USPatent applicationPatented

Method for storing energy in the form of hydrazine carbonate

Granted 17 Aug 2021 · 1 office action

Life of the application

9 dated events
⤢ drag to zoom20182020202220242026202820302032203420362038ProsecutionOwnershipTerm & fees
ProsecutionOwnershipTerm & feeshover for detail · click to open

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.

Description

6 parts
›CROSS-REFERENCE TO RELATED APPLICATIONS

This application is the U.S. National Phase of PCT Appln. No. PCT/DE2017/100808 filed Sep. 22, 2017, which claims priority to DE 10 2016 223 001.8 filed Nov. 22, 2016, the entire disclosures of which are incorporated by reference herein.

›TECHNICAL FIELD

The disclosure relates to a process for storing energy in the form of hydrazine carbonate and subsequently reconverting the hydrazine carbonate into usable energy.

›BACKGROUND

AT 514 461 A1 discloses a process for storing energy in the form of hydrazine carbonate and subsequently reconverting the hydrazine carbonate into usable energy. Water is converted in an electrolysis process into hydrazine carbonate by means of energy and with introduction of nitrogen and carbon dioxide in the presence of a transition metal catalyst which decreases the activation energy of the stable nitrogen-nitrogen triple bond. The anode is here surrounded by an oxygen-impermeable diaphragm. A metal salt is used to inhibit hydrogenolytic cleavage of the hydrazine. The hydrazine carbonate is isolated in the form of a solid or in the form of a concentrated solution from the mixture, and the hydrazine carbonate is later decomposed thermally in order to recover the energy by combustion of the hydrogen or by use of the hydrogen in a fuel cell.

›SUMMARY

It is an object of the present disclosure to propose an inexpensive and industrially usable process for the long-term storage of energy in the form of hydrazine carbonate and also the subsequent reconversion of the hydrazine carbonate into usable energy. In particular, it is an object of the present disclosure to provide sustainable energy storage proceeding from readily available raw materials.

›BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 illustrates a process for storing energy as Hydrazine Carbonate.

FIG. 2 illustrates a process for releasing energy stored as Hydrazine Carbonate.

›DETAILED DESCRIPTION

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.

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.

The sea water (H 2 O) is used to prepare hypochlorite (OCl − ) by sea water electrolysis. The following reactions take place here:

2H 2 O+2 e − →H 2 +2OH −   Cathode reaction:

2Cl − −2 e − →Cl 2 ,  Anode reaction:

Cl 2 +2OH→H 2 O+OCl − +Cl −   Reaction 1:

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.

The hypochlorite reacts as a result of introduction of ammonia (NH 3 ) via the formation of monochloramine (NH 2 Cl) to give hydrazine (N 2 H 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 3 +HOCl→NH 2 Cl+H 2 O  Reaction 2:

According to a subsequent reaction 3, the monochloramine reacts with the ammonia and forms hydrogen chloride (HCl) and hydrazine.

NH 2 Cl+NH 3 →N 2 H 4 +HCl  Reaction 3:

The hydrazine then reacts according to reaction 4 as a result of introduction of carbon dioxide (CO 2 ) to give hydrazine carbonate ((N 2 H 5 ) 2 CO 3 ).

N 2 H 4 +CO 2 →(N 2 H 5 ) 2 CO 3   Reaction 4:

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.

The hydrazine carbonate serves as stable, long-term store for hydrogen (H 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.

As noble metal-free catalyst, preference is given to using a catalyst composed of oxidic materials, for example of Al 2 O 3 , Cu-doped Al 2 O 3 or a calcium-aluminum silicate such as CaAl 2 Si 3 O 8 (OH) 4 .H 2 O. Over such a noble metal-free catalyst, for example CaAl 2 Si 3 O 8 (OH) 4 .H 2 O, the hydrazine carbonate is decomposed, in particular at temperatures in the range from 100 to 150° C., into hydrogen, CO 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 2 H 5 ) 2 CO 3 →N 2 +H 2 +CO 2 +H 2 O  Reaction 5:

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 2 -neutral.

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.

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.

Claims as granted

13 claims

Log in to read the claims of this application.

Log in to unlock

Classifications

3 codes
IPC · International Patent Classification
Section C — Chemistry; metallurgy
  • C25B3/25
  • C01B21/16
  • C25B1/26

Claim changes

Soon
Coming soonHow the claims changed between publication and grant

See which claims were amended, added or cancelled during examination, with every added and removed word marked.

AmendedAddedCancelledUnchanged

The published claims of this application are not paired with the granted ones in what we hold.

File wrapper

⤢ drag to zoomJul 2017Jan 2018Jul 2018Jan 2019Jul 2019Jan 2020Jul 2020Jan 2021Jul 2021USPTOApplicantNon-final rejection
USPTOApplicanthover for detail · click to open
Pendency
3.9 y
1,425 days filing → grant
Office actions
1
non-final + final
Responses
1
no RCE
Examiner
Anthony J Zimmer
art unit 1736 · TC 1700
Citations: 8 back · 0 forward

See the full prosecution history — every USPTO and applicant action on this file, in order.

Log in to unlock

Documents

Log in to open the documents of this file: the application as filed, every office action and response, the notice of allowance.

Log in to unlock

Chain of title

⤢ drag to zoom2020202220242026202820302032203420362038Owner 1
Titlehover for detail · click to open

See the full assignment history — every owner this patent has passed through, with recordation dates and reel/frame numbers.

Log in to unlock