METHOD FOR STORING ENERGY IN THE FORM OF HYDRAZINE CARBONATE
20200087800 · 2020-03-19
Assignee
Inventors
Cpc classification
Y02P20/133
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
Y02P70/50
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
Y02E60/50
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
Y02E60/36
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
C25B15/08
CHEMISTRY; METALLURGY
C07C281/00
CHEMISTRY; METALLURGY
International classification
Abstract
Energy storage is accomplished by producing hydrazine carbonate and later reconverting the hydrazine carbonate to release the energy. Sea water is firstly used in an electrolysis process to prepare hypochlorite. The hypochlorite reacts as a result of introduction of ammonia to produce monochloramine and then hydrazine. The hydrazine reacts as a result of introduction of carbon dioxide to give hydrazine carbonate. To release the energy, the hydrazine carbonate liberates hydrogen or at least a hydrogen-containing gas by reaction over a noble metal-free catalyst. The hydrogen may then be enriched before being fed to a fuel cell.
Claims
1. A process for storing energy in the form of hydrazine carbonate and subsequently reconverting the hydrazine carbonate into usable energy, wherein sea water is firstly used in an electrolysis process to prepare hypochlorite, wherein the hypochlorite reacts as a result of introduction of ammonia via the formation of monochloramine to give hydrazine and wherein the hydrazine subsequently reacts as a result of introduction of carbon dioxide to give hydrazine carbonate, and wherein the hydrazine carbonate liberates hydrogen or at least a hydrogen-containing gas by reaction over a noble metal-free catalyst in order to liberate the stored energy.
2. The process of claim 1, wherein a separation step for enriching the hydrogen is provided after the reaction of the hydrazine carbonate over the noble metal-free catalyst.
3. The process of claim 1, wherein the hydrogen or at least the hydrogen-containing gas is fed to a low-temperature fuel cell.
4. The process of claim 1, wherein the carbon dioxide is taken from an exhaust gas stream of a combustion plant.
5. The process of claim 1, wherein a catalyst composed of oxidic materials is used as the noble metal-free catalyst.
6. The process of claim 1, wherein the energy used in the sea water electrolysis for preparing hypochlorite is obtained from renewable energy sources.
7. The process of claim 1, wherein the hydrazine carbonate is heated to less than 100 C. in order to liberate the stored energy by reaction over the noble metal-free catalyst.
8. A process comprising: using sea water, ammonia and carbon dioxide to prepare hydrazine carbonate.
9. A process for storing and releasing energy comprising: storing energy by preparing hypochlorite from sea water using an electrolysis process; introducing ammonia which reacts with the hypochlorite to form hydrazine; introducing carbon dioxide which react with the hydrazine to give hydrazine carbonate; and reacting the hydrazine carbonate over a noble metal-free catalyst to liberates hydrogen or a hydrogen-containing gas.
10. The process of claim 9, further comprising enriching the hydrogen after the reaction of the hydrazine carbonate over the noble metal-free catalyst.
11. The process of claim 9, further comprising feeding the hydrogen or hydrogen-containing gas to a low-temperature fuel cell.
12. The process of claim 9, wherein the carbon dioxide is taken from an exhaust gas stream of a combustion plant.
13. The process of claim 9, wherein the noble metal-free catalyst comprises oxidic materials.
14. The process of claim 9, wherein the hydrazine carbonate is heated to less than 100 C. in order to liberate the stored energy by reaction over the noble metal-free catalyst.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0005]
[0006]
DETAILED DESCRIPTION
[0007] In the process for storing energy in the form of hydrazine carbonate and subsequently reconverting the hydrazine carbonate into usable energy, sea water is firstly used in an electrolysis process to prepare hypochlorite, where the hypochlorite reacts as a result of introduction of ammonia via the formation of monochloramine to give hydrazine and where the hydrazine subsequently reacts as a result of introduction of carbon dioxide to give hydrazine carbonate, where the hydrazine carbonate liberates hydrogen or at least a hydrogen-containing gas by reaction over a noble metal-free catalyst in order to liberate the stored energy and where the hydrogen or the at least hydrogen-containing gas is intended for being fed to a fuel cell or burnt in order to release the usable energy. In particular, the hydrogen-containing gas is a gas mixture of at least hydrogen and nitrogen.
[0008] Both hydrazine and hydrazine carbonate are known at least from the abovementioned AT 514 461 A1. Accordingly, hydrazine has an aqueous form and is mainly used industrially as a reducing agent and as a free-radical scavenger. Hydrazine carbonate is a nonvolatile, water-soluble salt which is used as an antioxidant in the chemical industry.
[0009] The sea water (H.sub.2O) is used to prepare hypochlorite (OCl.sup.) by sea water electrolysis. The following reactions take place here:
2H.sub.2O+2e.sup..fwdarw.H.sub.2+2OH.sup.Cathode reaction:
2Cl.sup.2e.sup..fwdarw.Cl.sub.2,Anode reaction:
Cl.sub.2+2OH.fwdarw.H.sub.2O+OCl.sup.+Cl.sup.Reaction 1:
[0010] The energy used in the sea water electrolysis for preparing hypochlorite is preferably obtained from renewable energy sources. In particular, this energy is made up of wind power energy, solar energy and/or bioenergy.
[0011] The hypochlorite reacts as a result of introduction of ammonia (NH.sub.3) via the formation of monochloramine (NH.sub.2Cl) to give hydrazine (N.sub.2H.sub.4). In other words, gaseous ammonia is firstly introduced into the hypochlorite-comprising aqueous solution, resulting in water and monochloramine being formed according to reaction 2.
NH.sub.3+HOCl.fwdarw.NH.sub.2Cl+H.sub.2OReaction 2:
[0012] According to a subsequent reaction 3, the monochloramine reacts with the ammonia and forms hydrogen chloride (HCl) and hydrazine.
NH.sub.2Cl+NH.sub.3.fwdarw.N.sub.2H.sub.4+HClReaction 3:
[0013] The hydrazine then reacts according to reaction 4 as a result of introduction of carbon dioxide (CO.sub.2) to give hydrazine carbonate ((N.sub.2H.sub.5).sub.2CO.sub.3).
N.sub.2H.sub.4+CO.sub.2.fwdarw.(N.sub.2H.sub.5).sub.2CO.sub.3Reaction 4:
[0014] The carbon dioxide is preferably taken from an exhaust gas stream of a combustion plant. For example, the exhaust stream is produced by a coal-fired power station. Exploitation of the high concentration of carbon dioxide in the exhaust gas stream of the combustion plant is particularly advantageous.
[0015] The hydrazine carbonate serves as stable, long-term store for hydrogen (H.sub.2). To liberate the energy stored in the hydrazine carbonate, a noble metal-free catalyst is used, with the hydrogen or at least the hydrogen-containing gas being liberated according to reaction 5.
[0016] As noble metal-free catalyst, preference is given to using a catalyst composed of oxidic materials, for example of Al.sub.2O.sub.3, Cu-doped Al.sub.2O.sub.3 or a calcium-aluminum silicate such as CaAl.sub.2Si.sub.3O.sub.8(OH).sub.4.H.sub.2O. Over such a noble metal-free catalyst, for example CaAl.sub.2Si.sub.3O.sub.8(OH).sub.4.H.sub.2O, the hydrazine carbonate is decomposed, in particular at temperatures in the range from 100 to 150 C., into hydrogen, CO.sub.2 and water. In particular, the catalyst has a high porosity. The porosity serves, in particular, to increase the reactive surface area of the catalyst.
(N.sub.2H.sub.5).sub.2CO.sub.3.fwdarw.N.sub.2+H.sub.2+CO.sub.2+H.sub.2OReaction 5:
[0017] A separation step for enriching the hydrogen is preferably provided after the reaction of the hydrazine carbonate over the noble metal-free catalyst. In particular, the separation step is provided for separating the hydrogen from the nitrogen. The carbon dioxide liberated according to reaction 5 is the carbon dioxide which was previously introduced and reversibly bound in the hydrazine carbonate. The process is thus CO.sub.2-neutral.
[0018] In order to liberate the stored energy, in particular to liberate the hydrogen or to liberate the at least hydrogen-containing gas by reaction over the noble metal-free catalyst, the hydrazine carbonate is heated to less than 100 C. The hydrogen or at least the hydrogen-containing gas is preferably fed to a fuel cell or burnt in order to release the usable energy. For example, the hydrogen or at least the hydrogen-containing gas is fed to a low-temperature fuel cell.
[0019] The use of the hydrogen in fuel cells counters, in particular, the discontinuity of the supply of power from renewable energy sources. Furthermore, the hydrogen stored in the hydrazine carbonate can be used both for fuel cells in stationary applications and also for fuel cells in mobile applications such as passenger cars, goods vehicles, ships and aircraft.