GB2108312A - Electrochemical cells - Google Patents

Electrochemical cells Download PDF

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Publication number
GB2108312A
GB2108312A GB08227964A GB8227964A GB2108312A GB 2108312 A GB2108312 A GB 2108312A GB 08227964 A GB08227964 A GB 08227964A GB 8227964 A GB8227964 A GB 8227964A GB 2108312 A GB2108312 A GB 2108312A
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GB
United Kingdom
Prior art keywords
cell
copc
cathode
fepc
carbon
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Withdrawn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
GB08227964A
Inventor
Narayan Doddapaneni
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.)
Honeywell Inc
Original Assignee
Honeywell Inc
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 Honeywell Inc filed Critical Honeywell Inc
Priority to GB08227964A priority Critical patent/GB2108312A/en
Publication of GB2108312A publication Critical patent/GB2108312A/en
Withdrawn legal-status Critical Current

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/96Carbon-based electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9008Organic or organo-metallic compounds
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/14Cells with non-aqueous electrolyte
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Hybrid Cells (AREA)

Abstract

An electrochemical cell with a lithium anode, an electrolyte solution comprising an electrolyte salt dissolved in sulfuryl chloride and a cathode doped with a macrocyclic complex of a transition metal such as CoPc, FePc or (CoPc)n.

Description

SPECIFICATION Electrochemical cells An electrochemical cell based on lithium-sulfuryi chloride (LiiSO2Cl2) electrochemical system offers a potentially higher energy performance than the lithium thionyl chloride (Li/SOCI2) system. Poor electrochemical discharge and relatively narrow operating temperature range have, however, hindered a practical cell development. One of the factors believed responsible for poor discharge performance is cathode substrate. High surface area Teflon (trademark of E.l. du Pont DeNemours)bonded carbon cathodes, where S02C12 undergoes reduction, and irreversibility of the cathode reaction contribute excessive cathode overpotential. Another factor contributing to premature cell failure, particularly at high discharge rates, is the presence of reactive intermediate reduction species.
According to the present invention, there is provided an electrochemical cell with an improved current producing capability, the cell comprising a metal anode; a sulfuryl chloride depolarizer and an electrolyte salt; and a cathode doped with a macrocyclic complex of a transition metal.
The catalysts may be such as polymeric and monomeric cobalt and iron phthalocyanines.
It has been discovered that the rate of S02C12 reduction can be increased substantially by doping the porous carbon cathodes with CoPo, FePc and (CoPc) catalysts. Both monomeric CoPe and FePc are soluble in acid (AICI3/SQ2CI2) as well as neutral (LiAlClSO2Cl2) electrolytes. However, the heat treated (500 to 600 C) polymeric (CoPcXn, which is synthesized by heating a mixture of 3,3,4, 4-benzophenone tetracarboxylic dianhydride (BTDA), CoCI2 and urea at 200 C for one hour, does not dissolve and is stable in both acid and neutral electrolytes.
A preferred cathode material is Shawinigan (Registered Trade Mark) carbon black. A binder, such as Teflon (trademark of E.l. du Pont DeNemours) may also be included.
Embodiments of the present invention will now be described. A number of cells were constructed employing a lithium anode, a sulfuryl chloride depolarizer and lithium tetrachloroaluminate elec troiyte salt, and porous carbon cathodes doped with a macrocyclic complex of a transition metal. Experiments, as described below, were performed on these various cells having cathodes catalyzed with FePc, CoPo, or (CoPc) and compared to a cell with uncatalyzed cathode. Catalyst doping of cathodes can be achieved by mixing the catalyst with carbon before cathode fabrication or, in the case of FePc and CoPc, by dissolving the catalyst in the electrolyte.
Each of the cells for which data is given in Table 1 below comprised a lithium anode, an electrolyte of 1.5 mole solution of lithium tetrachloroaluminate in sulfuryl chloride and a porous carbon cathode.
In the cells with FePc and CoPe, the catalyst doping of the cathode was accomplished by adding catalyst to the electrolyte. Approximately 3 milligrams of catalyst per cc of electrolyte were used. It has been found, however, that much smaller amounts of the catalyst, i.e. less than 0.5 milligrams per cc of electrolyte, produce a significant improvement in the cell operation. On the other hand, much larger amounts of the catalyst will, beyond a certain point, not produce any further improvement.
Cathode doping with (CoPc) was accomplished by adding it to the cathode during the manufacture of the cathode. The cathode was formed by mixing (CoPc) with Shawinigan (R.T.M.) carbon black in approximate ratio of 5% to 95% and heat treating the mixture at 55000 or higher for two or morn hours.
Upon cooling, a scurry was formed by adding to the mixture a nonaqueous solvent and binder, such as Teflon. The scurry was then shaped into the desired cathode shape and allowed to dry.
Although in the specific example given here, the ratio of (CoPc) to carbon was almost 5% to 95%, it has been found that the amount of (CoPc) could vary from 0.5% to 20% by weight based on the weight of carbon. Preferrably, from 2% to 10% by weight, based on the weight of carbon, is employed.
TABLE 1 POLARIZATION CHARACTERISTICS OF Li/SO2Sl2 CELLS WITH VARIOUS CATALYSTS (1.SM LiALCl,,'SO2Cl2 at 72 F)
CURRENT CELL VOLTAGE-volts milliamperes per cm No Catalyst FePc CoPc (CoPc)n 5 3.55 3.52 3.55 3.58 10 3.17 3.25 3.48 3.50 20 3.05 3.15 3.37 3.45 30 3.00 3.10 3.30 3.38 40 2.95 3.06 3.25 3.33 As can be seen from Table 1 above, the cells doped with FePc, CoPc, and (CoPc) produced significantly higher voltages.The greatest improvement throughout the entire current rate discharge range was shown by the cell having its cathode catalyzed by (CoPc).
Table 2 below comparative polarization character istics of cells similartothose represented byTable 1, but utilizing 2.3M AICI3/SO2CI2 as the electrolyte.
TABLE 2 POLARIZATION CHARECTERISTICS Li/SO2Cl2 CELLS WITH VARIOUS CATALYSTS (2.3M AlCl3/SO2Cl2 AT72 F.
CURRENT CELL VOTAGE - volts milliamperes per cm No Catalyst FePc CoPc (CoPc)n 10 3.21 3.76 3.31 3.85 20 3.02 3.30 3.45 3.55 30 2.94 3.21 3.37 3.34 40 2.88 3.15 3.32 3.28 60 2.75 3.05 3.20 3.13 80 2.45 2.90 3.11 3.04

Claims (7)

1. An electrochemical cell comprising d petal anode; a sulfuryl chloride depolari.r and an electro lyte salt; and a cathode doped with a macrocyclic complex of a transition metal.
2 The electrochemical cell of Claim 1, wherein the cathode is doped with a catalyst selected from CoPc, FePc and (CoPc)n.
3. The cell of Claim 1 or 2, wherein the cathode consists primarily of carbon.
4 The cell of Claim 3,wherein said carbon comprises Shawinigan carbon black.
5. The cell of any one of Claim 1 to 4, wherein said electrolyte salt is lithium tetrachloroaluminate or aluminium chloride.
6. The cell of any one of the preceding claims, wherein the anode is an alkaline metal, for example lithium.
7. An electrochemical cell substantially as herein described.
GB08227964A 1982-09-30 1982-09-30 Electrochemical cells Withdrawn GB2108312A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB08227964A GB2108312A (en) 1982-09-30 1982-09-30 Electrochemical cells

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB08227964A GB2108312A (en) 1982-09-30 1982-09-30 Electrochemical cells

Publications (1)

Publication Number Publication Date
GB2108312A true GB2108312A (en) 1983-05-11

Family

ID=10533283

Family Applications (1)

Application Number Title Priority Date Filing Date
GB08227964A Withdrawn GB2108312A (en) 1982-09-30 1982-09-30 Electrochemical cells

Country Status (1)

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GB (1) GB2108312A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2164785A (en) * 1984-09-06 1986-03-26 Nat Res Dev Electrode for reducing oxygen
WO1986001940A1 (en) * 1984-09-19 1986-03-27 Honeywell Inc. High rate metal oxyhalide cells
EP0580506A1 (en) * 1992-07-23 1994-01-26 Alcatel Lithium cell with liquid cathode
WO2012064279A1 (en) * 2010-11-12 2012-05-18 Anders Palmqvist Fuel cell electrode having porous carbon core with macrocyclic metal chelates thereon

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2164785A (en) * 1984-09-06 1986-03-26 Nat Res Dev Electrode for reducing oxygen
WO1986001940A1 (en) * 1984-09-19 1986-03-27 Honeywell Inc. High rate metal oxyhalide cells
EP0580506A1 (en) * 1992-07-23 1994-01-26 Alcatel Lithium cell with liquid cathode
FR2694135A1 (en) * 1992-07-23 1994-01-28 Alsthom Cge Alcatel Lithium battery with liquid cathode.
US5512386A (en) * 1992-07-23 1996-04-30 Alcatel Alsthom Compagnie Generale D'electricite Liquid cathode lithium cell
WO2012064279A1 (en) * 2010-11-12 2012-05-18 Anders Palmqvist Fuel cell electrode having porous carbon core with macrocyclic metal chelates thereon
US10115971B2 (en) 2010-11-12 2018-10-30 Appem Ltd. Fuel cell electrode having porous carbon core with macrocyclic metal chelates thereon
US11721813B2 (en) 2010-11-12 2023-08-08 Celcibus Ab Fuel cell electrode having porous carbon core with macrocyclic metal chelates thereon

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