Continuous element decontamination and sterilization system
By designing a purification and sterilization system with multiple operating rooms and transition rooms, and utilizing a conveyor system to continuously transfer containers, the problems of variability and resource waste in the sterilization process were solved, achieving a highly efficient sterilization process and resource conservation.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- 埃尔南·马佐斯基
- Filing Date
- 2021-10-29
- Publication Date
- 2026-06-02
AI Technical Summary
Existing sterilization systems suffer from variability in the sterilization process, resulting in low productivity, resource waste, and high energy consumption, and are unable to achieve continuous or semi-continuous element processing.
A purification and sterilization system comprising multiple operating chambers and transition chambers was designed. Containers are continuously transported via a conveyor system, and conditions are regulated using multiple transition chambers to ensure that each operating chamber maintains a stable physicochemical environment, thereby reducing energy loss and resource waste.
It achieves a more efficient sterilization process, reduces system downtime, increases productivity, reduces energy and resource consumption, and enables continuous or semi-continuous element processing.
Smart Images

Figure CN116472070B_ABST
Abstract
Description
Technical Field
[0001] This invention generally relates to the purification and / or sterilization and / or physicochemical treatment of elements and / or devices used in the medical industry. More specifically, it pertains to the purification and / or sterilization and / or physicochemical treatment of elements and / or medical devices found in hospitals, pharmaceutical industries, biotechnology industries, or research laboratories. Furthermore, this invention is not limited to this application and is also applicable to the food industry, chemical industry, purification of biological waste, and curing of polymers, rubbers, and composite materials. Background Technology
[0002] Most sterilization systems used in hospitals, laboratories, and other industries perform sterilization processes using a batch method. Depending on the machine's capacity, problematic elements are kept in a queue until there are enough elements to be processed within the same cycle parameters and the chamber's capacity is met.
[0003] The capacity of the chamber is directly related to the economics of performing the sterilization cycle; therefore, the number of elements in the queue must be a reasonable and economical quantity to continue the process. The productivity and idle time of these machines are directly related to the regulation and variation of the environmental conditions within the chamber and the elements within the chamber.
[0004] The aforementioned machines suffer from inherent sterilization process variability issues due to so-called "load weight," which is characterized by the distribution, type, and quantity of elements loaded into the chamber. Various attempts to improve upon these distribution and weight issues have been investigated and explored in previous patents.
[0005] One of the main factors users consider when selecting a sterilizer is the consumption of resources and waste, as this results in significant costs and ecological impacts. For example, a traditional autoclave requires the following steps to be performed on the overall volume of the chamber: purging air (vacuum), preheating, filling with steam, compensating for water loss and heat in the form of condensation, purging steam, reducing the temperature of the discharge fluid before it reaches the sewer (usually using cooling water), drying the wet elements, and cooling the interior. The preceding steps consume a large amount of energy in the form of heat and the mechanical work of the vacuum pump, with water in the form of steam acting as a coolant and creating a vacuum (water ring pump).
[0006] In patent EP0138688A2, the system refers to one or more baskets as flow guiding devices with fans to generate crossflow of gas or mixture. However, similar to existing technology and popular devices used in various industries, the device describes a chamber in which all elements and baskets are processed simultaneously under exactly the same circulation conditions. In fact, the main purpose of EP0138688A2 is to homogenize the processing conditions along all baskets in this embodiment.
[0007] Patent US20140301895A1 describes an in-line sterilizer with a conveyor that moves elements to be processed through chambers isolated by a sliding door system. This system does not demonstrate the concept of standardizing conditions using what we refer to as a transition chamber in our embodiments. A dwell chamber is mentioned, but it is used in a manner similar to what we refer to as a pre-conditioning chamber or post-conditioning chamber in our embodiments. Because a standardization or equalization chamber is not included, conditions in the different chambers cannot be kept constant during the processing and transport of elements.
[0008] Therefore, the elements to be sterilized cannot flow continuously or semi-continuously through the steps in the cycle without affecting the environment of each module. To enable the embodiment to perform as a continuous online sterilizer, the chamber needs to be adjusted, whereby the process allows the chamber door to be opened using the connecting modules. The aforementioned patent also limits the concept to the series connection of modules.
[0009] US Patent 4707334A relates to a sterilization system. This patent describes a chamber in which an atmosphere containing toxic vapors is established, the chamber being pneumatically isolated from the surrounding environment. This isolation technology allows objects to be sterilized, transported into, and removed from the chamber without any vapor leakage or air entering the chamber.
[0010] US4707334A is only applicable to sterilization processes that do not require pressure or low / medium vacuum. Therefore, its application is limited. Thus, an invention that overcomes the above-mentioned drawbacks is needed. Attached Figure Description
[0011] Figure 1 This is an overview of an embodiment of the working sequence of the method of the present invention.
[0012] Figure 2 This is a diagram showing multiple containers moving from the operating room to the transition room.
[0013] Figure 3This is a diagram showing multiple containers moving from the transition chamber to the operating chamber.
[0014] Figure 4 This refers to the configuration and arrangement of the system used in this invention.
[0015] Figure 5 This is an alternative configuration and arrangement of the system of the present invention.
[0016] Figure 6 This is an isometric perspective view of the transition chamber of the present invention.
[0017] Figure 7 This is a right view of the transition chamber of the present invention.
[0018] Figure 8 Is it like this? Figure 7 An enlarged view of the multiple transition chambers of the present invention is shown.
[0019] Figure 9 This is a front view of the transition chamber of the present invention.
[0020] Figure 10 This is a left view of the transition chamber of the present invention.
[0021] Figure 11 This is a rear view of the transition chamber of the present invention.
[0022] Figure 12 This is a top view of the transition chamber of the present invention.
[0023] Figure 13 This is a bottom view of the transition chamber of the present invention.
[0024] Figure 14 This is an isometric perspective view of the operating room of the present invention.
[0025] Figure 15 This is a right view of the operating room of the present invention.
[0026] Figure 16 Is it like this? Figure 15 An enlarged view of the various operating chambers of the present invention is shown.
[0027] Figure 17 This is a front view of the operating room of the present invention.
[0028] Figure 18 This is a left view of the operating room of the present invention.
[0029] Figure 19 This is a rear view of the operating room of the present invention.
[0030] Figure 20 This is a top view of the operator's compartment of the present invention.
[0031] Figure 21This is a bottom view of the operator's compartment of the present invention.
[0032] Figure 22 This is an isometric perspective view of one of the containers in the present invention.
[0033] Figure 23 This is a front view of one of the containers in the present invention.
[0034] Figure 24 This is a top view of one of the containers in the present invention.
[0035] Figure 25 This is a schematic diagram of the operating chamber sandwiched between the two transition chambers used in this invention.
[0036] Figure 26 It is an isometric perspective view of the container in the open configuration.
[0037] Figure 27 It is an isometric perspective view of a container in a closed configuration. Detailed Implementation
[0038] All figures in the accompanying drawings are intended to illustrate selected versions of the invention and not to limit the scope of the invention.
[0039] Reference Figures 1 to 24 This invention is a purification and disinfection system designed to perform various types of disinfection processes. The invention includes multiple operating chambers 3 and multiple transition chambers 2. A conveyor system 15 passes through each of the multiple operating chambers 3 and each of the multiple transition chambers 2. The element to be disinfected travels throughout the invention via the conveyor system 15. The element travels within a container 18, which travels through the arrangement and sequence of the operating chambers 3 and transition chambers 2. The internal conditions of each operating chamber 3 and each transition chamber 2 vary to perform specific processing stages, ensuring a complete disinfection cycle.
[0040] A preferred embodiment of the present invention includes a plurality of transition chambers 2, a plurality of operating chambers 3, a plurality of transition ports 4, a plurality of operating ports 8, at least one conveying system 15, and at least one container 18. The plurality of transition chambers 2 consist of an assembly of tubular structures that serve as waypoints between the various chambers of the system. The plurality of operating chambers consist of an assembly of chambers used to perform stages of the sterilization process. The plurality of transition ports 4 consist of an assembly of ports located on the transition chambers from the plurality of transition chambers 2. The transition ports 4 allow fluids and / or the like to enter and exit from the transition chambers of the present invention. The geometric profile of the transition ports 4 from the plurality of transition ports 4 is circular; however, this geometric profile can include any shape to meet manufacturing, design, and / or user requirements. Similarly, the plurality of operating ports 8 consist of an assembly of ports located on the operating chambers from the plurality of operating chambers 3. The operating ports allow fluids and / or the like to enter and exit from the operating chambers of the present invention. The geometric profile of the operating ports 8 from the plurality of operating ports 8 is circular; however, the geometric profile can include any shape to meet manufacturing, design, and / or user requirements. The conveying system 15 of the present invention is a continuous conveying system 15. The continuous conveying system 15 is a system in which an object placed at a starting point is continuously moved through the system until it reaches the end of a cycle, and this movement is sustained in time. For a preferred embodiment of the invention, the conveying system 15 is designed and arranged to match a configuration of multiple operating chambers 3 and multiple transition chambers 2. Therefore, the conveying system 15 is not limited to this configuration, as the accompanying drawings are intended to simply describe the invention and not to limit its scope. The container 18 used in the invention is a permeable container comprising a cylindrical profile. However, the invention is not limited to this geometry and may include any geometry that meets manufacturing, design, and / or user requirements. Each of the multiple operating chambers is connected between a preceding chamber 16 and a following chamber 17. As a result, the physicochemical conditions in the first operating chamber are isolated from the physicochemical conditions in the second operating chamber. Furthermore, the preceding chamber 16 and the following chamber 17 are derived from multiple transition chambers 2. This configuration allows the operating chambers 3 and transition chambers 2 to form a continuous sterilization unit in which a batch of contaminated items undergoes a series of physicochemical operations to sterilize the items. Furthermore, the configuration of multiple operating chambers 3 and multiple transition chambers 2 allows the present invention to isolate each operating chamber, ensuring that the conditions required for each operation are maintained at their optimal state for processing without any cross-exchange of physicochemical environmental characteristics used in any of the operating chambers 3. That is, the multiple transition chambers 2 serve as adjustment paths between the operating conditions of the multiple operating chambers 3. Additionally, any number of transition ports 37 are integrated into each of the multiple transition chambers 2, wherein the arbitrary number of transition ports 37 originate from multiple transition ports 4. As a result, the arbitrary number of transition ports 37 originating from the multiple transition ports 4 provide access points for controlling the environment of the transition chamber 2.Therefore, the transition port 4 allows the entry or exit of fluids and / or similar substances used in the sterilization cycle. Similarly, any plurality of operating ports 38 are integrated into each of the plurality of operating chambers 3, wherein any plurality of operating ports 38 originate from the plurality of operating ports 8. Thus, any plurality of operating ports 38 originating from the plurality of operating ports 8 provide access points for controlling the environment of the operating chamber 3. Thus, the operating ports allow the entry or exit of fluids and / or similar substances used in the sterilization cycle. Furthermore, the conveying system 15 for the present invention is operatively coupled between the plurality of operating chambers 3 and the plurality of transition chambers 2, wherein the conveying system 15 moves the container 18 between the plurality of operating chambers and the plurality of transition chambers 2. Thus, the container 18 then travels safely and reliably through the plurality of transition chambers 2 and the operating chambers 3. When using the present invention, the fixation of the container 18 ensures proper sterilization.
[0041] Furthermore, the plurality of operating chambers 3 include at least one preconditioning chamber 39, at least one sterilization chamber 40, and at least one postconditioning chamber 41. The preconditioning chamber allows for the preconditioning of elements within container 18. Due to the importance of performing several different steps or sub-cycles before and after the sterilization stage or sub-cycle to accommodate the elements to be treated, in order to achieve the required level of performance and reliability during the sterilization cycle, the application of the stage performed within the preconditioning chamber 39 is necessary, and therefore the presence of the preconditioning chamber 39 is essential for continuous processing. The sterilization chamber 40 of the present invention allows for the sterilization of elements within container 18. The environment of the sterilization chamber 40 is maintained under the correct physicochemical conditions for successful sterilization of the elements within container 18. The postconditioning chamber 41 allows for the postconditioning of elements within container 18. Similar to the preconditioning chamber 39, the postconditioning chamber 41 allows for changes in temperature, pressure, reduction of chemical concentration levels, or any other physicochemical conditioning after the elements in container 18 have been sterilized. Therefore, the postconditioning chamber 41 also avoids undesirable effects such as thermal shock and fatigue. A pretreatment chamber 39, a sterilization chamber 40, a post-treatment chamber 41, and a plurality of transition chambers 2 are connected in series. As a result, the pretreatment chamber 39 is always located before the sterilization chamber 40, and the post-treatment chamber 41 is always located after the sterilization chamber 40. Furthermore, there are always transition chambers before and after the pretreatment chamber 39, sterilization chamber 40, and post-treatment chamber 41. As previously mentioned, the sterilization chamber 40 is located between the pretreatment chamber 39 and the post-treatment chamber 41. As a result, the present invention ensures that the various stages in the cycle are carried out continuously with minimal or no system downtime as the container 18 undergoes the sterilization process. Furthermore, a transfer system 15 is operatively coupled between the pretreatment chamber 39, sterilization chamber 40, post-treatment chamber, and the plurality of transition chambers 2, wherein the transfer system 15 moves the container 18 between the pretreatment chamber 39, sterilization chamber 40, post-treatment chamber, and the plurality of transition chambers 2. As a result, the plurality of transition chambers 2 of the present invention change their environmental conditions to adapt to the conditions of adjacent chambers, circulating between the conditions of each of their adjacent operating chambers. Specifically, multiple transition chambers 2 act as conditioning chambers, which are prepared to transfer container 18 to subsequent chambers 17. This conditioning operation allows each operating chamber 3 to maintain a stable and repeatable sub-cycle, thereby reducing energy loss and the time required to perform sterilization operations.
[0042] Furthermore, the present invention includes at least one operating mesh 11. The operating mesh 11 is a permeable layer that matches the geometric profile of a plurality of operating ports 8. The plurality of operating ports 8 also include at least one operating inlet port 9 and at least one operating outlet port 10. The operating inlet port 9 serves as a direct input port for fluids and / or the like used in the sterilization cycle. Similarly, the operating outlet port 10 serves as a direct output port for fluids and / or the like used in the sterilization cycle. The operating inlet port 9 is positioned across any operating chamber offset from the operating outlet port 10, wherein such operating chamber originates from a plurality of operating chambers 3. Therefore, the operating inlet port 9 and the operating outlet port 10 remain independent of each other and are unaffected during use. Furthermore, the operating mesh 11 is mounted above the operating outlet port 10. Therefore, the operating mesh 11 allows for the capture and / or filtration of any unwanted substances, such as small particles or fibers, to prevent clogging of the down-flow components.
[0043] Furthermore, the present invention includes at least one transition mesh 7. The transition mesh 7 is a permeable layer that matches the geometric profile of a plurality of transition ports 4. Furthermore, the plurality of transition ports 4 include at least one transition inlet port 5 and at least one transition outlet port 6. The transition inlet port 5 serves as a direct input port for the fluid and / or similar substances used in the sterilization cycle. Similarly, the transition outlet port 6 serves as a direct outlet port for the fluid and / or similar substances used in the sterilization cycle. The transition inlet port 5 is positioned across any transition chamber offset from the transition outlet port 6, wherein the any transition chamber originates from a plurality of transition chambers 2. Therefore, the transition inlet port 5 and the transition outlet port 6 remain independent of each other in use. Furthermore, the transition mesh 7 is mounted above the transition outlet port 6. Therefore, the transition mesh 7 allows for the capture and / or filtration of any unwanted substances, such as small particles or fibers, to prevent clogging of downstream components.
[0044] Furthermore, a preferred embodiment of the invention includes multiple transition instrument systems 13. The multiple transition instrument systems 13 consist of sensors selected from a group including temperature sensors, pressure sensors, chemical sensors, biomaterial sensors, and humidity sensors. Moreover, each of the multiple transition instrument systems 13 is integrated into a corresponding transition chamber 42, wherein the corresponding transition chamber 42 is derived from multiple transition chambers 2. Therefore, data measurement and monitoring are feasible during operation. Specifically, the multiple transition instrument systems 13 monitor the environmental conditions within each transition chamber and provide feedback to a control system capable of modifying the conditions within the transition chamber to optimize the disinfection operation.
[0045] Similarly, a preferred embodiment of the invention includes a plurality of operating instrument systems 12. The plurality of operating instrument systems 12 comprises sensors selected from the group including temperature sensors, pressure sensors, chemical sensors, biomaterial sensors, and humidity sensors. Furthermore, each of the plurality of operating instrument systems 12 is integrated into a corresponding operating chamber 43, wherein the corresponding operating chamber 43 is derived from a plurality of operating chambers 3. Therefore, data measurement and monitoring are feasible during operation. Specifically, the plurality of operating instrument systems 12 monitor the environmental conditions within each operating chamber and provide feedback to a control system capable of modifying the conditions within the operating chamber to optimize the disinfection operation.
[0046] Furthermore, a preferred embodiment of the invention also includes a plurality of insulating liner 14. The insulating liner 14 is a structural layer that may be present inside or outside each of the plurality of transition chambers 2 and each of the plurality of operating chambers 3. The insulating liner 14 provides insulation for each of the plurality of transition chambers 2 and the plurality of operating chambers 3. The insulating liner 14 may include any geometric profile to meet manufacturing, design, and / or user requirements. As previously described, each of the plurality of transition chambers 2 and each of the plurality of operating chambers 3 is surrounded by a corresponding liner from the plurality of insulating liners 14. Thus, insulation is maintained for each of the plurality of transition chambers 2 and each of the plurality of operating chambers 3. In some embodiments, the insulating liner 14 is superimposed on all pipes, conduits, and other fluid delivery components, as well as on instrument ports or similar connections that contact or are adjacent to the chambers.
[0047] Furthermore, the container 18 of a preferred embodiment of the present invention includes a first end cap 23, a second end cap 44, a passage door 19, at least one permeable sidewall 20, at least one first gasket 21, and at least one second gasket 22. The end caps comprise a solid plate geometry and are made of any feasible material that can safely retain operating conditions. Preferably, the end caps include thermal insulation material between the two solid plates forming the end caps to maintain insulation between the chambers. In some embodiments, the passage door 19 is removable from the container 18, meaning it allows the input and output of elements within the container 18. The permeable sidewall 20 is a mesh structure comprising, but not limited to, a cylindrical geometry. The permeable sidewall 20 can also be made of any material capable of withstanding operating conditions. Furthermore, the passage door 19 is integrated into the container 18, allowing a user to open the container 18 and retrieve any items stored therein. The first gasket 21 and the second gasket 22 are annular structures that provide a seal between the container 18 and any transition chamber. The first gasket 21 and the second gasket 22 are made of any material capable of withstanding operating conditions, but are also non-rigid bodies. The first end cap 23 and the second end cap 44, used in this invention, are connected and adjacent to the opposite ends of the permeable sidewall 20. Specifically, the first end cap 23 is end-to-end connected to the permeable sidewall 20, and the second end cap 44 is end-to-end connected to the permeable sidewall 20, opposite to the first end cap 23. In some embodiments, the passage door 19 is integrated into the permeable sidewall 20 and can be attached or removed in any way, such as by threads, hinges and retaining pins, sliding, etc. Therefore, the user is assured that contaminated items placed in the container 18 will not be lost in the multiple operating chambers 3 or the multiple transition chambers 2. Furthermore, the first gasket 21 is connected around the first end cap 23. Similarly, the second gasket 22 is connected around the second end cap 44. As a result, when the container 18 moves between the operating chambers 3, the first gasket 21 and the second gasket 22 press against the walls of the multiple transition chambers 2. This forms an airtight seal, preventing conditions in any operating chamber from leaking into adjacent operating chambers. Furthermore, the contents of container 18 are safely transported throughout the sterilization cycle. Additionally, the permeable sidewalls 20 of container 18 allow the contents of container 18 to come into direct contact with the conditions of each of the plurality of transition chambers 2 and each of the plurality of operating chambers 3.
[0048] An alternative embodiment of the invention further includes a plurality of hatches 24. The hatches 24 comprise at least one of, but are not limited to, lateral sliding doors, vertical sliding doors, hydraulic sliding doors, pneumatic sliding doors, and electric sliding doors. The hatches allow isolation between each of the plurality of transition chambers 2 and each of the plurality of operating chambers 3, performing the functions of end caps and seals of the container 18 as described in the preceding alternative. A preceding hatch 25 is integrated into the connection between a preceding chamber 16 and any operating chamber, wherein the operating chamber originates from the plurality of operating chambers 3, and wherein the preceding hatch 25 originates from the plurality of hatches 24. As a result, the preceding hatch 25 acts as a barrier to the exchange of fluid and physicochemical conditions between the preceding chamber 16 and any operating chamber. Similarly, a rear hatch 26 is integrated into the connection between a rear chamber 17 and any operating chamber, wherein the rear hatch 26 originates from the plurality of hatches 24. Therefore, the rear hatch 26 acts as a barrier to the exchange of fluid and physicochemical conditions between the rear chamber 17 and any operating chamber.
[0049] Furthermore, a preferred embodiment of the invention also includes a plurality of cavity gaskets 27 and a plurality of thermal hatch liner 28. The cavity gaskets 27 are sealingly extensible components that match the geometry of the cavities from the plurality of cavities 24 and provide an hermetically tight seal between the gasket and any transition chamber or any operating chamber. Each of the plurality of cavity gaskets 27 is integrally formed around a corresponding cavity. Thus, the cavity gasket hermetically seals the opening of the corresponding cavity. The thermal hatch liner 28 provides insulation similar to that of the plurality of thermal liners 14 found in each of the plurality of operating chambers 3 and each of the plurality of transition chambers 2. Furthermore, each of the plurality of thermal hatch liners 28 is housed within a corresponding cavity. Specifically, each of the plurality of thermal hatch liners 28 is contained within a solid outer surface of a cavity exposed to the interior of the plurality of transition chambers 2 and the plurality of operating chambers 3. As a result, thermal isolation is achieved between each of the plurality of transition chambers 2 and each of the plurality of operating chambers 3. Furthermore, the insulated cavity liner 28 is protected from exposure to fluids and chemicals required for cleaning operations. Additionally, the cavities among the multiple cavities 24 include safety locking mechanisms. These safety locking mechanisms prevent the multiple cavities 24 from opening in the event of a hazardous situation within the multiple operating chambers 3 and the multiple transition chambers 2.
[0050] Some embodiments also include a plurality of linear actuators 29. The linear actuators among the plurality of actuators are at least one selected from the group including pneumatic actuators and hydraulic actuators. Each of the plurality of linear actuators 29 is integrated into the sidewall of a corresponding transition chamber 42, wherein the corresponding transition chamber 42 originates from a plurality of transition chambers 2. Thus, the linear actuators help overcome the pressure differential experienced by the container 18 when entering any transition chamber from the preceding operating chamber, and when entering any operating chamber from the preceding transition chamber. Furthermore, the container 18 is operatively coupled to the linear actuators of the corresponding transition chambers 42, thus, as previously described, the linear actuators provide sufficient force to overcome the pressure differential between the operating chamber of the preceding chamber 16 and any adjacent operating chambers from the plurality of operating chambers 3. In this case, the linear actuators 29 can be any possible configuration capable of overcoming the pressure differential. Thus, one possible arrangement is a plurality of hydraulic actuators that are activated once the container 18 enters any transition chamber. The hydraulic actuators then contact the container 18 and propel it through the arbitrary transition chamber.
[0051] Furthermore, the conveying system 15 used in this invention includes a loading section 30, an unloading section 31, a processing section 32, and a feedback section 33. The loading section 30 is the starting point of the conveying system 15, where the container 18 is placed before the sterilization cycle. The unloading section 31 is the ending point of the conveying system 15, where the container 18 is unloaded after the sterilization cycle. The processing section 32 is the portion of the conveying system 15 extending from the first transition chamber to the last transition chamber. Therefore, the processing section 32 traverses the arrangement of each of the plurality of operating chambers 3 and each of the plurality of transition chambers 2. The feedback section 33 is the portion of the conveying system 15 located after the unloading section 31 and before the loading section 30. The feedback section 33 of the conveying system 15 moves the container 18 back to the starting point, thus forming a closed-loop arrangement. The loading section 30 is located adjacent to the first front chamber 34, which originates from the plurality of transition chambers 2. Therefore, once the container 18 is placed on the loading section 30, the container 18 safely travels and enters the first front chamber 34. The unloading section 31 is located adjacent to the last subsequent chamber 35, which is derived from the plurality of transition chambers 2. Therefore, once the container 18 leaves the last subsequent chamber 35, the container 18 safely travels and enters the unloading section 31. The processing section 32 is connected between the loading section 30 and the unloading section 31. Therefore, the processing section 32 safely moves the container 18 from the start to the end of the sterilization cycle. The processing section 32 passes through the plurality of transition chambers 2 and the plurality of operating chambers 3. As a result, the processing section 32 helps to hold the container 18 within each of the plurality of transition chambers 2 and each of the plurality of operating chambers 3. The feedback section 33 is connected between the loading section 30 and the unloading section 31. Therefore, the feedback section 33 helps to move the container 18 back to the starting point of the sterilization cycle. The feedback section 33 is positioned offset from the processing section 32, surrounding the conveying system 15. As a result, the conveying system 15 allows for a modular configuration, where the sterilization system can be arranged in various locations. In each variation and possible arrangement of the plurality of transition chambers 2 and each of the plurality of operating chambers 3, the sterilization system maintains its continuous operation configuration.
[0052] Furthermore, a preferred embodiment of the invention also includes a programmable controller 36 with a human machine interface (HMI). The HMI is part of a control system that manages the operation of the invention. For example, the programmable controller 36 allows activation of any operating injection or discharge port and / or any transition injection or discharge port, any conveyor, actuator, cavity, or other automated component. It also receives signals from various sensors and instruments. Simultaneously, the HMI can provide options for setting operating parameters, such as time, temperature, pressure, etc., which can be understood by the operator of the machine based on the direct operating parameters leading to the desired final disinfection result. Furthermore, the controller acts based on the settings introduced by the HMI to obtain the desired result by operating the components under its control as mentioned above. Thus, the programmable controller 36 and the HMI provide control and monitoring of operating parameters for any operating chamber and / or transition chamber, communicatively coupled to multiple transition chambers 2, the conveyor system 15, and multiple operating chambers 3. Therefore, the disinfection system is fully controllable and monitorable via the HMI. Furthermore, data values and readings from multiple instrument systems are visible via the HMI. Various possible manual overrides and programmable automation are implemented in the HMI.
[0053] Although the invention has been explained with reference to its preferred embodiments, it should be understood that many other possible modifications and variations may be made without departing from the spirit and scope of the invention as described below.
[0054] Supplementary Explanation
[0055] The existing problems solved by this invention:
[0056] The time of idle elements or medical equipment; the actual system is batch-based and, depending on the capacity of the machine, the elements to be processed need to remain in the queue until there are enough elements that can be processed with the same loop parameters and the capacity of the chamber can be filled so that processing can be carried out reasonably and economically.
[0057] Faster turnaround time; when medical devices or instruments are reused, such as in healthcare applications, elements can be processed immediately, and because each stage of the cycle is already in the appropriate condition for processing, elements can be circulated without waiting for the machine to adjust the intermediate chamber conditions.
[0058] The machine occupies space and the sterilization area as a whole; compared to conventional machines on the market, this machine may be similar in size or slightly larger, but can achieve several times the productivity of the aforementioned machines. The sterilization area can use one of the proposed machines to replace several conventional machines, and because the machine's shape can be adapted to the limitations of the room where it is installed, the area can optimize its space utilization.
[0059] The variability of sterilization processes based on load weight can lead to process failure. Studies have shown that the variability of sterilization processes is based on the type and quantity (weight and distribution) of the load. Results indicate a significant increase in required time and pretreatment. This invention reduces the impact of the aforementioned factors on variability, thereby reducing its effectiveness in cycles. This is because the elements added to the process at any given time are few and easily overcome by the machine; furthermore, the chamber is more stable because it is designed to maintain constant conditions during its operation; and compared to conventional machines, there is no impact on efficiency due to load distribution within the chamber.
[0060] Energy and resources (e.g., water, chemicals); a major factor users evaluate when selecting a sterilizer is resource consumption, which can constitute significant costs and waste, as well as their ecological impact. For example, a conventional autoclave requires the following operations on the total volume of the chamber: purging air (vacuum), preheating, filling with steam, compensating for water and heat losses in the form of condensation, purging steam, reducing the temperature of the discharge fluid before it reaches the sewer (usually using cooling water), drying wet elements, and cooling the interior. All these steps consume a significant amount of energy in the form of heat and the mechanical work of the vacuum pump, with water in the form of steam acting as a coolant and typically creating a vacuum (water ring pump). The proposed design must do the same thing, but because the conditions in each chamber are maintained, the amount of variation, wasted water, and energy is significantly lower. The injected steam is only what is needed to satisfy the introduction of elements and compensate for heat losses through the chamber walls. A vacuum is maintained, and only the amount of air purged along with the new load is required. The cooling process is similar; there is no residual heat from the machine structure, only elements from previous stages. Furthermore, since no steam needs to be discharged, the drainage volume is reduced, and the only steam and water wasted during the process comes from the pretreatment stage of condensation and steam pulse.
[0061] Brief description:
[0062] Systems and / or equipment for the purification and / or sterilization and / or physical treatment of elements, and / or in the medical industry, such as hospitals, pharmaceutical, medical device, biotechnology, or research laboratories. However, it can also be applied to the food, chemical, and biological waste purification, and the curing of plastics, rubber, and composite materials. And any other industry requiring purification, and / or sterilization, and / or physical treatment. The system is demonstrated using a steam sterilizer or autoclave, but is not limited to this type of method, and can be used with, for example, ethylene oxide, ozone, hydrogen peroxide, formaldehyde (LTSF), or any other sterilizing chemical or physical conditions.
[0063] Full description:
[0064] A system consisting of a set of containers in which the elements to be processed are placed. Containers can be continuously fed into the system and pass through a series of chambers, in which the necessary stages of the cycle are performed according to established industry best practices.
[0065] We will use a steam sterilizer (autoclave) as an application example of this system. The chosen machine's shape and size represent what we consider the simplest form for explanation and construction; however, this embodiment can be applied to different shapes, sizes, and methods (e.g., ethylene oxide, ozone, hydrogen peroxide, formaldehyde (LTSF), etc.). The container is a basket that can be made cylindrical (or any shape), made of perforated, mesh, or permeable materials, such as corrosion-resistant metals, other materials like plastics, fibers, etc.
[0066] The elements to be processed are stored in containers, which are then placed on a conveyor that feeds the machine into transition chamber #1 (TC#1) through a cavity port. The machine contains several transition chambers that act as channels to balance conditions between chambers, preventing direct communication and exchange of fluids or temperatures. The cavity port can be a sliding door or any other device for opening and achieving tight closure of the chamber. Automation of the cavity port is achieved through rack and pinion, pneumatic / hydraulic pistons, or other mechanisms.
[0067] Conveyors are installed within each section of the machine to transport containers along the various stages of the process. The following description is an example of an implementation applied to a Class B steam sterilizer [Transition #1 (T#1), Pretreatment (PrC), Transition #2 (T#2), Sterilization (S), Transition #3 (T#3), Posttreatment (PtC), Transition #4 (T#4)]. The conveyor can be of any type (e.g., belt, cable / wire, roller, chain, rack and pinion, pneumatic, etc.).
[0068] The pretreatment, sterilization, and post-treatment chambers can accommodate several containers, while the transition chamber receives one container at a time (potentially more, depending on the specific application design). The chambers have a cylindrical shape similar to, but not limited to, piping (they can be parallelepiped or any other shape) and can be made of stainless steel or any other material sufficient to withstand the operating conditions, with walls of sufficient thickness. The chambers are connected to services necessary for their function, such as steam, vacuum, drainage, instrumentation and inspection ports, and safety devices such as rupture discs and pressure relief valves. Operator-accessible chambers and other surfaces (including ports, piping, connections, instruments, and external surfaces) are insulated with the most suitable material, i.e., mineral wool, rock wool, glass wool, ceramic coatings, carbon composites, silica fibers, vacuum, or others. Piping, connections, valves, and sensors are part of the components necessary for the operation of the embodiment.
[0069] The system utilizes a controller, such as a computer, PLC, or microcontroller, to drive conveyors, cavities, valves, and vacuum pumps (for simplicity, the example machine used to explain the embodiment assumes that the required steam, water, compressed air, and any other services are supplied from an external source. If not, the controller would also need to command a steam generator, compressor, or any other service source). In addition to controlling the automation functions, the PLC will receive input signals from sensors and instruments to make logical decisions for functional and safety handling. Backup controllers and record-keeping devices may also be included, a common industry requirement for safety or traceability reasons.
[0070] Elements are loaded into containers, which are then placed sequentially in a first conveyor forming a row. The conveyors, controlled by a controller, move the containers while simultaneously opening the first chamber port, allowing one container to enter TC#1, and then closing the port. Inside TC#1, steam is injected through the injection port, while the exhaust port is controlled to expel air from the chamber to replace it with steam; once the air is considered purged, the exhaust valve is closed, thus raising the pressure inside the chamber to approximately 1.5 bar(a), matching the conditions in the pretreatment chamber at a certain point in time. Note that the circulation temperatures and pressures shown herein are for reference only; mature or other circulations may be used. Generally, it is set in the range of approximately 115°C to 138°C. Some sterilization apparatuses can be set at approximately 142°C, with corresponding pressures for saturated steam. Time conditions vary depending on the temperature conditions during the sterilization step. Generally, they are set between approximately 3 minutes and 60 minutes. Some types of sterilization apparatuses can be set at approximately 100 minutes. During the pre-vacuum step (pretreatment), the pressure inside the chamber is typically set to between approximately 0.03 bar(a) and 0.01 bar(a), and the same applies during the drying step (posttreatment).
[0071] The pretreatment chamber maintains a pulsed cycle of injected steam, pressurized to 1.5 bar(a), with a vacuum of 0.04 bar(a). At the aforementioned moment, matching 1.5 bar(a), the second port between TC#1 and the pretreatment chamber opens, and the third port between the pretreatment chamber and TC#2 also opens. The conveyor from the transition chamber and the pretreatment chamber moves all containers forward one position, introducing containers from TC#1 into the pretreatment chamber, and from there finally introducing the last container in the chamber into TC#2. The port closes, and TC#2 increases its pressure to 3 bar(a) and 132°C by adding more steam. Now the conditions in this chamber are the same as in the sterilization chamber, so the fourth port can open, connecting TC#2 to the sterilization chamber and conveying containers into the aforementioned chamber. TC#3 also matches the conditions of the sterilization chamber, and the fifth port between the sterilization chamber and TC#3 opens simultaneously with the fourth port, allowing the last container in the sterilization chamber to move to TC#3 via the conveyor, while the remaining containers in the sterilization chamber move one position.
[0072] When the valve is opened and the chamber and vacuum pump are connected, the chamber port closes, and TC#3 discharges vapor through the discharge pipe. Vacuuming continues until 0.04 bar(a) is reached, equal to the conditions in the post-processing chamber. At this point, the sixth and seventh chamber ports open, connecting to the PtC. The conveyor moves the container from TC#3 into the PtC and moves all containers in the PtC one step, including the last container in the PtC, into TC#4.
[0073] Before the seventh chamber is opened, the conditions in TC#4 are matched to those in PtC; once it receives a new container and the chamber is closed, air is allowed to enter through the filter and inlet valve until TC#4 reaches atmospheric pressure. At this point, the last chamber on the machine output side (the eighth chamber) can be opened, and the conveyor transports the container outside the machine to the receiving section so that the operator can remove the element from the container. It must be mentioned that TC#1 performs a similar procedure to TC#4; once the container at 1.5 bar(a) pressure is transferred to PrC, the chamber is closed, the vapor in TC#1 is vented, and replaced with filtered air matched to atmospheric pressure.
[0074] Alternative Design 1
[0075] An alternative to the cavity system is the use of the containers described above, but with improved end caps. The caps may be solid plates made of stainless steel, but are not limited to this material. Resilient seals or other materials are installed along their circumference to withstand operating conditions and friction. These containers are introduced and pass through the various stages of the machine in the same manner as described above. The difference lies in the method of transfer from one stage to another; now there are no cavities separating the chambers from each other, and the containers themselves are closed or sealed by their caps. The transition chamber walls are designed to make sealing contact with the container caps, preventing the exchange of fluid and physical conditions between them. Another difference from the previously described method is the need to maintain container recirculation (looping), regardless of whether it contains elements, because the chambers must maintain the full internal capacity of the container along the loop during the process of sealing and opening the chambers. For container recirculation or looping, a conveyor outside the chambers transports the containers from the machine's output (unloading area) to the input (loading area). Various choices of chamber configurations serve as examples of design flexibility in this invention.
[0076] Alternative Design 2
[0077] For this option, we chose to use a parallelepiped shape for our preferred embodiment because it allows for greater load capacity and is better suited to accommodating industry-standard containers. In the same manner as Alternative Design 1, two of their faces are blind (solid), which we call caps, while the remaining faces are made of a mesh material, such as stainless steel mesh or other suitable material. The caps may be solid plates made of stainless steel, but are not limited to this material. Resilient seals or other materials are installed along their perimeter to withstand operating conditions and friction. The edges of the containers are rounded, giving them a more robust structure, better cleanliness, and a better seal between the container and the transition chamber walls through which the container will pass. The size and shape of the transition chambers allow containers to pass through them while their seals contact the chamber walls, producing the desired sealing effect.
[0078] This alternative must also maintain a closed loop for the containers to preserve the container transfer sequence, while ensuring proper isolation between chambers. For container recirculation or recycling, a conveyor outside the chambers transfers the containers from the machine's output (unloading area) to its input (loading area).
[0079] The pretreatment, sterilization, and post-treatment chambers are sized to accommodate a number of containers. Containers are received and transported using a conveyor; for our embodiment, we describe a vertical chain magazine conveyor type (also known as a vertical conveyor lift). The transition chamber feeds through a port into its corresponding adjacent chamber (PrC / S / PtC), where the container is fed into the magazine conveyor. The conveyor, controlled by a computer, PLC, or microcontroller, moves the containers within in a continuous or step-by-step mode until it reaches the exit position of the next transition chamber. The time required to move a container from the inlet point to the outlet point is necessary to complete a sub-cycle for that particular container.
[0080] The length, speed, and dimensions of conveyors and chambers need to be designed and programmed according to the production flow (rhythm) required by the application. Tank-type conveyors are a highly efficient way to load multiple containers into processing chambers (such as PrC, S, and PtC) while maintaining a minimal footprint by utilizing vertical space. Multidirectional displacement of the containers can be increased if four sides are solid plates with seals, rather than just two of the six sides, while the remaining two sides are made of mesh material. With this design, containers can move in four directions, allowing for more flexible transport of containers from one chamber to another, thus enabling chambers to be organized in different arrangements, resulting in space optimization.
[0081] To achieve the same goal of multi-directional displacement without adding an additional cap (as previously described), another possible arrangement is to add a rotating base to realign the axis of the container lid with the same direction as the chamber to be introduced. Processing and transition chambers can be arranged and connected in different positions and shapes. This modular and flexible design of sequential arrangement adds the advantage of allowing chambers to be interconnected, enabling parallel processing lines to be implemented simultaneously, and / or allowing containers to follow different paths under different circulation conditions. For example, in the same machine, it can be configured to utilize saturated steam circulation at 135°C (rapid sterilization), 121°C (standard sterilization), and cryogenic sterilization using other fluid and environmental conditions (ETO, H2O2, O3, LTSF, etc.).
[0082] Other improvements
[0083] Heat loss can be compensated by adding resistors or other heating devices within the chamber, and condensate can be re-evaporated, thus recirculating and maintaining steam volume. These resistors are located at the end of the condensate tank at the bottom of the chamber. Since only a small amount of heat is needed to return the condensed steam to saturated steam, this addition improves machine efficiency and reduces heat and water consumption. This system is feasible without repressurization, for example, in sterilization chambers, because it remains in a sealed and stable operating state even when containers are introduced or removed, thanks to matching the container's condition before transfer. A small amount of additional steam can compensate for pressure drops due to leaks or other reasons.
[0084] Another efficiency improvement is the use of a steam recovery system, collected from T#1, PrC, T#3, and any other steam traps or separators. When extracted from the respective chambers using a vacuum pump or similar device, it is introduced into the steam recovery tank and repressurized by a steam compressor or pump; then reheated to the necessary operating conditions using a resistance or other heat-generating device. The tank also has a connection to fresh steam from the steam generation source to compensate for losses, and from which the main steam distribution line to the chambers is obtained. PtC and T#4 include a second vacuum pump, as no steam is to be recovered, and air from T#4 is undesirable; the vacuum fluid is vented to the sewer or atmospheric vent.
Claims
1. A continuous elemental purification and sterilization system, comprising: Multiple transition rooms; Multiple control rooms; Multiple transition ports; Multiple operating ports; At least one transmission system; At least one container; Each of the plurality of operating chambers is connected between a preceding chamber and a following chamber, wherein the preceding chamber and the following chamber are derived from the plurality of transition chambers; Any number of operation ports are integrated into each of the plurality of operation rooms, wherein the arbitrary number of operation ports are derived from the plurality of operation ports; The plurality of transition ports include at least one transition injection port and at least one transition discharge port integrated into each of the plurality of transition chambers, for guiding fluid into each of the plurality of transition chambers or discharging fluid from each of the plurality of transition chambers, so as to allow the establishment of predetermined transition conditions in each of the plurality of transition chambers; The conveying system is operatively coupled between the plurality of operating chambers and the plurality of transition chambers, wherein the conveying system moves at least one of the containers through the plurality of operating chambers and the plurality of transition chambers; During use, as the container is conveyed through each transition chamber, the predetermined transition conditions in each transition chamber are controllable, varying substantially between the predetermined operating conditions of the preceding operating chamber and the predetermined operating conditions of the following operating chamber. A magazine-type conveyor is provided in at least a portion of the plurality of operating rooms to receive the plurality of the at least one container and to temporarily store and move the plurality of the at least one container in an intermittent manner during the corresponding purification and / or sterilization steps in at least a portion of the operating rooms.
2. The continuous elemental purification and sterilization system according to claim 1, wherein, The magazine-type conveyor is configured to temporarily store and move a plurality of the at least one container in a vertically spaced manner within at least a portion of the operating room.
3. The continuous elemental purification and sterilization system according to claim 1, comprising: The plurality of operating rooms includes at least one pretreatment room, at least one sterilization room and at least one posttreatment room; The pretreatment chamber, the sterilization chamber, the post-treatment chamber, and the plurality of transition chambers are connected in series; The sterilization chamber is located between the pretreatment chamber and the posttreatment chamber; as well as The conveying system is operatively coupled between the pretreatment chamber, the sterilization chamber, the post-treatment chamber, and the plurality of transition chambers, wherein the conveying system moves the container between the pretreatment chamber, the sterilization chamber, the post-treatment chamber, and the plurality of transition chambers.
4. The continuous elemental purification and sterilization system according to claim 1, comprising: At least one operating network; The plurality of operation ports include at least one operation injection port and at least one operation discharge port; The operation injection port is positioned to deviate from the operation discharge port across any operation chamber, wherein the arbitrary operation chamber comes from the plurality of operation chambers; as well as The operating net is installed above the operating discharge port.
5. The continuous elemental purification and sterilization system according to claim 1, comprising: At least one transition network; The transition injection port is positioned to deviate from the transition discharge port across any transition chamber, wherein the arbitrary transition chamber originates from the plurality of transition chambers; and The transition net is installed above the transition discharge port.
6. The continuous elemental purification and sterilization system according to claim 1, comprising: Multiple transitional instrument systems; and Each of the plurality of transition instrument systems is integrated into a corresponding transition chamber, wherein the corresponding transition chamber is derived from the plurality of transition chambers.
7. The continuous elemental purification and sterilization system according to claim 1, comprising: Multiple operating instrument systems; as well as Each of the plurality of operating instrument systems is integrated into a corresponding operating room, wherein the corresponding operating room is derived from the plurality of operating rooms.
8. The continuous elemental purification and sterilization system according to claim 1, comprising: Multiple insulation layers; and Each of the plurality of transition chambers and each of the plurality of operating chambers is surrounded by a corresponding liner of the plurality of insulating liner layers.
9. The continuous elemental purification and sterilization system according to claim 1, comprising: Multiple cavities; The anterior cavity port is integrated into the connection between the anterior chamber and any operating chamber, wherein the any operating chamber originates from the plurality of operating chambers, and the anterior cavity port originates from the plurality of cavities; and The rear port is integrated into the connection between the rear chamber and the arbitrary operating chamber, wherein the rear port originates from the plurality of ports.
10. The continuous elemental purification and sterilization system according to claim 9, comprising: Multiple cavity gaskets; Multiple insulation cavity linings; Each of the plurality of cavity gaskets is integrated around a corresponding cavity, wherein the cavity gasket hermetically seals the opening of the corresponding cavity; and Each of the plurality of insulating cavity linings is housed within the corresponding cavity.
11. The continuous elemental purification and sterilization system according to claim 1, comprising: Multiple linear actuators; Each of the plurality of linear actuators is integrated into the sidewall of a corresponding transition chamber, wherein the corresponding transition chamber is derived from the plurality of transition chambers; and The container is operatively coupled to a linear actuator of the respective transition chamber, wherein the linear actuator provides sufficient force to overcome the pressure difference between the front chamber and adjacent operating chambers among the plurality of operating chambers.
12. The continuous elemental purification and sterilization system according to claim 1, comprising: The transmission system includes a loading unit, an unloading unit, a processing unit, and a feedback unit; The loading section is located adjacent to the first front chamber, wherein the first front chamber originates from the plurality of transition chambers; The unloading section is located adjacent to the last rear chamber, which is derived from the plurality of transition chambers; The processing unit is connected between the loading unit and the unloading unit; The processing unit passes through the plurality of transition chambers and the plurality of operating chambers; The feedback unit is connected between the loading unit and the unloading unit; and The feedback unit is positioned around the transmission system, offset from the processing unit.
13. The continuous elemental purification and sterilization system according to claim 1, comprising: Programmable Logic Controller (PLC); and The programmable controller is communicatively coupled to the plurality of transition chambers, the transmission system, and the plurality of operating chambers.
14. A continuous elemental purification and sterilization system, comprising: Multiple transition rooms; Multiple control rooms; Multiple transition ports; Multiple operating ports; At least one transmission system; At least one container; Each of the plurality of operating chambers is connected between a preceding chamber and a following chamber, wherein the preceding chamber and the following chamber are derived from the plurality of transition chambers; Any number of operation ports are integrated into each of the plurality of operation rooms, wherein the arbitrary number of operation ports are derived from the plurality of operation ports; The plurality of transition ports include at least one transition injection port and at least one transition discharge port integrated into each of the plurality of transition chambers, for guiding fluid into each of the plurality of transition chambers or discharging fluid from each of the plurality of transition chambers, so as to allow the establishment of predetermined transition conditions in each of the plurality of transition chambers; The conveying system is operatively coupled between the plurality of operating chambers and the plurality of transition chambers, wherein the conveying system moves at least one of the containers through the plurality of operating chambers and the plurality of transition chambers; During use, as the container is conveyed through each transition chamber, the predetermined transition conditions in each transition chamber are controllable, varying substantially between the predetermined operating conditions of the preceding operating chamber and the predetermined operating conditions of the following operating chamber. The container includes a first end cap, a second end cap, a channel door, a permeable sidewall, a first gasket, and a second gasket. The first end cap is connected to a first end of the adjacent permeable sidewall; the second end cap is connected to a second end of the adjacent permeable sidewall, and crosses the permeable sidewall opposite to the first end cap. The first gasket is connected around the first end cap; the second gasket is connected around the second end cap; and the channel door is integrated into the container. The container is configured such that, when moved between the operating chambers, the first gasket and the second gasket press against the wall of the transition chamber, such that the wall of the transition chamber is in sealing contact with the first end cap and the second end cap, to prevent conditions in either operating chamber from leaking into the adjacent operating chamber.
15. The continuous elemental purification and sterilization system according to claim 14, wherein, A magazine-type conveyor is provided in at least a portion of the plurality of operating rooms to receive the plurality of the at least one container and to temporarily store and move the plurality of the at least one container in an intermittent manner during the corresponding purification and / or sterilization steps in at least a portion of the operating rooms.
16. The continuous elemental purification and sterilization system according to claim 15, wherein, The magazine-type conveyor is configured to temporarily store and move a plurality of the at least one container in a vertically spaced manner within at least a portion of the operating room.
17. The continuous elemental purification and sterilization system according to claim 14, comprising: The plurality of operating rooms includes at least one pretreatment room, at least one sterilization room and at least one posttreatment room; The pretreatment chamber, the sterilization chamber, the post-treatment chamber, and the plurality of transition chambers are connected in series; The sterilization chamber is located between the pretreatment chamber and the posttreatment chamber; as well as The conveying system is operatively coupled between the pretreatment chamber, the sterilization chamber, the post-treatment chamber, and the plurality of transition chambers, wherein the conveying system moves the container between the pretreatment chamber, the sterilization chamber, the post-treatment chamber, and the plurality of transition chambers.
18. The continuous elemental purification and sterilization system according to claim 14, comprising: At least one operating network; The plurality of operation ports include at least one operation injection port and at least one operation discharge port; The operation injection port is positioned to deviate from the operation discharge port across any operation chamber, wherein the arbitrary operation chamber comes from the plurality of operation chambers; as well as The operating net is installed above the operating discharge port.
19. The continuous elemental purification and sterilization system according to claim 14, comprising: At least one transition network; The transition injection port is positioned to deviate from the transition discharge port across any transition chamber, wherein the arbitrary transition chamber originates from the plurality of transition chambers; and The transition net is installed above the transition discharge port.
20. The continuous elemental purification and sterilization system according to claim 14, comprising: Multiple transitional instrument systems; and Each of the plurality of transition instrument systems is integrated into a corresponding transition chamber, wherein the corresponding transition chamber is derived from the plurality of transition chambers.
21. The continuous elemental purification and sterilization system according to claim 14, comprising: Multiple operating instrument systems; as well as Each of the plurality of operating instrument systems is integrated into a corresponding operating room, wherein the corresponding operating room is derived from the plurality of operating rooms.
22. The continuous elemental purification and sterilization system according to claim 14, comprising: Multiple insulation layers; and Each of the plurality of transition chambers and each of the plurality of operating chambers is surrounded by a corresponding liner of the plurality of insulating liner layers.
23. The continuous elemental purification and sterilization system according to claim 14, comprising: Multiple cavities; The anterior cavity port is integrated into the connection between the anterior chamber and any operating chamber, wherein the any operating chamber originates from the plurality of operating chambers, and the anterior cavity port originates from the plurality of cavities; and The rear port is integrated into the connection between the rear chamber and the arbitrary operating chamber, wherein the rear port originates from the plurality of ports.
24. The continuous elemental purification and sterilization system according to claim 23, comprising: Multiple cavity gaskets; Multiple insulation cavity linings; Each of the plurality of cavity gaskets is integrated around a corresponding cavity, wherein the cavity gasket hermetically seals the opening of the corresponding cavity; and Each of the plurality of insulating cavity linings is housed within the corresponding cavity.
25. The continuous elemental purification and sterilization system according to claim 14, comprising: Multiple linear actuators; Each of the plurality of linear actuators is integrated into the sidewall of a corresponding transition chamber, wherein the corresponding transition chamber is derived from the plurality of transition chambers; and The container is operatively coupled to a linear actuator of the respective transition chamber, wherein the linear actuator provides sufficient force to overcome the pressure difference between the front chamber and adjacent operating chambers among the plurality of operating chambers.
26. The continuous elemental purification and sterilization system according to claim 14, comprising: The transmission system includes a loading unit, an unloading unit, a processing unit, and a feedback unit; The loading section is located adjacent to the first front chamber, wherein the first front chamber originates from the plurality of transition chambers; The unloading section is located adjacent to the last rear chamber, which is derived from the plurality of transition chambers; The processing unit is connected between the loading unit and the unloading unit; The processing unit passes through the plurality of transition chambers and the plurality of operating chambers; The feedback unit is connected between the loading unit and the unloading unit; and The feedback unit is positioned around the transmission system, offset from the processing unit.
27. The continuous elemental purification and sterilization system according to claim 14, comprising: Programmable Logic Controller (PLC); and The programmable controller is communicatively coupled to the plurality of transition chambers, the transmission system, and the plurality of operating chambers.