WO2012049689A2 - Dispositif de commande permettant de réguler la production d'un gaz détonant à partir de l'eau, comprenant un ensemble d'électrodes de modules électrolyseurs pourvues d'orifices disposés de façon asymétrique - Google Patents

Dispositif de commande permettant de réguler la production d'un gaz détonant à partir de l'eau, comprenant un ensemble d'électrodes de modules électrolyseurs pourvues d'orifices disposés de façon asymétrique Download PDF

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Publication number
WO2012049689A2
WO2012049689A2 PCT/IN2011/000704 IN2011000704W WO2012049689A2 WO 2012049689 A2 WO2012049689 A2 WO 2012049689A2 IN 2011000704 W IN2011000704 W IN 2011000704W WO 2012049689 A2 WO2012049689 A2 WO 2012049689A2
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WO
WIPO (PCT)
Prior art keywords
gas
water
electrolysis
regulating
production
Prior art date
Application number
PCT/IN2011/000704
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English (en)
Other versions
WO2012049689A3 (fr
Inventor
Maheshbhai Thakore Pratik
Original Assignee
Maheshbhai Thakore Pratik
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Publication date
Application filed by Maheshbhai Thakore Pratik filed Critical Maheshbhai Thakore Pratik
Publication of WO2012049689A2 publication Critical patent/WO2012049689A2/fr
Publication of WO2012049689A3 publication Critical patent/WO2012049689A3/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C25B1/04—Hydrogen or oxygen by electrolysis of water
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/02—Process control or regulation
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00—Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/10—Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture adding acetylene, non-waterborne hydrogen, non-airborne oxygen, or ozone
    • F02M25/12—Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture adding acetylene, non-waterborne hydrogen, non-airborne oxygen, or ozone the apparatus having means for generating such gases
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Definitions

  • the present invention relates Method and Apparatus for regulating the production of browns gas by electrolysis of water with an Electronic controller and Asymetrical arrangement of Electrodes in Modular type Electrolysers .
  • the present invention is useful for retrofit system of IC engines & automobile industry as fuel supplement to increase the efficiency and reduce carbon emission, Flame application in various industries, As additive gas in Furnaces and Incinerators, Atomic waste neutralization.
  • Electrolysis processes involving water are of considerable importance commercially. Such processes involve the electro deposition of metals, electrochemical synthesis procedures, electrochemical loading of electrodes for batteries, etc.
  • a particularly important industrial process involving the electrolysis of water is the production of hydrogen gas. Hydrogen gas is an excellent source of energy and has many other uses in chemical technology and industry.
  • HHO gas is Less of various electrolyzer unit due to over heating of electrolyte water caused due to leakage current flow between the plates or pipe type electrode in electrolysers unit cell (EUC).
  • EUC electrolysers unit cell
  • the primary drawback of current machinery is the lack of control over the rate of electrolysis, with the result that even for slight differences in the rate of required output, different designs have to be made.
  • the current machinery state of art
  • the existing state of art needs robust over heating protection systems. This leads to difficulties in manufacturing because a large number of models of different requirement have to be manufactured to cater to different applications, and also results in the need to hold large inventory of components.
  • This drawback has been overcome by a method of regulating the average rate of electrolysis by connecting the rectified (DC) power supply to a frequency switching of Power transistors and modular type of Electrolysers
  • the primary objective of the invention is to regulate the production of Brown's gas by using a frequency switching of Power transistors.
  • the utility of Brown's gas in various fields need not be specified.
  • the present invention has following object and which are not limited thereof.
  • Oxyhydrogen gas flame can melt down any element as molecular fusion of Hydrogen and Oxygen material.
  • Oxy hydrogen flame has the capacity of thermonuclear reaction. Flames from oxyhydrogen gas can be used in Metal cutting, soldering and brazing, Jewelry manufacturing, I.C processing in electronics, Acrylic polishing, Bead-making, Glass processing.
  • Oxy-hydrogen flame has the capacity to reduce radioactive radiation by 90 % from radio active waste and other ancillary materials to be disposed safely.
  • the traditional method of varying the rate of electrolysis involves varying the voltage so that the current varies.
  • Current is related to voltage by the relation
  • I is the current in amperes
  • V is the applied voltage
  • R is the resistance in Ohms.
  • the voltage at which electrolysis starts is dependent upon the chemical and physical properties of the electrolyte, and once the threshold voltage is applied, electrolysis will start. Higher voltages, though resulting in higher current, and resulting in higher rate of electrolysis, result in wastage of energy through heating the electrolyte.
  • the non-obviousness is that instead of varying the voltage to vary the rate of electrolysis, the electrolytic cell is switched on and off, thus varying the average rate of electrolysis
  • the invention device has provided with a controller to control for the manufacturing of Brown's gas generators for a variety of industrial and other purposes
  • Fig.2a represents the Modular type Pipe type Electrode
  • Fig.2. la represents the different views of non liner pipes
  • Fig.2.2a represents the different views of non liner pipes
  • Fig.2.3a represents the different views of non liner pipes
  • Fig.2b represents the complete assembly of Flat plate electrode
  • Fig 2.1b represents the Flat Plate Electrodes arrangement
  • Fig.2.2b represents the flat plate electrodes arrangement expanded views
  • FIG.l The schematic block diagram of the present invented layout and details of each is shown in Fig.l.
  • This invention is intended to (control the reaction in the cell ⁇ regulate the power supply (1) to the electrolytic reaction cell.
  • This supply is fed to a Switching Mode Power Supply, which results in a DC supply, with specific voltage and current depending upon the customize requirements of the electrolytic cell to be used.
  • This DC supply is supplied to a power transistor, which acts as the switch.
  • This circuit generates pulses of DC at a specific frequency, and the width of the pulses can be varied.
  • the pulses emanating from this circuit are fed to the Power Transistor, which results in switching the transistor On for the duration of the pulse and switching the transistor off for the remaining period.
  • the above arrangement results in switching the transistor on and off as per required output of Brown's gas, at constant voltage and current.
  • One of the additional advantages is the saving of energy by avoiding unnecessary high voltages for the electrolysis
  • FIG.l block diagram of present invented device where the Transformer or SMPS base D.C power supply source (1) with Electronics system of self and manual regulating system to the average rate of electrolysis by High frequency switching of Power transistors attached with Current, Voltage, Power or Energy measuring devices is connected with the Modular type Electrolyzer with asymmetrical or non linear arrangement of Water Vents and Gas Vents of Pipe or Plate electrodes as shown in diagram Fig.2a & 2b.
  • the complete assembly view of the non liner arrangement of Water Vents and 5 Gas outlet vents pipes are shown in Fig.2a and the expanded view of non liner pipes are shown in Fig.2. la, 2.2a and 2.3a details of the electrolyzer 2a.
  • the Gas Outlet Vents ( 2C ) at top of Electrodes ( 2A) arranged non-linear (asymmetrical) with io angular displacement to avoid inter Electrode leakage of current.
  • FIG 2.1a & 2.2a - Pipe type Electrodes (2A) arranged in series combination together with separators (2B) at top & bottom to hold the pipes.
  • Separator(2B) has circular grooves on inner sides to hold the Pipe Electrodes (2A) for electrical and mechanical separation. 2B Seperators are fixed on top and bottom of the Electrodes 2A. Separators 2B are made from Insulating 20 Plastic polymers viz. Acrylic, Polypropalene or nylon.
  • FIG. 2b The complete assembly view of the flat plate arrangement is shown in Fig. 2b and the View of the Flat Plate Electrodes arrangement in the Electrolyzer-2b in 25 the above Fig 2.1b, 2.2b and 2.3b details of the Electrolyzer-2b. Where 2.2b and 2.3b viewed from two sides of expanded views.
  • Fig. 2.2b the series of the flat plate Electrodes 2A arranged in series combination together with separators 2B.
  • the Flat plate Electrodes (2A) of Stainless steel or Nickel or Carbon and gasket separator(2B) of Nitrile rubber or Neoprene rubber or any polymer insulating material is provided between two plate electrodes.(2A).
  • FIG 2.2b where Gas outlet vents (2C) arrangement with alternate sides of each electrode (2A) and the Water inlet vents(2D) smaller than gas outlet vent (2C). Gas outlet vents (2C) arranged in alternate sides of each electrode (2A) to decrease the Inter-electrode leakage current and increase the over all efficiency of the system.
  • Vessel(3) and Vessel (4) made from any acid or alkali proof material like Stainless steel or Plastic polymers in existing state of art.
  • Vessel(3) made from any acid or alkali proof material to hold the Water electrolyte to feed the Electrolyser and also bubble pass the output HHO gas into it to remove the vapours of Electrolyte added in water.
  • Electrolyte added water input is connected with vessel (3) as shown in Fig.l. Vessel (4) to hold the Plain water (Portable drinking) from which the HHO gas is again passed to make output gas free from residual Electrolyte and also work as active flame or flash back arrestor. Summary of the invention -
  • the Electrolyser 2 has Electrodes 2A with Asymmetrical or Non-linear arrangement of Water inlet vent for water flow at bottom level.
  • the Water inlet vents are smaller in proportion than the Gas outlet vents.
  • the Asymmetrical vents are arranged at the maximum distance between the (Gas outlet Vent) GOV and Water inlet Vent (WIV) in the same electrode pipe or plate form to avoid leakage of current.
  • the asymmetrical arrangement does not allow the flow of water between the electrode plate in single line and the asymmetrical or Non-linear arrangement does not allow the Gas flow in single line.
  • the asymmetrical or Non- linear arrangement reduces flow of inter electrode leakage electric current thus increasing the overall efficiency of the electrolysis process.
  • the asymmetrical arrangement of Water vents and Gas Vents reduces the Heat losses occurring in the existing state of art. This eliminates the need of temperature control system, water pumping or cooling system.
  • Electrodes 2A of Flate plate or pipe type are arranged in series combination with Bipolar potential difference created when the Voltage between the 2 end electrodes in the series parallel combination of Electrolyser cell.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Automation & Control Theory (AREA)
  • Inorganic Chemistry (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

La présente invention se rapporte à un électrolyseur qui comprend des électrodes présentant un agencement asymétrique ou non linéaire d'orifices d'entrée d'eau pour permettre une circulation de l'eau au niveau de la partie inférieure. Les orifices d'entrée d'eau sont proportionnellement plus petits que les orifices de sortie de gaz. Les orifices de sortie de gaz qui présentent un agencement asymétrique ou non linéaire pour permettre une circulation du gaz au niveau de la partie supérieure sur les électrodes dans l'unité de cellule d'électrolyseur sont agencés de façon alternée sur des électrodes bipolaires en forme de plaque ou de tuyau. Les orifices asymétriques sont agencés à la distance maximale entre l'orifice de sortie de gaz (GOV, Gas outlet Vent) et l'orifice d'entrée d'eau (WrV, Water inlet Vent) de la même forme d'électrode en plaque ou en tuyau pour éviter une fuite de courant entre les électrodes. L'agencement asymétrique ne permet pas l'écoulement de l'eau entre la plaque d'électrode sur une seule ligne et l'agencement asymétrique ou non linéaire ne permet pas l'écoulement de gaz sur une seule ligne. Ceci augmente l'efficacité globale et réduit les pertes de chaleur. Ceci élimine la nécessité d'un système de commande de température. L'électrolyseur a une forme modulaire d'une combinaison série et parallèle avec un dispositif de commande électronique pour l'alimentation en courant continu avec une commutation de fréquences des transistors de puissance afin de réguler la sortie de gaz pour des multiples besoins d'application.
PCT/IN2011/000704 2010-10-10 2011-10-10 Dispositif de commande permettant de réguler la production d'un gaz détonant à partir de l'eau, comprenant un ensemble d'électrodes de modules électrolyseurs pourvues d'orifices disposés de façon asymétrique WO2012049689A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IN1191MU2010 2010-10-10
IN1191/MUM/2010 2010-10-10

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WO2012049689A2 true WO2012049689A2 (fr) 2012-04-19
WO2012049689A3 WO2012049689A3 (fr) 2012-07-19

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015115881A1 (fr) 2014-01-31 2015-08-06 Delgado Rodriguez Luis Alfonso Réacteur électrochimique pour la production de gaz oxyhydrogène
US10494992B2 (en) 2018-01-29 2019-12-03 Hytech Power, Llc Temperature control for HHO injection gas
US10605162B2 (en) 2016-03-07 2020-03-31 HyTech Power, Inc. Method of generating and distributing a second fuel for an internal combustion engine
US11879402B2 (en) 2012-02-27 2024-01-23 Hytech Power, Llc Methods to reduce combustion time and temperature in an engine

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2113278U (zh) * 1992-02-19 1992-08-19 董向阳 电解氢氧机
JP2003294207A (ja) * 2002-04-03 2003-10-15 Oriental Bridge Kk 燃焼装置
KR100677668B1 (ko) * 2006-06-22 2007-02-02 김재화 수소-산소 혼합가스 발생기용 전극판 및 전해조
CN101775612A (zh) * 2010-02-12 2010-07-14 陈志远 一种发动机节油用的氢氧生产机
CN201560238U (zh) * 2009-12-08 2010-08-25 刘海英 氢氧气体发生器

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2113278U (zh) * 1992-02-19 1992-08-19 董向阳 电解氢氧机
JP2003294207A (ja) * 2002-04-03 2003-10-15 Oriental Bridge Kk 燃焼装置
KR100677668B1 (ko) * 2006-06-22 2007-02-02 김재화 수소-산소 혼합가스 발생기용 전극판 및 전해조
CN201560238U (zh) * 2009-12-08 2010-08-25 刘海英 氢氧气体发生器
CN101775612A (zh) * 2010-02-12 2010-07-14 陈志远 一种发动机节油用的氢氧生产机

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11879402B2 (en) 2012-02-27 2024-01-23 Hytech Power, Llc Methods to reduce combustion time and temperature in an engine
WO2015115881A1 (fr) 2014-01-31 2015-08-06 Delgado Rodriguez Luis Alfonso Réacteur électrochimique pour la production de gaz oxyhydrogène
US10329675B2 (en) 2014-01-31 2019-06-25 Luis Alfonso Delgado Rodriguez Electrochemical reactor for producing oxyhydrogen gas
US10605162B2 (en) 2016-03-07 2020-03-31 HyTech Power, Inc. Method of generating and distributing a second fuel for an internal combustion engine
US11280261B2 (en) 2016-03-07 2022-03-22 HyTech Power, Inc. Systems for HHO gas second fuel distribution and control
US11815011B2 (en) 2016-03-07 2023-11-14 Hytech Power, Llc Generation and regulation of HHO gas
US10494992B2 (en) 2018-01-29 2019-12-03 Hytech Power, Llc Temperature control for HHO injection gas
US10619562B2 (en) 2018-01-29 2020-04-14 Hytech Power, Llc Explosion safe electrolysis unit
US11828219B2 (en) 2018-01-29 2023-11-28 Hytech Power, Llc Rollover safe electrolysis unit for vehicles

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