JP2008272727A - Manufacturing method of equipment for decomposing and separating molecule of gas - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method of decomposing and separating harmful substance, bacteria and molecules of carbon dioxide gas as causative substance in a mechanism of global warming, and to provide equipment for distributing decomposed substances to carbon and oxygen. <P>SOLUTION: Liquid static electricity induction generation pipes 29a, 29b, 29c for treating material included in an electrolyte aqueous solution are disposed in a tank body, and carbon dioxide gas and an electrolyte aqueous solution are mixed in the pipes, are caused to flow along the inner surface of the pipes 29a, 29b, 29c and are recovered into an electrolyte aqueous solution storage tank 4a which is separately disposed. The electrolyte aqueous solution is replenished by a pump 8a and carbon dioxide is replenished by a blower 11b to a centrifugal separator rotation drum 2. After decomposing molecules of carbon dioxides, carbon is adsorbed by a liquid static electricity induction selective membrane filter 21a disposed in the centrifugal separator rotation drum 2 and, on the other hand, oxygen passes through the liquid static electricity induction selective membrane filter 21a and is recovered by a blower 11c. Carbon particles are recovered by the electrolyte aqueous solution pump 8a. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

The present invention relates to a gas decomposition and separation apparatus manufacturing method capable of decomposing and separating molecules of harmful substances such as submicron or nanometer or more and bacteria and carbon dioxide (CO ₂ ) gas.

  As conventional techniques, there are an application number submitted by the applicant, Masao Niioka, Japanese Patent Application No. 11-51310, and Japanese Patent Application No. 2003-418708.

Problems to be solved by the invention

A method of decomposing and separating carbon dioxide (CO ₂ ) gas molecules, which are said to be harmful substances, bacteria, and the mechanism of global warming, can be invented and distributed to carbon and oxygen.
Plants can be cultivated in factories, power plants, sealed living spaces, large and small engines used in vehicles, aircraft and other spacecraft.

Means for solving the problem

Since it is necessary to reduce carbon dioxide (CO ₂ ) in order to prevent global warming, the gas molecular decomposition and separation device manufacturing method according to the present invention is introduced to the world and manufactured at low cost so as to prevent global warming. It aims to provide a method.

The invention's effect

This invention separates carbon dioxide (CO ₂₎ carbon dioxide (CO ₂₎ is effective to perform the molecule and resolved separation of carbon from the molecule (C) oxygen 20% or more to the decomposition and separation 90% be able to.
Carbon dioxide (CO ₂ ) molecules are bound in a ratio of oxygen 2 and carbon molecules 1 (2: 1), and the molecular decomposition and separation are performed by installing a liquid electrostatic induction generating pipe in the contents of the electrolytic aqueous solution. Rotating electrode wings having a shaft axis at the center of the inner diameter of the pipe and spirally formed on the shaft surface are rotated and the contents of the electrolytic aqueous solution described in [Claim 1] are dissolved in water inside the pipe. Carbon dioxide (CO ₂ ) gas is injected from the nozzles 4b and 10a installed at the center of the pipe 29a shown in the cross section of the main body 1 of FIG. 5 by a pump and a floor into the pipes 29a, 29b, and 29c. there CO ₂₎ installed pipe 29a is mixed gas and the electrolyte solution is, 29b, the electrolyte solution in the body tank 1 described flows inside surface of 29c [1] to the pipe 5] is injected from the injection port 27 in the cross-sectional view of the main body tank 1 described in FIG. 5 and the arbitrary electrolytic aqueous solution is retained in the main body tank 1 of FIG. 1 and is collected in the optional aqueous electrolytic solution storage tank 4a. The
The electrolytic aqueous solution is replenished by the pump 8a, and the carbon dioxide (CO ₂ ) is replenished by the blower 11b. The rotations of the pump 8a and the blower 11b11c are each controlled by an electric motor at 1900 rpm, and the number of rotations is controlled by the concentration of the gas.
In the embodiment, since the carbon dioxide (CO ₂ ) concentration is 100%, the rotation speed of the electric motor 7a is set to 1500 rpm to 2000 rpm.
From such a configuration, a liquid electrostatic induction selective membrane filter using a liquid electrostatic induction rotating electrode blade having a spiral shape that is formed in the pipe 29a29b29c and has an arbitrary flow controlled in the pipe 29a29b29c by controlling the speed of the electrolytic aqueous solution and gas. A mechanism based on a synergistic effect with the 21a configuration was created, and a method for molecular decomposition and separation of carbon dioxide (CO ₂ ) using an electrolytic aqueous solution was discovered and invented.
The process of separating the decomposed oxygen and carbon will be described in FIG. 4b.
Carbon is adsorbed by the liquid electrostatic induction selective membrane filter 21a described in FIG. 11 installed inside the rotating drum of the centrifuge, and oxygen passes through the liquid electrostatic induction selective membrane filter 21a and passes through the oxygen tank [FIG. 1]. The carbon particles recovered by the blower 11c are recovered from the water tank 4a shown in FIG. 1 by the electrolytic aqueous solution pump 8a.
Thus, (1) electrolytic aqueous solution (shown in claim 1) (2) liquid electrostatic induction rotating electrode blades 26a, 26b, 26c having a spiral shape shown in the perspective view of FIG. 6a (3) liquid static Electrostatic induction generating pipes 29a, 29b, 29c (4) Constructed from these parts of the liquid electrostatic induction selective membrane filter 21a, which has invented and completed the molecular decomposition and separation device for this gas, thereby preventing global warming And a manufacturing method with high mass productivity can be provided.

Next, referring to the block diagram of the embodiment of the present invention (FIG. 1), the name gas molecular decomposition and the manufacturing method of the separation apparatus will be explained. As for the material parts of the gas molecular decomposition and separation apparatus, the length of the main tank is 1600 ^t and the diameter. The main body covers 13a and 13b of the tank with 600φ have a width of 300 ^{t and an} inner diameter of 600φ, each made of plastic.
The shaft shaft has a length of 1500 ^t , a diameter of 25φ, and three SUS-304 materials are used. The liquid electrostatic induction generating pipe has an outer diameter of 145φ and a thickness of 3.0, and uses three SUS-304 materials.
The spiral-shaped rotating electrode blade has an outer diameter of 100φ and a length of 150 ^t , and is made of 15 SUS-304. The mounting method is an argon gas welding method.
The electrolytic aqueous solution storage tank 4a and the electrolytic aqueous solution auxiliary tank 4b have a diameter of 600φ and a height of 900 ^t , and are made of plastic.
The outer shape of the oxygen collecting tank 5 is 1200φ length is 1300 ^t , the material is iron, and the inside of the tank is coated with epoxy resin.
The length of the pipe is about 60 m, the size of the hose band is 35φ25φ15φ, and the number is 180 pieces.
The length of the upper and lower casings of the main body centrifuge 2a2b is 1400 ^t , and the outer shape is a maximum of 600φ.
The centrifugal rotating drum 23a has a length of 1200 ^t and a central drum diameter of 500φ.
The exhaust gas pipe 6a6b has an outer diameter of 120φ, a length of 400 ^t , and a quantity of two.
Other necessary components are a blower motor output of 1.7 KW, a motor output of 3.7 KW, and a water pump output of 1.5 KW.
With the above components, the liquid electrostatic induction generating pipes 29a and 29b described in the perspective view of [FIG. 6a] are connected to 28a, 29c and 29b are connected to 28b, and the mixed water of gas and electrolytic solution is flowed to the main body tank. Arbitrarily configured by connecting pipes.
Centering on the pipes of the connected 29a29b29c, 15 shafts 31a31b31c shown in FIG. 6a are arbitrarily attached to the shaft surface with a quantity of 15 liquid electrostatic induction generating rotating electrode blades having a 26a26b26c spiral shape. The center of the pipe 29a29b29c is constructed with 6 caps and the shaft 32 is processed with a hole 28φ around the cap 32, and six caps 32 are attached to the three pipes 29a29b29c on the left and right to leak water from the cap 32. And arbitrarily configured by a method without gas leakage. 6B, the blind flange 33a is assembled in the main body tank 1 by machining a 28φ hole in the plane of the blind flange 33a shown in the perspective view and the side view. The flange 33Fa and the bolt hole are arbitrarily configured blinds The shaft 33 holes on the left and right sides are arbitrarily machined on the flange 33a surface, and [FIG. 9] the shaft rotating part is supported to form the sleeve body 34 in the machining holes. FIG. 3d shows a surface on which six shafts 16a are arbitrarily installed on the entire rotating shaft 31, and the shaft rotating part is in contact with the shaft.
[FIG. 9] shows a place where an electric motor is installed.
The body cover 13a13b is installed so that the gas and the electrolyte solution do not leak [FIG. 6b], and the shape of the completed side view of the body tank 1 is shown in FIG.
An exhaust gas pipe 6a6b is connected to the casing 2b at the lower part of the centrifuge in FIG.
Exhaust gas pipes 6a6b are horizontally installed on the left and right of the centrifuge rotating drum 23a shown in the sectional view of FIG. 4b.
A cleaning pipe is installed from the cleaning pump around the exhaust gas pipe 6a6b, and a liquid electrostatic induction selective membrane filter 21a is attached to the center of the centrifuge rotating drum 23a.
Since the filter surface is contaminated with exhaust gas when the operation is performed for a long time, it is necessary to install a timer arbitrarily to control the cleaning.
In this way, the exhaust gas flows to the left and right of the centrifuge rotating drum 23a, the exhaust gas flows through the center of the pipe 6a6b, and the method of installing the bearing 16a16b serving as the central axis of the rotating drum 23a on the outer diameter is rotated in the other direction. Motors 7a7b7c, which rotate the drum 23a, are a manufacturing method in which exhaust gas flows while arbitrarily rotating the transmission from the shaft 17 for the centrifuge rotating drum.
A centrifuge rotating drum 23a is arbitrarily installed at the center of the centrifuge upper casing 2a and the centrifuge lower casing 2b of the main body tank 1.
The cross-sectional view [FIG. 4b] is constituted by such a method.
FIG. 7 shows a diagram of a replacement part main body 42P solved by a ceramic coating having corrosion resistance and wear resistance of the shaft 31.
A total of six shaft shafts 31 are installed in the main body tank 1.
The shaft shaft 31 is composed of a sleeve main body 34 as shown in the sectional view of FIG. 9, the shaft shaft 31 is installed around the sleeve 34, and a gland packing 36 is installed on the outer periphery of the shaft shaft 31, Washer 37 spring 38 sleeve cap 39 bearing mounting bracket 40 bearing 16a.
The rotation of the shaft 31 can be arbitrarily performed by the electric motor 7a.
Since the corrosion resistance and wear resistance of the shaft 31 shown in FIG. 7 has been solved by ceramic coating, the explanation will be made as follows. The replacement part 42P (shown in the sectional view) is formed with a groove 42V at the outer periphery, and the corrosion resistance and resistance. This is a method in which the surface of the worn shaft 31 is arbitrarily selected, the outer diameter of the shaft is drilled into the inner diameter of the replacement part 42P, and the entire outer peripheral surface of the replacement part 42P is coated with a ceramic coating.
The ceramic material can be arbitrarily selected depending on the liquid used, heat resistance and chemical resistance.
In this embodiment, the thickness of the ceramic material is 50 μm of chromium oxide processed by a plasma spraying device manufactured by Meteco.
The replacement part has an outer diameter of 50φ, a length of 150 ^t , and is made of SUS304 using an NC lathe.
In the prior art, since the entire shaft could only be pulled out from the machine, it took a lot of time to detach the parts, and there was a problem in terms of cost and cost.
The service life of the shaft which is the replacement part according to the present invention has a service life of 100 times or more than that of the conventional shaft technology.
Furthermore, as described in [FIG. 7], [FIG. 8], and [FIG. 9], the mechanical device itself can be operated in a short time with a small amount of component removal.
In the conventional technology, the shaft is directly coated with a ceramic coating, and the method is still used, but the test result of the service life when the conventional shaft is directly used in the molecular decomposition and separation apparatus of gas is about 50 hours. And it was short.
If the shaft wears out in 50 hours and water leaks, a problem will occur in the entire apparatus, and the conventional shaft cannot be used.
Even if the replacement part 41P according to the present invention has a water leak before its useful life and it is time to replace it, the replacement part main body 41P42P is manufactured in advance so that the part 42P is replaced with the machining surface 42V when the part is replaced [FIG. 10]. The replacement part main body 42P can be easily attached / detached / replaced with a dedicated tool for attaching / detaching the parts formed in the sleeve main body 34.
Further, the material of 42P can be freely selected as desired, and replacement parts can be recycled.
Although a part of the parts shown in the replacement part of FIG. 8 according to the present invention can be attached / detached in a short time, the conventional technique attaches / detaches the entire shaft and directly applies a wear-resistant coating to the shaft. It takes a long time to complete the production and the cost is high.
The replacement part main body 41P42P of the manufacturing method with the ceramic coating with high quality and reliability according to the present invention is an apparatus for the molecular decomposition of the main body tank gas and the manufacturing method of the separation apparatus in FIG. It is intended only for use.
Therefore, the highly reliable replacement part 41P42P can be provided by the present invention.
The manufacturing method of the liquid electrostatic induction selective membrane filter shown in FIG. 11 will be described. Using a synthetic fiber 44, a synthetic resin silicon layer 45a, and a synthetic resin silicon adhesive 45b, a pile cut woven fiber is attached to the entire surface to produce a sandwich structure. did.
The area required for the liquid electrostatic induction selective membrane filter of the sandwich structure is about 1,000 ^t × 800 ^t and a thickness of 10 ^t is manufactured. The pipe of the sandwich structure is made of plastic pipe 47 and has a total length of 35. ^t Outer diameter 15φ Inner diameter hole 10φ Inner diameter hole 10φ Lower 8φ The number of pipes manufactured is 1280, and 14φ holes are drilled from the surface to the back of the sandwich structure, and the outer diameter 15φ pipe is forced around the mounting pipe 47 It fixed so that there might be no gas leak with the synthetic resin silicon adhesive.
The fiber shown in Fig. 51 is arbitrarily knitted by a method of vertically orienting the fibers shown in Fig. A-1 [52] and processed into a shape of one fiber core [Fig. A-2] 50 and removed. The hole of the pipe 47 having a diameter of 15φ and an inner diameter of 10φ is forcibly compressed by a method of slightly compressing the hole of the lower mounting portion 8φ. The fiber 52 knitted in the longitudinal direction is explained. One fiber string 50 is a base material of the liquid electrostatic induction selective membrane filter, and the purpose of attaching the pipe 47 does not drop the string 50 in the lower direction. In order to control the flow of gas and to make it so. In this manner, the drilling of the inner diameter of the pipe 47 is a manufacturing method configured by selecting the upper and lower hole diameters to be large or small.
This is a method of forming a liquid electrostatic induction selective membrane filter by forming large and small holes in the inner diameter of the pipe 47 and forming the inner diameter portion of the pipe 47 in the vertical direction with fibers 52 knitted in a string shape in the hole.
Since carbon dioxide (CO ₂ ) gas is acidic and the aqueous electrolytic solution is alkaline, a jelly-like film 53 is grown by arbitrarily mixing alkaline water with carbon dioxide (CO ₂ ) gas.
The mechanism of molecular decomposition and separation reaction will be described with reference to the cross-sectional view of [FIG. 11], which is generated by applying electrostatic induction to the membrane.
Therefore, the discovery of this reaction has led to the invention of a molecular decomposition and separation apparatus.
When the molecular decomposition and separation apparatus of the present invention was operated and a measurement was requested from the Tokai Technical Center and Unichemy Corporation, the following results were found.
Measurement date April 6, 2007 Measurement location is 28 Ichinomiya, Ichinomiya, Aichi Pref., Nagahata 28, Tomitsuka, where 100% carbon dioxide (CO ₂ ) was driven into the molecular decomposition and separation device at Cytecs Research Institute, Inc.
Carbon dioxide (CO ₂ ) is 2% or less
The measurement result of oxygen (O ₂ ) was 20% or more.
Measuring instruments Ltd. Best Hakaki CO, CO ₂ gas analyzer BCC-611 (non-dispersive infrared)
Best Instrument Co., Ltd. Oxygen Analyzer BMG-100 (Magnetic)
Furthermore, the electrolytic solution used in the same molecular decomposition and separation apparatus was collected on April 6, 2007, and we asked Unichemy to inspect the total carbon content.
Rainwater A 4mg / l
Rainwater B 3,600mg / l
The above measurement results were obtained.
The inspection method is the TOC measurement method.
The rainwaters A and B described above are temporarily assigned names. Actually, the rainwater A is an electrolytic aqueous solution before driving the molecular decomposition and separation device, and the rainwater B is an electrolytic aqueous solution after driving the device.
The above measurement results confirm that carbon dioxide (CO ₂ ) undergoes a decomposition and separation reaction in the molecular decomposition and separation apparatus.
Details of the measurement results are in the reference material.

The arrangement | sequence chart part of the whole molecule | numerator decomposition | disassembly of the main body tank 1 gas and the manufacturing method of a separation device is shown. The bottom of the main body tank 1 gas molecular decomposition and manufacturing apparatus arrangement diagram of the separation apparatus is shown. The part decomposition | disassembly sectional drawing of a main body tank 1 gas and the manufacturing method of a separation device, a perspective view, a fracture | rupture part, and a one part enlarged view are shown. An exploded view of the centrifuge upper casing 2a, the centrifuge rotating drum body 18, and the centrifuge lower casing 2b is shown. A partial cross-sectional view of the main body tank 1 is shown. Sectional drawing of the centrifuge rotary drum cross section 23a, the casing 2a of the centrifuge upper part, and the casing 2b of the lower part is shown. The block diagram inside a main body tank 1 sectional drawing is shown. The perspective view of the components comprised inside the main body tank 1 is shown. The perspective view and side view of the main body tank 1 are shown. The figure of the replacement | exchange part which solved the corrosion resistance abrasion resistance of the shaft 31 by the ceramic coating is shown. The exploded view of the components which support the whole rotation part of the shaft 31 is shown. A sectional view of a configuration diagram of a sleeve 34 that supports a rotating portion of the shaft 31 is shown. FIG. 4 is a cross-sectional view of a dedicated tool for attaching and detaching components configured inside the sleeve 34. Sectional drawing, a top view, a perspective view, and a partial sectional view of a manufacturing method of the liquid electrostatic induction selective membrane filter 21a are shown. [FIG. A-1] The state which is winding the fiber used as a string is shown. FIG. B-2 shows a fiber string. A front view, a plan view, and a side view of a gas molecular decomposition and separation apparatus are shown. System configuration diagram showing gas molecular decomposition and separation device layout, piping diagram, and flow of gas and electrolyte solution

Explanation of symbols

1 Body tank
(Shows the shape of the completed tank side view)
2a Main body centrifuge upper casing 2b Main body centrifuge lower casing 2c Solenoid valve magnet 3 Carbon dioxide (CO ₂ ) cylinder 4a Electrolyte solution storage tank 4b Electrolyte solution auxiliary tank 4c Electrolyte solution injection nozzle 5 Oxygen collection tank 6a6b Exhaust gas pipe 7a Centrifuge Rotating Drum Motor 7b Pulley 7c Belt 7d Electric Motor 8a Electrolysis Solution Pump 8b Cleaning Pipe 8c Liquid Electrostatic Induction Selective Membrane Filter Cleaning Pump and Nozzle 9 Liquid Electrostatic Induction Selective Membrane Filter Replacement Door 10a Carbon Dioxide (CO ₂₎ injection nozzle 10b-1 carbon dioxide (CO ₂₎ pipe 10b10c overflow pipe (pressure regulating valve)
11a Oxygen piping 11b11c Blower 12 Body mounting tank base 13a13b Body cover 13c13d Drain nozzle 14 Arrow 15a15b showing an enlarged view Shield packing 16a16b Bearing 17a Rotating drum shaft shaft 17s Connection shaft 18a Centrifuge rotating drum body 18b Filter cover holder 19 Rotation Drum casing and 6a6b cover 20 Exhaust gas pipe 6a6b cover 21a Liquid electrostatic induction selective membrane filter 21b Filter washing nozzle and pipe 21c Drainage solenoid valve 21d Drainage nozzle 22 Gas takeout nozzle 23a Centrifuge rotary drum cross section 23b Drainage solenoid valve 24 Drainage Nozzle 25 Bolt hole 26a26b26c Liquid electrostatic induction rotating electrode blade 27 having spiral shape Injection nozzle 28a28b Flow of gas and electrolytic aqueous solution Connecting pipe 28c arrows showing the flow of the gas and the electrolyte solution 28G CO ₂ shows a flow arrows 28W electrolytic solution showing a flow of a gas arrow 29a29b29c liquid electrostatic induction generator pipe 30 shaft resolved spare parts abrasion of 31 shaft axis 32 Cap 33a Blind Flange 33b Packing 33Fa Flange 34 Sleeve body 35a35b Bolt 36 Gland packing 37 Washer 38 Spring 39 Sleeve body cap 40 Bearing mounting bracket 40a Exhaust gas pipe 41P with outer diameter acting as bearing receiver and inner diameter as exhaust gas pipe 6a6b Ceramic coating Replacement part main body 42V Tool mounting part 42P for machining the groove of the replacement part into a V shape. Cross section of replacement part with ceramic coating 42Z Part removal / departure use only Tool 42Y Dedicated tool handle 42U Arrow 43 indicating the direction to pull out parts Keyway 44 Synthetic fiber 45a Synthetic resin silicone 45b Synthetic resin silicone adhesive 46 Pile cut fabric 47 Manufacturing method surrounded by pipes and other surroundings 48 Processed pipe 49 Arrow 50 indicating gas outlet 50 Fiber string 51 Expanded fiber string 52 Wrapped string fiber 53 Jelly-like film 54 grown by chemical reaction between alkali and acid Black dots Is the point to which the substance is adsorbed 55 Surface without gas leakage

Claims (15)

The contents of the electrolytic solution is hydroxide Karyuumu, (KOH), silicon antifoaming agent (Si) surfactant, sodium silicate compound _{(Na2O, nSiO 2, H 2} O) molecules of gas which combines raw material of these chemicals Method used for the manufacturing method of the decomposition and separation device The above chemicals will be referred to as electrolytic aqueous solution. The liquid electrostatic induction generating pipes 29a, 29b and 29c described in FIG. 5 are installed in the main body tank 1 described in FIG. 1 and a shaft shaft indicated by 31 in FIG. 5 is installed in the center of the pipe. Manufacturing method for installing liquid electrostatic induction rotating electrode blade having spiral shape of shaft shaft length [Fig. 5] 29a liquid electrostatic induction generating pipe in which the 28a, 28b running water connection pipe of [Fig. 5] is installed so that the electrolytic solution described in [Claim 1] can flow arbitrarily 29a, 29b, 29c of [Fig. 5] described in [Claim 2] before and after the liquid electrostatic induction generating pipe, the number of caps 32 in [Fig. Manufacturing method in which gas and electrolytic aqueous solution are mixed at rear outlet and jet port 27 is arbitrarily installed Carbon dioxide (CO ₂ ) injection nozzles 10a and electrolytic aqueous solution injection nozzles 4b are installed on the left and right of the liquid induction generating pipe 29a inside the main body tank described in FIG. 1 (explained by FIG. 5). Manufacturing method for installing liquid electrostatic induction rotating electrode blades 26a, 26b, 26c having a spiral shape installed on a central shaft 31 of a pipe The pressure adjusting valve 10b10c for adjusting the gas pressure and water pressure from the inside of the main body tank described in FIG. 1 and the exhaust gas discharge pipes 6a and 6b are connected to the tank of the main body tank 1 and the centrifuge rotating drum lower casing 2b. Manufacturing method to connect The centrifuge housings 2a and 2b are formed, and the exhaust gas pipes 6a and 6b are connected to the left and right from the horizontal portion of the centrifuge rotating drum 23 at the center, and bearings 16a and 16b shield packings 15a and 15b are connected to the outer periphery of the connecting pipe. Manufacturing method to install A manufacturing method comprising a motor 7a, a belt 7c, a pulley 7b, a shaft shaft 17a, and a bearing 16a16b for arbitrary rotation in the left and right direction of the centrifuge rotating drum described in FIG. 4a. In the centrifuge described in FIG. 4b, the left direction is a filter cleaning nozzle 21a, an electrolytic aqueous solution pump 8a, a cleaning pipe 8b, a liquid electrostatic induction selective membrane filter 21a, and a filter in the left direction. Manufacturing method comprising cleaning nozzle 21b, drainage electromagnetic valve 21c, gas extraction nozzle 22, and drainage nozzle 21d As a method of solving the wear of the rotating shaft surface by the gas molecule decomposition and separation device manufacturing method, the outer dimensions of the shaft main body 31 described in the replacement part [FIG. 7] are processed into the inner diameter of the replacement part and installed. This is shown at 31a31b31c in FIG.
The shaft replacement part 41P is shown in the plan view of FIG.
Ceramic coating body 41P Replacement part manufacturing method with ceramic coating that can solve corrosion resistance and wear resistance on the entire replacement part 41P with the tool 42V and keyway 43 processed arbitrarily The material relating to the manufacture of the external body of the liquid electrostatic induction selective membrane filter 21a described in FIG. 11 is a manufacturing method comprising plastic, rubber, ceramic, cement, synthetic fiber, metal fiber, wood, etc. The material described in [Claim 11] is used to surround the periphery by 47, and the inner diameter is formed in a hollow state. The lower inner diameter hole of the hollow body is formed into a hole having an inner diameter that is arbitrarily narrower than the upper inner diameter. [Fig. 11] [Fig. A-1] knitting a string 50 of fibers [Fig. 11] [Fig. A-2] on the inner diameter, and forming the shape of one string of [Fig. In order to form the liquid electrostatic induction selective membrane filter 21a in a circular body, a method of arbitrarily winding 360 ° fibers in the inner surface direction and manufacturing a flat liquid electrostatic induction selective membrane filter can be installed horizontally in the apparatus. Method A method for producing an apparatus utilizing the electrolytic aqueous solution described in claim 1 for the decomposition and separation of bacterial molecules related to molecules and bacteria A method of using a molecular decomposition apparatus for bacteria or gas using the industrial chemicals described in [Claim 1] arbitrarily and using the structure of the invention shown in claims 1 to 15 [Claim 12] Constructing a mixed aqueous solution of acid and alkali as set forth in claim 12, and rotating the centrifuge using energy such as pressure, mixing, collision, ultrasonic vibration, etc. by passing an electrostatic derivative or any current in the aqueous solution An arbitrary current is generated in a jelly-like membrane constituted by growing alkali and acid in the gap between the fibers of the liquid electrostatic induction selective membrane filter according to the present invention, and the current and the current. The name of the method of collecting a material while forming a film in the gap between the fibers by the manufacturing method described in the above and growing a liquid electrostatic derivative in the form of the device using a part called a liquid electrostatic induction selective membrane filter The name is called molecular decomposition and separation device.

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