CN115245942A

CN115245942A - Environment-friendly treatment system and method for mammary gland drainage bag

Info

Publication number: CN115245942A
Application number: CN202111645417.XA
Authority: CN
Inventors: 段馨; 郭广成; 李凯强
Original assignee: First Affiliated Hospital of Zhengzhou University
Current assignee: First Affiliated Hospital of Zhengzhou University
Priority date: 2021-12-30
Filing date: 2021-12-30
Publication date: 2022-10-28

Abstract

The invention belongs to the technical field of medical plastic recovery equipment, and discloses an environment-friendly treatment system for a mammary gland drainage bag, which comprises a sorting mechanism and a control module, wherein a crushing mechanism is arranged at an outlet of the sorting mechanism, the crushing mechanism is communicated with a solid treatment module through a conveying mechanism, and is also communicated with a sewage treatment module through a waste liquid pipe, the crushing mechanism comprises a crushing module and a cleaning module, the conveying mechanism is arranged on the cleaning module, the end, far away from the crushing mechanism, of the conveying mechanism is provided with the solid treatment module, and the solid treatment module comprises a disinfection module and a decoloration module.

Description

Environment-friendly treatment system and method for mammary gland drainage bag

Technical Field

The invention belongs to the technical field of medical plastic recovery equipment, and particularly relates to an environment-friendly treatment system and method for a mammary gland drainage bag.

Background

After the drainage bag is used, a large amount of disposable plastic medical appliances, plastic wastes and the like are often generated, if the plastic wastes are directly discarded, the environment is seriously polluted, and the plastic wastes can possibly become a source of epidemic diseases, so the plastic wastes need to be treated before being discarded, but for the existing plastic waste treatment device, the plastic wastes are directly thrown into the medical wastes, when the plastic wastes are treated, more time is usually consumed for sorting, the treatment speed is slowed down, the treatment effect in subsequent further treatment is greatly influenced, the disease propagation rate is increased, the treatment cost is increased, and after some viruses are inactivated by ultraviolet rays, if visible light is used for irradiating, the inactivated viruses can be revived due to the reason of activating enzymes, so the common ultraviolet disinfection is not applicable any more, characters are usually printed on the drainage bag, the requirements on the ink are higher along with the technical development, various environment-friendly printing inks are rapidly developed, the overall price is high, the popularization difficulty is high, and the printing ink recycling process of the drainage bag needs to remove printing ink, and the existing industrial printing ink is formed by a pasty pigment, a mixed pigment and a color colloid material which is dispersed and a printing colloid material; the binder serves as a carrier of the colorant on one hand and as a binder for fixing the colorant on the surface of the printing material on the other hand; the filler enables the ink to have proper properties, so that the ink has better printing adaptability, and the binder is a sticky fluid and plays a role of enabling the pigment carrier to fix the pigment on the surface of a printing stock. The main components of the raw materials of the connecting material comprise oil, resin, an organic 29794 agent and auxiliary materials, the traditional industrial printing ink cleaning agent mainly takes stone organic solvents such as gasoline, kerosene and the like, and under the drive of the trend of energy saving and carbon reduction, the traditional industrial printing ink cleaning agent recycles plastics and other recyclable articles, is beneficial to saving resources, is beneficial to processing plastic medical articles which are difficult to degrade, and accords with the green environmental protection concept, so that a drainage bag processing system for preprocessing in a medical institution is needed.

Disclosure of Invention

The invention aims to provide a system and a method for environment-friendly treatment of a mammary gland drainage bag, which are used for sorting ropes and plastics on the drainage bag through a sorting mechanism, then performing pretreatment through a sewage treatment module by crushing and cleaning, discharging the pretreated granules into a municipal pipeline, and then performing disinfection and decoloration treatment on the crushed granules through a solid treatment module, so that the drainage bag is recycled, and resources are saved.

Based on the purpose, the invention adopts the following technical scheme: the utility model provides a mammary gland drainage bag environmental protection processing system, includes letter sorting mechanism and control module, is equipped with rubbing crusher and constructs in letter sorting mechanism exit, and rubbing crusher constructs through conveying mechanism and solid processing module is linked together, still is linked together through waste liquid pipe and sewage treatment module, rubbing crusher constructs including crushing module and cleaning module, is equipped with conveying mechanism in cleaning module, keeps away from the crushing mechanism end on conveying mechanism and is equipped with solid processing module, and solid processing module includes disinfection module and decoloration module.

Preferably, rubbing crusher constructs including rubbing crusher structure shell, is equipped with the feed inlet that is linked together with letter sorting mechanism on rubbing crusher constructs the shell, is equipped with crushing module in rubbing crusher constructs the shell, and crushing module includes two matched with cutter rolls, is equipped with the crushing motor who is connected with crushing module on rubbing crusher constructs the shell, and crushing motor is connected with control module, is equipped with the feed opening with crushing module matched with in rubbing crusher constructs the shell, is equipped with cleaning module on the feed opening, still includes the steam generator who is linked together with rubbing crusher constructs.

Preferably, the cleaning module comprises a second motor connected to the shredder mechanism housing; the cleaning device also comprises a cleaning barrel matched with the feed opening, a coupling matched with the second motor is arranged on the cleaning barrel, a cleaning feed opening communicated with the feed opening is arranged on the cleaning barrel, and the projection of the cleaning barrel on the section vertical to the axis is U-shaped; the cleaning device comprises a cleaning barrel, a first cleaning barrel and a second cleaning barrel, wherein the first cleaning barrel and the second cleaning barrel are coaxially arranged, at least one high-pressure first nozzle is arranged on the inner side surface of the first cleaning barrel, a hole convenient for water to pass through is formed in the first cleaning barrel, a first water collecting area is formed in an area between the outer side surface of the first cleaning barrel and the cleaning barrel, a first conveying roller matched with a coupler is arranged in the first cleaning barrel, and a first conveying plate is arranged on the first conveying roller.

Preferably, an air inlet pipe ring which is matched with the cleaning barrel in a rolling manner is arranged on the outer side surface of the second cleaning barrel, which is close to the first cleaning barrel, a first bearing which is matched with the air inlet pipe ring is arranged on the cleaning barrel, an air inlet pipe is arranged on the air inlet pipe ring, the air inlet pipe ring is fixedly connected and communicated with the second cleaning barrel, a water retaining ring which is fixedly connected with the cleaning barrel is arranged on the outer side surface of the second cleaning barrel, which is far away from the first cleaning barrel, and a second bearing which is matched with the second cleaning barrel is arranged on the inner side surface of the water retaining ring; a speed reducer matched with the first conveying roller is arranged on the second cleaning barrel close to the first cleaning barrel, and a connecting rod fixedly connected with the second cleaning barrel is arranged at the output end of the speed reducer; the second cleaning barrel is divided into an air inlet part and a spin-drying part, a second cleaning barrel shell of the air inlet part is of a hollow structure communicated with the air inlet pipe ring, and a water outlet hole is formed in the second cleaning barrel shell of the spin-drying part; a second conveying plate in a spiral structure is arranged on the inner side surface of the second cleaning barrel along the circumference, the second conveying plate is divided into an air inlet part conveying plate and a spin-drying part conveying plate, the interior of the air inlet part conveying plate is of a hollow structure communicated with the shell of the second cleaning barrel of the air inlet part, and at least one air outlet is formed in the air inlet part conveying plate; the pipe diameter of second washing bucket along keeping away from first washing bucket axis direction reduces gradually, is equipped with slope surface with second washing bucket matched with washing bucket medial surface, and slope surface parallels with the outside inclined plane of second washing bucket, washs the regional second water-collecting area that constitutes between domatic and the manger plate ring.

Preferably, the sterilization module comprises a supporting seat, a sterilization tank is arranged on the supporting seat, a protective cover is arranged on the outer side of the sterilization tank along the circumference, and a discharge hole is formed in the end, close to the supporting seat, of the sterilization tank; the sterilizing tank is provided with a feeding module far away from the end of the discharge port, the feeding module comprises a feeding port communicated with a conveying mechanism, the feeding port is a cylindrical pipeline, a first flange is arranged on the outer side surface of the feeding port, which is close to the end of the conveying mechanism, an air inlet pipe orifice communicated with a steam generator is arranged on the outer side surface of the feeding port, two air inlets are arranged on the air inlet pipe orifice, the cross section of the inner side surface of the air inlet pipe orifice in the parallel direction along the axis of the feeding port is trapezoidal, the inner diameters of the air inlet pipe orifices are the same at the front section of the feeding port, then the inner diameters of the air inlet pipe orifices are gradually reduced along the axis of the feeding port, a main air passage is formed in the area between the feeding port and the inner side surface of the air inlet pipe orifice, a first air inlet in an inclined state is arranged on the pipe body of the feeding port, a gas-solid mixing area is formed in the area far away from the end of the first flange and the inner side surface of the air inlet pipe orifice, a section extends for a distance along the axis to form a mixing discharge port, and a scattering mechanism is arranged on the mixing port, and the end, which is close to the mixing port; the air baffle plate connected with the scattering mechanism is arranged on the feeding hole, a scattering air passage communicated with the scattering mechanism is formed in the area between the air baffle plate and the air inlet pipe opening, and the scattering air passage is communicated with an air inlet.

Preferably, a disinfection mechanism communicated with the mixed discharge hole is arranged in the disinfection tank; the disinfection mechanism comprises a spiral material pipe, the material pipe comprises a pipe shell, the pipe shell comprises a protective layer made of transparent materials, the protective layer comprises two layers, a transparent heat-preservation coating is coated on the outer protective layer, and an inert gas layer is arranged between the protective layers; the material pipe is characterized in that a reflective collision block is arranged on the inner side surface of the material pipe along the circumference and is hemispherical, at least one small pit is arranged on the reflective collision block, the surface of the small pit is hemispherical, a second scattering mechanism fixed with a protective layer is arranged in the material pipe, the second scattering mechanism comprises a collision plate connected with the protective layer, the included angle between the collision plate and the protective layer is an acute angle, the second scattering mechanism is made of transparent materials, a scattering pit is arranged on the outer surface of the second scattering mechanism, the material pipe further comprises an X-ray generator matched with the material pipe, at least one electron source is contained in the X-ray generator, and the orientation of the X-rays of the electron source is spirally and annularly distributed with the material pipe.

Preferably, the decoloring module comprises an organic solvent decoloring tank, and the organic solvent decoloring tank is communicated with a decoloring cleaning device; comprises a water-based and semi-water-based decoloring tank communicated with a decoloring cleaning device, wherein the water-based and semi-water-based decoloring tank is communicated with the decoloring cleaning device; the device also comprises a lipase type water-based decoloring tank communicated with the decoloring cleaning device, a second decoloring cleaning device communicated with the lipase type water-based decoloring tank, and a solid-liquid separator communicated with the organic solvent decoloring tank, the water-based and semi-water-based decoloring tanks and the lipase type water-based decoloring tank.

Preferably, the organic solvent decoloring tank comprises support legs, a tank body is arranged on the support legs, a particle feeding pipe communicated with the discharge port is arranged on the outer side surface of the tank body, an electromagnetic valve is arranged on the particle feeding pipe, and an adjusting valve is arranged on the outer side surface of the tank body; an organic solvent feed port is arranged on the outer side surface of the tank body, a meter connected with the control module is arranged on the organic solvent feed port, and an organic solvent discharge port communicated with the decoloring cleaning device is also arranged; a stirring motor connected with the control module is arranged at the top of the tank body, stirring blades matched with the stirring motor are arranged in the tank body, and a particulate matter concentration sensor, a temperature sensor and a pressure sensor which are connected with the control module are arranged on the inner side surface of the tank body; the water-based and semi-water-based decoloring tank is provided with a second particle feeding pipe communicated with the decoloring and cleaning device, a water-based and semi-water-based solvent feeding pipe and a water-based and semi-water-based decoloring tank discharging port communicated with the decoloring and cleaning device.

Preferably, the lipase type water-based decoloring tank is provided with a third particulate matter feeding pipe communicated with the decoloring cleaning device, a lipase type water-based solvent feeding pipe, and a discharge port of the lipase type water-based decoloring tank connected with the second decoloring cleaning device; the structure of the second decoloring and cleaning device comprises a cleaning unit with the same structure as that of the decoloring and cleaning device and a drying unit matched with the cleaning unit; the sorting mechanism comprises a conveying belt, a protective cover is arranged on the conveying belt, a sorting manipulator is arranged on one side of the conveying belt, and a 3D recognition module is arranged on the manipulator.

An environmentally friendly treatment method with a breast drainage bag according to any of the preceding claims, comprising the steps of:

a. sorting the mammary gland drainage bags by a sorting mechanism, and then conveying the mammary gland drainage bags into a crushing module by a conveying mechanism;

b. the crushing module cuts and crushes the drainage bag, water is sprayed to reduce dust and pre-clean the drainage bag during crushing, the crushed drainage bag is cleaned through the cleaning module, sewage is sent into the sewage treatment module through the waste liquid pipe for environmental protection treatment, and the crushed particles are sent into the disinfection module through the conveying mechanism;

c. irradiating the material pipe by an X-ray generator in the disinfection module, wherein the material passes through the material pipe at a speed of 1.5-2.5 meters per second, the electron energy of the X-ray generator is 240-290 kilovolts, and the plastic particles in the material pipe are exposed to the radiation quantity of 45-55 kilograys, preferably 46-53 kilograys;

d. the material treated by the disinfection module is sent into a decoloring module for decoloring, when an organic solvent decoloring tank is used for decoloring, an organic ink cleaning agent mixed by 35-45% of absolute ethyl alcohol, 25-30% of dichloromethane, 28-35% of tetrachloroethylene, 0.5-1.2% of antioxidant and 0.1-0.8% of corrosion inhibitor is adopted to dissolve organic pigment on plastic, meanwhile, stirring blades are used for stirring plastic particles to accelerate the dissolution speed, the stirring speed is 1-3 cubic meters per second, the stirring time is 48-96 hours, the PH value is controlled between 6-10, after decoloring, the organic ink cleaning agent and the plastic particles are separated by a solid-liquid separator, the organic ink reflows into the organic solvent decoloring tank, the plastic particles enter a decoloring cleaning device for cleaning, and after cleaning, the plastic particles are sent into a water-based and semi-water-based decoloring tank;

e. when the water-based and semi-water-based decoloration tanks are decolored, semi-water-based ink cleaning agent which is formed by mixing 4-7% of lipase polyoxyethylene ether, 2-3% of alkylphenol polyoxyethylene ether, 3-7% of surfactant, 0.5-1.5% of triethanolamine, 12-25% of kerosene and water in a mass ratio is adopted to decolor pigments on plastics, meanwhile, stirring blades are used for stirring plastic particles to accelerate the dissolution speed, the stirring speed is 1-3 cubic meters per second, the decoloring time is 10-20 minutes, the PH value is controlled to be 6-11, the temperature is controlled to be 27-38 ℃, after the decoloration is finished, the semi-water-based ink is cleaned by a solid-liquid separator and separated from the plastic particles, the semi-water-based ink is cleaned and reflowed to the water-based and semi-water-based tanks or enters a recovery tank, the plastic particles enter a decoloration cleaning device to be cleaned, and are cleaned and then sent to the lipase-based decoloration tank;

or the mass ratio is as follows: 1-3% of fatty alcohol-polyoxyethylene ether, 8-12% of fatty alcohol-polyoxyethylene ether sulfate, 0.5-2% of benzotriazole, 0.5-1.5% of triethanolamine, 0.5-1.5% of sodium silicate, 1-3% of urea, 1-5% of sodium chloride and the balance of water to form a water-based ink cleaning agent, wherein the decoloring time is 10-20 minutes, the pH value is controlled to be 6-11, and the temperature is controlled to be 27-38 ℃; separating the water-based ink cleaning agent from the plastic particles through a solid-liquid separator after the decolorization is finished, refluxing the water-based ink cleaning agent into the water-based and semi-water-based decolorization tanks or entering the recovery tank, washing the plastic particles in a decolorization washing device, and sending the plastic particles into a lipase-based decolorization tank after the washing;

f. when the lipase type water-based decoloring tank is used for decoloring, the lipase type water-based decoloring tank adopts the following components in percentage by mass: 0.1-0.6% of lipase, 71-92% of AEO, 6-8% of AES, 1-3% of benzotriazole, 1-2.5% of urea, 0.5-1.5% of triethanolamine, 1-3.5% of sodium carbonate, 3-7% of ethanol, 0.1-0.6% of defoamer and deionized water are added to 100% of the mixed lipase type water-based ink cleaning agent, the decoloring time is 2-5 hours, the pH value is controlled between 5 and 10, and the stirring speed is 1-2 cubic meters per second; and after the decoloration is finished, separating the lipase type water-based ink cleaning agent from the plastic particles through a solid-liquid separator, refluxing the lipase type water-based ink cleaning agent into a lipase type water-based decoloration tank or entering a recovery tank, washing the plastic particles in a second decoloration washing device, sending sewage generated in the washing process into a sewage treatment module for treatment, drying the plastic particles through a drying unit after the washing is finished, and storing the dried plastic particles for recycling.

Compared with the prior art, the invention has the following beneficial effects: according to the drainage bag processing device, the drainage bags are sorted by the sorting mechanism and then are sent to the crushing mechanism, so that links and time required for processing of the drainage bags are reduced, breeding and propagation of bacteria and viruses are weakened, the drainage bags are crushed by the crushing mechanism, the crushed drainage bags are cleaned by the cleaning module, produced sewage is sent to medical sewage treatment equipment of a hospital through a waste liquid pipe, cleaning water can be recycled water after being treated by the wastewater treatment equipment of the hospital, solid particles are subjected to sterilization treatment through the sterilization module and then are sent to the decoloring module for decoloring treatment, and the treated plastic particles can be sent to a recycling mechanism or a medical equipment manufacturer for reprocessing and recycling, so that resource waste is reduced, and carbon emission is reduced.

Drawings

FIG. 1 is a flow chart of the breast drainage bag environmental protection treatment system of the present invention;

FIG. 2 is a schematic view of the breast drainage bag environmental protection system of the present invention;

FIG. 3 is a front view of the cleaning module of the present invention;

FIG. 4 is a schematic view of a cleaning module of the present invention;

FIG. 5 is a schematic view of a second wash tank of the present invention;

FIG. 6 is a sectional view of a second washing tub of the present invention;

FIG. 7 is a side view of the water dam ring of the present invention;

FIG. 8 is a schematic view of the disinfection module of the present invention;

FIG. 9 is a schematic view of a feed module of the present invention;

FIG. 10 is a schematic view of the break-up mechanism of the present invention;

FIG. 11 is a schematic view of the disinfection mechanism of the present invention;

FIG. 12 is a cross-sectional view of a material tube of the present invention;

figure 13 is a cross-sectional view of a material tube of the present invention;

FIG. 14 is a block diagram of a decolorizing module of the present invention;

FIG. 15 is a schematic view of an organic solvent decolorizing tank of the present invention;

FIG. 16 is a schematic illustration of a decolorizing module of the present invention;

FIG. 17 is a schematic diagram of a decoloring module according to a second embodiment of the present invention.

In the figure: a crushing mechanism 1, a conveying mechanism 2, a solid treatment module 3, a waste liquid pipe 4, a sewage treatment module 5, a crushing module 6, a cleaning module 7, a coupler 701, a cleaning feed inlet 702, a cleaning barrel 703, a first conveying roller 704, a first conveying plate 705, a first cleaning barrel 706, a first water collecting area 707, an air inlet pipe ring 708, a second cleaning barrel 709, a high-pressure first nozzle 710, a second water collecting area 711, a second bearing 712, a reducer 713, a drying part conveying plate 714, an air inlet part conveying plate 715, a connecting rod 716, an air inlet pipe 717, a water retaining ring 718, an air inlet part 719, a drying part 720, a sterilization module 8, a discharge port 801, a protective cover 802, a sterilization tank 803, a feeding module 804, a sterilization mechanism 805, a feed inlet 806, an air inlet pipe orifice 807, a gas-solid mixing area 808, a mixing discharge port 809, a first air inlet 810, a dispersing air channel 811, a dispersing mechanism 812, a material pipe 813, a material dispersing mechanism 805, a material outlet and a material outlet an X-ray generator 814, a protective layer 815, an inert gas layer 816, a second break-up mechanism 817, an impingement plate 818, a reflective impingement block 819, a de-coloring module 9, support legs 901, an organic solvent de-coloring tank 902, a particulate concentration sensor 903, an organic solvent feed 904, a regulating valve 905, a solenoid valve 906, a particulate feed pipe 907, a stirring motor 908, stirring blades 909, an organic solvent feed outlet 910, a second particulate feed pipe 911, a water-based and semi-water-based de-coloring tank 912, a water-based and semi-water-based solvent feed pipe 913, a water-based and semi-water-based de-coloring tank discharge outlet 914, a lipase-based de-coloring tank 915, a third particulate feed pipe 916, a lipase-based solvent feed pipe 917, a lipase-based de-coloring tank discharge outlet 918, a de-coloring cleaning device 919, a second de-coloring cleaning device, a passive friction body 921, an active kneading ball 922, and a sorting mechanism 10.

Detailed Description

In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail below with reference to examples and the accompanying drawings, and the exemplary embodiments and descriptions thereof are only used for explaining the present invention and are not used as limiting the present invention.

Example one

As shown in fig. 1-16, a mammary gland drainage bag environmental protection processing system, including letter sorting mechanism 10 and control module, be equipped with rubbing crusher mechanism 1 in letter sorting mechanism 10 exit, rubbing crusher mechanism 1 is linked together through conveying mechanism 2 and solid treatment module 3, still is linked together through waste liquid pipe 4 and sewage treatment module 5, its characterized in that: the crushing mechanism 1 comprises a crushing module 6 and a cleaning module 7, a conveying mechanism 2 is arranged on the cleaning module 7, a solid treatment module 3 is arranged at the end, far away from the crushing mechanism 1, of the conveying mechanism 2, and the solid treatment module 3 comprises a disinfection module 8 and a decoloration module 9.

Rubbing crusher constructs 1 and includes the rubbing crusher structure shell, be equipped with the feed inlet that is linked together with letter sorting mechanism on the rubbing crusher structure shell, be equipped with crushing module 6 in the rubbing crusher structure shell, crushing module 6 includes two matched with cutter rolls, be equipped with the crushing motor that is connected with crushing module 6 on the rubbing crusher structure shell, crushing motor is connected with control module, be equipped with in the rubbing crusher structure shell with crushing module 6 matched with feed opening, be equipped with cleaning module 7 on the feed opening, still include the steam generator who is linked together with rubbing crusher constructs 1.

The cleaning module 7 comprises a second motor connected with the crushing mechanism shell; the cleaning device further comprises a cleaning barrel 703 matched with the feed opening, a coupler 701 matched with the second motor is arranged on the cleaning barrel 703, a cleaning feed opening 702 communicated with the feed opening is arranged on the cleaning barrel 703, and the projection of the cleaning barrel 703 on the section vertical to the axis is U-shaped; a first cleaning barrel 706 and a second cleaning barrel 709 are arranged in the cleaning barrel 703, the first cleaning barrel 706 and the second cleaning barrel 709 are coaxially arranged, at least one high-pressure first nozzle 710 is arranged on the inner side surface of the first cleaning barrel 706, a hole convenient for water to pass through is arranged on the first cleaning barrel 706, a first water collecting area 707 is formed in an area between the outer side surface of the first cleaning barrel 706 and the cleaning barrel 3, a first conveying roller 704 matched with the coupler 701 is arranged in the first cleaning barrel 706, and a first conveying plate 705 is arranged on the first conveying roller 704.

An air inlet pipe ring 708 which is matched with the cleaning barrel 703 in a rolling way is arranged at the end, close to the first cleaning barrel 706, of the outer side surface of the second cleaning barrel 709, a first bearing which is matched with the air inlet pipe ring 708 is arranged on the cleaning barrel 703, an air inlet pipe 717 is arranged on the air inlet pipe ring 708, the air inlet pipe ring 708 is fixedly connected and communicated with the second cleaning barrel 709, a water retaining ring 718 which is fixedly connected with the cleaning barrel 703 is arranged at the end, far away from the first cleaning barrel 706, of the outer side surface of the second cleaning barrel 709, and a second bearing 712 which is matched with the second cleaning barrel 709 is arranged at the inner side surface of the water retaining ring 718; a speed reducer 713 matched with the first conveying roller 704 is arranged on the second cleaning barrel 709 close to the first cleaning barrel 706, and a connecting rod 716 fixedly connected with the second cleaning barrel 709 is arranged at the output end of the speed reducer 713; the second cleaning barrel 709 is divided into an air inlet part 719 and a drying part 720, the second cleaning barrel shell of the air inlet part 719 is of a hollow structure communicated with the air inlet pipe ring 708, and a water outlet hole is formed in the second cleaning barrel shell of the drying part 720; a second conveying plate in a spiral structure is circumferentially arranged on the inner side surface of the second cleaning barrel 708, the second conveying plate is divided into an air inlet part conveying plate 715 and a spin-drying part conveying plate 714, the inside of the air inlet part conveying plate 715 is in a hollow structure communicated with the second cleaning barrel shell of the air inlet part 719, and at least one air outlet is formed in the air inlet part conveying plate 715; the pipe diameter of the second cleaning barrel 709 is gradually reduced along the direction far away from the axis of the first cleaning barrel 706, an inclined slope is arranged on the inner side surface of the cleaning barrel 703 matched with the second cleaning barrel 709, the inclined slope is parallel to the outer inclined surface of the second cleaning barrel 709, and a second water collecting area 711 is formed by the area between the cleaning slope and the water retaining ring 718.

In a real-time mode, the mammary gland drainage bag is sorted by the sorting mechanism 10, impurities in the mammary gland drainage bag are removed, the mammary gland drainage bag is sent into the crushing module 6 of the solid treatment module 3 through the conveying mechanism 2, the drainage bag is crushed under the action of the cutter roller, drainage liquid in the drainage bag is released after the drainage bag is crushed, then the drainage liquid enters the first cleaning barrel 706 in the cleaning module 7 through the discharge opening, the first conveying roller 704 in the first cleaning barrel 706 is driven by the second motor to rotate to convey crushed plastic particles to the second cleaning barrel 709, the plastic particles are cleaned by the high-pressure first nozzle 710 in the conveying process to flush body fluid, generated sewage is sent into the sewage treatment module 5 through the waste liquid pipe 4 to be subjected to harmless treatment, the steam generator works, high-temperature and high-pressure steam generated by the steam generator enters the air inlet part conveying plate of the air inlet part 719 of the second cleaning barrel 709 through the conveying pipeline and is discharged into the air inlet part 719 through the air outlet, the plastic particles after being flushed by the high-pressure water flow enters the air inlet part conveying plate of the second cleaning barrel 709 through the waste liquid pipe 4, the high-temperature and high-pressure water steam enters the lower cleaning part conveying roller 719, the lower cleaning barrel 720, the water collecting barrel 706, and is collected by the lower centrifugal force of the second cleaning water collecting barrel 706, and the high-collecting zone 706, and the high-pressure water collecting zone 706, and the high-speed water collecting zone 704 is collected by the high-collecting zone 706 through the high-pressure water-speed plastic particles 704.

The sterilization module 8 comprises a supporting seat, a sterilization tank 803 is arranged on the supporting seat, a protective cover 802 is arranged on the outer side of the sterilization tank 803 along the circumference, and a discharge hole 801 is formed in the end, close to the supporting seat, of the sterilization tank 803; a feeding module 804 arranged on the disinfection tank 803 far away from the end of the discharge port 801, the feeding module 804 comprises a feeding port 806 communicated with the conveying mechanism 2, the feeding port 806 is a cylindrical pipeline, a first flange is arranged on the outer side surface of the feeding port 806 near the end of the conveying mechanism 2, an air inlet pipe orifice 807 communicated with the steam generator is arranged on the outer side surface of the feeding port 806, the air inlet pipe orifice 807 is provided with two air inlets, the section of the inner side surface of the air inlet pipe orifice 807 in the parallel direction along the axis of the feeding port 806 is trapezoidal, the inner diameter of the air inlet pipe orifice 807 is the same at the front section part of the feeding port 806, then the inner diameter of the air inlet pipe orifice 807 is gradually reduced along the axis of the feeding port 806, a main air passage is formed in the area between the feeding port 806 and the inner side surface of the air inlet pipe orifice 807, a first air inlet 810 in an inclined state is arranged on the pipe body of the feeding port 807, an area on the feeding port 806 far away from the first flange end and the inner side surface of the air inlet pipe orifice 807 forms an air-solid mixing area 808, the inner diameter of the air inlet pipe orifice 807 extends for a certain distance along the axis to form a mixing discharge port 809, and a mixing discharge port 809 is arranged on the end near the end 808; the feed inlet 806 is provided with an air baffle plate connected with the scattering mechanism 812, the area between the air baffle plate and the air inlet pipe orifice 807 forms a scattering air channel 811 communicated with the scattering mechanism 812, and the scattering air channel 811 is communicated with an air inlet.

A disinfection mechanism 805 communicated with a mixed discharge port 809 is arranged in the disinfection tank 803; the disinfection mechanism 805 comprises a spiral material pipe 813, the material pipe 813 comprises a pipe shell, the pipe shell comprises a protective layer 815 made of transparent materials, the protective layer 815 is provided with two layers, a transparent heat-preservation coating is coated on the outer protective layer 815, and an inert gas layer 186 is arranged between the protective layers 815; the inner side surface of the material pipe 813 is circumferentially provided with a reflecting collision block 816, the reflecting collision block 816 is hemispherical, the reflecting collision block 816 is provided with at least one small pit, the surface of the small pit is hemispherical, a second scattering mechanism 817 fixed with a protective layer 815 is arranged in the material pipe 813, the second scattering mechanism 817 comprises a collision plate 818 connected with the protective layer 815, the included angle between the collision plate 818 and the protective layer 815 is an acute angle, the second scattering mechanism 817 is made of transparent materials, the outer surface of the second scattering mechanism 817 is provided with a scattering pit, the X-ray generator 814 matched with the material pipe 813 is further included, the X-ray generator 814 comprises at least one electron source, and the orientation of the X-rays of the electron source is distributed in a spiral ring shape matched with the material pipe 813.

In a real-time mode, after being cleaned by the cleaning module 7, the cleaning module is conveyed into the sterilization module 8 through the conveying mechanism 2, high-temperature and high-pressure steam generated by the steam generator enters the feeding module 804 through the air inlet pipe orifice 807, plastic particles enter the feeding module 804 through the feeding hole 806, the high-temperature, high-pressure and high-speed steam is mixed with the plastic particles in the gas-solid mixing zone 808 through the main air passage and the first air inlet 810, then the materials are fully mixed by gas-solid under the action of the scattering mechanism 812, the gas-solid mixture enters the spiral material pipe 813 of the sterilization mechanism 805 through the mixing discharge hole 809, high-energy rays generated by the X-ray generator 814 irradiate on the plastic particles to kill germs on the plastic particles, meanwhile, the high-temperature steam also kills the germs to improve the killing effect, the plastic particles collide with the reflection collision block 819 and the second reflection collision block 817 when moving in the material pipe 813, so that the plastic particles are not gathered, and simultaneously the plastic particles are turned over constantly, and the reflection block is coated with an X-ray reflective film, thereby increasing the sterilization effect.

The decoloring module 9 comprises an organic solvent decoloring tank 902, and the organic solvent decoloring tank 902 is communicated with a decoloring cleaning device 919; comprises a water-based and semi-water-based decoloring tank 912 communicated with a decoloring cleaning device 919, wherein the water-based and semi-water-based decoloring tank 912 is communicated with the decoloring cleaning device 919; the device also comprises a lipase type water-based decoloring tank 915 communicated with the decoloring cleaning device 919, a second decoloring cleaning device 920 communicated with the lipase type water-based decoloring tank 915, and a solid-liquid separator communicated with the organic solvent decoloring tank 902, the water-based and semi-water-based decoloring tanks 912 and the lipase type water-based decoloring tank 915.

The organic solvent decoloring tank 902 comprises a support leg 901, a tank body is arranged on the support leg 901, a particle feeding pipe 907 communicated with a discharge port 801 is arranged on the outer side surface of the tank body, an electromagnetic valve 906 is arranged on the particle feeding pipe 907, and an adjusting valve 905 is arranged on the outer side surface of the tank body; an organic solvent feed port 904 is arranged on the outer side surface of the tank body, a meter connected with the control module is arranged on the organic solvent feed port 904, and an organic solvent discharge port 901 communicated with the decoloring cleaning device 919 is also arranged; a stirring motor 908 connected with the control module is arranged at the top of the tank body, stirring blades 909 matched with the stirring motor 908 are arranged in the tank body, and a particulate matter concentration sensor 903, a temperature sensor and a pressure sensor connected with the control module are arranged on the inner side surface of the tank body; the water-based and semi-water-based decoloration tank 912 is provided with a second particle feeding pipe 911 communicated with the decoloration cleaning device 919, a water-based and semi-water-based solvent feeding pipe 913 and a water-based and semi-water-based decoloration tank discharge port 914 communicated with the decoloration cleaning device 919.

A third particle feeding pipe 916 communicated with the decoloring and cleaning device 919 is arranged on the lipase type water-based decoloring tank 915, a lipase type water-based solvent feeding pipe 917 is also arranged on the lipase type water-based decoloring tank, and a discharging hole 918 of the lipase type water-based decoloring tank connected with the second decoloring and cleaning device 920 is also arranged on the tank body; the structure of the decoloring cleaning device 919 is the same as that of the first cleaning barrel 706 of the cleaning module 7, and the second decoloring cleaning device 920 comprises a cleaning unit with the same structure as that of the decoloring cleaning device 919 and a drying unit matched with the cleaning unit; the sorting mechanism 10 comprises a conveying belt, a protective cover is arranged on the conveying belt, a sorting manipulator is arranged on one side of the conveying belt, and a 3D recognition module is arranged on the manipulator.

In a real-time mode, plastic particles treated by the disinfection module 8 are sent into an organic solvent decoloration tank 902 for decoloration treatment, the plastic particles are sent into a decoloration cleaning device 919 for cleaning after decoloration treatment, then the generated sewage is sent into a sewage treatment module 5 for treatment, then the plastic particles are sent into a water-based and semi-water-based decoloration tank 912 for decoloration treatment again, the plastic particles are sent into the decoloration cleaning device 919 for cleaning after decoloration treatment, then the generated sewage is sent into a sewage treatment module 5 for treatment, finally the plastic particles are sent into a lipase type water-based decoloration tank 915 for decoloration treatment, the plastic particles are sent into a second decoloration cleaning device 920 for cleaning after decoloration treatment, then the generated sewage is sent into the sewage treatment module 5 for treatment, and finally the dry plastic particles are obtained through treatment of a drying unit.

Example two

As shown in fig. 17, compared with the embodiment 1, in the environmental protection treatment system for mammary gland drainage bag, a high-speed ozone generator is connected to another air inlet pipe orifice 807 of the feeding module 804 in the disinfection module 8, a kneading mechanism is arranged in the organic solvent decoloring tank 902, the water-based and semi-water-based decoloring tank 912 and the lipase-type water-based decoloring tank 915, the kneading mechanism comprises an active kneading ball 922 matched with the stirring motor 908, the active kneading ball 922 is in an ellipsoid shape, a spiral flexible protrusion is arranged on the outer side surface of the active kneading ball 922, a passive friction body 921 matched with the active kneading ball 922 is arranged on the inner side surface of the tank body, and a spiral flexible groove matched with the flexible protrusion is arranged on the inner side surface of the passive friction body 921.

In a real-time mode, after being cleaned by a cleaning module 7, the cleaning fluid is conveyed into a sterilization module 8 through a conveying mechanism 2, high-temperature and high-pressure steam generated by a steam generator enters a feeding module 804 through an air inlet pipe orifice 807, ozone generated by an ozone generator enters the feeding module 804 through the air inlet pipe orifice 807, plastic particles enter the feeding module 804 through a feeding port 806, the high-temperature, high-pressure and high-speed steam and the plastic particles are mixed in a gas-solid mixing zone 808 through a main air passage and a first air inlet 810, the high-speed ozone is mixed with the plastic particles through a scattering air passage 811, then the materials are fully gas-solid mixed under the action of a scattering mechanism 812, a gas-solid mixture enters a spiral material pipe 813 of the sterilization mechanism 805 through a mixing discharge port 809, and high-energy rays generated by an X-ray generator 814 irradiate on the plastic particles to kill germs on the plastic particles, meanwhile, high-temperature water vapor also kills germs to improve the killing effect, plastic particles collide with the reflecting collision block 819 and the second scattering collision block 817 when moving in the material pipe 813, so that the plastic particles are not gathered and are continuously turned over, an X-ray reflective film is coated on the reflecting collision block 819 to enable X-rays to generate diffuse reflection and increase the sterilization effect, ozone performs primary decolorization treatment on the plastic particles during disinfection, the plastic particles treated by the disinfection module 8 are sent into the organic solvent decolorization tank 902 to be decolorized, the plastic particles after being decolorized are sent into the decolorization cleaning device 919 to be cleaned, the generated sewage is sent into the sewage treatment module 5 to be treated, then the sewage is sent into the water-based and semi-water-based decolorization tanks 912 again to be decolorized, the plastic particles after being decolorized are sent into the decolorization cleaning device 919 to be cleaned, and then the generated sewage is sent to a sewage treatment module 5 for treatment, finally, the plastic particles are sent to a lipase type water-based decoloring tank 915 for decoloring treatment, the decolored sewage is sent to a second decoloring and cleaning device 920 for cleaning, then the generated sewage is sent to the sewage treatment module 5 for treatment, when the materials enter an organic solvent decoloring tank 902, a water-based and semi-water-based decoloring tank 912 and the lipase type water-based decoloring tank 915 for decoloring treatment, a stirring motor 908 drives an active kneading ball 922 to rotate, and when the plastic particles move to a region between the active kneading ball 922 and a passive friction body 921, the plastic particles are rubbed with each other and between the plastic particles and the flexible protrusions under the action of the flexible protrusions, so that the decoloring treatment effect is better, and finally, the dried plastic particles are obtained through the treatment of a drying unit.

EXAMPLE III

a. the mammary gland drainage bags are sorted by the sorting mechanism 10 and then are sent into the crushing module 6 by the conveying mechanism 2;

b. the crushing module 6 cuts and crushes the drainage bag, water is sprayed to reduce dust and pre-clean the drainage bag during crushing, the crushed drainage bag is cleaned through the cleaning module 7, sewage is sent into the sewage treatment module 5 through the waste liquid pipe 4 to be subjected to environmental protection treatment, and crushed particles are sent into the disinfection module 8 through the conveying mechanism 2;

c. irradiating the material pipe 813 by the X-ray generator 814 in the sterilizing module 8, wherein the material passes through the material pipe 813 by 1.5 m to 2.5 m per second, the electron energy of the X-ray generator 814 is 240 kilovolts to 290 kilovolts, and the plastic particles in the material pipe 813 are exposed to the radiation amount of 45-55 kilograys, preferably 46-53 kilograys;

d. the material treated by the disinfection module 8 is sent into a decolorization module 9 for decolorization, when an organic solvent decolorization tank 902 is decolorized, an organic ink cleaning agent mixed by 35-45% of absolute ethyl alcohol, 25-30% of dichloromethane, 28-35% of tetrachloroethylene, 0.5-1.2% of antioxidant and 0.1-0.8% of corrosion inhibitor is adopted to dissolve organic pigment on plastic, meanwhile, a stirring fan blade 909 is used for stirring plastic particles to accelerate the dissolution speed, the stirring speed is 1-3 cubic meters per second, the stirring time is 48-96 hours, the PH value is controlled between 6 and 10, after decolorization is finished, the organic ink and the plastic particles are separated by a solid-liquid separator, the organic ink cleaning agent flows back into the organic solvent tank 902, the plastic particles enter a decolorization cleaning device 919 for cleaning, and after cleaning, the plastic particles are sent into a water-based and semi-water-based decolorization tank 912;

e. when the water-based and semi-water-based decoloration tanks 912 are decolored, 4-7% of lipase polyoxyethylene ether, 2-3% of alkylphenol polyoxyethylene ether, 3-7% of surfactant, 0.5-1.5% of triethanolamine, 12-25% of semi-water-based ink cleaning agent mixed by kerosene and water are adopted to decolor the pigment on the plastic, meanwhile, stirring blades 909 are used for stirring the plastic particles to accelerate the dissolving speed, the stirring speed is 1-3 cubic meters per second, the decoloring time is 10-20 minutes, the pH value is controlled between 6-11, the temperature is controlled between 27-38 ℃, after the decoloration is finished, the semi-water-based ink is cleaned by a solid-liquid separator and separated from the plastic particles, the semi-water-based ink is cleaned and reflowed to the water-based and semi-water-based decoloration tanks 912 or enters a recovery tank, the plastic particles enter a cleaning device 919 for cleaning, and are cleaned and then sent to the lipase-based decoloration tank 915;

or the mass ratio is as follows: 1-3% of fatty alcohol-polyoxyethylene ether AEO-9,8-12% of fatty alcohol-polyoxyethylene ether sulfate AES,0.5-2% of benzotriazole, 0.5-1.5% of triethanolamine, 0.5-1.5% of sodium silicate, 1-3% of urea, 1-5% of sodium chloride and the balance of water to form a water-based ink cleaning agent, wherein the decoloring time is 10-20 minutes, the pH value is controlled to be 6-11, and the temperature is controlled to be 27-38 ℃; after the decolorization is finished, separating the water-based ink cleaning agent from the plastic particles through a solid-liquid separator, refluxing the water-based ink cleaning agent into the water-based and semi-water-based decolorization tank 912 or entering a recovery tank, washing the plastic particles in a decolorization washing device 919, and sending the washed plastic particles into a lipase type water-based decolorization tank 915;

f. when the lipase type water-based decoloration tank 915 is used for decoloration treatment, the ratio of the mass fraction is as follows: 0.1-0.6% of lipase, 71-92% of AEO, 6-8% of AES, 1-3% of benzotriazole, 1-2.5% of urea, 0.5-1.5% of triethanolamine, 1-3.5% of sodium carbonate, 3-7% of ethanol, 0.1-0.6% of defoamer and water are added to 100% to form the lipase type water-based ink cleaning agent, the decoloring time is 2-5 hours, the pH value is controlled to be 5-10, and the stirring speed is 1-2 cubic meters per second; after the decolorization is finished, the lipase type water-based ink cleaning agent and the plastic particles are separated through the solid-liquid separator, the lipase type water-based ink cleaning agent flows back to the lipase type water-based decolorization tank 915 or enters the recovery tank, the plastic particles enter the second decolorization cleaning device 920 for cleaning, sewage generated in the cleaning process is sent to the sewage treatment module 5 for treatment, and after the cleaning is finished, the drying unit is used for drying, and the dried plastic particles are stored for recycling.

In a real-time manner, the drainage bag is processed through the following process: a. the mammary gland drainage bags are sorted by the sorting mechanism 10 and then are sent into the crushing module 6 by the conveying mechanism 2;

b. the crushing module 6 cuts and crushes the drainage bag, water is sprayed to reduce dust and the drainage bag is pre-cleaned while crushing, the crushed drainage bag is cleaned through the cleaning module 7, sewage is sent into the sewage treatment module 5 through the waste liquid pipe 4 to be subjected to environment-friendly treatment, and crushed particles are sent into the disinfection module 8 through the conveying mechanism 2;

c. irradiating the material pipe 813 by the X-ray generator 814 in the sterilization module 8, wherein the material passes through the material pipe 813 at 2 meters per second, the electron energy of the X-ray generator 814 is 260 kilovolts, and the plastic particles in the material pipe 813 are exposed to 49 kilogray radiant quantity;

d. the material treated by the disinfection module 8 is sent into a decolorization module 9 for decolorization, when an organic solvent decolorization tank 902 is decolorized, an organic ink cleaning agent mixed by 41 mass percent of absolute ethyl alcohol, 26 mass percent of dichloromethane, 1 mass percent of sorbitan fatty acid ester, 31 mass percent of tetrachloroethylene, 0.9 mass percent of antioxidant, 0.1 mass percent of corrosion inhibitor and trace essence is adopted to dissolve organic pigment on plastic, meanwhile, a stirring fan blade 909 is used for stirring plastic particles to accelerate the dissolution speed, the stirring speed is 2 cubic meters per second, the stirring time is 72 hours, the PH value is controlled between 6 and 10, after decolorization is finished, the cleaning agent separates the organic ink cleaning agent from the plastic particles through a solid-liquid separator, the organic ink reflows to the organic solvent decolorization tank 902, the plastic particles enter a decolorization cleaning device 919 for cleaning, and after cleaning, the plastic particles are sent into a water-based and semi-aqueous-based decolorization tank 912;

e. when the water-based and semi-water-based decoloration tanks 912 are decolored, semi-water-based ink cleaning agent mixed by 6% of lipase polyoxyethylene ether, 2.5% of alkylphenol polyoxyethylene ether, 6.5% of surfactant, 1.1% of triethanolamine, 15% of kerosene and water is adopted to decolor the pigment on the plastic, meanwhile, stirring fan blades 909 are used for stirring the plastic particles to accelerate the dissolving speed, the stirring speed is 1-3 cubic meters per second, the decoloring time is 16 minutes, the PH value is controlled between 6 and 11, the temperature is controlled at 36 ℃, after the decoloration is finished, semi-water-based ink is cleaned and separated from the plastic particles through a solid-liquid separator, the semi-water-based ink is cleaned and reflowed to the water-based and semi-water-based decoloration tanks 912 or enters a recovery tank, the plastic particles enter a decoloration cleaning device 919 for cleaning, and are cleaned and then sent to the lipase-based decoloration tank 915;

or the mass ratio is as follows: 1.5 percent of fatty alcohol-polyoxyethylene ether AEO-9, 10 percent of fatty alcohol-polyoxyethylene ether sulfate AES,0.5 percent of benzotriazole, 0.8 percent of triethanolamine, 1.2 percent of sodium silicate, 2.5 percent of urea, 3 percent of sodium chloride and the balance of water are mixed to form the water-based ink cleaning agent, the decoloring time is 10-20 minutes, the PH value is controlled between 6 and 11, and the temperature is controlled between 27 ℃ and 38 ℃; after the decoloration is finished, separating a water-based ink cleaning agent from plastic particles through a solid-liquid separator, refluxing the water-based ink cleaning agent to a water-based and semi-water-based decoloration tank 912 or entering a recovery tank, washing the plastic particles in a decoloration washing device 919, and sending the washed plastic particles into a lipase-based decoloration tank 915;

f. when the lipase type water-based decoloring tank 915 is used for decoloring, the lipase type water-based decoloring tank adopts the following components in percentage by mass: 0.5 percent of lipase, 80 percent of AEO, 7 percent of AES, 1.5 percent of benzotriazole, 1.5 percent of urea, 1 percent of triethanolamine, 2 percent of sodium carbonate, 6 percent of ethanol, 0.2 percent of defoaming agent and water are added to 100 percent of the mixture to form the lipase type water-based ink cleaning agent, the decoloring time is 3.5 hours, the PH value is controlled between 5 and 10, and the stirring speed is 1 to 2 cubic meters per second; after the decoloration is finished, the lipase type water-based ink cleaning agent and the plastic particles are separated through the solid-liquid separator, the lipase type water-based ink cleaning agent flows back to the lipase type water-based decoloration tank 915 or enters the recovery tank, the plastic particles enter the second decoloration cleaning device 920 for cleaning, sewage generated in the cleaning process is sent to the sewage treatment module 5 for treatment, the cleaning is finished, the drying unit is used for drying, and then the dried plastic particles are stored for recovery and reuse.

While the invention has been described with reference to specific embodiments, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention.

Claims

1. The utility model provides a mammary gland drainage bag environmental protection processing system, includes letter sorting mechanism and control module, is equipped with rubbing crusher structure in letter sorting mechanism exit, and rubbing crusher structure is linked together through conveying mechanism and solid treatment module, still is linked together its characterized in that through waste liquid pipe and sewage treatment module: the crushing mechanism comprises a crushing module and a cleaning module, a conveying mechanism is arranged on the cleaning module, a solid treatment module is arranged at the end, far away from the crushing mechanism, of the conveying mechanism, and the solid treatment module comprises a disinfection module and a decoloration module.

2. The environment-friendly treatment system for the breast drainage bag according to claim 1, wherein: the crushing mechanism comprises a crushing mechanism shell, a feed inlet communicated with the sorting mechanism is formed in the crushing mechanism shell, a crushing module is arranged in the crushing mechanism shell and comprises two cutter rollers matched with each other, a crushing motor connected with the crushing module is arranged on the crushing mechanism shell and connected with a control module, a feed opening matched with the crushing module is formed in the crushing mechanism shell, a cleaning module is arranged on the feed opening, and the steam generator communicated with the crushing mechanism is further included.

3. The environment-friendly treatment system for the breast drainage bag according to claim 2, wherein: the cleaning module comprises a second motor connected with the shell of the crushing mechanism; the cleaning device also comprises a cleaning barrel matched with the feed opening, a coupling matched with the second motor is arranged on the cleaning barrel, a cleaning feed opening communicated with the feed opening is arranged on the cleaning barrel, and the projection of the cleaning barrel on the section vertical to the axis is U-shaped; the cleaning device comprises a cleaning barrel, a first cleaning barrel and a second cleaning barrel, wherein the first cleaning barrel and the second cleaning barrel are coaxially arranged, at least one high-pressure first nozzle is arranged on the inner side surface of the first cleaning barrel, a hole convenient for water to pass through is formed in the first cleaning barrel, a first water collecting area is formed between the outer side surface of the first cleaning barrel and the cleaning barrel, a first conveying roller matched with a coupler is arranged in the first cleaning barrel, and a first conveying plate is arranged on the first conveying roller.

4. The environment-friendly treatment system for the breast drainage bag according to claim 3, wherein: an air inlet pipe ring which is matched with the cleaning barrel in a rolling way is arranged on the outer side surface of the second cleaning barrel, which is close to the first cleaning barrel end, a first bearing which is matched with the air inlet pipe ring is arranged on the cleaning barrel, an air inlet pipe is arranged on the air inlet pipe ring, the air inlet pipe ring is fixedly connected and communicated with the second cleaning barrel, a water retaining ring which is fixedly connected with the cleaning barrel is arranged on the outer side surface of the second cleaning barrel, which is far away from the first cleaning barrel end, and a second bearing which is matched with the second cleaning barrel is arranged on the inner side surface of the water retaining ring; a speed reducer matched with the first conveying roller is arranged on the second cleaning barrel close to the first cleaning barrel, and a connecting rod fixedly connected with the second cleaning barrel is arranged at the output end of the speed reducer; the second cleaning barrel is divided into an air inlet part and a spin-drying part, a second cleaning barrel shell of the air inlet part is of a hollow structure communicated with the air inlet pipe ring, and a water outlet hole is formed in the second cleaning barrel shell of the spin-drying part; a second conveying plate in a spiral structure is arranged on the inner side surface of the second cleaning barrel along the circumference, the second conveying plate is divided into an air inlet part conveying plate and a spin-drying part conveying plate, the interior of the air inlet part conveying plate is of a hollow structure communicated with the shell of the second cleaning barrel of the air inlet part, and at least one air outlet is formed in the air inlet part conveying plate; the pipe diameter of second washing bucket along keeping away from first washing bucket axis direction reduces gradually, is equipped with slope surface with second washing bucket matched with washing bucket medial surface, and slope surface parallels with the outside inclined plane of second washing bucket, washs the regional second water-collecting area that constitutes between domatic and the manger plate ring.

5. The environment-friendly treatment system for the breast drainage bag according to claim 4, wherein: the sterilization module comprises a supporting seat, a sterilization tank is arranged on the supporting seat, a protective cover is arranged on the outer side of the sterilization tank along the circumference, and a discharge hole is formed in the sterilization tank close to the supporting seat; the sterilizing tank is provided with a feeding module far away from the end of the discharge port, the feeding module comprises a feeding port communicated with a conveying mechanism, the feeding port is a cylindrical pipeline, a first flange is arranged on the outer side surface of the feeding port, which is close to the end of the conveying mechanism, an air inlet pipe orifice communicated with a steam generator is arranged on the outer side surface of the feeding port, two air inlets are arranged on the air inlet pipe orifice, the cross section of the inner side surface of the air inlet pipe orifice in the parallel direction along the axis of the feeding port is trapezoidal, the inner diameters of the air inlet pipe orifices are the same at the front section of the feeding port, then the inner diameters of the air inlet pipe orifices are gradually reduced along the axis of the feeding port, a main air passage is formed in the area between the feeding port and the inner side surface of the air inlet pipe orifice, a first air inlet in an inclined state is arranged on the pipe body of the feeding port, a gas-solid mixing area is formed in the area far away from the end of the first flange and the inner side surface of the air inlet pipe orifice, a section extends for a distance along the axis to form a mixing discharge port, and a scattering mechanism is arranged on the mixing port, and the end, which is close to the mixing port; the air baffle plate connected with the scattering mechanism is arranged on the feeding hole, a scattering air passage communicated with the scattering mechanism is formed in the area between the air baffle plate and the air inlet pipe opening, and the scattering air passage is communicated with an air inlet.

6. The environment-friendly treatment system for the breast drainage bag according to claim 5, wherein: a disinfection mechanism communicated with the mixed discharge port is arranged in the disinfection tank; the disinfection mechanism comprises a spiral material pipe, the material pipe comprises a pipe shell, the pipe shell comprises a protective layer made of transparent materials, the protective layer comprises two layers, a transparent heat-preservation coating is coated on the outer protective layer, and an inert gas layer is arranged between the protective layers; the material pipe is characterized in that a reflective collision block is arranged on the inner side surface of the material pipe along the circumference and is hemispherical, at least one small pit is arranged on the reflective collision block, the surface of the small pit is hemispherical, a second scattering mechanism fixed with a protective layer is arranged in the material pipe, the second scattering mechanism comprises a collision plate connected with the protective layer, the included angle between the collision plate and the protective layer is an acute angle, the second scattering mechanism is made of transparent materials, a scattering pit is arranged on the outer surface of the second scattering mechanism, the material pipe further comprises an X-ray generator matched with the material pipe, at least one electron source is contained in the X-ray generator, and the orientation of the X-rays of the electron source is spirally and annularly distributed with the material pipe.

7. The environment-friendly treatment system for the breast drainage bag according to claim 6, wherein: the decoloring module comprises an organic solvent decoloring tank, and the organic solvent decoloring tank is communicated with a decoloring cleaning device; comprises a water-based and semi-water-based decoloring tank communicated with a decoloring cleaning device, wherein the water-based and semi-water-based decoloring tank is communicated with the decoloring cleaning device; the device also comprises a lipase type water-based decoloring tank communicated with the decoloring cleaning device, a second decoloring cleaning device communicated with the lipase type water-based decoloring tank, and a solid-liquid separator communicated with the organic solvent decoloring tank, the water-based and semi-water-based decoloring tanks and the lipase type water-based decoloring tank.

8. The environment-friendly treatment system for the breast drainage bag according to claim 7, wherein: the organic solvent decoloring tank comprises supporting legs, a tank body is arranged on the supporting legs, a particle feeding pipe communicated with a discharging port is arranged on the outer side surface of the tank body, an electromagnetic valve is arranged on the particle feeding pipe, and an adjusting valve is arranged on the outer side surface of the tank body; an organic solvent feed port is arranged on the outer side surface of the tank body, a meter connected with the control module is arranged on the organic solvent feed port, and an organic solvent discharge port communicated with the decoloring cleaning device is also arranged; a stirring motor connected with the control module is arranged at the top of the tank body, stirring blades matched with the stirring motor are arranged in the tank body, and a particulate matter concentration sensor, a temperature sensor and a pressure sensor which are connected with the control module are arranged on the inner side surface of the tank body; the water-based and semi-water-based decoloring tank is provided with a second particle feeding pipe communicated with the decoloring cleaning device, a water-based and semi-water-based solvent feeding pipe and a water-based and semi-water-based decoloring tank discharge port communicated with the decoloring cleaning device.

9. The environment-friendly treatment system for the breast drainage bag according to claim 8, wherein: the lipase type water-based decoloring tank is provided with a third particulate matter feeding pipe communicated with the decoloring cleaning device, a lipase type water-based solvent feeding pipe, and a discharge hole of the lipase type water-based decoloring tank connected with the second decoloring cleaning device; the structure of the second decoloring and cleaning device comprises a cleaning unit with the same structure as that of the decoloring and cleaning device and a drying unit matched with the cleaning unit; the sorting mechanism comprises a conveying belt, a protective cover is arranged on the conveying belt, a sorting manipulator is arranged on one side of the conveying belt, and a 3D recognition module is arranged on the manipulator.

10. An environmentally friendly treatment method with a breast drainage bag according to any of the preceding claims, comprising the steps of:

b. the crushing module cuts and crushes the drainage bag, water is sprayed to reduce dust and the drainage bag is pre-cleaned while crushing, the crushed drainage bag is cleaned through the cleaning module, sewage is sent into the sewage treatment module through the waste liquid pipe to be subjected to environment-friendly treatment, and crushed particles are sent into the disinfection module through the conveying mechanism;

d. the material treated by the disinfection module is sent into a decoloring module for decoloring, when an organic solvent decoloring tank is used for decoloring, an organic ink cleaning agent mixed by 35-45% of absolute ethyl alcohol, 25-30% of dichloromethane, 28-35% of tetrachloroethylene, 0.5-1.2% of antioxidant and 0.1-0.8% of corrosion inhibitor is adopted to dissolve organic pigment on plastic, meanwhile, stirring blades are used for stirring plastic particles to accelerate the dissolving speed, the stirring speed is 1-3 cubic meters per second, the stirring time is 48-96 hours, the PH value is controlled between 6-10, after decoloring, the organic ink cleaning agent and the plastic particles are separated by a solid-liquid separator, the organic ink cleaning agent flows back into the organic solvent decoloring tank, the plastic particles enter a decoloring cleaning device for cleaning, and after cleaning, the plastic particles are sent into a water-based and semi-water-based decoloring tank;

e. when the water-based and semi-water-based decoloration tanks are decolored, 4-7% of lipase polyoxyethylene ether, 2-3% of alkylphenol polyoxyethylene ether, 3-7% of surfactant, 0.5-1.5% of triethanolamine, 12-25% of semi-water-based ink cleaning agent mixed by kerosene and water are adopted to decolor the pigment on the plastic, meanwhile, stirring fan blades are used for stirring plastic particles to accelerate the dissolving speed, the stirring speed is 1-3 cubic meters per second, the decoloring time is 10-20 minutes, the pH value is controlled between 6-11, the temperature is controlled between 27-38 ℃, after the decoloration is finished, the semi-water-based ink is cleaned by a solid-liquid separator and separated from the plastic particles, the semi-water-based ink is cleaned and refluxed into the water-based and semi-water-based tanks or enters a recovery tank, the plastic particles enter a decoloration cleaning device for cleaning, and are cleaned and then sent into the lipase-based decoloration tank;

or the mass ratio is as follows: 1-3% of fatty alcohol-polyoxyethylene ether, 8-12% of fatty alcohol-polyoxyethylene ether sulfate, 0.5-2% of benzotriazole, 0.5-1.5% of triethanolamine, 0.5-1.5% of sodium silicate, 1-3% of urea, 1-5% of sodium chloride and the balance of water to form a water-based ink cleaning agent, wherein the decoloring time is 10-20 minutes, the pH value is controlled to be 6-11, and the temperature is controlled to be 27-38 ℃; separating the water-based ink cleaning agent from the plastic particles through a solid-liquid separator after the decolorization is finished, refluxing the water-based ink cleaning agent into a water-based decolorization tank and a semi-water-based decolorization tank or entering a recovery tank, washing the plastic particles in a decolorization washing device, and sending the plastic particles into a lipase-type water-based decolorization tank after the plastic particles are washed;

f. when the lipase type water-based decoloration tank is used for decoloration treatment, the ratio of the mass fraction is as follows: 0.1-0.6% of lipase, 71-92% of AEO, 6-8% of AES, 1-3% of benzotriazole, 1-2.5% of urea, 0.5-1.5% of triethanolamine, 1-3.5% of sodium carbonate, 3-7% of ethanol, 0.1-0.6% of defoamer and deionized water are added to 100% of the mixed lipase type water-based ink cleaning agent, the decoloring time is 2-5 hours, the pH value is controlled to be 5-10, and the stirring speed is 1-2 cubic meters per second; and after the decoloration is finished, separating the lipase type water-based ink cleaning agent from the plastic particles through a solid-liquid separator, refluxing the lipase type water-based ink cleaning agent into a lipase type water-based decoloration tank or entering a recovery tank, washing the plastic particles in a second decoloration washing device, sending sewage generated in the washing process into a sewage treatment module for treatment, drying the plastic particles through a drying unit after the washing is finished, and storing the dried plastic particles for recycling.