DE3048433A1 - Liquid hydrogen produced from water - by electrolysis and adiabatic expansion - Google Patents

Liquid hydrogen produced from water - by electrolysis and adiabatic expansion

Info

Publication number
DE3048433A1
DE3048433A1 DE19803048433 DE3048433A DE3048433A1 DE 3048433 A1 DE3048433 A1 DE 3048433A1 DE 19803048433 DE19803048433 DE 19803048433 DE 3048433 A DE3048433 A DE 3048433A DE 3048433 A1 DE3048433 A1 DE 3048433A1
Authority
DE
Germany
Prior art keywords
hydrogen
water
electrolysis
liquid hydrogen
adiabatic expansion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
DE19803048433
Other languages
German (de)
Inventor
Christoph 8711 Kaltensondheim Baare
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to DE19803048433 priority Critical patent/DE3048433A1/en
Publication of DE3048433A1 publication Critical patent/DE3048433A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • 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
    • C25B1/02Hydrogen or oxygen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Combustion & Propulsion (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Liquid hydrogen is produced by electrolysis, under pressure, of water, followed by adiabatic expansion to liquefy the hydrogen. The two processes are combined into a single process. Process is used for production of liquid hydrogen, esp. for use as an energy carrier (fuel). No additional energy is required for the process other than that required for decomposing the water to produce the hydrogen.

Description

Beschreibung zu meiner Patentanmeldung:Description of my patent application:

Flüßigwasserstoffgewinnung durch Elektrolyse.Production of liquid hydrogen by electrolysis.

Anwendungsgebiet: Die Erfindung betrifft die Herstellung flüßigen Wasserstoffes durch die Zusammenlegung der beiden Verfahrensweisen: Wasserelektrolyse und adiabatischer oder ähnlicher Expansion mit dem Ziel flüßigen Wasserstoff herzustellen.Field of application: The invention relates to the production of liquids Hydrogen by combining the two processes: water electrolysis and adiabatic or similar expansion with the aim of producing liquid hydrogen.

Zweck: Flüßiger Wasserstoff wird als Energieträger in immer größeren Mengen gebraucht. Dieses Verfahren soll dazu beitragen diesen billig herzustellen und so eine breitere Anwendung zu ermöglichen.Purpose: Liquid hydrogen is used as an energy carrier in ever larger Quantities needed. This process should help to manufacture it cheaply and thus to enable a wider application.

Es ist bekannt nach D.R.P. 600583 und dem Buch: Die technische Elektrolyse der Nichtmetalle, Springer Verlag Berlin 1954, daß sich Wasser auch unter Druck in seine Bestandteile zerlegen läßt. Außerdem ist hinreichend bekannt, das Gase durch arbeitsleistende Entspannung und adiabatischer Entspannung so niedrige Temperaturen erreichen, daß eine Verflüßigung derselben eintritt, vorrausgesetzt die Anfangstemperatur und der Druck wurden entsprechend eingestellt.It is known according to D.R.P. 600583 and the book: The technical electrolysis der nichtmetalle, Springer Verlag Berlin 1954, that water is also under pressure can be broken down into its components. It is also well known that gases through work-performing relaxation and adiabatic relaxation such low temperatures achieve that a liquefaction of the same occurs, provided the initial temperature and the pressure were adjusted accordingly.

Bisher wurde nicht beachtet, daß beide Verfahren als Einheit gesehen eine hohe Einsparung an Energie mit sich bringt.So far it has not been considered that both procedures are seen as a unit brings a high saving of energy with it.

Denn es muß ausser der Zersetzungsenergie keine weitere Energie aufgewendet werden.Because apart from the decomposition energy, no further energy has to be used will.

Die Verflüßigung des Wasserstoffes kann erreicht werden unter Beachtung der bekannten Verfahrensweisen, indem der Druck im Elektrolyseur so hoch gewählb wird, dass durch entspannen des entstehenden gasförmigen Sauerstoffes der-entstehende gasförmige Wasserstoff in einen Zustand gebracht wird, von dem an durch weiteres Entspannen des Wasserstoffes dieser den flüßigen Zustand erreicht.The liquefaction of the hydrogen can be achieved under consideration the known procedures, in that the pressure in the electrolyzer is so high gewählb is that by relaxing the gaseous oxygen that is created, the one that is created gaseous hydrogen is brought into a state from which on by further Relaxation of the hydrogen this reaches the liquid state.

Der Vorteil der Erfindung ist vor allem, daß ähnlich im Dampfmaschinenprozeß, jedoch nicht als Kreisprozeß, die beiden verschiedenen Aggregatzustände flüßig und gasförmigtdie beiden Gase im für den jeweiligen Arbeitsprozeß günstigsten Aggregatzustand benutzt werden. D.h. als Wasser im flüßigen Zustand der Verbindung Wasserstoff - Sauerstoff auf hohen entsprechenden Druck gebracht werden und als Gase nach der Trennung der Verbindung so entspannt werden, daß der Sauerstoff der ebenfalls entsteht,entspannt wird im gasförmigen Zustand ebenso wie der Wasserstoff im gasförmigen Zustand so daß der letztere verflüßigt wird.The main advantage of the invention is that, similarly in the steam engine process, but not as a cycle process, the two different states of aggregation liquid and gaseous, the two gases are used in the most favorable aggregate state for the respective work process. That means that as water in the liquid state of the connection hydrogen - oxygen are brought to a high corresponding pressure and as gases are so relaxed after the separation of the connection that the oxygen which is also formed is relaxed in the gaseous state just like the hydrogen in the gaseous state so that the latter is liquefied.

Das Energiegefälle welches durch die Entspannung des Sauerstoffes zum Wasserstoff entsteht wird ausgenutzt um dem Wasserstoff saviel Energie zu entnehmen, dass durch intspannen des gasförmigen Wasserstoffes dieser verflüßigt wird.The energy gradient caused by the relaxation of the oxygen to produce hydrogen is used to extract less energy from the hydrogen, that by expanding the gaseous hydrogen it is liquefied.

Der Sauerstoff hat sich nach diesem Prozeß entspannt, abgekühlt und wieder angewärmt. Der Wasserstoff entspannt und verflüßigt.After this process, the oxygen has relaxed, cooled and warmed up again. The hydrogen relaxes and liquefies.

Der Patentanspruch: Die Verbindung der beiden Verfahrensweisen mit dem Ziel der Verflüßigung des Wasserstoffes.The claim: The combination of the two procedures with the goal of liquefying the hydrogen.

Das heißt: Die Druckelektrolyse zum Zweck der späteren Verflüßigung des Wasserstoffes bei entsprechendem Druck durchzufuhren, den Prozeß oder die Verfahrensweise als eine Einheit anzusehen.That means: the pressure electrolysis for the purpose of the later liquefaction to carry out the process or procedure of the hydrogen at the appropriate pressure to be regarded as a unit.

Claims (1)

P a t e n t a n s p r u c h Verfahren zur Gewinnung von Flüssigwasserstoff durch Kombination von Wasserelektrolyse und adiabatischer Entspannung. P a t e n t a n s p r u c h Process for the production of liquid hydrogen through a combination of water electrolysis and adiabatic relaxation.
DE19803048433 1980-12-22 1980-12-22 Liquid hydrogen produced from water - by electrolysis and adiabatic expansion Withdrawn DE3048433A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE19803048433 DE3048433A1 (en) 1980-12-22 1980-12-22 Liquid hydrogen produced from water - by electrolysis and adiabatic expansion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19803048433 DE3048433A1 (en) 1980-12-22 1980-12-22 Liquid hydrogen produced from water - by electrolysis and adiabatic expansion

Publications (1)

Publication Number Publication Date
DE3048433A1 true DE3048433A1 (en) 1982-07-08

Family

ID=6119922

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19803048433 Withdrawn DE3048433A1 (en) 1980-12-22 1980-12-22 Liquid hydrogen produced from water - by electrolysis and adiabatic expansion

Country Status (1)

Country Link
DE (1) DE3048433A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10076540B1 (en) 2017-08-08 2018-09-18 Perricone Hydrogen Water Company, Llc Medication enhancement using hydrogen
US10155010B1 (en) 2017-08-08 2018-12-18 Perricone Hydrogen Water Company, Llc Barriers for glass and other materials
US11123365B2 (en) 2019-11-18 2021-09-21 Perricone Hydrogen Water Company, Llc Compositions comprising palmitoylethanolamide and hydrogen water, and methods thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10076540B1 (en) 2017-08-08 2018-09-18 Perricone Hydrogen Water Company, Llc Medication enhancement using hydrogen
US10155010B1 (en) 2017-08-08 2018-12-18 Perricone Hydrogen Water Company, Llc Barriers for glass and other materials
US11129848B2 (en) 2017-08-08 2021-09-28 Perricone Hydrogen Water Company, Llc Medication enhancement using hydrogen
US11123365B2 (en) 2019-11-18 2021-09-21 Perricone Hydrogen Water Company, Llc Compositions comprising palmitoylethanolamide and hydrogen water, and methods thereof

Similar Documents

Publication Publication Date Title
DE2535132C3 (en) Process and device for the production of pressurized oxygen by two-stage low-temperature rectification of air
DE1112997B (en) Process and device for gas separation by rectification at low temperature
DE1226616B (en) Process and device for the production of gaseous pressurized oxygen with simultaneous production of liquid decomposition products by low-temperature air separation
DE2164795B2 (en) Process for the recovery of compression energy in an air separation plant
DE2854508C2 (en) Method and device for the low-temperature decomposition of a gas mixture
DE1234747B (en) Process for the production of oxygen enriched air
DE3048433A1 (en) Liquid hydrogen produced from water - by electrolysis and adiabatic expansion
DE69416558T2 (en) Manufacturing process of pure gaseous carbon dioxide and apparatus for use therefor
DE2542705C2 (en) Process and plant for the production of water enriched with deuterium in the production of hydrogen
DE1235346B (en) Method and device for washing out impurities from hydrogen-rich gas mixtures by means of liquid nitrogen
EP2084722A1 (en) Method for cooling superconducting magnets
DE3229883A1 (en) METHOD AND DEVICE FOR PRODUCING PURIFIED AETHYLENE
DE276718C (en)
CH620176A5 (en)
DE1230407B (en) Process for separating ammonia from the circulating gas of the ammonia synthesis
DE921809C (en) Process for the production of pure oxygen in addition to the production of oxygen of lower purity
DE2603577C3 (en) Water electrolyzer operating under pressure
DE2131341C3 (en) Process for the separation of gas mixtures
DE1501732C3 (en) Process for the liquefaction of oxygen or nitrogen obtained by air rectification when the demand for decomposition products changes
DE942515C (en) Multi-fuel thermal power process
DE426112C (en) Process for the extraction of argon from atmospheric air
DE880893C (en) Process for the separation of air with the simultaneous production of liquid or compressed oxygen
DE2047363A1 (en) Evaporated liquefied gas blanket - is utilised by feeding it directly to gas bottles
DE88824C (en)
AT140566B (en) Process for extracting air components with a higher boiling point than oxygen

Legal Events

Date Code Title Description
8139 Disposal/non-payment of the annual fee