Liquid compounds and method for the use thereof as hydrogen stores
10450194 ยท 2019-10-22
Assignee
Inventors
- Andreas Boesmann (Hessdorf, DE)
- Peter Wasserscheid (Erlangen, DE)
- Nicole Brueckner (Erlangen, DE)
- Daniel Teichmann (Munich, DE)
- Jennifer Dungs (Stuttgart, DE)
Cpc classification
B01J19/24
PERFORMING OPERATIONS; TRANSPORTING
Y02E60/32
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
C01B3/0015
CHEMISTRY; METALLURGY
International classification
C01B3/00
CHEMISTRY; METALLURGY
B01J19/24
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The invention relates to a mixture, which is liquid at room temperature and which is composed of two or more compounds, which are constructed exclusively of the elements carbon and hydrogen and, in individual known compositions, form a synthetic substance mix that can be used as a heat-transfer liquid. The mixture is characterized in that the mixture contains at least one compound having at least two non-condensed, non-pi-conjugated aromatic units and is used in catalytic methods to bind hydrogen to or release hydrogen from the mixture.
Claims
1. A method of fully or partially supplying a consumer with hydrogen, comprising using a liquid mixture to bind hydrogen to the liquid mixture catalytically at a hydrogen pressure of 5 to 200 bar and at a reaction temperature between 20 C. and 230 C. and to release hydrogen from the liquid mixture, wherein the liquid mixture comprises two or more compounds selected from isomers of benzyltoluene and/or dibenzyltoluene, wherein the liquid mixture in its hydrogen-rich form, which contains a mass fraction of at least 6% loaded hydrogen, stably retains bonded hydrogen above 280 C., and wherein a first storage tank for the liquid mixture carrying hydrogen supplies the liquid mixture to a reactor via a feed line and the hydrogen-carrying liquid mixture is dehydrogenated in the reactor and the dehydrogenated liquid mixture is discharged from the reactor into a second storage tank via a discharge line, wherein the reactor supplies the consumer with hydrogen via a connecting line.
2. The method according to claim 1, wherein a mass fraction of two or more compounds selected from isomers of benzyltoluene and dibenzyltoluene is more than 50% by mass, based on the overall mass of the liquid mixture.
3. The method according to claim 2, wherein the consumer is an internal combustion engine or at least a fuel cell.
4. The method according to claim 2, wherein the consumer contributes to the energy supply of a motor vehicle.
5. The method according to claim 1, wherein a mass fraction of two or more compounds selected from isomers of benzyltoluene and dibenzyltoluene is more than 90% by mass, based on the overall mass of the liquid mixture.
6. The method according to claim 5, wherein the consumer is an internal combustion engine or at least a fuel cell.
7. The method according to claim 5, wherein the consumer contributes to the energy supply of a motor vehicle.
8. The method according to claim 1, wherein the consumer is an internal combustion engine or at least a fuel cell.
9. The method according to claim 1, wherein the consumer contributes to the energy supply of a motor vehicle.
10. The method according to claim 1, wherein the mixture is contacted in the reactor with a metal-containing catalyst and binds or releases hydrogen in the process, wherein the metal-containing catalysts used for hydrogen loading and hydrogen unloading are identical or different solid catalysts comprising one or more of the metals palladium, nickel, platinum, iridium, ruthenium, cobalt, rhodium, copper, gold, rhenium and iron in finely divided form on a porous apolar carrier.
11. The method according to claim 1, wherein hydrogen is released in the reactor from a hydrogen-laden mixture by catalytic dehydrogenation.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
(3)
DETAILED DESCRIPTION OF THE DRAWINGS
(4) General examples of heat carriers advantageously useful as hydrogen carriers will now be adduced and described with reference to three figures. Marlotherm (from SASOL for example) or similar technically utilized heat carrier oils are mixtures of different isomers of benzyltoluene (Marlotherm LH, SASOL) and dibenzyltoluene (Marlotherm SH, SASOL). The different isomers differ because the benzyl groups on the central toluene ring are attached to the central toluene ring at different ring positions in relation to the methyl group of the toluene. When the methyl group of the toluene ring is assigned ring position 1, Marlotherm LH (SASOL) is a mixture of benzyltoluenes whose benzyl group is attached to the toluene ring at positions 2, 3 or 4.
(5) Marlotherm SH (SASOL) is a mix of dibenzyltoluene. When the methyl group on the toluene ring is again assigned ring position 1, then the two benzyl groups in Marlotherm SH (SASOL) are attached in positions 2 and 3, 2 and 4, 2 and 5, 2 and 6, 3 and 4 or 3 and 5.
(6) The substance mixes used as heat carriers, under Marlotherm LH (SASOL) and Marlotherm SH (SASOL) and also under other tradenames and other brand owners, for example Hills, can be more generally characterized in that they contain compounds having two or more non-fused non-pi-conjugated aromatic units. A general depiction of a typical structural unit in such mixes is shown by
(7) The foregoing disclosure has been set forth merely to illustrate the invention and is not intended to be limiting. Since modifications of the disclosed embodiments incorporating the spirit and substance of the invention may occur to persons skilled in the art, the invention should be construed to include everything within the scope of the appended claims and equivalents thereof.