obtain the dyeing, the wool fiber has a scale layer on the surface, which has a shielding effect on the dye dyeing. The conventional dyeing usually needs to be carried out in a boiling manner, and the dyeing time is also long. Therefore, the dyeing energy is large, Fiber damage is large. In addition, since the reactive dye usually reacts with water in a high temperature and an alkaline solution, the dyeing efficiency of the reactive dye is lowered, and after the dyeing is finished, the dye in the dyeing residue is not exhausted, or the dyed fabric is post-treated. The floating color in the wash will cause serious water pollution.

In short, one of the first conditions for dye-dyed fibers is that the dye must be dissolved in the working fluid. Only the dye that is broken down into a single molecule can be quickly adsorbed to the fiber and diffused into the fiber. The dye crystal particles and the bulky dye aggregate. The body cannot diffuse into the interior of the fiber. If the "physical mechanical mechanism generated by high-energy wave or high-energy particles" is used in the present invention, the solubility of the poorly soluble dye can be increased in a very small amount and a high concentration of the working solution, and the solution can be accelerated. The adsorption speed of the fiber to the dye, and solubilization or plasticization of the fiber, accelerates the diffusion speed of the dye in the fiber, thereby speeding up the entire dyeing speed. As long as the selected dye has a higher binding force to the fiber molecules, it not only has good dyeing power, but also has high color fastness.

Therefore, in order to increase the dyeing rate and shorten the dyeing time, in addition to reducing the water consumption, select the appropriate dyeing equipment, strengthen the relative movement between the dye liquor and the fabric, and select the dye suitable for the fiber. In addition to dyeing auxiliaries and dyeing media, the chemical structure and physical microstructure of the fiber fabric itself are also key factors that must be considered. If the fiber fabric is pre-treated by a good pre-treatment or modification pretreatment or simultaneously modified while dyeing, speeding up the adsorption speed of the dye onto the fiber surface and the diffusion rate into the fiber, the dyeing speed can be greatly increased, the dyeing time can be shortened, or the dyeing can be reduced. Temperature, improve production efficiency, and achieve the goal of clean production of energy saving and carbon reduction.

The so-called detonation wave dyeing machine of the present invention refers to the expansion acceleration effect of a common configuration nozzle during dyeing or other processing, and promotes the dyeing liquid, the treatment liquid or the low temperature plasma, or other processing medium. , etc., can be dispersed in a high-speed air stream, and the form of homogenization with the fiber fabric is concentrated in the field of a high-energy wave field, so that all the participating reactants can obtain the required activation energy. Energy), in order to achieve the most economical clean production in the shortest possible time.

In the processing, when the high-speed flowing air, vapor, dye, treatment agent, low-temperature plasma and the fiber fabric sprayed by the co-structure nozzle collide with each other, the fiber fabric that is being turned down may be utilized. The curved end face is configured to obtain a large impact force and impulse force for high-efficiency energy conversion; when in the process, the dye liquor and the treatment liquid are fine-grained or particulate in a high momentum manner or Dispersed in a high-molecular air stream in a single molecule, impacting the fiber fabric that is being steered in a direct close-up manner, so that the surface of the moving fabric is continuously repeated to obtain a strong elastic collision (Note: refers to air or General gas) and inelastic collisions (Note: refers to working fluids or dyes or treatment agents, including plasma), in which in addition to promoting non-elastic collisions, the fabric can achieve high efficiency kinetic energy transfer, accelerate fabric movement, It can simultaneously provide enough liquid film on the surface of the fiber fabric to generate cavitation. The elastic collision can promote a high-speed air flow between the lower end surface of the fiber fabric and the reflective substrate, and can also cause a pressure difference between the air static pressure between the upper and lower end faces of the fabric to make the upper end surface of the fabric static. The pressure is greater than the static pressure of the lower end surface, thereby causing the moving fiber fabric to utilize the pressure difference effect to continuously generate periodic strong wave motion when passing through the reflection actuating plate, and simultaneously perform the effect of free spreading. .

When the wet processing is carried out, if the amount of liquid film adsorbed on the surface of the fiber fabric is sufficiently thick, the velocity energy of the high-speed air stream is sufficiently large to cause a large number of holes to be generated in the boundary region of the fiber fabric in the wave, causing A shock wave effect is produced. In the dry operation, the high-speed air flow can also use a corona discharge or a glow discharge to ionize the air molecules of a part of the high-speed air stream to generate a high-speed flowing low-temperature plasma. (low temperature plasma), in addition to the treatment effect of the fabric to obtain high-energy particles, it can also obtain more ecological benefits brought by the waterless processing.

During the processing, the fiber fabric dropped in the collecting groove can utilize the moment of inertia of the momentum and the instantaneous occlusion caused by the rapid detachment of the air flow, causing the air impact effect, thereby generating a strong force. The oscillating phenomenon causes the fabric to be forced to use the oscillating mechanism to remove the residual working fluid attached to the surface of the fabric and the exfoliated free fibers and other impure solid objects during the process of dropping the fabric. De-liquidization and separation, and at the same time, the folding operation is performed, so that the working fluid and free fibers and other impure solid objects leaving the surface of the fabric can be directly introduced into the sump through the lower side outlet of the collecting tank, and filtered through a precision sieve filter. And collecting, which can promote the fiber fabric in the collecting trough to obtain a relatively clean state, thereby causing the fiber fabric to be prevented from being blocked by the residual working liquid film barrier when it is in contact with the dyeing liquid or the treatment liquid in the next cycle. Through the filtered working fluid, in the process of circulating transportation, the pumpless feeding device can be used. The replenishment of the dye or the treatment agent enables the high-concentration dissolving dye or the treatment agent in the pumpless charging device to be put in the system of the circulating conveying pipe by the suction port of the liquid pressure circulation pump to make the high concentration Dissolving dyes or treating agents can achieve a very small bath ratio and a high uniformity mixing operation in a limited amount of circulating working fluid. Therefore, when the fiber fabric is brought into contact with the dye liquor or the treatment liquid again, high energy and kinetic energy can be obtained, and the concentration gradient, temperature gradient and chemical affinity gradient are also increased, and the dye liquor or the treatment liquid is quickly infiltrated. And the diffusion effect, so it is conducive to the rapid processing; in addition to promoting the force of the stacking fabric in the collecting groove to minimize the mutual pressing force, it can also promote the rapid movement of the fiber fabric in the guide tube At the time, the tension generated is minimized. In operation, the pressurized dyeing liquid or the treatment liquid is pumped through the pressurized circulation, and the action of the alternating current flow distributor on the conveying pipeline system can be utilized to enable each hydraulic atomizing nozzle to be sprayed and pressure-equalized. Atomized droplets of average, average temperature and average velocity.

The air flow pressurized by the air blower can utilize the AC air flow distributing device on the conveying pipeline system to perform a 90-degree steering to form a rectangular cloth flow, and then into the respective distribution pipes, and the air flow can be borrowed from the distribution pipe. The function of the diffusion structure converts the kinetic energy of the moving airflow into static pressure energy, which can induce a large expansion acceleration efficiency and a uniformity when the air flow passes through each of the air-floating nozzles and each of the co-structured nozzles. The distribution effect of pressure, average, average temperature and average speed, in addition to preventing various colors and unevenness of the fabric from being caused by various colors and colors, it can also promote all other processing operations and obtain various types of A uniform feel and appearance. During operation, the return air in the treatment tank can also be distributed and recirculated by the alternating flow type recirculating device to promote the airflow inside the treatment tank without excessive disturbance, thereby obtaining a more stable and regular circulation. flow.

The invention particularly relates to a horizontal tube wall end spanning the left and right side walls of the passage under the guide tube On the surface, along the direction of the passage, on the upstream and midstream sections, a set of air-floating nozzles and a section on the downstream section are provided, and a row is arranged across the left and right side walls to be combined in parallel. a configuration nozzle, and a U-shaped revolving plate disposed at a lower side of the outlet of the duct pipe passage and an inner side space of the inlet of the distribution section upstream of the collecting duct, in the downstream direction of the common nozzle opening The upstream side end of the U-shaped rotating plate is overlapped and fixed on the lower side of the common-purpose nozzle opening in a stepwise manner, so that the upstream outer end surface of the U-shaped rotating plate constitutes a flat reflective substrate, which is located downstream of the U-shaped rotating plate. On the end face, the separation grid is disposed on the inner and outer sides of the distribution section upstream of the collecting groove, so that when performing dyeing or other processing, the circulating air in the tank and the dyeing liquid of the working fluid and the preparation tank or The treatment fluid can be connected to the blower and the pressurized circulation pump via respective piping systems to provide pressurized air and pressurized dye liquor or treatment liquid, which is sprayed through the co-structure nozzle, and also can partially charge air Via air flotation The nozzle is ejected. In operation, the fiber fabric can spray a small amount of air flow through the air-floating nozzle, and the fiber fabric can be floated, so that most of the power energy can be concentrated in the co-structure nozzle, under the action of the U-shaped rotating plate. It can cause the jetted high-speed air flow to change direction to form a reverse discharge, thus promoting the fiber fabric to obtain a strong driving force. Therefore, in operation, the co-construction nozzle can be used as the main power source for fabric circulation movement, which can abandon the operation mode of the traditional power belt cloth wheel, and can also improve the multi-stage guide nozzle of the prior invention, due to the working airflow energy. Excessive dispersion, it is not easy to achieve high-energy processing problems. In operation, the hydraulic atomizing nozzle mechanism and the corona or glow discharge mechanism provided on the co-configuration nozzle can be used to perform the process of alternating with each other to obtain complementary processing modes, so that various fiber fabrics are processed. A wider and wider process creation space is available.

The main object of the present invention is to provide an impulse detonation wave fast dyeing machine, which can utilize a co-structured nozzle according to the processing requirements when performing dyeing or other processing processes. Spray high-speed hot or dry heat air flow, high-speed and evenly dispersed dye molecules, high-speed uniform dispersion of treatment liquid molecules, high-speed flow of low-temperature plasma, or other high-speed and uniformly dispersed fine particles, so that all the ejection media can be formed The way of gathering focuses on a high-energy wave field and colliding with the fiber fabric repeatedly, so that the participating reactants and fiber fabrics can transmit energy in a more orderly manner in a very short time. In addition to enabling all the participating reactants to obtain the required activation energy, it can also promote the fiber fabric in the shortest time, with the most energy-saving, water-saving, minimum dye, and minimum treatment agent. Achieve clean production.

The main object of the present invention is to provide an impulse detonation wave fast dyeing machine which can promote dyeing liquid or the like by the high frequency strong fluctuation or the fluctuating wave effect caused by the fluctuation when performing dyeing or other processing. The treatment liquid forms a low-viscosity, low-resistance, high-potential, high-permeability, high-diffusion environmental condition, and the fiber fabric is subjected to a small liquid volume, a high concentration, and a high-efficiency wet processing. The detonation wave effect referred to in the present invention means that the fiber fabric can be subjected to high-speed air flow to generate high-energy-level fluctuations during processing, and a peak region forms a compression zone during the fluctuation process, and a valley region is formed in the valley region. Sparse area. Further, any particle on the surface area of the fiber fabric is caused to continuously fluctuate in the compression zone and the sparse zone, and in the fluctuating compression zone, the average distance of the air molecules around the surface of the fiber fabric in the zone is shortened, and the density is changed. Large, and in the sparse zone, the average distance of the air molecules will increase, and the density will become smaller. If the particle point of the fiber fabric fluctuates fast enough, the generated wave power is strong enough, which will cause the work attached to the surface of the fiber fabric. The liquid molecules are also subjected to the alternating action between the compressed zone and the sparse zone. When the negative pressure of the sparse zone is reduced below the critical value of the saturated vapor pressure, the average distance between the working fluid molecules increases beyond the limit distance, thereby destroying the working fluid. Gravitational knot between molecules or fabrics The integrity of the structure, therefore, causes the surface of the fiber fabric and the inner and outer pores of the fiber or the inner and outer gap regions of the fiber to induce holes (referring to a very small vacuolar core), and once the cavity is formed, it will always grow to a negative pressure. The value results in the generation of a large number of cavitation bubbles (note: a very low density vapor bubble or air bubble), and in successive compression zones, most of the cavitation bubbles are crushed and collapsed. And the detonation wave effect is referred to herein. The so-called detonation wave effect refers to the process in which the cavitation bubble is crushed and shattered. It is a combination of the wave energy of the concentrated fiber fabric and the compression wave energy generated by the peripheral pressure environment. Force to perform unobstructed jet motion in a cavitation environment. Therefore, when the cavitation bubble collapses, the force will be from the outside to the inside, and a detonation wave will be instantaneously generated to rush toward the center of the cavitation bubble. When the surface of the fiber fabric or the inside and outside of the fiber is subjected to a shock wave or impact, the surface of the fiber fabric may be The density pressure of all media in the inner and outer boundary regions of the tissue changes sharply, and the extremely high temperature and extreme pressure are generated in a very small space on the fiber surface or in the amorphous region of the fiber in a very short time. Therefore, when dyeing or other processing is performed, the dyeing liquid or the treatment liquid can generate a strong impact force on the surface of the fiber or in the amorphous region of the fiber by the detonation wave generated by the bursting of the cavitation bubble, thereby promoting the dyeing liquid. Or the treatment liquid can obtain the energy to re-enhance the solubility and accelerate the penetration and rapid diffusion in the fiber, and also cause the accelerated swelling and plasticization of the fiber molecular structure to promote the conversion of the non-activated molecules on the surface of the fiber fabric to the activated molecule. And cause the fibrous molecular structure to produce swelling or plasticizing effects to achieve rapid dyeing or other processing Reasonable purpose.

The main object of the present invention is to provide an impact type detonation wave fast dyeing machine which can modify the fiber fabric or modify one side by using the detonation wave effect caused by a high-energy wave place during dyeing or other processing. Dye on one side.

According to the fiber microstructure, both natural cellulose fibers or synthetic fibers are composed of carbon atoms. a chain of molecules formed by interconnecting a hydrogen atom, an oxygen atom, a nitrogen atom, and a chlorine atom, and these are all macromolecular compounds, and both include a crystalline region and an amorphous region, and in the crystalline region of the fiber, the molecule It will be regularly arranged, the interaction between molecules is strong, and its molecular structure is tight, making it difficult for dye molecules to enter; while the amorphous regions of fibers, the molecules are disorderly arranged, the interaction between molecules is weak, and the molecular structure is relatively loose. There is a certain gap. Therefore, in dyeing or other processing, the dye or treating agent molecules can only enter the amorphous region of the fiber, and if it is dry or at room temperature, the dye molecules are difficult to enter.

In addition, according to the dyeing theory, whether the dye is diffused by the channel or by the free-volume diffusion model, it is nothing more than increasing the voids in the amorphous region, that is, increasing the specific surface area inside and outside the fiber. The dyeing process proceeds smoothly, so any factors that contribute to the increase of voids in the amorphous region of the fiber and the increase in the specific surface area of the fiber inside and outside are beneficial to the smooth progress of dyeing or other processing. According to the mechanics of materials, the damage and destruction of any material originates from the excessive concentration of stress in the material and the origin of the original defects and cracks, and the voids in the amorphous region of the fiber polymer provide this possibility. Therefore, whenever the fiber fabric is subjected to strong rapid fluctuation and cavitation bubble formation or destruction, it will inevitably cause misalignment between the crystallites or cause partial breakage or recombination of the fiber molecules, so that the specific surface area inside the fiber is increased. The gap in the shaped area increases. Therefore, the purpose of fiber modification can be obtained, and the purpose of dyeing while modifying can be obtained at the same time.

The main object of the present invention is to provide an impact type detonation wave fast dyeing machine, which can use the function of high-speed flowing low-temperature plasma to perform anhydrous desizing or removing impurities or fabric modification when performing pre-dyeing treatment. Quality and modification. The high-speed flowing low-temperature plasma according to the present invention means that the gas pressure can be a large amount of high-speed flowing air or other gas as a medium under atmospheric pressure, and can pass through a co-structured nozzle when passing through a co-structured nozzle. of Between the electrode tip provided on the injection pipe passage and the annular electric target, it is generated by a corona discharge or a secondary glow discharge. During discharge, due to the application of a high voltage at the tip of the electrode, the electric field of the electrode tip and the annular electric target are unbalanced. Where the curvature of the electrode tip surface is large, the voltage equipotential surface is dense due to the concentration of the power line. Under the action of high electric field and high voltage, the free electrons in the electric field obtain energy into high-level electrons, forcing high-energy electrons to be released from the tip of the electrode and accelerate toward the annular electric target, so that high-energy electrons lead to the ring-shaped electric target. On the way, it collides with part of the high-speed air flow. During the collision, the energy of the high-energy electrons is large, and the electrons around the air molecules or atoms are dissociated to generate a variety of high-energy active particles. In the case of non-aqueous processing, it can eject electrons, ions, radicals, excited atoms or molecules, unreacted molecules, etc. by means of a co-structured nozzle, and these high-energy active particles can be mutually reacted with each other. In addition to radiant energy, most of them will have a strong impact on the surface of the fabric to dissipate the energy. In the process of dissipating, their effect on the surface of the fiber fabric not only produces relatively free radicals, but also oxidizes the surface of the fiber fabric, thereby promoting the addition of a large number of polar groups on the surface of the non-polar fiber fabric, and also utilizing high speed. The flowing low-temperature plasma removes impurities such as natural impurities contained on the surface of the fiber fabric and the slurry and oil stain applied in the textile processing, so that the fiber fabric has good moisture absorption and penetration effects to meet subsequent processing steps. Because the conventional pre-treatment process is long, the amount of chemicals is large, and the water consumption is high, the energy consumption is high, the wastewater discharge amount is large, and the production efficiency is low. High-speed flow low-temperature plasma treatment, with good de-cleaning effect, can replace some pre-treatment chemical wet processing steps, or high-speed flow low-temperature plasma surface treatment, can use a mild pre-treatment process Shorten processing time, reduce the amount of chemical additives, reduce the processing temperature, thereby reducing the consumption and pollution of water resources, improving production efficiency, and also achieving festivals. Can reduce the purpose of carbon. Therefore, in the pre-processing, if high-speed flow low-temperature plasma technology can be utilized, it has significant environmental and economic benefits.

The main object of the present invention is to provide an impulse detonation wave fast dyeing machine which can perform various fiber fabric dyeing by a multi-functional technical field mechanism, and can also modify and desizing various fiber fabrics. Treatment, refining treatment, bleaching treatment, biological enzyme treatment, fiber opening treatment, relaxation treatment, fading treatment, untwisting treatment, fluffing treatment, soft treatment, fibrillation treatment, stretching treatment, fading treatment, color treatment, etc. It is convenient, fast, effective, safe and saves dyes, saves chemicals, saves energy, saves water resources, reduces environmental pollution by means of clean production and facilitates automatic control.

The main object of the present invention is to provide an impulse detonation wave fast dyeing machine in which the circulating moving power of the fabric is driven by only one row of co-construction nozzles, which can abandon the traditional machinery during dyeing or other processing. The power belt is driven by the cloth wheel. At the same time, the fabric can also automatically complete the folding operation by the high-speed air flow sprayed by the co-structure nozzle. Therefore, the traditional mechanical power arrangement can also be abandoned. Therefore, the fabric is In the rapid cycle movement, it is no longer damaged by the frictional impact of the power belt pulley and the power swing device, and is no longer affected by the discontinuity of the moving speed generated by the fabric and the power belt cloth wheel. Easy handling and the purpose of moving at a constant speed.

The main object of the present invention is to provide an impulse detonation wave fast dyeing machine, in which dyeing or other processing is performed, wherein before the fiber fabric enters the collecting groove, the folding operation can be completed by the pneumatic swing. The air-shock effect caused by the moment of the fiber fabric produces a strong oscillating phenomenon, and the residual working fluid attached to the surface of the fiber fabric, and the free fiber and the unreacted floating dye or other solid objects are forcibly driven away. Make access to the collection slot The stacked fabrics can fully obtain the liquid-removing and pollution-reducing and reduce the gravity of each other, and the residual working liquid adhered to the fiber fabric is minimized to obtain the minimum liquid amount operation, and therefore, in addition to facilitating rapid processing. In addition, it is also possible to create a minimum amount of operating fluid and a high concentration of treatment.

The main object of the present invention is to provide an impact type detonation wave fast dyeing machine, in which dyeing or other processing can be carried out, wherein the fiber fabric can be desizing and refining in a dry environment by using a high-speed flowing low-temperature plasma. The surface modification, polymerization and grafting, in addition to providing waterless processing, can also provide fiber fabrics with a wider creative process space during processing.

The main object of the present invention is to provide an impact type detonation wave fast dyeing machine, in which dyes and treatment agents can be pumped into a container of a pumpless feeding device in advance for processing, and corresponding to the variable processing in the processing tank. The pressure environment, dyes and treatment agents can be used to obtain high-precision replenishment by the action of potential energy. In addition to the environmental changes that increase or increase the pressure in the treatment tank, which affects the flow rate required for replenishment, it can also save high For the purpose of pumping electrical energy with a small amount of liquid.

The main object of the present invention is to provide an impact type detonation wave fast dyeing machine, in which a power belt cloth wheel is not required to be provided at the front end of the guide tube, and a mechanical swinging device is not required at the outlet end of the cloth tube. Therefore, in operation, in addition to providing a safer working environment, the operator can no longer be subjected to the mental pressure or damage caused by the power belt pulley, and the fabric can be provided without the power belt pulley. The resulting slidability friction and the wandering phenomenon caused by the out-of-synchronization, the fabric does not have to be subjected to the mechanical arranging device when passing through the guide tube, so that the moving speed is no longer subject to the control.

Referring to Figures 1 to 7, the impulse detonation wave fast dyeing machine of the present invention comprises a processing tank 1. Cloth groove 2, fiber fabric 3, high-voltage power supply device 5, guide tube 11, working door hole 12, reflective substrate 13, U-shaped rotating plate 14, guide plate 15, blower 16, droplet collecting plate 18, preparation barrel 19. Pumpless charging device 20, inner separating grid 21, outer separating grid 22, sliding strip 23, mesh plate 24, upstream falling section 31, split port 42, passage port 43, return port 46, arc type The shunt pipe 61, the chute pipe 62, the gas flow pipe system 71, the liquid pressure circulation pump 72, the feed pump 73, the upstream inlet 111, the downstream outlet 112, the effluent mechanism 113, and the co-structured nozzle 121, air-floating nozzle 122, wedge-shaped gap passage 151, airflow return pipe 160, air heater 161, airflow filter 162, alternating current airflow device 163, right-inclined manifold 164, left-inclined manifold 165, confluence Port 166, co-construction distribution pipe 167, air flotation distribution pipe 168, air flow regulating valve 169, dye liquid return pipe 170, distribution port 172, AC flow distributor 173, right intake manifold 174, left feed manifold 175, pressure equalizing distribution pipe 176, diverting hole 178, jet port 179, collecting diversion groove 181, diversion tube 1 82, working fluid collecting plate 184, alternating current flow recirculating device 190, single oblique collecting pipe 191, T-shaped confluent return pipe 192, exhaust gas discharge port and control valve 200, fresh air introduction port and control valve 201, flow regulating valve 203, pressurized circulating liquid flow conveying pipe 210, steam input port and control valve 211, other gas inlet and control valve 212, working fluid collecting tank 213, working fluid recovery and discharge valve 214, working fluid sieve filter 215, work The liquid heat exchanger 220, the circulation passage 221, the annular electric target 12111, the injection tube 12121, the replacement electric shock rod 12122, the high-voltage power connection terminal 12123, the ground connection terminal 12124, the hydraulic atomization nozzle 1216, and the hydraulic atomization nozzle port 12161 Slide valve stem 12164, valve seat 12165, spring piston 12167, and actuating fluid inlet 12169.

Please refer to FIG. 1 to FIG. 3 at the same time. For the structure of the processing tank 1, the multi-tank processing tank 1 can be arranged in a single trough or in parallel, and is generally round in shape when used at high temperature and high pressure, and is used frequently. The temperature and pressure may not be limited by the pressure-resistant structure, and the shape may be matched with the processing amount and the special processing demand or the volume of the processing tank 1 may be arbitrarily increased or increased according to the environmental site. For example, as shown in Figure 2, for the heightened type, it can obtain a larger amount of processing. For example, as shown in FIG. 3, it is an extended type of machine which can correspond to the fiber fabric 3 which is particularly prone to creases, and which is suitable for the waterless processing environment in terms of appearance and structure, and can make the fiber fabric 3 move smoothly, and the material cost. Under various considerations, it is more suitable for round shape during implementation to achieve the best use and minimum floor space. As shown in Figure 1, it is suitable for high and low temperature or high and low pressure, and its shape is designed with the O word in the English alphabet. Therefore, the cloth collecting groove 2 and the guide tube 11 in the processing tank 1 can be along The inner space of the groove wall is formed to form a loop path of a ring shape. The guide tube 11 is disposed directly above the collecting trough 2 and is disposed in the same axial direction. For convenience of explanation, the direction of movement of the fiber fabric 3 is clockwise, the front end of the processing tank 1 at the nine o'clock direction, and the rear end of the processing tank 1 at the three o'clock direction, and the lowest portion of the bottom of the processing tank 1 is A dyeing liquid return pipe 170 is disposed at a direction of six o'clock, and a gas flow return pipe 160 is disposed at a space in the center of the processing tank 1, and a working door hole 12 is formed in the front wall of the processing tank 1.

In addition, the upstream inlet portion 111 of the guide tube 11 is disposed adjacent to the working door hole 12 in the inner space of the front end of the processing tank 1, and communicates with the downstream outlet of the collecting groove 2, and is located near the working door hole 12, and the The downstream outlet 112 of the guide tube 11 is located at the rear end of the processing tank 1, and is located in communication with the upstream of the collecting tank 2, so that the front and rear ends of the duct 11 and the collecting trough 2 are respectively connected to each other to form a wide cycle. path. It provides for the dyeing or other processing of the fabric 3 in a freely expanded or open manner over the passage. A plurality of air-floating nozzles 122 are disposed on the horizontal pipe wall end faces on the left and right sides of the passage under the guide pipe 11 in the direction of the passage, and a plurality of air-floating nozzles 122 are disposed in the upstream and mid-stream sections, on the section of the downstream section There is a row of co-structured nozzles 121 which are arranged in parallel and arranged in parallel between the left and right side walls of the passage. Please refer to FIG. 4A and FIG. Construction. At the upstream of the inlet 1213 on the expansion accelerating injection tube passage of the co-configuration nozzle 121, and is provided with a hydraulic atomizing nozzle 1216, the hydraulic atomizing nozzle 1216 is composed of a valve seat 12165 and a sliding valve stem 12164. In order to achieve a precise flow rate, the preset optimum opening is maintained under normal conditions, and the injection flow rate is determined by the gap sectional area of the valve seat 12165 and the sliding valve stem 12164 and the magnitude of the liquid pressure. The sliding valve stem 12164 is provided with a spring piston 12167 mechanism. When the hydraulic atomizing nozzle port is blocked, it can be introduced into the air chamber of the spring piston 12167 mechanism through the working fluid inlet 12169 by using the air pressure or hydraulic fluid to make the spring piston 12167 mechanism. The cylinder pressure is greater than the spring force, and the sliding valve stem 12164 can be immediately slid rearward to increase the gap cross-sectional area, thereby eliminating free fibers or other solids retained in the hydraulic atomizing nozzle opening 12161. In order to increase the spray flow during operation, the desired spray flow rate can be obtained by balancing the pressure applied by the cylinder with the spring force.

Referring to FIG. 1 and FIG. 4A, in operation, the hydraulic atomizing nozzle 1216 can be interconnected with the liquid pressure circulating pump 72 via the AC flow distributor 173 and the pressurized circulation delivery pipe 210, by the liquid flow. The pressurized circulation pump 72 applies pressure to the dyeing liquid or the treatment liquid, and the dyeing liquid or the treatment liquid is introduced into the hydraulic atomizing nozzle opening 12161 capable of generating a strong shearing force to be sprayed and atomized, and the dyeing liquid or the processing liquid is usually pressurized. A good atomization effect can be obtained up to 5 kg/cm ² or more. The higher the pressure, the higher the temperature, and the atomization effect is greatly improved. In order to maintain the impact energy of the atomized dye liquor or the treatment liquid, the impact energy is improved. The spray angle is controlled to be atomized in a small angle range, so that the dyeing liquid or the treatment liquid disintegrated into fine particles can be sufficiently dispersed in the spray pipe 12121 to be mixed with the high-speed air flow which is expanding and accelerating, so that the atomization dyeing is performed. When the liquid or the treatment liquid passes through the co-structured nozzle opening 1211, it can be crushed and dissociated again to form smaller particles, so that when the fiber fabric 3 is impacted, a uniform dye solution can be obtained on the surface of the fiber fabric 3. Or treatment fluid and balanced Strike force. In order to achieve a more perfect cleaning production purpose, a replacement electric shock bar 12122 may be additionally disposed at the center of the passage of the hydraulic atomizing nozzle port 12161. Referring to FIG. 4B, the replacement electric shock bar 12122 is set in the hydraulic atomization. The sliding valve stem 12164 of the nozzle 1216 is integrally formed with the sliding valve stem 12164 of the insulator, and the other end extends to the outside of the hydraulic atomizing nozzle 1216 to form a high-voltage power connection terminal 12123, which can be externally disposed through the cable 1 The high voltage power supply facilities 5 are connected to each other. The wall of the injection pipe 12121 on the passage of the common-type nozzle 121 is replaced with an insulator 12121, so that the common-shaped nozzle opening 1211 constitutes an annular-shaped electric target 12111 which is disposed in the injection pipe of the insulator, which is formed in the common-structure nozzle 121. Integrated, a ring-shaped electrical target 12111 is provided with a ground connection terminal 12124, which can be connected to the ground via a cable.

The lower side of the guide pipe 11 spans the outer space of the horizontal pipe wall on the left and right sides of the passage, and the air float is provided along the passage direction at the entrance of the upstream and midstream sections with respect to the area of the air floating nozzle 122. The pipe 168 is provided with an air flow regulating valve 169 at the upstream inlet of the air flotation distribution pipe. At the entrance of the co-configuration nozzle 121, in the outer space of the air flotation distribution pipe 168, a co-construction distribution pipe 167 is provided, which is located outside the co-construction distribution pipe at the entrance of the co-construction distribution pipe 167. And an AC-type airflow device 163 is disposed in the processing tank 1 near the central portion. The AC-type airflow device 163 is shown in FIG. 1, FIG. 5, FIG. 5A and FIG. It mainly consists of two adjacent symmetric left-inclined manifolds 165 and right-inclined manifolds 164, which are oriented transversely to the processing tank 1, left-to-right oblique manifold 165 from left to right, and right-inward oblique manifold 164 from From right to left, the length is the same width as the width of the guide tube 11, and if it is in the double tube guide tube 11, the width of the double tube guide tube 11 is the same width, and if it is in the four tube guide tube 11, the four tubes are used. The width of the guide tube 11 is the same width, and the length thereof can be arbitrarily widened or reduced according to the number of the guide tubes 11. On the oblique side wall of the inclined manifold, a row of shunt ports 42 arranged in parallel are arranged along the direction of the passage. Each of the split ports 42 is provided with an arc type shunt The tube 61 and the arc-shaped shunt tube 61 can geometrically calculate each of the shunt tubes arranged in the upper and lower rows to form a row of the same direction of the passage port 43. Each of the arc-shaped shunt tubes 61 can be made by the action of the arc-shaped shunt tube 61. The downstream end outlet forms a row of confluence ports 166 arranged in parallel in the same direction, and at the downstream side end of the confluence port 166, a confluence passage pipe 62 is provided, and the upstream side end inlet and the inlet port 166 are in communication with each other, and the downstream side end The outlet is connected to the common distribution pipe 167 and the air flotation pipe 168.

Referring to FIG. 6, an AC-type flow distributor 173 is disposed on the lower side space at the working fluid inlet 12162 of the hydraulic atomizing nozzle 1216. Please refer to FIG. 1 and FIG. The configuration of the flow device 173. The utility model mainly comprises two adjacent symmetrically arranged left-inward manifolds 175 and right-inward manifolds 174, and a pressure equalizing distribution pipe 176, which is oriented laterally of the processing tanks 1, on the left and right sides of the pressure equalizing distribution pipe 176, left into The manifold 175 is from left to right, the right inlet manifold 174 is from right to left, and the length is the same width as the width of the guide tube 11. If used in the double tube guide tube 11, the width of the double tube guide tube 11 is the same Width, if used in the four-tube guide tube 11, the width and width of the four-tube guide tube 11 are the same width, and the length can be arbitrarily widened or reduced according to the number of the guide tube 11, in the left-inward manifold 175 and the right-in A plurality of rows of diverting holes 178 are defined in the downstream direction of the side wall of the manifold 174, and a proper gap is maintained between the diverting holes 178 and the diverting holes 178. Between the two diverting holes 178, two rows are arranged in a relatively staggered arrangement. Different direction or staggered spout 179, on the upper side wall of the equalizing distribution pipe 176, with respect to the hydraulic atomizing nozzle working fluid inlet 12161, each of which is provided with a dispensing port 172 which can be interconnected with the hydraulic atomizing nozzle 1216 by a communicating pipe Into the pathway.

Referring to FIG. 1 to FIG. 3 simultaneously, an AC-type airflow reflow device 190 is disposed on the upper side of the working fluid collecting plate 184 at the central portion of the processing tank 1, as shown in FIG. 7 , FIG. 7A, and FIG. The configuration of the airflow reflow device 190 is structurally and AC-flowing device 163 Very close, mainly comprising two adjacent symmetric single oblique manifolds 191 and T-shaped manifold return tubes 192, which are oriented transversely to the treatment tank 1, the left side of the manifold is from left to right, and the right side is from right to left. The length is the same as the width of the guide tube 11, and if it is in the double tube guide tube 11, the width of the double tube guide tube 11 is the same width, and if it is in the four tube guide tube 11, the four tube guide tube 11 is used. The width is the same as the width, and the length thereof can be arbitrarily widened or reduced according to the number of the guide tubes 11. On the lower side wall of the single oblique bus tube 191, a row of parallel return ports 193 are arranged in parallel along the path direction. At the downstream outlet end of the single oblique manifold, the left and right ends of the T-shaped confluence return pipe 192 are connected to each other through a 180-degree connecting rotary pipe 194, so that the return airflow can be at the T-shaped central exit. Then, the airflow return pipe 160 and the air blower 16 communicate with each other.

Therefore, in operation, the hydraulic atomizing nozzle 1216 can utilize the action of the AC flow distributor 173 to cause each of the hydraulic atomizing nozzles 1216 to eject the same flow rate value. Therefore, in operation, the co-configuration nozzle 121 can utilize the action of the AC-type airflow device 163 to cause each of the co-configuration nozzles 121 and each of the air-floating nozzles 122 to eject the same flow rate value. Therefore, in operation, it can utilize the co-configuration nozzle 121 as the main power source for driving the fabric 3 to perform cyclic movement. In the dyeing or other processing, the rotation period of the blower 16 blade can be adjusted according to the characteristics of the fiber fabric 3 and the processing requirements. Increasing or decreasing, the required working air flow rate and flow rate can be obtained, and the air flotation nozzle 122 can be sprayed with an appropriate amount of airflow according to the basis weight of the fiber fabric 3 by using the regulating valve 169 at the inlet of the air flotation distribution pipe. The fiber fabric 3 is floated, so that the fiber fabric 3 obtains a relatively smooth airflow to form an air cushion sliding manner, and promotes no frictional contact and disturbance between the fiber fabric 3 and the pipe wall to promote the rapid movement of the fiber fabric 3 during rapid movement. Resistance is minimized. Therefore, under the action of the co-structured nozzle 121, a high-speed air stream to be ejected, or a high-speed atomizing dye solution and a treatment agent, or a high-speed low-temperature plasma, or a high-speed vapor stream, or the like Gas or liquid The body can be sprayed directly onto the lower surface of the fabric 3 in a direct close manner. Under the action of the reflective substrate 13, the fiber fabric 3 can be caused to fluctuate drastically, and under the action of the reflective substrate 13, the high-speed air flow is caused. By the end surface pulling action of the reflecting substrate 13, the lower side of the fiber fabric 3 is advanced toward the downstream direction, thereby causing a pressure difference, thereby causing the fiber fabric 3 to generate an accelerated movement and a wave motion, and passing through the guide tube 11 The side spans across the horizontal tube wall end face between the left and right side walls of the passage, and the fiber fabric 3 in the upstream and midstream sections along the passage direction is caused by the accelerated movement of the fiber fabric 3 to cause air on the upper surface boundary of the fiber fabric 3. Being subjected to traction, thereby forming a fast flowing low pressure region, thus causing the fiber fabric 3 to continuously generate vertical downward pressure when passing through the guide tube 11, and whenever the fiber fabric 3 is continuously subjected to co-construction The driving of the push-pull of the nozzle 121, in addition to causing the fiber fabric 3 to spread in the downstream section of the co-structured nozzle 121, also affects the fiber Flotation embodiment 3 was moved web-shaped opening in the fabric guide tube 11 upstream and midstream section through fast, located immediately below the end wall of the passage surface 121 toward the direction of movement along a common path configuration nozzles.

Referring to FIG. 1 to FIG. 3 simultaneously, in the downstream section of the common-type nozzle 121 in the discharge direction, between the lower side of the outlet of the duct 11 and the inner side of the inlet of the upstream section 31 of the collecting duct 2, The U-shaped swivel plate 14 is provided, and the upstream end of the U-shaped swivel plate 14 is overlapped and fixed on the lower side of the common-type nozzle 121 in a stepwise manner, so that the upstream outer end surface of the U-shaped swivel plate 14 is formed to be straight. The reflecting substrate 13 is provided on the downstream outer end surface of the U-shaped rotating plate 14 with the inner separating grid 21 and the outer separating grid 22 in the falling section 31, and is located in the downstream section of the passage of the guide tube 11 The upper side of the construction nozzle 121 is provided with a guide plate 15, and the upstream side end of the guide plate 15 extends toward the upstream side end of the guide tube 11 and overlaps the side wall of the guide tube 11, and the downstream end thereof The outer separating grids 22 of the falling section 31 of the cloth groove 2 are connected to each other by the guide plate 15 The space between the upper and lower ends of the downstream section of the passage of the guide pipe 11 forms a tapered wedge-shaped gap 151. When the fiber fabric 3 passes through the wedge-shaped gap 151, it can be borrowed from the lower end surface of the guide plate 15 and The relative movement of the upper end surface of the fiber fabric 3 causes the air in the guide tube 11 to squeeze the air above the fiber fabric 3 into the wedge gap to generate pressure, so that the fiber fabric 3 passing through the co-structure nozzle 121 is again obtained downward. The pressure action can cause the co-structured nozzle 121 to obtain a large reaction force when the high-speed air stream is ejected and the fiber fabric 3 is impacted, and can also promote the fiber fabric 3 when passing through the U-shaped revolving plate 14 to make the fiber fabric. 3 The air flow on the upper end face continuously provides a large static air flow, which can provide the reflected energy generated by the fiber fabric 3 between the reflective substrate 13 and the guide plate 15, which can be transmitted to the fiber fabric 3, thereby increasing Large fluctuation energy and fluctuation frequency.

At the downstream outlet of the guide pipe 11 and the upstream distribution section 31 of the collecting trough 2, a distracting mechanism is disposed. The tiling mechanism is composed of the U-shaped rotating plate 14, the guiding plate 15, the inner separating grid 21, the outer separating grid 22, the droplet collecting plate 18, and the working fluid collecting plate 184 described above. The inner and outer side walls of the falling section 31 on the upstream side end of the groove 2 passage are respectively provided with an inner separating grid 21 and an outer separating grid 22, and the upstream side of the inner separating grid 21 is provided on the U-shaped rotating plate 14 and the droplet collecting At a portion where the plates 18 are connected to each other, the upstream side of the collecting groove 2 is located on the inner side of the falling cloth section 31 in an upright manner, and the downstream side end thereof is connected to the upstream side end of the working fluid collecting plate 184. The downstream side end of the droplet collecting plate 18 is provided with a collecting guide groove 181. On the lower side wall of the collecting guiding groove 181 and the lowest portion of the working fluid collecting plate 184, a draft tube 182 is provided. The collected working fluid is introduced into the discharge port 170 below the collecting tank 2 to be discharged. The upstream side end of the outer separating grid 22 is in contact with the downstream side end of the guiding plate 15, and the downstream side end thereof is connected with the sliding strip 23 and the meshing plate 24 on the lower side of the collecting groove 2 to form a cloth. Outside of slot 2 A circulation passage 221 for forming an air flow between the square and the inner side wall of the treatment tank 1 is provided, and the air flow discharged from the outer separation grid 22 is guided by the circulation passage 221 to the passage of the guide pipe 11 at the front end of the treatment tank 1. The liquid droplets discharged from the outer separation grid 22 and the free fibers and other impure solid objects can be collected through the inner side wall of the treatment tank 1, and discharged along the wall surface to the lower discharge port 170, and introduced into the working fluid collection tank 213. In operation, the fiber fabric 3 can be forcedly deflected by the guide plate 15 to form a curved end surface, and the high-speed air jetted by the co-structured nozzle 121 flows on the lower side of the fiber fabric along the end surface of the reflective substrate 13 and The outer end surface of the U-shaped revolving plate 14 is discharged through the upper side of the inner separating grid 21, and at the same time, the fiber fabric 3 that is falling toward the collecting groove 2 can be pulled, and moved to the inner separating grid 21, whenever the fiber fabric is subjected to the inner separating grid. When the net 21 blocks, it will instantaneously block the passage of the air flow to the inner separation grid 21, and the high-speed air flow instantaneously generates an air impact effect to develop the expansion potential energy, forcing the fiber fabric 3 to rapidly move toward the outer separation grid 22 and The fiber fabric 3 on the inner side separating mesh 21 is subjected to a downwardly expanding air flow, forcing the fiber fabric 3 to move from the upper side to the lower side of the inner side separating grid 21, as it continues to develop right below the falling section 31. When the fiber fabric 3 leaves the upper side of the inner separating grid 21, the inner separating grid 21 passage is opened again, so that the high-speed air flow subjected to the U-shaped rotating plate 14 is returned again. Discharged to the passage of the inner separating grid 21, and the above-mentioned action continues to occur continuously during operation, so that the fiber fabric 3 passes through the U-shaped rotating plate 14 and the fiber fabric 3 is changed due to the direction of high-speed air flow. Producing a strong oscillating phenomenon, during the swinging process, whenever the fabric 3 is in the reverse swing, it will cause the residual working fluid attached to the surface of the fabric 3 to induce strong tensile and reverse motion fibers. The fabric 3 is separated. Therefore, in addition to causing a large amount of residual working fluid to be separated from the surface of the fabric 3 in such a manner as to instantaneously generate droplets, the air flow is separated from the collecting trough 2 by the inner separating grid 21 and the outer separating grid 22 passage. In addition to the falling cloth section 31, it is also possible to drop the fabric of the fabric into the collecting groove 2, and the folding operation can be smoothly performed by the swinging action.

Please refer to FIG. 1 to FIG. 3 at the same time, on the airflow return pipe 160, and set up the airflow filter 162, the exhaust gas discharge port and the control valve 200, the fresh air inlet port and the control valve 201, the exhaust gas discharge port and the control valve 200 and fresh A flow regulating valve 202 is disposed between the air inlet port and the control valve 201, and a steam inlet port and a control valve 211 and other gas inlet ports and a control valve 212 are disposed on the pressurized circulating fluid flow pipe 210, in the processing tank 1 The bottom of the lower side is provided with a working fluid collecting tank 213, and a working fluid recovery or discharge valve 214, which can arbitrarily control each of the introduced or discharged valves due to the process requirements.

It also includes an air heater 161 and a gas flow filter 162 which are respectively connected to the air flow conveying pipe 71 and the air flow return pipe 160 to form a passage with the air blower 16.

Therefore, in the dyeing or other processing, the circulating air and the working fluid in the treatment tank 1 and the dyeing liquid or the treatment liquid of the pumpless charging device 20 or the preparation tank 19 can be pumped through the respective piping system and the blower 16 and the feed pump. The 73 is connected to each other, and the pressurized air and the pressurized dye solution or the treating agent can be sprayed by the co-structured nozzle 121, and a part of the pressurized air can be ejected through the air floating nozzle 122, respectively.

1‧‧‧Processing tank

2‧‧‧Setting trough

3‧‧‧Fiber fabric

5‧‧‧High-voltage power supply facilities

11‧‧‧ Guide tube

12‧‧‧Working door hole

13‧‧‧Reflective substrate

14‧‧‧U type rotary plate

15‧‧‧ Guide plate

16‧‧‧Blowers

18‧‧‧Drop collection board

19‧‧‧Material bucket

20‧‧‧No pumping device

21‧‧‧Inside separation grid

22‧‧‧Outside separation grid

23‧‧‧ slider

24‧‧‧Mesh plate

31‧‧‧Upstream section

42‧‧ ‧ splitter

43‧‧‧ access

46‧‧‧Return port

61‧‧‧Arc shunt

62‧‧‧Confluence channel

71‧‧‧Air flow duct

72‧‧‧Liquid pressure pressurized circulation pump

73‧‧‧feeding pump

111‧‧‧Upstream entrance

112‧‧‧Downstream exit

113‧‧‧Disposed liquid removal mechanism

121‧‧‧Common construction nozzle

122‧‧‧Air floating nozzle

151‧‧‧Wedge gap path

160‧‧‧Airflow return pipe

161‧‧ Air heater

162‧‧‧Airflow filter

163‧‧‧AC airflow device

164‧‧‧Right into the oblique manifold

165‧‧‧Left forward skew manifold

166‧‧‧ confluence

167‧‧‧Communication distribution tube

168‧‧‧Air flotation tube

169‧‧‧Air flow control valve

170‧‧‧ dyeing liquid return pipe

172‧‧‧Distribution

173‧‧‧AC flow distributor

174‧‧‧Right into the manifold

175‧‧‧Left into the manifold

176‧‧‧pressure distribution pipe

178‧‧ ‧Distribution

179‧‧‧ spout

181‧‧‧ Collecting diversion trenches

182‧‧‧drain tube

184‧‧‧ working fluid collection board

190‧‧‧AC airflow reflow device

191‧‧‧ single oblique manifold

192‧‧‧T-shaped confluence return tube

193‧‧‧ Array of return ports

194‧‧‧Connected rotary tube

200‧‧‧Exhaust gas outlet and control valve

201‧‧‧Fresh air inlet and control valve

202‧‧‧Flow regulating valve

203‧‧‧Flow regulating valve

210‧‧‧ Pressurized circulating fluid flow tube

211‧‧‧Vapor input port and control valve

212‧‧‧Other gas inlets and control valves

213‧‧‧Working fluid collection tank

214‧‧‧Working fluid recovery or discharge valve

215‧‧‧Working liquid sieve

220‧‧‧Working fluid heat exchanger

221‧‧‧Circular access

12111‧‧‧Circular shaped electrical target

12121‧‧‧Steam tube

12122‧‧‧Replaceable electric shock rod

12123‧‧‧High voltage power connection terminal

12124‧‧‧Ground connection terminal

1216‧‧‧Hydraulic atomizing nozzle

12161‧‧‧Hydraulic atomizing nozzle

12162‧‧‧Working fluid inlet

12164‧‧‧Sliding valve stem

12165‧‧‧ valve seat

12167‧‧‧Spring piston

12169‧‧‧Activity fluid inlet

Figure 1: The structural side section of the impulsive detonation wave fast dyeing machine; Figure 2: The side section of the model of the high-speed model of the impulse detonation wave fast dyeing machine; Figure 3: The system is impulsive Side section of an extended model of a type detonation wave fast dyeing machine Figure 4A: is a structural cross-sectional view of a co-structured nozzle opening; Figure 4B is a structural cross-sectional view of a common-type nozzle opening with a replacement electric shock bar; Figure 5: Fig. 5A is a structural sectional view of an alternating current airflow device; Fig. 5B is a structural sectional view of a double pipe alternating current flow device; Fig. 6: It is a structural sectional view of an AC flow distributor. Figure 7 is a perspective view of the AC flow recirculation device; Figure 7A is a structural cross-sectional view of the AC flow recirculation device; Figure 7B is a structural cross-sectional view of the dual-tube AC flow recirculation device.

1‧‧‧Processing tank

2‧‧‧Setting trough

3‧‧‧Fiber fabric

5‧‧‧High-voltage power supply facilities

11‧‧‧ Guide tube

12‧‧‧Working door hole

13‧‧‧Reflective substrate

14‧‧‧U type rotary plate

15‧‧‧ Guide plate

16‧‧‧Blowers

18‧‧‧Drop collection board

19‧‧‧Material bucket

20‧‧‧No pumping device

21‧‧‧Inside separation grid

22‧‧‧Outside separation grid

23‧‧‧ slider

24‧‧‧Mesh plate

31‧‧‧Upstream section

42‧‧ ‧ splitter

43‧‧‧ access

46‧‧‧Return port

61‧‧‧Arc shunt

62‧‧‧Confluence channel

71‧‧‧Air flow duct

72‧‧‧ Pressurized circulation pump

73‧‧‧feeding pump

111‧‧‧Upstream entrance

112‧‧‧Downstream exit

113‧‧‧Disposed liquid removal mechanism

121‧‧‧Common construction nozzle

122‧‧‧Air floating nozzle

151‧‧‧Wedge gap path

160‧‧‧Airflow return pipe

161‧‧ Air heater

162‧‧‧Airflow filter

163‧‧‧AC airflow device

164‧‧‧Right into the oblique manifold

165‧‧‧Left forward skew manifold

166‧‧‧ confluence

167‧‧‧Communication distribution tube

168‧‧‧Air flotation tube

169‧‧‧Air flow control valve

170‧‧‧ dyeing liquid return pipe

172‧‧‧Distribution

173‧‧‧AC flow distributor

174‧‧‧Right into the manifold

175‧‧‧Left into the manifold

176‧‧‧pressure distribution pipe

178‧‧ ‧Distribution

179‧‧‧ spout

181‧‧‧ Collecting diversion trenches

182‧‧‧drain tube

184‧‧‧ working fluid collection board

190‧‧‧AC airflow reflow device

191‧‧‧ single oblique manifold

192‧‧‧T-shaped confluence return tube

200‧‧‧Exhaust gas outlet and control valve

201‧‧‧Fresh air inlet and control valve

202‧‧‧Flow regulating valve

210‧‧‧ Pressurized circulating fluid flow tube

211‧‧‧Vapor input port and control valve

212‧‧‧Other gas inlets and control valves

213‧‧‧Working fluid collection tank

214‧‧‧Working fluid recovery or discharge valve

215‧‧‧Working liquid sieve

220‧‧‧Working fluid heat exchanger

221‧‧‧Circular access

Claims (7)

An impulse detonation wave fast dyeing machine, which has at least one processing tank (1) combined side by side, and with an air flow conveying pipe (71), a gas flow return pipe (160), a pressurized circulating liquid flow conveying pipe (210), a dyeing liquid The return pipes (170) are connected to each other, and each of the processing tanks (1) is provided with a collecting groove (2) for providing textile stacking and a guiding pipe (11) for providing accelerated movement of the textile, both of which The front and rear ends are connected to each other and form a wide circulation passage, which can be used for rapidly completing the dyeing and other processing in the passage of the textile on the passage, and is characterized by comprising: an air floating nozzle (122), the air floatation The nozzle (122) is composed of a plurality of small orifice passages, and is disposed on the lower wall of the upstream and midstream sections along the passage of the conduit (11), and the air-floating nozzle (122) is divided by air flotation The piping (168) and the air flow conveying pipe (71), the airflow return pipe (160) and the air blower (16) are connected to each other; the common structure nozzle (121) is a gas injection pipe (12121) And a hydraulic atomizing nozzle (1216), which is disposed on the wall below the downstream section of the conduit (11) In the cross section, close to the outlet of the duct (11), a plurality of rows of co-constructed nozzles (121) combined side by side, which can be shared by a common distribution pipe (167) and an air flow pipe (71), The gas flow return pipe (160) and the pressurized circulating liquid flow pipe (210), the dye liquid return pipe (170) are connected to the blower (16) and the pressurized circulation pump (72); the movable substrate (13) is reflected. The reflection actuation substrate (13) is slidably fixed to the lower side of the co-structure nozzle (121) in a stepwise manner in the downstream direction of the co-structure nozzle (121); the U-shaped revolving plate (14), The U-shaped rotary plate (14) is disposed on the downstream side of the reflective actuation substrate (13) and is formed by extending the reflective actuation substrate (13) to form an arc shape in a progressive manner. a guide plate (15) disposed on an upper side of the co-structured nozzle (121), the upstream side end of which extends toward the upstream side end of the guide tube (11) and overlaps the guide tube (11) The upper side end wall is connected to the outer separating grid (22) of the collecting section (2) of the collecting section (2); the droplet collecting plate (18) is disposed at a downstream side end of the U-shaped rotating plate (14); a collecting guide groove (181) disposed at a downstream side end of the liquid droplet collecting plate (18); and a draft tube (182) disposed at the collecting guiding groove On the lower side wall of (181); the inner separating grid (21) is disposed at the upstream side end at a portion where the U-shaped rotating plate (14) and the droplet collecting plate (18) are connected to each other, to be vertical or nearly vertical The manner is set at the inner side of the falling section (31) at the upstream side end of the collecting groove (2); the upstream side end of the outer separating grid (22) is provided at the downstream end of the guiding plate (15), and the downstream side thereof Then, the slider (23) and the mesh plate (24) on the lower side of the collecting groove passage are connected to each other; and the working fluid collecting plate (184) is disposed at the downstream side end of the inner separating grid (21) at the collecting The upper side of the channel (2) path. The impulsive detonation wave fast dyeing machine according to claim 1, further comprising a hydraulic circuit at an upstream side of the inlet (1213) at a central passage of the injection pipe (12121) of the co-construction nozzle (121) The atomizing nozzle (1216) is provided with a replacement electric hammer (12122) at the center of the passage of the hydraulic atomizing nozzle port (12161), wherein the discharge tip is located at the center of the hydraulic atomizing nozzle opening (12161), and the other end is extended. To the outside of the body of the hydraulic atomizing nozzle (1216), and having a high-voltage connecting terminal (12123) connected to the high-voltage power supply (5) via a cable, and a ring-shaped type on the common-purpose nozzle opening (1211) Electric target (12111) with a ground connection The sub-port (12124) forms a co-structure with the co-facial nozzle opening (1211) that is interconnected to the surface via a cable. The impulsive detonation wave fast dyeing machine according to claim 1, further comprising: an alternating current flow cloth disposed between the hydraulic atomizing nozzle (1216) and the pressurized circulating liquid flow conveying tube (210) a flow device (173) comprising two adjacent symmetrically arranged left and right manifolds (175) and a right inlet manifold (174), and a pressure equalizing distribution tube (63) to The treatment tank (1) is oriented laterally, on the left and right sides of the pressure equalization distribution pipe (63), the left inlet manifold (175) is from left to right, the right inlet manifold (174) is from right to left, and the length is guided by cloth. The width of the tube (11) is the same width. If used in the double tube guide tube (11), the width of the double tube guide tube (11) is the same width. If used in the four tube guide tube (11), The width of the four-tube guide tube (11) is the same width, and the length can be arbitrarily widened or reduced according to the number of the guide tubes (11), on the side walls of the left-inward manifold (175) and the right-inward manifold (174). In the downstream direction, each row is provided with a row of diverting holes (178), and a proper gap is maintained between the diverting holes (178) and the diverting holes (178), and between the two diverting holes (178), they are arranged in a relatively staggered arrangement. Two rows of different directions or staggered spouts (179), On the upper side wall of the pressure equalizing distribution pipe (176), opposite to the working fluid inlet (12161) of the hydraulic atomizing nozzle (1216), each is provided with an outlet (172) which can be connected to the hydraulic atomizing nozzle (1216). ) Connected to each other as a pathway. The impulsive detonation wave fast dyeing machine according to claim 1, further comprising an alternating current type between the air floating nozzle (122) and the co-structured nozzle (121) and the air flow conveying pipe (71). a flow distribution device (163), the AC flow device (163) comprising two adjacent symmetric left-inclined manifolds (165) and right-inclined manifolds (164) for processing the tanks (1) The lateral direction shall prevail, the left-inclined manifold (165) is from left to right, the right-inclined manifold (164) is from right to left, and the length is the same width as the guide tube (11), if it is in the double-tube guide Tube (11), with double tube guide tube (11) The width is the same as the width. If it is in the four-tube guide tube (11), the width of the four-tube guide tube (11) is the same width, and the length can be arbitrarily widened or reduced according to the number of the guide tube (11). An oblique side wall of the inclined manifold is arranged along the direction of the passage, and each is provided with a row of shunting ports (42) arranged in parallel, and each of the diverting ports (42) is provided with an arc-shaped shunt tube (61), and an arc shunt tube (61) Each of the shunt tubes arranged in the upper and lower staggered rows can be geometrically calculated to form a row of the same direction of the passage port (43), and each arc type shunt tube can be made by the action of the arc type shunt tube (61). The downstream end outlet forms a row of confluence ports (166) arranged in parallel in the same direction, and the downstream side end outlets at the confluence ports (166) are respectively associated with the co-construction distribution pipe (167) and the air flotation distribution pipe ( 168) Connected to each other, and an air flow regulating valve (169) is provided at the inlet of the air flotation distribution pipe (168). The impulsive detonation wave fast dyeing machine according to claim 1, further comprising, in the center of the treatment tank (1), on the downstream side of the working fluid collecting plate (184) and the gas recovery pipe (160) An alternating airflow recirculating device (190) is disposed between the two, and the two alternating symmetrical single oblique manifolds (191) and the T-shaped confluent returning tubes (192) are The treatment tank (1) is horizontally correct, the left side of the manifold is from left to right, the right side of the right is from right to left, and the length is the width of the guide tube (11). If it is in the double tube (11), then The width of the double-tube guide tube (11) is the same width. If it is in the four-tube guide tube (11), the width of the four-tube guide tube (11) is the same width, and the length can be based on the guide tube (11). The number of any ones is arbitrarily widened or reduced. On the lower side wall of the single oblique manifold (191), there is a row of parallel return ports (193) arranged in parallel along the direction of the passage, and the downstream outlet end of the single oblique manifold is borrowed. The 180-degree connecting rotary pipe (194) and the left and right ends of the T-shaped return pipe (192) are connected to each other to make the return air flow in the center of the T-shape. Mouth, and then communicate with each other by reflux delivery pipe (160) and the blower (16). The impulse detonation wave fast dyeing machine according to the first aspect of the invention, wherein the upstream passage of the suction port of the air blower (16) is provided with a new air introduction port (201), an exhaust gas discharge port and a control valve (200). And the treatment liquid recovery or discharge port at the bottom of the lower side of the treatment tank (1), and control valves are provided on each of the introduction and discharge ports, which can be arbitrarily controlled according to the process. The impulse detonation wave fast dyeing machine described in claim 1 further includes an air heat exchanger (161) and a gas flow filter (162), and a working fluid heat exchanger (220) and a working fluid sieve filter. (215), which is respectively connected to the air flow conveying pipe (71), the air flow return pipe (160), the pressurized circulating liquid flow conveying pipe (210), and the dye liquid return pipe (170).