WO2023191194A1 - Apparatus for preparing ammonium sulfate by using combustion exhaust gas - Google Patents

Apparatus for preparing ammonium sulfate by using combustion exhaust gas Download PDF

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Publication number
WO2023191194A1
WO2023191194A1 PCT/KR2022/011751 KR2022011751W WO2023191194A1 WO 2023191194 A1 WO2023191194 A1 WO 2023191194A1 KR 2022011751 W KR2022011751 W KR 2022011751W WO 2023191194 A1 WO2023191194 A1 WO 2023191194A1
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WO
WIPO (PCT)
Prior art keywords
electrode plate
exhaust gas
combustion exhaust
ammonium sulfate
discharge
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PCT/KR2022/011751
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French (fr)
Korean (ko)
Inventor
김태일
김동연
최영철
유정현
Original Assignee
주식회사 블루텍
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Publication of WO2023191194A1 publication Critical patent/WO2023191194A1/en

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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/24Sulfates of ammonium
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/02Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
    • C25B11/03Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form perforated or foraminous
    • C25B11/031Porous electrodes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00Operating or servicing cells
    • C25B15/02Process control or regulation
    • C25B15/023Measuring, analysing or testing during electrolytic production
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00Operating or servicing cells
    • C25B15/08Supplying or removing reactants or electrolytes; Regeneration of electrolytes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y02A50/2351Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust

Definitions

  • the present invention relates to a device for producing ammonium sulfate from combustion exhaust gas.
  • Patent Document 001 is an automated cleaning device for an electric precipitator for removing harmful substances from exhaust gases, and includes an electrostatic precipitator (10) in which a plurality of dust collection filters (20) are installed in multiple stages at regular intervals, and the electrostatic precipitator (10) Between the cleaning liquid main pipe 110, which is installed on one side and receives the cleaning liquid from an external pump, and each dust collection filter body 20, which is installed in multiple branches in the cross direction from the washing liquid main pipe 110 and arranged in multiple stages at regular intervals.
  • a dust collector internal branch pipe 120 branched to one side, one branch or more installed in a direction crossing each of the dust collector internal branch pipes 120, and extending deep into the interior via one central side of the dust collection filter body 20.
  • a pipe cross-connection means 140 is coupled to the end of the pipe cross-connection means 140, has a left injection pipe 310 and a right injection pipe 310′ on both sides and rotates about the center.
  • a cleaning liquid rotary spray pipe 300 sprays the cleaning liquid toward the dust collection filter body 20 while spraying the washing liquid towards the dust collection filter body 20, and is formed on the left and right spray pipes 310 and 310' of the washing liquid rotary spray pipe 300, respectively, and a constant distance is maintained.
  • left and right spray nozzle holes (311, 311') each drilled, and the left and right spray nozzle holes (311, 311') are located at the lower part of the cleaning liquid rotary spray pipe (300) with respect to its longitudinal center.
  • the left and right spray nozzle holes ( 311,311′) is formed as a long hole having an elongated shape due to the length (L) being large compared to the width (W), and the long hole is a rectangular long hole with both sides angled or a round long hole with round shapes on both sides, and the left and right spray nozzle holes (311,311') disclose an automated cleaning device for an electrostatic precipitator for removing harmful substances from exhaust gases, which is characterized in that the width (W) is 1 mm to 2 mm and the length (L) is 8 mm to 20 mm.
  • Patent Document 002 is an exhaust gas purification agent and an exhaust gas purification method using the same, and includes a step of preparing a harmful gas absorbent at a concentration of 0.1 to 1 g/L by adding a CKD (Cement Kiln Dust) exhaust gas purification agent to water and stirring it, and a bubble reactor. Including the step of injecting the harmful gas absorbent and the exhaust gas into contact with the harmful gas absorbent and the exhaust gas, so that the SO2 conversion rate in the exhaust gas is 95% or more under conditions of pH less than 3 after 50 minutes of contact.
  • a method for purifying exhaust gas is disclosed.
  • Patent document 003 is a fuel saving and exhaust gas reduction device and a manufacturing method thereof, and is a fuel saving and exhaust gas reduction device that is detachably installed on the outer peripheral surface of the fuel supply pipe 30 to reduce fuel supply and reduce exhaust gas emissions, A pair consisting of 40 to 70% by weight of heat-resistant plastic including ultra-heat-resistant engineering plastic and 30 to 60% by weight of ultra stone powder, arranged to face each other, and detachably installed on the outer peripheral surface of the fuel supply pipe (30).
  • the pair of arc-shaped structures (110) (210) (310) (410) (510) It includes fastening means (20) (120) for fastening to each other, and an arc-shaped neodymium insertion hole (H) is formed on the inner peripheral surface of the arc-shaped structure (110) (210) (310) (410) (510),
  • a fuel saving and exhaust gas reduction device is disclosed, characterized in that an arc-shaped Neodymium (Nd) 130 is installed in an arc-shaped Neodymium insertion hole (H).
  • Patent Document 004 is an induction heating high-temperature pyrolysis device with an exhaust gas purification function, a skeletal structure formed in a multi-level shelf structure with a plurality of wheel ball casters installed on the lower bottom, and a skeletal structure installed on the upper shelf of the skeletal structure.
  • eddy currents eddy currents
  • Induction having a carbonization furnace assembly that thermally decomposes, the upper surface of which is fixed to the lower part of the upper shelf of the skeletal structure at a certain distance from the bottom of the carbonization furnace assembly, and a mid- and low-frequency band (X kHz) output from the control unit.
  • X kHz mid- and low-frequency band
  • the carbonization furnace assembly has a square box shape with an open top and is placed at the innermost part.
  • An inner box of a carbonization furnace that maintains the interior heated to a set temperature range by a mid- and low-frequency alternating electromagnetic field generated when induction heating power is applied from a tubular working coil and high-temperature pyrolysis of various wastes introduced therein; It has a form in which a plurality of exhaust gas intake pipes are installed vertically through the upper part of the duct body in the shape of a hollow square frame with an exhaust gas discharge pipe on the bottom of one side, and various wastes are discharged at ultra-high temperature within the inner box of the carbonization furnace.
  • An exhaust gas preheating duct that collects the exhaust gas generated during the pyrolysis process and delivers it to the exhaust gas purifier while simultaneously preheating the inner box of the carbonization furnace, and is installed at the bottom of the carbonization furnace lower plate of the inner box of the carbonization furnace and electrically It is equipped with an insulation function and a mica plate on the lower side of the carbonization furnace that primarily prevents the heat generated in the inner box of the carbonization furnace from being transferred directly to the lower side where the working coil assembly is installed, and a plurality of sensor insertion holes in the front part.
  • a refractory and heat-resistant ceramic insulating plate that secondarily prevents heat generated in the inner box of the carbonization furnace from being transmitted to the lower side where the working coil assembly is installed when installed at the bottom of the mica plate on the lower side of the furnace, and a refractory and heat-resistant ceramic insulating plate provided on the refractory and heat-resistant ceramic insulating plate.
  • a plurality of temperature detection sensors each installed in the sensor insertion hole, detect the heating temperature of the heating object of the carbonization furnace assembly in real time for each heating section and transmit it to the control unit, the outer surface is closely adhered to the inside of the upper shelf of the skeletal structure, and the inner surface is carbonized.
  • a roller assembly that supports the steel wire of the electric winch while installed in the middle of a light metal profile or metal angle or pipe installed in the horizontal direction at the rear upper part, a light metal profile or metal angle or pipe at the top of the skeletal structure, and the lid assembly.
  • Induction heating with an exhaust gas purification function which is composed of a door sealing latch assembly that not only applies pressure to the closed lid assembly when installed at predetermined intervals along the periphery of the upper surface of the door, but also maintains the locked state of the lid assembly.
  • a high-temperature pyrolysis device is being disclosed.
  • Patent Document 1 KR 10-2352941 B1 (Announcement date 2022.01.19.)
  • Patent Document 2 KR 10-2349120 B1 (Announcement date 2022.01.12)
  • Patent Document 3 KR 10-2344332 B1 (Announcement date 2021.12.27.)
  • Patent Document 4 KR 10-2330682 B1 (Announcement date 2021.11.24)
  • the present invention relates to an apparatus for producing ammonium sulfate using nitrogen oxides and sulfur oxides in combustion exhaust gas.
  • the apparatus for manufacturing ammonium sulfate using combustion exhaust gas includes an inflow passage through which combustion exhaust gas flows, a first electrode plate disposed at the discharge end of the inflow passage and through which the combustion exhaust gas passes; an electrolyte portion disposed on a side of the first electrode plate and containing an electrolyte solution; a second electrode plate disposed between the first electrode plate and the electrolyte portion and through which gas discharged from the electrolyte portion permeates; It includes an exhaust flow path through which the gas transmitted from the second electrode plate is discharged, a power supply unit that applies voltage to the first electrode plate and the second electrode plate, and a control unit that controls the power supply unit, wherein the power supply unit is connected to the first electrode plate. A voltage is applied so that the potential difference between the second electrode plate and the second electrode plate is 1.2 to 1.8 V.
  • the present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas in order to solve the problems of the prior art, wherein the first electrode plate includes a porous plate and a coating layer coated on the surface of the porous plate.
  • the present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas in order to solve the problems of the prior art, wherein the second electrode plate includes a porous plate and a coating layer coated on the surface of the porous plate.
  • the present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas to solve the problems of the prior art, and the porous plate is made of carbon, iron, gold, silver, copper, nickel, titanium, cobalt, platinum, rhodium, and iridium. , palladium, and at least one of the oxides of these metals.
  • the present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas in order to solve the problems of the prior art, and the coating layer is composed of at least one of Teflon and ionic polymer.
  • the present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas to solve the problems of the prior art, comprising a supply unit disposed on the inflow passage side to supply the combustion exhaust gas to the inflow passage side, and a supply portion disposed on the discharge passage side. It includes a discharge unit that discharges the gas in the discharge passage to the outside, and the supply unit and the discharge unit are controlled by the control unit.
  • the present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas in order to solve the problems of the prior art
  • the first device is installed in the inflow passage and senses the flow rate or supply pressure of the combustion exhaust gas supplied through the inflow passage. It includes a sensor and a second sensor installed in the discharge passage to sense the flow rate or discharge pressure of the gas discharged through the discharge passage, and the control unit detects the sensor according to the sensing values of each of the first sensor and the second sensor.
  • the supply unit and the discharge unit are controlled.
  • the method for producing ammonium sulfate using combustion exhaust gas according to the present invention can treat combustion exhaust gas and generate ammonia even without an ion separation membrane, and the product can be produced according to the potential difference between the appropriate first electrode plate 200 and the second electrode plate 400. It can change sulfur oxides (SOx) and nitrogen oxides (NOx), which are types of harmful combustion exhaust gases, into useful resources, and can be operated under room temperature/normal pressure conditions, and can be driven even with low concentration reactants. It works.
  • SOx sulfur oxides
  • NOx nitrogen oxides
  • FIG. 1 is a schematic diagram of an ammonium sulfate production device using combustion exhaust gas according to an embodiment of the present invention
  • Figure 2 is a schematic diagram of an ammonium sulfate production device using combustion exhaust gas according to another embodiment of the present invention.
  • Figure 3 is a graph of the conversion rate of sulfate ions and ammonium ions according to the potential difference between the first and second electrode plates of the present invention.
  • the apparatus for producing ammonium sulfate using combustion exhaust gas includes an inflow passage 100 through which combustion exhaust gas flows, and a first electrode plate disposed at the discharge end of the inflow passage and through which the combustion exhaust gas passes ( 200), an electrolyte portion 300 disposed on the side of the first electrode plate and containing an electrolyte solution, disposed between the first electrode plate and the electrolyte portion, and through which gas discharged from the electrolyte portion permeates.
  • the inflow passage 100 may be formed of a material that is rigid enough to withstand the pressure of the incoming combustion exhaust gas, has heat resistance that can withstand a relatively high temperature, and is less reactive with compounds contained in the combustion exhaust gas. there is.
  • the first electrode plate 200 Since the first electrode plate 200 allows gas to pass through, it may be formed of a porous material. A predetermined voltage is applied to the first electrode plate 200 to induce an oxidation reaction of sulfur oxides (SOx) contained in combustion exhaust gas. When an oxidation reaction of sulfur oxides occurs in the combustion exhaust gas, sulfate ions are generated and dissolved in the electrolyte solution contained in the electrolyte unit 300, which will be described later.
  • SOx sulfur oxides
  • the first electrode plate 200 is a part that ionizes sulfur oxide (SOx) to generate sulfuric acid ions.
  • the first electrode plate 200 is an anode and can be called a positive electrode.
  • the electrolyte of the electrolyte solution accommodated in the electrolyte unit 300 is a material that is split into ions in an aqueous solution state and through which current flows.
  • the electrolyte solution contained in the electrolyte unit 300 may be prevented from being discharged to the outside through the first electrode plate 200, the second electrode plate 400, and the outer wall.
  • the second electrode plate 400 forms a pair with the first electrode plate 200, and the gas located in the electrolyte solution of the electrolyte unit 300 is transmitted. A predetermined voltage is also applied to the second electrode plate 400, which induces a reduction reaction of nitrogen oxides (NOx) contained in the gas.
  • the chemical formula of the reduction reaction occurring in the second electrode plate 400 is as follows.
  • the control unit 800 determines that the potential difference between the first electrode plate 200 and the second electrode plate 400 is 1.2 ⁇ 1.8V vs.
  • the power supply so that RHE occurs, only the oxidation reaction of sulfur oxides occurs in the first electrode plate 200, and only the reduction reaction of nitrogen oxides occurs in the second electrode plate 400, thereby causing ammonium sulfate Manufacturing efficiency can be increased.
  • combustion exhaust gas can be treated and ammonia can be generated without an ion separation membrane, and the product can be changed according to the potential difference between the appropriate first electrode plate 200 and the second electrode plate 400. It can convert sulfur oxides (SOx) and nitrogen oxides (NOx), which are types of harmful combustion exhaust gases, into useful resources, and can be operated even under room temperature/normal pressure conditions, with the effect of being able to operate even with low concentration reactants. there is.
  • SOx sulfur oxides
  • NOx nitrogen oxides
  • control unit 800 is a type of control device that controls the power unit and includes a central processing unit (CPU) like a computer. It may be implemented as an electronic device or an electronic device including an electronic device.
  • CPU central processing unit
  • the first electrode plate and the second electrode plate include the porous plates 210 and 410 and the It includes coating layers 220 and 420 coated on the surface of the porous plate.
  • the porous plates 210 and 410 refer to parts that serve as electrodes by applying voltage from the power source, and have T to serve as electrodes. That is, both porous plates 210 and 410 can be connected to the power supply.
  • the coating layers 220 and 420 are shown as being coated only on the electrolyte unit 300 side, but in the present invention, the portion on which the coating layers 220 and 420 are coated is applied to only one side of the electrolyte unit 300 among the electrode plates. It is not limited to being coated, and there may be embodiments such as coating the entire electrode plate.
  • the coating layers 220 and 420 can serve as a catalyst that allows oxidation/reduction reactions to occur more easily while providing waterproofing to prevent the electrolyte solution from penetrating the electrode plate.
  • the porous plate is made of carbon, iron, gold, silver, copper, nickel, titanium, cobalt, It is composed of at least one of platinum, rhodium, iridium, palladium, and oxides of these metals, and the coating layers 220 and 420 are composed of at least one of Teflon and ionic polymer.
  • the materials of the porous plates 210 and 410 and the coating layers 220 and 420 included in each of the first and second electrode plates 200 and 400 may be appropriately selected taking into account various factors. Matters to be considered at this time may include cost, gas permeability, and catalyst efficiency.
  • the porous plate and coating layer included in each of the first electrode plate and the second electrode plate are electrodes. Each plate may be different.
  • the reactions occurring in the first electrode plate 200 and the second electrode plate 400 are different. More specifically, this is because an oxidation reaction of sulfur oxides occurs in the first electrode plate 200, and a reduction reaction of nitrogen oxides occurs in the second electrode plate 400. Because of this difference between the oxidation reaction and the reduction reaction, a material that allows the oxidation reaction to occur more easily is selected for the first electrode plate 200, and a material that allows the reduction reaction to occur more easily is selected for the second electrode plate 400. Thus, the production efficiency of ammonium sulfate can be improved. However, there may also be an embodiment in which the first electrode plate 200 and the second electrode plate 400 are made of the same material.
  • the apparatus for producing ammonium sulfate using combustion exhaust gas according to the present invention is disposed on the side of the inflow passage 100 and directs the combustion exhaust gas toward the inflow passage 100. It includes a supply unit 600 for supplying water and a discharge unit 700 disposed on the side of the discharge passage 500 to discharge the gas in the discharge passage 500 to the outside, wherein the supply unit 600 and the discharge unit 700 ) is controlled by the control unit 800.
  • the supply unit 600 and the discharge unit 700 may be implemented as a device that allows gas to be introduced and discharged, such as a kind of impeller.
  • the supply unit 600 and the discharge unit 700 are implemented as a device such as an impeller, the efficiency of the ammonium sulfate production device according to the present invention may vary depending on the rotation speed of the supply unit 600 and the discharge unit 700. Therefore, the control unit can control the rotation speeds of the supply unit 600 and the discharge unit 700 in conjunction with each other.
  • the apparatus for producing ammonium sulfate using combustion exhaust gas of the present invention is installed in the inflow passage 100 and supplies the combustion exhaust gas through the inflow passage 100.
  • the first sensor 910 and the second sensor 920 may be implemented as a pressure sensor or a flow sensor.
  • the first sensor 910 and the second sensor 920 may be connected to the control unit 800 in a wired or wireless manner to transmit sensing values to the control unit 800.
  • the sensing values of each of the first sensor 910 and the second sensor 920 can more accurately sense the flow rate of incoming combustion exhaust gas or discharged gas than the rotational speed of the supply unit 600 and discharge unit 700 described above. Since it is a sensing value, there is an effect of controlling the ammonium sulfate production device according to the present invention more accurately and efficiently.

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  • Engineering & Computer Science (AREA)
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Abstract

The present invention relates to a method for preparing ammonium sulfate by using nitrogen oxide and sulfur oxide in combustion exhaust gas, and comprises: an introduction flow path through which the combustion exhaust gas is introduced; a first electrode plate arranged at a discharge end of the introduction flow path so that the combustion exhaust gas passes therethrough; an electrolyte part which is arranged on a side surface of the first electrode plate and which accommodates an electrolyte solution; a second electrode plate which is arranged to be spaced from the first electrode plate with the electrolyte part therebetween and which allows gas discharged from the electrolyte part to pass therethrough; a discharge flow path through which gas having passed through the second electrode plate is discharged; a power source unit for applying a voltage to the first electrode plate and the second electrode plate; and a control unit for controlling the power source unit, wherein the power source unit applies the voltage so that the potential difference between the first electrode plate and the second electrode plate is 1.2 V to 1.8 V.

Description

연소배기가스를 이용한 황산암모늄 제조장치Ammonium sulfate manufacturing device using combustion exhaust gas
본 발명은 연소배기가스 중 황산암모늄 제조장치에 관한 것이다.The present invention relates to a device for producing ammonium sulfate from combustion exhaust gas.
특허문헌 001은 배기가스 유해물질 제거용 전기 집진기의 자동화 세척장치이고, 내부에 다수의 집진필터체(20)들이 일정한 등간격 다단으로 설치되어 있는 전기 집진기(10), 상기 전기 집진기(10)의 일측에 설치되고 외부의 펌프로부터 세척액을 전달받는 세척액메인배관(110), 상기 세척액메인배관(110)으로부터 교차방향 다수 갈래로 설치되고 일정간격 다단으로 배치된 각 집진필터체(20)들 사이의 일측으로 분기되는 집진기내부일측분기관(120), 상기 각 집진기내부일측분기관(120)으로부터 교차되는 방향으로 1 갈래 이상 설치되고 집진필터체(20) 중심 일측을 거쳐 내부 깊숙한 곳까지 연장되는 집진기내부중앙측공급관(130), 상기 집진기내부중앙측공급관(130)의 하나 이상 지점에 설치되고 양측의 수평배관을 서로 교차방향으로 연결하며 일측 배관의 회전에도 세척액 공급이 가능하도록 하는 로터리조인트(141)를 포함하는 배관교차연결수단(140), 상기 배관교차연결수단(140)의 끝단부에 결합되고, 양측에 좌측 분사관(310)과 우측 분사관(310′)을 가지며 중심을 기준으로 회전하면서 집진필터체(20)를 향해 세척액을 분사하는 세척액로터리분사관(300), 상기 세척액로터리분사관(300)의 좌,우측 분사관(310,310′) 각각에 형성되고, 일정한 간격이 유지된 상태로 각 다수개씩 천공되는 좌,우측 분사노즐홀(311,311′)을 포함하여 구성되며, 상기 좌,우측 분사노즐홀(311,311′)은 세척액로터리분사관(300)의 길이방향 중심을 기준으로 그 하부 또는 상부를 향하여 형성되되, 각각 10° 내지 30° 범위의 각도(∝)로 경사지게 형성되어 세척액 분사시 세척액로터리분사관(300) 전체가 자동으로 회전되도록 한 것으로, 상기 좌,우측 분사노즐홀(311,311′)은 폭(W) 대비 길이(L)가 커 길쭉한 형태를 갖는 장홀로 형성되고, 상기 장홀은 양측 모두 각진 직사각형장홀 또는 양측이 라운드 형태인 라운드형장홀로서, 상기 좌,우측 분사노즐홀(311,311′)들은 그 폭(W)이 1mm 내지 2mm, 길이(L)는 8mm 내지 20mm로 천공되는 것을 특징으로 하는 배기가스 유해물질 제거용 전기 집진기의 자동화 세척장치를 개시하고 있다.Patent Document 001 is an automated cleaning device for an electric precipitator for removing harmful substances from exhaust gases, and includes an electrostatic precipitator (10) in which a plurality of dust collection filters (20) are installed in multiple stages at regular intervals, and the electrostatic precipitator (10) Between the cleaning liquid main pipe 110, which is installed on one side and receives the cleaning liquid from an external pump, and each dust collection filter body 20, which is installed in multiple branches in the cross direction from the washing liquid main pipe 110 and arranged in multiple stages at regular intervals. A dust collector internal branch pipe 120 branched to one side, one branch or more installed in a direction crossing each of the dust collector internal branch pipes 120, and extending deep into the interior via one central side of the dust collection filter body 20. A rotary joint (141) installed at one or more points of the inner central supply pipe (130) and the inner central supply pipe (130) of the dust collector, connects horizontal pipes on both sides in a cross direction, and enables supply of cleaning solution even when one side of the pipe rotates. ), which includes a pipe cross-connection means 140, is coupled to the end of the pipe cross-connection means 140, has a left injection pipe 310 and a right injection pipe 310′ on both sides and rotates about the center. A cleaning liquid rotary spray pipe 300 sprays the cleaning liquid toward the dust collection filter body 20 while spraying the washing liquid towards the dust collection filter body 20, and is formed on the left and right spray pipes 310 and 310' of the washing liquid rotary spray pipe 300, respectively, and a constant distance is maintained. It is composed of a plurality of left and right spray nozzle holes (311, 311') each drilled, and the left and right spray nozzle holes (311, 311') are located at the lower part of the cleaning liquid rotary spray pipe (300) with respect to its longitudinal center. Or, it is formed toward the top, but is inclined at an angle (∝) in the range of 10° to 30°, so that the entire cleaning liquid rotary spray pipe 300 is automatically rotated when the washing liquid is sprayed, and the left and right spray nozzle holes ( 311,311′) is formed as a long hole having an elongated shape due to the length (L) being large compared to the width (W), and the long hole is a rectangular long hole with both sides angled or a round long hole with round shapes on both sides, and the left and right spray nozzle holes (311,311') disclose an automated cleaning device for an electrostatic precipitator for removing harmful substances from exhaust gases, which is characterized in that the width (W) is 1 mm to 2 mm and the length (L) is 8 mm to 20 mm.
특허문헌 002는 배기가스 정화제 및 이를 이용한 배기가스 정화방법이고, CKD(Cement Kiln Dust) 배기가스 정화제를 물에 투입해 교반하여 0.1 내지 1 g/L 농도로 유해가스 흡수제를 제조하는 단계 및 버블반응기에 상기 유해가스 흡수제와 배기가스를 주입하여, 상기 유해가스 흡수제와 상기 배기가스를 접촉시키는 단계를 포함하여, 상기 접촉 50분 이후 pH 3 미만의 조건에서 상기 배기가스 중 SO2 전환율이 95% 이상이 되도록 하는 배기가스 정화방법을 개시하고 있다.Patent Document 002 is an exhaust gas purification agent and an exhaust gas purification method using the same, and includes a step of preparing a harmful gas absorbent at a concentration of 0.1 to 1 g/L by adding a CKD (Cement Kiln Dust) exhaust gas purification agent to water and stirring it, and a bubble reactor. Including the step of injecting the harmful gas absorbent and the exhaust gas into contact with the harmful gas absorbent and the exhaust gas, so that the SO2 conversion rate in the exhaust gas is 95% or more under conditions of pH less than 3 after 50 minutes of contact. A method for purifying exhaust gas is disclosed.
특허문헌 003은 연료 절감 및 배기가스 저감장치 및 그 제조방법이고, 연료 공급관(30)의 외주면에 탈착 가능하게 설치되어 연료 공급을 절감하고 배기가스 배출을 저감하는 연료 절감 및 배기가스 저감장치로서, 초 내열성 엔지니어링 플라스틱을 포함하는 내열 플라스틱 40~70 중량%와, 울트라 스톤 파우더 30~60 중량%로 이루어지며, 서로 마주보게 배치되고, 상기 연료 공급관(30)의 외주면에 탈착 가능하게 설치되는 한 쌍의 호형 구조물(110)(210)(310)(410)(510) 및 상기 연료 공급관(30)의 외주면에, 상기 한 쌍의 호형 구조물(110)(210)(310)(410)(510)을 서로 체결하기 위한 체결 수단(20)(120)을 포함하며, 상기 호형 구조물(110)(210)(310)(410)(510) 내주면에는 호형 네오디윰 삽입홀(H)이 형성되고, 그 호형 네오디윰 삽입홀(H) 안에 호형 네오디윰(Neodymium;Nd)(130)이 설치되는 것을 특징으로 하는 연료 절감 및 배기가스 저감장치를 개시하고 있다.Patent document 003 is a fuel saving and exhaust gas reduction device and a manufacturing method thereof, and is a fuel saving and exhaust gas reduction device that is detachably installed on the outer peripheral surface of the fuel supply pipe 30 to reduce fuel supply and reduce exhaust gas emissions, A pair consisting of 40 to 70% by weight of heat-resistant plastic including ultra-heat-resistant engineering plastic and 30 to 60% by weight of ultra stone powder, arranged to face each other, and detachably installed on the outer peripheral surface of the fuel supply pipe (30). On the outer peripheral surface of the arc-shaped structures (110) (210) (310) (410) (510) and the fuel supply pipe (30), the pair of arc-shaped structures (110) (210) (310) (410) (510) It includes fastening means (20) (120) for fastening to each other, and an arc-shaped neodymium insertion hole (H) is formed on the inner peripheral surface of the arc-shaped structure (110) (210) (310) (410) (510), A fuel saving and exhaust gas reduction device is disclosed, characterized in that an arc-shaped Neodymium (Nd) 130 is installed in an arc-shaped Neodymium insertion hole (H).
특허문헌 004는 배기가스 정화기능을 갖는 유도가열 고온 열분해장치이고, 다단 선반 구조로 성형하되, 하단 저면에는 복수의 바퀴 볼캐스터가 설치된 형태를 갖는 골격 구조체와, 상기 골격 구조체의 상단 선반 상에 설치된 상태에서 워킹코일 조립체에서 방사되는 유도가열 교번 전자계장에 의해 생성되는 와전류(맴돌이 전류)에 의한 주울열로 변환되며 내부가 정해진 초고온 범위로 유도 가열된 상태를 유지하며 내부에 투입되는 각종 폐기물을 초고온으로 열분해시켜 주는 탄화로 조립체와, 상면이 상기 탄화로 조립체의 저면과 일정거리 떨어지게 상기 골격 구조체의 상단 선반 하부에 고정 설치된 형태를 갖고, 제어부에서 출력되는 중,저주파수 대역(X ㎑)을 갖는 유도가열 전원이 관형의 워킹코일에 통전되면서 전자계장을 발생시켜 탄화로 조립체의 피가열체가 발열되고, 그 유도가열에 의한 발열로 탄화로 내부가 설정된 온도로 가열되게 하는 워킹코일 조립체와, 상기 골격 구조체의 중간 선반 상에 설치된 상태에서 워킹코일 조립체의 냉각은 물론 각종 전장품의 구동을 제어하는 제어부와, 상기 골격 구조체의 하단 선반 상에 설치된 상태에서 상기 탄화로 조립체 내에서 폐기물을 열분해시키는 과정에서 발생되는 유해 배기가스의 열을 정해진 온도 이하로 냉각시켜 줌과 동시에 정화시켜 외부로 배출해 주는 배기가스 정화기로 구성하되, 상기 탄화로 조립체는, 상부가 개구된 사각 함체 형상을 갖고 맨 안쪽에 배치된 상태에서 관형의 워킹코일에서 유도가열 전원이 인가될 때 발생하는 중,저주파 교번 전자계장에 의해 내부가 정해진 온도 범위로 가열된 상태를 유지하며 내부에 투입된 각종 폐기물을 고온 열분해시켜 주는 탄화로 내부 박스와, 일측 저면에 배기가스 배출관을 구비한 속이빈 사각 틀체 형상의 덕트 본체 상방부에서 수직 방향으로 복수의 배기가스 흡입 파이프가 내부로 관통되게 설치된 형태를 갖고, 상기 탄화로 내부 박스 내에서 각종 폐기물이 초고온으로 열분해시키는 과정에서 발생되는 배기가스를 포집하여 배기가스 정화기 측으로 전달함과 동시에 탄화로 내부 박스를 예열시켜 주는 배기가스 예열 덕트와, 상기 탄화로 내부 박스의 탄화로 하판 저부에 설치된 상태에서 전기적인 절연기능과 탄화로 내부 박스에서 발생되는 열이 워킹코일 조립체가 설치되는 하부 측으로 바로 전달되는 것을 1차적으로 방지하는 탄화로 하부측 운모판과, 전방부에 복수의 센서 삽입공을 구비하고 상기 탄화로 하부측 운모판의 저부에 설치된 상태에서 탄화로 내부 박스에서 발생되는 열이 워킹코일 조립체가 설치되는 하부 측으로 전달되는 것을 2차적으로 방지하는 내화 내열 세라믹 단열판과, 상기 내화 내열 세라믹 단열판에 구비된 센서 삽입공 내에 각각 설치된 상태에서 탄화로 조립체의 피가열체 발열온도를 발열 구획 별로 실시간 검출하여 제어부로 전달하는 복수의 온도검출센서와, 상기 골격 구조체의 상단 선반 내측에 외면이 밀착되고 내면은 탄화로 내부 박스 및 배기가스 예열 덕트의 전,후,좌,우면에서 일정거리 이격되는 탄화로 외측 케이스와, 상기 탄화로 외측 케이스의 내면과 탄화로 내부 박스 및 배기가스 예열 덕트에 형성되는 공간부 내에 투입시켜 경화시킨 단열 경량 캐스터블과, 상기 탄화로 내부 박스의 후방부에 설치되는 복수의 힌지 조립체를 중심으로 상기 탄화로 내부 박스와 단열 경량 캐스터블 및 탄화로 외측 케이스의 상방 개구부위를 수동 또는 자동으로 개폐시켜 줄 수 있도록 설치되는 뚜껑 조립체와, 상기 탄화로 내부 박스 및 탄화로 외측 케이스의 상단부에 각각 설치된 형태를 갖고 상기 탄화로 조립체의 상단면과 상기 뚜껑 조립체의 저면 사이의 기밀을 2중으로 유지시켜 주는 1,2차 기밀유지수단과, 상기 골격 구조체의 상단 선반 중 후방 저부에 고정 설치된 상태에서 제어부의 출력신호에 부응하여 상기 뚜껑 조립체를 개폐시켜 주는 전동 윈치와, 상기 골격 구조체의 상단 선반 중 후방 상부에서 가로방향으로 설치된 경금속 프로파일 내지는 금속 앵글이나 파이프의 중간부에 설치된 상태에서 전동 윈치의 스틸 와이어를 지지해 주는 롤러 조립체와, 상기 골격 구조체의 상단 경금속 프로파일 내지는 금속 앵글이나 파이프과 상기 뚜껑 조립체의 상면 주연부를 따라 정해진 간격을 두고 설치된 상태에서 닫힌 뚜껑 조립체에 대해 가압력을 주게 됨은 물론 뚜껑 조립체의 잠김상태를 유지시켜 주는 도어 밀폐용 걸쇠 조립체로 구성한 것을 특징으로 하는 배기가스 정화기능을 갖는 유도가열 고온 열분해장치를 개시하고 있다.Patent Document 004 is an induction heating high-temperature pyrolysis device with an exhaust gas purification function, a skeletal structure formed in a multi-level shelf structure with a plurality of wheel ball casters installed on the lower bottom, and a skeletal structure installed on the upper shelf of the skeletal structure. In this state, it is converted into Joule heat by eddy currents (eddy currents) generated by the induction heating alternating electromagnetic field radiated from the working coil assembly, and the inside is maintained in a state of induction heating within a set ultra-high temperature range, and various wastes input inside are kept at ultra-high temperatures. Induction having a carbonization furnace assembly that thermally decomposes, the upper surface of which is fixed to the lower part of the upper shelf of the skeletal structure at a certain distance from the bottom of the carbonization furnace assembly, and a mid- and low-frequency band (X kHz) output from the control unit. As the heating power is passed through the tubular working coil, an electromagnetic field is generated so that the heating object of the carbonization furnace assembly is heated, and the inside of the carbonization furnace is heated to a set temperature by the heat generated by the induction heating, and the skeletal structure A control unit that controls the cooling of the working coil assembly as well as the operation of various electrical components when installed on the middle shelf of the skeletal structure, and a control unit that controls the operation of various electrical components when installed on the middle shelf of the skeletal structure, It consists of an exhaust gas purifier that cools the heat of harmful exhaust gas below a set temperature, purifies it, and discharges it to the outside. The carbonization furnace assembly has a square box shape with an open top and is placed at the innermost part. An inner box of a carbonization furnace that maintains the interior heated to a set temperature range by a mid- and low-frequency alternating electromagnetic field generated when induction heating power is applied from a tubular working coil and high-temperature pyrolysis of various wastes introduced therein; It has a form in which a plurality of exhaust gas intake pipes are installed vertically through the upper part of the duct body in the shape of a hollow square frame with an exhaust gas discharge pipe on the bottom of one side, and various wastes are discharged at ultra-high temperature within the inner box of the carbonization furnace. An exhaust gas preheating duct that collects the exhaust gas generated during the pyrolysis process and delivers it to the exhaust gas purifier while simultaneously preheating the inner box of the carbonization furnace, and is installed at the bottom of the carbonization furnace lower plate of the inner box of the carbonization furnace and electrically It is equipped with an insulation function and a mica plate on the lower side of the carbonization furnace that primarily prevents the heat generated in the inner box of the carbonization furnace from being transferred directly to the lower side where the working coil assembly is installed, and a plurality of sensor insertion holes in the front part. A refractory and heat-resistant ceramic insulating plate that secondarily prevents heat generated in the inner box of the carbonization furnace from being transmitted to the lower side where the working coil assembly is installed when installed at the bottom of the mica plate on the lower side of the furnace, and a refractory and heat-resistant ceramic insulating plate provided on the refractory and heat-resistant ceramic insulating plate. A plurality of temperature detection sensors, each installed in the sensor insertion hole, detect the heating temperature of the heating object of the carbonization furnace assembly in real time for each heating section and transmit it to the control unit, the outer surface is closely adhered to the inside of the upper shelf of the skeletal structure, and the inner surface is carbonized. In the outer case of the carbonization furnace, which is spaced a certain distance from the front, rear, left, and right sides of the furnace inner box and the exhaust gas preheating duct, and in the space formed in the inner surface of the outer case of the carbonization furnace and the inner box of the carbonization furnace and the exhaust gas preheating duct. Manually or It has a lid assembly that is installed to automatically open and close, and is installed on the upper part of the inner box of the carbonization furnace and the outer case of the carbonization furnace, and provides double airtightness between the upper surface of the carbonization furnace assembly and the bottom of the lid assembly. Primary and secondary airtight maintenance means for maintaining the lid assembly, an electric winch that opens and closes the lid assembly in response to an output signal from the control unit while fixed to the rear bottom of the upper shelf of the skeletal structure, and an upper shelf of the skeletal structure A roller assembly that supports the steel wire of the electric winch while installed in the middle of a light metal profile or metal angle or pipe installed in the horizontal direction at the rear upper part, a light metal profile or metal angle or pipe at the top of the skeletal structure, and the lid assembly. Induction heating with an exhaust gas purification function, which is composed of a door sealing latch assembly that not only applies pressure to the closed lid assembly when installed at predetermined intervals along the periphery of the upper surface of the door, but also maintains the locked state of the lid assembly. A high-temperature pyrolysis device is being disclosed.
(특허문헌 1) KR 10-2352941 B1 (공고일 2022.01.19.)(Patent Document 1) KR 10-2352941 B1 (Announcement date 2022.01.19.)
(특허문헌 2) KR 10-2349120 B1 (공고일 2022.01.12)(Patent Document 2) KR 10-2349120 B1 (Announcement date 2022.01.12)
(특허문헌 3) KR 10-2344332 B1 (공고일 2021.12.27.)(Patent Document 3) KR 10-2344332 B1 (Announcement date 2021.12.27.)
(특허문헌 4) KR 10-2330682 B1 (공고일 2021.11.24)(Patent Document 4) KR 10-2330682 B1 (Announcement date 2021.11.24)
본 발명은 연소배기가스 중 질소산화물과 황산화물을 이용한 황산암모늄 제조장치에 관한 것이다.The present invention relates to an apparatus for producing ammonium sulfate using nitrogen oxides and sulfur oxides in combustion exhaust gas.
종래기술의 문제점을 해결하기 위한 본 발명에 의한 연소배기가스를 이용한 황산암모늄 제조장치는, 연소배기가스가 유입되는 유입 유로, 상기 유입 유로의 배출단에 배치되어 상기 연소배기가스가 투과하는 제1전극판, 상기 제1전극판의 측면에 배치되며, 전해질 용액이 수용되는 전해질부, 상기 제1전극판과 상기 전해질부를 사이에 두고 배치되며, 상기 전해질부에서 배출되는 가스가 투과하는 제2전극판, 상기 제2전극판에서 투과된 가스가 배출되는 배출 유로, 상기 제1전극판과 상기 제2전극판에 전압을 인가하는 전원부 및 상기 전원부를 제어하는 제어부를 포함하되, 상기 전원부는 상기 제1전극판과 상기 제2전극판의 전위차가 1.2~1.8V가 되도록 전압을 인가한다.The apparatus for manufacturing ammonium sulfate using combustion exhaust gas according to the present invention to solve the problems of the prior art includes an inflow passage through which combustion exhaust gas flows, a first electrode plate disposed at the discharge end of the inflow passage and through which the combustion exhaust gas passes; an electrolyte portion disposed on a side of the first electrode plate and containing an electrolyte solution; a second electrode plate disposed between the first electrode plate and the electrolyte portion and through which gas discharged from the electrolyte portion permeates; It includes an exhaust flow path through which the gas transmitted from the second electrode plate is discharged, a power supply unit that applies voltage to the first electrode plate and the second electrode plate, and a control unit that controls the power supply unit, wherein the power supply unit is connected to the first electrode plate. A voltage is applied so that the potential difference between the second electrode plate and the second electrode plate is 1.2 to 1.8 V.
종래기술의 문제점을 해결하기 위한 본 발명에 의한 연소배기가스를 이용한 황산암모늄 제조장치에 관한 것이고, 상기 제1전극판은, 다공성 판 및 상기 다공성 판의 표면에 코팅된 코팅층을 포함한다.The present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas in order to solve the problems of the prior art, wherein the first electrode plate includes a porous plate and a coating layer coated on the surface of the porous plate.
종래기술의 문제점을 해결하기 위한 본 발명에 의한 연소배기가스를 이용한 황산암모늄 제조장치에 관한 것이고, 상기 제2전극판은, 다공성 판 및 상기 다공성 판의 표면에 코팅된 코팅층을 포함한다.The present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas in order to solve the problems of the prior art, wherein the second electrode plate includes a porous plate and a coating layer coated on the surface of the porous plate.
종래기술의 문제점을 해결하기 위한 본 발명에 의한 연소배기가스를 이용한 황산암모늄 제조장치에 관한 것이고, 상기 다공성 판은, 탄소, 철, 금, 은, 동, 니켈, 티타늄, 코발트, 백금, 로듐, 이리듐, 팔라듐 및 이들 금속의 산화물들 중 적어도 어느 하나로 구성된다.The present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas to solve the problems of the prior art, and the porous plate is made of carbon, iron, gold, silver, copper, nickel, titanium, cobalt, platinum, rhodium, and iridium. , palladium, and at least one of the oxides of these metals.
종래기술의 문제점을 해결하기 위한 본 발명에 의한 연소배기가스를 이용한 황산암모늄 제조장치에 관한 것이고, 상기 코팅층은, 테프론, 이온중합체 중 적어도 어느 하나로 구성된다.The present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas in order to solve the problems of the prior art, and the coating layer is composed of at least one of Teflon and ionic polymer.
종래기술의 문제점을 해결하기 위한 본 발명에 의한 연소배기가스를 이용한 황산암모늄 제조장치에 관한 것이고, 상기 유입 유로측에 배치되어 상기 연소배기가스를 상기 유입 유로측으로 공급하는 공급부 및 상기 배출 유로측에 배치되어 상기 배출 유로의 가스를 외부로 배출하는 배출부를 포함하되, 상기 공급부와 상기 배출부는 상기 제어부에 의해 제어된다.The present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas to solve the problems of the prior art, comprising a supply unit disposed on the inflow passage side to supply the combustion exhaust gas to the inflow passage side, and a supply portion disposed on the discharge passage side. It includes a discharge unit that discharges the gas in the discharge passage to the outside, and the supply unit and the discharge unit are controlled by the control unit.
종래기술의 문제점을 해결하기 위한 본 발명에 의한 연소배기가스를 이용한 황산암모늄 제조장치에 관한 것이고, 상기 유입 유로에 설치되어 상기 유입 유로를 통해 공급되는 상기 연소배기가스의 유량이나 공급 압력을 센싱하는 제1센서 및 상기 배출 유로에 설치되어 상기 배출 유로를 통해 배출되는 가스의 유량이나 배출 압력을 센싱하는 제2센서를 포함하고, 상기 제어부는, 상기 제1센서와 상기 제2센서 각각의 센싱값에 따라 상기 공급부와 상기 배출부를 제어한다.The present invention relates to an apparatus for producing ammonium sulfate using combustion exhaust gas in order to solve the problems of the prior art, and the first device is installed in the inflow passage and senses the flow rate or supply pressure of the combustion exhaust gas supplied through the inflow passage. It includes a sensor and a second sensor installed in the discharge passage to sense the flow rate or discharge pressure of the gas discharged through the discharge passage, and the control unit detects the sensor according to the sensing values of each of the first sensor and the second sensor. The supply unit and the discharge unit are controlled.
본 발명에 의한 연소배기가스를 이용한 황산암모늄 제조방법은, 이온분리막 없이도 연소배기가스의 처리 및 암모니아를 생성할 수 있고, 적절한 제1전극판(200)과 제2전극판(400)의 전위차에 따라 제조물을 변경할 수 있으며, 연소배기가스 유해물질의 일종인 황산화물(SOx)과 질소산화물(NOx)를 유용한 자원으로 전환할 수 있고, 상온/상압 조건에서도 운전 가능하며, 낮은 농도의 반응물로도 구동이 가능한 효과가 있다.The method for producing ammonium sulfate using combustion exhaust gas according to the present invention can treat combustion exhaust gas and generate ammonia even without an ion separation membrane, and the product can be produced according to the potential difference between the appropriate first electrode plate 200 and the second electrode plate 400. It can change sulfur oxides (SOx) and nitrogen oxides (NOx), which are types of harmful combustion exhaust gases, into useful resources, and can be operated under room temperature/normal pressure conditions, and can be driven even with low concentration reactants. It works.
도 1은 본 발명의 일실시예에 의한 연소배기가스를 이용한 황산암모늄 제조장치의 개략도이고,1 is a schematic diagram of an ammonium sulfate production device using combustion exhaust gas according to an embodiment of the present invention;
도 2는 본 발명의 다른 실시예에 의한 연소배기가스를 이용한 황산암모늄 제조장치의 개략도이며,Figure 2 is a schematic diagram of an ammonium sulfate production device using combustion exhaust gas according to another embodiment of the present invention;
도 3은 본 발명의 제1전극판과 제2전극판 사이의 전위차에 따른 황산이온과 암모늄이온의 전화율 그래프이다.Figure 3 is a graph of the conversion rate of sulfate ions and ammonium ions according to the potential difference between the first and second electrode plates of the present invention.
이하, 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자가 본 발명을 용이하게 실시할 수 있을 정도로 상세히 설명하기 위하여, 본 발명의 가장 바람직한 실시 예를 상세하게 설명한다.Hereinafter, the most preferred embodiments of the present invention will be described in detail in order to enable those skilled in the art to easily practice the present invention.
아래의 실시예에서 인용하는 번호는 인용대상에만 한정되지 않으며, 모든 실시예에 적용될 수 있다. 실시예에서 제시한 구성과 동일한 목적 및 효과를 발휘하는 대상은 균등한 치환대상에 해당된다. 실시예에서 제시한 상위개념은 기재하지 않은 하위개념 대상을 포함한다.Numbers cited in the examples below are not limited to the objects of citation and can be applied to all examples. An object that has the same purpose and effect as the configuration presented in the examples is an equivalent replacement object. The high-level concept presented in the examples includes low-level concept objects that are not described.
(실시예 1-1) 본 발명인 연소배기가스를 이용한 황산암모늄 제조장치는, 연소배기가스가 유입되는 유입 유로(100), 상기 유입 유로의 배출단에 배치되어 상기 연소배기가스가 투과하는 제1전극판(200), 상기 제1전극판의 측면에 배치되며, 전해질 용액이 수용되는 전해질부(300), 상기 제1전극판과 상기 전해질부를 사이에 두고 배치되며, 상기 전해질부에서 배출되는 가스가 투과하는 제2전극판(400), 상기 제2전극판에서 투과된 가스가 배출되는 배출 유로(500), 상기 제1전극판과 상기 제2전극판에 전압을 인가하는 전원부(미도시) 및 상기 전원부를 제어하는 제어부(800)를 포함하되, 상기 전원부는 상기 제1전극판과 상기 제2전극판의 전위차가 1.2~1.8V가 되도록 전압을 인가한다.(Example 1-1) The apparatus for producing ammonium sulfate using combustion exhaust gas according to the present invention includes an inflow passage 100 through which combustion exhaust gas flows, and a first electrode plate disposed at the discharge end of the inflow passage and through which the combustion exhaust gas passes ( 200), an electrolyte portion 300 disposed on the side of the first electrode plate and containing an electrolyte solution, disposed between the first electrode plate and the electrolyte portion, and through which gas discharged from the electrolyte portion permeates. A second electrode plate 400, an exhaust passage 500 through which gas transmitted from the second electrode plate is discharged, a power supply unit (not shown) that applies voltage to the first electrode plate and the second electrode plate, and the power supply unit. It includes a control unit 800 that controls, wherein the power unit applies a voltage so that the potential difference between the first electrode plate and the second electrode plate is 1.2 to 1.8 V.
유입 유로(100)는 유입되는 연소배기가스의 압력을 견딜 수 있을 정도로 강성을 가지면서, 상대적으로 높은 온도를 견딜 수 있는 내열성과, 연소배기가스에 포함되는 화합물들과의 반응성이 적은 재질로 형성될 수 있다.The inflow passage 100 may be formed of a material that is rigid enough to withstand the pressure of the incoming combustion exhaust gas, has heat resistance that can withstand a relatively high temperature, and is less reactive with compounds contained in the combustion exhaust gas. there is.
제1전극판(200)은 가스가 투과되기 때문에, 다공성 재질로 형성될 수 있다. 제1전극판(200)에는 소정의 전압이 인가되어, 연소배기가스에 포함된 황산화물(SOx)의 산화 반응을 유도한다. 연소배기가스에서 황산화물의 산화 반응이 발생하면 황산이온이 발생해 후술할 전해질부(300)에 포함된 전해질용액에 녹게 된다. 이러한 제1전극판(200)에서 발생하는 산화반응의 화학식은 아래와 같다.Since the first electrode plate 200 allows gas to pass through, it may be formed of a porous material. A predetermined voltage is applied to the first electrode plate 200 to induce an oxidation reaction of sulfur oxides (SOx) contained in combustion exhaust gas. When an oxidation reaction of sulfur oxides occurs in the combustion exhaust gas, sulfate ions are generated and dissolved in the electrolyte solution contained in the electrolyte unit 300, which will be described later. The chemical formula of the oxidation reaction occurring in the first electrode plate 200 is as follows.
Figure PCTKR2022011751-appb-C000001
Figure PCTKR2022011751-appb-C000001
즉, 제1전극판(200)은 황산화물(SOx)을 이온화 시켜 황산이온을 발생시키는 부분이다. 이때 제1전극판(200)은 애노드(Anode)로, 양극이라고 할 수 있다.That is, the first electrode plate 200 is a part that ionizes sulfur oxide (SOx) to generate sulfuric acid ions. At this time, the first electrode plate 200 is an anode and can be called a positive electrode.
전해질부(300)에 수용되는 전해질 용액의 전해질은 수용액 상태에서 이온으로 쪼개져 전류가 흐르는 물질이다. 전해질부(300)에 수용되는 전해질 용액은 제1전극판(200)과 제2전극판(400) 그리고, 외벽을 통해 외부로 배출되지 못하도록 할 수 있다. The electrolyte of the electrolyte solution accommodated in the electrolyte unit 300 is a material that is split into ions in an aqueous solution state and through which current flows. The electrolyte solution contained in the electrolyte unit 300 may be prevented from being discharged to the outside through the first electrode plate 200, the second electrode plate 400, and the outer wall.
제2전극판(400)은 제1전극판(200)과 한 쌍을 이루며, 전해질부(300)의 전해질 용액에 위치한 가스가 투과된다. 제2전극판(400) 또한 소정의 전압이 인가되며, 가스에 포함된 질소산화물(NOx)의 환원 반응을 유도한다. 이러한 제2전극판(400)에서 발생하는 환원반응의 화학식은 아래와 같다.The second electrode plate 400 forms a pair with the first electrode plate 200, and the gas located in the electrolyte solution of the electrolyte unit 300 is transmitted. A predetermined voltage is also applied to the second electrode plate 400, which induces a reduction reaction of nitrogen oxides (NOx) contained in the gas. The chemical formula of the reduction reaction occurring in the second electrode plate 400 is as follows.
Figure PCTKR2022011751-appb-C000002
Figure PCTKR2022011751-appb-C000002
가스에서 질소산화물(NOx)의 환원 반응이 발생하면, 암모늄이온이 발생해 전해질용액에 녹게 되고, 최종적으로는 황산이온과 암모늄이온을 통해 황산암모늄을 제조할 수 있다.When a reduction reaction of nitrogen oxides (NOx) occurs in gas, ammonium ions are generated and dissolved in the electrolyte solution, and ultimately ammonium sulfate can be produced through sulfate ions and ammonium ions.
다만, 상기한 바와 같은 본 발명에서 제1전극판(200)에서는 황산이온만 생성되면 바람직하나, 제1전극판(200)에서도 질소산화물(NOx)이 산화될 수 있으며, 제2전극판(400)에서도 황산화물(SOx)이 환원될 수 있다. 이럴 경우 본 발명에서 제조하고자 하는 암모니아의 제조 효율이 저하되므로, 제1전극판(200)에서는 황산화물의 환원만이 일어나고, 제2전극판(400)에서는 질소산화물의 산화만이 일어나게 하는 것이 중요하다.However, in the present invention as described above, it is preferable if only sulfate ions are generated in the first electrode plate 200, but nitrogen oxides (NOx) can also be oxidized in the first electrode plate 200, and the second electrode plate 400 ) Sulfur oxides (SOx) can also be reduced. In this case, the production efficiency of ammonia to be produced in the present invention decreases, so it is important to ensure that only reduction of sulfur oxides occurs in the first electrode plate 200 and only oxidation of nitrogen oxides occurs in the second electrode plate 400. do.
이에 실험을 했을 때, 도면에 도시된 바와 같이 1.1 ~ 1.3V vs. RHE에서는 황산화물이 90% 이상 황산이온으로 전환된 것을 확인할 수 있으며, -0.1 ~ -0.5V vs. RHE에서는 질소산화물 70% 이상 암모늄이온으로 전환되는 것을 확인할 수 있었다. 이때 마이너스 값을 가지는 V vs. RHE값은 제2전극판(400)의 전위가 제1전극판(200)의 전위보다 높다는 의미이며, 플러스값을 가지는 V vs. RHE값은 제1전극판(200)의 전위가 제2전극판(400)의 전위보다 높다는 의미이다. 이러한 실험결과에 따라 본 실시예에서 제어부(800)는 제1전극판(200)과 제2전극판(400)의 전위차가 1.2 ~ 1.8V vs. RHE가 되도록 전원부를 제어해, 제1전극판(200)에서는 황산화물의 산화반응만이 발생하게 하고, 제2전극판(400)에서는 질소산화물의 환원반응만이 발생하도록 유도하여, 황산암모늄의 제조 효율을 증가시킬 수 있다. 또한 필요에 따라 전압을 적절히 조절하여, 황산이온만을 제조하거나, 암모니아(암모늄 이온)만을 제조하는 등의 실시예 또한 있을 수 있다.When experimenting with this, as shown in the figure, 1.1 ~ 1.3V vs. In RHE, it can be confirmed that more than 90% of sulfur oxides have been converted to sulfate ions, -0.1 ~ -0.5V vs. In RHE, it was confirmed that more than 70% of nitrogen oxides were converted to ammonium ions. At this time, V vs. negative value. The RHE value means that the potential of the second electrode plate 400 is higher than the potential of the first electrode plate 200, and V vs. The RHE value means that the potential of the first electrode plate 200 is higher than the potential of the second electrode plate 400. According to these experimental results, in this embodiment, the control unit 800 determines that the potential difference between the first electrode plate 200 and the second electrode plate 400 is 1.2 ~ 1.8V vs. By controlling the power supply so that RHE occurs, only the oxidation reaction of sulfur oxides occurs in the first electrode plate 200, and only the reduction reaction of nitrogen oxides occurs in the second electrode plate 400, thereby causing ammonium sulfate Manufacturing efficiency can be increased. Additionally, there may be an embodiment in which only sulfate ions or only ammonia (ammonium ions) are produced by appropriately adjusting the voltage as needed.
본 실시예는 상기한 바와 같은 구성들을 통해, 이온분리막 없이도 연소배기가스의 처리 및 암모니아를 생성할 수 있고, 적절한 제1전극판(200)과 제2전극판(400)의 전위차에 따라 제조물을 변경할 수 있으며, 연소배기가스 유해물질의 일종인 황산화물(SOx)과 질소산화물(NOx)를 유용한 자원으로 전환할 수 있고, 상온/상압 조건에서도 운전 가능하며, 낮은 농도의 반응물로도 구동이 가능한 효과가 있다.In this embodiment, through the above-described configurations, combustion exhaust gas can be treated and ammonia can be generated without an ion separation membrane, and the product can be changed according to the potential difference between the appropriate first electrode plate 200 and the second electrode plate 400. It can convert sulfur oxides (SOx) and nitrogen oxides (NOx), which are types of harmful combustion exhaust gases, into useful resources, and can be operated even under room temperature/normal pressure conditions, with the effect of being able to operate even with low concentration reactants. there is.
본 실시예에서 제어부(800)는 상기 전원부를 제어하는 제어장치의 일종으로, 컴퓨터와 같이 중앙처리장치(CPU)를 포함하는 전자소자 또는 전자소자를 포함하는 전자기기로 구현될 수 있다.In this embodiment, the control unit 800 is a type of control device that controls the power unit and includes a central processing unit (CPU) like a computer. It may be implemented as an electronic device or an electronic device including an electronic device.
(실시예 1-2) 본 발명인 연소배기가스를 이용한 황산암모늄 제조장치는, (실시예 1-1)에 있어서, 상기 제1전극판과 제2전극판은, 다공성 판(210, 410) 및 상기 다공성 판의 표면에 코팅된 코팅층(220, 420)을 포함한다.(Example 1-2) In the apparatus for producing ammonium sulfate using combustion exhaust gas according to the present invention (Example 1-1), the first electrode plate and the second electrode plate include the porous plates 210 and 410 and the It includes coating layers 220 and 420 coated on the surface of the porous plate.
여기서 다공성 판(210, 410)은 전원부에서 전압을 인가하여 전극 역할을 하는 부분을 의미하며, 전극 역할을 할 T 있다. 즉, 다공성 판(210, 410) 모두는 전원부에 연결될 수 있다. 도면에서 코팅층(220, 420)은 전해질부(300)측에만 코팅된 것으로 도시되어 있지만, 본 발명은 코팅층(220, 420)이 코팅되는 부분을 전극판들 중, 전해질부(300)측 일면에만 코팅된 것으로 한정하지 않고, 전극판 전체에 코팅되는 등의 실시예가 있을 수 있다. 코팅층(220, 420)은 방수가 전해질 용액이 전극판을 투과하지 못하도록 방수처리함과 동시에 산화/환원 반응이 보다 용이하게 일어나도록 할 수 있는 촉매역할을 할 수 있다.Here, the porous plates 210 and 410 refer to parts that serve as electrodes by applying voltage from the power source, and have T to serve as electrodes. That is, both porous plates 210 and 410 can be connected to the power supply. In the drawing, the coating layers 220 and 420 are shown as being coated only on the electrolyte unit 300 side, but in the present invention, the portion on which the coating layers 220 and 420 are coated is applied to only one side of the electrolyte unit 300 among the electrode plates. It is not limited to being coated, and there may be embodiments such as coating the entire electrode plate. The coating layers 220 and 420 can serve as a catalyst that allows oxidation/reduction reactions to occur more easily while providing waterproofing to prevent the electrolyte solution from penetrating the electrode plate.
(실시예 1-3) 본 발명인 연소배기가스를 이용한 황산암모늄 제조장치는, (실시예 1-2)에 있어서, 상기 다공성 판은, 탄소, 철, 금, 은, 동, 니켈, 티타늄, 코발트, 백금, 로듐, 이리듐, 팔라듐 및 이들 금속의 산화물들 중 적어도 어느 하나로 구성되고, 상기 코팅층(220, 420)은, 테프론, 이온중합체 중 적어도 어느 하나로 구성된다.(Example 1-3) In the apparatus for producing ammonium sulfate using combustion exhaust gas according to the present invention (Example 1-2), the porous plate is made of carbon, iron, gold, silver, copper, nickel, titanium, cobalt, It is composed of at least one of platinum, rhodium, iridium, palladium, and oxides of these metals, and the coating layers 220 and 420 are composed of at least one of Teflon and ionic polymer.
상기한 제1전극판(200) 및 제2전극판(400) 각각에 포함되는 다공성 판(210, 410)과 코팅층(220, 420)의 재질은 여러 가지를 고려하여 적절히 선택될 수 있다. 이때 고려해야할 사항은 원가, 가스의 투과정도, 촉매효율 등이 있을 수 있다.The materials of the porous plates 210 and 410 and the coating layers 220 and 420 included in each of the first and second electrode plates 200 and 400 may be appropriately selected taking into account various factors. Matters to be considered at this time may include cost, gas permeability, and catalyst efficiency.
(실시예 1-4) 본 발명인 연소배기가스를 이용한 황산암모늄 제조장치는, (실시예 1-3)에 있어서, 상기 제1전극판과 상기 제2전극판 각각에 포함되는 다공성 판과 코팅층은 전극판끼리 다를 수 있다.(Example 1-4) In the apparatus for producing ammonium sulfate using combustion exhaust gas according to the present invention (Example 1-3), the porous plate and coating layer included in each of the first electrode plate and the second electrode plate are electrodes. Each plate may be different.
이는 상기한 제1전극판(200)과 제2전극판(400)에서 일어나는 반응이 서로 다르기 때문이다. 보다 구체적으로 제1전극판(200)에서는 황산화물의 산화반응이 일어나고, 제2전극판(400)에서는 질소산화물의 환원반응이 일어나기 때문이다. 이러한 산화반응과 환원반응의 차이 때문에, 제1전극판(200)에서는 산화반응이 보다 용이하게 일어나게 하는 재질을 선택하고, 제2전극판(400)에서는 환원반응이 보다 용이하게 일어나게 하는 재질을 선택하여, 황산암모늄의 제조효율을 향상시킬 수 있다. 단, 제1전극판(200)과 제2전극판(400)의 재질이 서로 동일한 등의 실시예 또한 있을 수 있다.This is because the reactions occurring in the first electrode plate 200 and the second electrode plate 400 are different. More specifically, this is because an oxidation reaction of sulfur oxides occurs in the first electrode plate 200, and a reduction reaction of nitrogen oxides occurs in the second electrode plate 400. Because of this difference between the oxidation reaction and the reduction reaction, a material that allows the oxidation reaction to occur more easily is selected for the first electrode plate 200, and a material that allows the reduction reaction to occur more easily is selected for the second electrode plate 400. Thus, the production efficiency of ammonium sulfate can be improved. However, there may also be an embodiment in which the first electrode plate 200 and the second electrode plate 400 are made of the same material.
(실시예 2-1) 본 발명인 연소배기가스를 이용한 황산암모늄 제조장치는, (실시예 1-1)에 있어서, 상기 유입 유로(100)측에 배치되어 상기 연소배기가스를 상기 유입 유로(100)측으로 공급하는 공급부(600) 및 상기 배출 유로(500)측에 배치되어 상기 배출 유로(500)의 가스를 외부로 배출하는 배출부(700)를 포함하되, 상기 공급부(600)와 상기 배출부(700)는 상기 제어부(800)에 의해 제어된다.(Example 2-1) In (Example 1-1), the apparatus for producing ammonium sulfate using combustion exhaust gas according to the present invention is disposed on the side of the inflow passage 100 and directs the combustion exhaust gas toward the inflow passage 100. It includes a supply unit 600 for supplying water and a discharge unit 700 disposed on the side of the discharge passage 500 to discharge the gas in the discharge passage 500 to the outside, wherein the supply unit 600 and the discharge unit 700 ) is controlled by the control unit 800.
공급부(600)와 배출부(700)는 일종의 임펠러와 같이 가스의 유입 및 배출이 가능하게 하는 장치로 구현될 수 있다. 공급부(600)와 배출부(700)가 임펠러와 같은 장치로 구현될 경우, 공급부(600)와 배출부(700)의 회전속도에 따라 본 발명에 의한 황산암모늄 제조장치의 효율이 달라질 수 있다. 따라서 제어부는 공급부(600)와 배출부(700)의 회전속도를 연동해 제어할 수 있다.The supply unit 600 and the discharge unit 700 may be implemented as a device that allows gas to be introduced and discharged, such as a kind of impeller. When the supply unit 600 and the discharge unit 700 are implemented as a device such as an impeller, the efficiency of the ammonium sulfate production device according to the present invention may vary depending on the rotation speed of the supply unit 600 and the discharge unit 700. Therefore, the control unit can control the rotation speeds of the supply unit 600 and the discharge unit 700 in conjunction with each other.
(실시예 2-2) 본 발명인 연소배기가스를 이용한 황산암모늄 제조장치는, (실시예 2-1)에 있어서, 상기 유입 유로(100)에 설치되어 상기 유입 유로(100)를 통해 공급되는 상기 연소배기가스의 유량이나 공급 압력을 센싱하는 제1센서(910) 및 상기 배출 유로(500)에 설치되어 상기 배출 유로(500)를 통해 배출되는 가스의 유량이나 배출 압력을 센싱하는 제2센서(920)를 포함하고, 상기 제어부(800)는, 상기 제1센서(910)와 상기 제2센서(920) 각각의 센싱값에 따라 상기 공급부(600)와 상기 배출부(700)를 제어한다.(Example 2-2) In (Example 2-1), the apparatus for producing ammonium sulfate using combustion exhaust gas of the present invention is installed in the inflow passage 100 and supplies the combustion exhaust gas through the inflow passage 100. A first sensor 910 that senses the flow rate or supply pressure of gas and a second sensor 920 installed in the discharge passage 500 to sense the flow rate or discharge pressure of gas discharged through the discharge passage 500. It includes, and the control unit 800 controls the supply unit 600 and the discharge unit 700 according to the sensing values of the first sensor 910 and the second sensor 920, respectively.
제1센서(910)와 제2센서(920)는 압력센서나 유량기로 구현될 수 있다. 제1센서(910)와 제2센서(920)는 제어부(800)측으로 센싱값을 송신하기 위해, 제어부(800)와 유선 또는 무선 방식으로 연결될 수 있다. 제1센서(910)와 제2센서(920) 각각의 센싱값은 앞서 설명한 공급부(600)와 배출부(700)의 회전속도보다 유입되는 연소배기가스 또는 배출되는 가스의 유량을 보다 정확하게 센싱할 수 있는 센싱값이므로, 보다 정확하고 효율적으로 본 발명에 의한 황산암모늄 제조장치를 제어할 수 있는 효과가 있다.The first sensor 910 and the second sensor 920 may be implemented as a pressure sensor or a flow sensor. The first sensor 910 and the second sensor 920 may be connected to the control unit 800 in a wired or wireless manner to transmit sensing values to the control unit 800. The sensing values of each of the first sensor 910 and the second sensor 920 can more accurately sense the flow rate of incoming combustion exhaust gas or discharged gas than the rotational speed of the supply unit 600 and discharge unit 700 described above. Since it is a sensing value, there is an effect of controlling the ammonium sulfate production device according to the present invention more accurately and efficiently.
본 발명은 상기한 실시예에 한정되지 아니하며, 적용범위가 다양함은 물론이고, 청구범위에서 청구하는 본 발명의 요지를 벗어남이 없이 다양한 변형 실시가 가능한 것은 물론이다.The present invention is not limited to the above-described embodiments, and the scope of application is diverse. Of course, various modifications and implementations are possible without departing from the gist of the present invention as claimed in the claims.
100 : 유입 유로100: Inflow Euro
200 : 제1전극판200: first electrode plate
210, 410 : 다공성 판210, 410: porous plate
220, 420 : 코팅층220, 420: Coating layer
300 : 전해질부300: Electrolyte unit
400 : 제2전극판400: Second electrode plate
500 : 배출 유로500: Discharge flow path
600 : 공급부600: Supply department
700 : 배출부700: Discharge unit
800 : 제어부800: Control unit
910 : 제1센서910: first sensor
920 : 제2센서920: Second sensor

Claims (7)

  1. 연소배기가스가 유입되는 유입 유로;An inlet flow path through which combustion exhaust gas flows;
    상기 유입 유로의 배출단에 배치되어 상기 연소배기가스가 투과하는 제1전극판;a first electrode plate disposed at the discharge end of the inlet flow path through which the combustion exhaust gas passes;
    상기 제1전극판의 측면에 배치되며, 전해질 용액이 수용되는 전해질부;an electrolyte portion disposed on a side of the first electrode plate and containing an electrolyte solution;
    상기 제1전극판과 상기 전해질부를 사이에 두고 배치되며, 상기 전해질부에서 배출되는 가스가 투과하는 제2전극판;a second electrode plate disposed between the first electrode plate and the electrolyte portion and through which gas discharged from the electrolyte portion passes;
    상기 제2전극판에서 투과된 가스가 배출되는 배출 유로;an exhaust passage through which gas transmitted from the second electrode plate is discharged;
    상기 제1전극판과 상기 제2전극판에 전압을 인가하는 전원부; 및a power supply unit that applies voltage to the first electrode plate and the second electrode plate; and
    상기 전원부를 제어하는 제어부;a control unit that controls the power unit;
    를 포함하되,Including,
    상기 전원부는 상기 제1전극판과 상기 제2전극판의 전위차가 1.2~1.8V가 되도록 전압을 인가하는 연소배기가스를 이용한 황산암모늄 제조장치.The power supply unit is an ammonium sulfate manufacturing device using combustion exhaust gas that applies a voltage so that the potential difference between the first electrode plate and the second electrode plate is 1.2 to 1.8V.
  2. 제1항에 있어서,According to paragraph 1,
    상기 제1전극판은,The first electrode plate is,
    다공성 판; 및porous plate; and
    상기 다공성 판의 표면에 코팅된 코팅층;A coating layer coated on the surface of the porous plate;
    을 포함하는 연소배기가스를 이용한 황산암모늄 제조장치.Ammonium sulfate manufacturing device using combustion exhaust gas containing.
  3. 제1항에 있어서,According to paragraph 1,
    상기 제2전극판은,The second electrode plate is,
    다공성 판; 및porous plate; and
    상기 다공성 판의 표면에 코팅된 코팅층;A coating layer coated on the surface of the porous plate;
    을 포함하는 연소배기가스를 이용한 황산암모늄 제조장치.Ammonium sulfate manufacturing device using combustion exhaust gas containing.
  4. 제2항 또는 제3항에 있어서,According to paragraph 2 or 3,
    상기 다공성 판은,The porous plate,
    탄소, 철, 금, 은, 동, 니켈, 티타늄, 코발트, 백금, 로듐, 이리듐, 팔라듐 및 이들 금속의 산화물들 중 적어도 어느 하나로 구성되는 연소배기가스를 이용한 황산암모늄 제조장치.A device for producing ammonium sulfate using combustion exhaust gas composed of at least one of carbon, iron, gold, silver, copper, nickel, titanium, cobalt, platinum, rhodium, iridium, palladium, and oxides of these metals.
  5. 제2항 또는 제3항에 있어서,According to paragraph 2 or 3,
    상기 코팅층은,The coating layer is,
    테프론, 이온중합체 중 적어도 어느 하나로 구성되는 연소배기가스를 이용한 황산암모늄 제조장치.A device for producing ammonium sulfate using combustion exhaust gas composed of at least one of Teflon and ionic polymer.
  6. 제1항에 있어서,According to paragraph 1,
    상기 유입 유로측에 배치되어 상기 연소배기가스를 상기 유입 유로측으로 공급하는 공급부; 및a supply unit disposed on the inlet flow path side to supply the combustion exhaust gas to the inlet flow path side; and
    상기 배출 유로측에 배치되어 상기 배출 유로의 가스를 외부로 배출하는 배출부;a discharge unit disposed on the discharge passage side to discharge gas from the discharge passage to the outside;
    를 포함하되,Including,
    상기 공급부와 상기 배출부는 상기 제어부에 의해 제어되는 연소배기가스를 이용한 황산암모늄 제조장치.An apparatus for producing ammonium sulfate using combustion exhaust gas, wherein the supply unit and the discharge unit are controlled by the control unit.
  7. 제6항에 있어서,According to clause 6,
    상기 유입 유로에 설치되어 상기 유입 유로를 통해 공급되는 상기 연소배기가스의 유량이나 공급 압력을 센싱하는 제1센서; 및A first sensor installed in the inlet flow path to sense the flow rate or supply pressure of the combustion exhaust gas supplied through the inlet flow path; and
    상기 배출 유로에 설치되어 상기 배출 유로를 통해 배출되는 가스의 유량이나 배출 압력을 센싱하는 제2센서;a second sensor installed in the discharge passage to sense the flow rate or discharge pressure of gas discharged through the discharge passage;
    를 포함하고,Including,
    상기 제어부는,The control unit,
    상기 제1센서와 상기 제2센서 각각의 센싱값에 따라 상기 공급부와 상기 배출부를 제어하는 연소배기가스를 이용한 황산암모늄 제조장치.An ammonium sulfate manufacturing device using combustion exhaust gas that controls the supply unit and the discharge unit according to the sensing values of each of the first sensor and the second sensor.
PCT/KR2022/011751 2022-03-31 2022-08-08 Apparatus for preparing ammonium sulfate by using combustion exhaust gas WO2023191194A1 (en)

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