Wearable and flexible electrochemical sweat sensor consisting of a polymer composite membrane containing graphene
A multi-composite electrochemical cell substantially consists of a thin polymer membrane including three different adjacent sectors, which are made of the same appropriately seamlessly modified polymer, incorporating in the polymer one or more conductive phases, or conductive fillers, such as graphene, metal, or a combination thereof. In the first sector the polymer material incorporates graphene nanoplatelets and acts as a cathode; in the second sector, interposed between the other two, the polymer material acts as an insulating spacer; in the third sector the polymer material incorporates graphene nanoplatelets and a metal filler or immersed metal contact rheophore, with negative standard reduction potential, and acts as an anode; wherein the metal filler is in the form of dispersed powder or dispersed flakes, or of a thin sheet incorporated in the polymer.
1. A multi-composite electrochemical cell consisting essentially of a thin polymer membrane comprising three different adjacent sectors, which are made of the same appropriately seamlessly modified polymer, incorporating in said polymer one or more conductive phases, or conductive fillers, and wherein:
in the first sector, the polymer material incorporates graphene nanoplatelets and acts as a cathode;
in the second sector, interposed between the other two, the polymer material acts as an insulating spacer;
in the third sector, the polymer material incorporates graphene nanoplatelets and a metal filler or immersed metal contact rheophore, with negative standard reduction potential, and acts as an anode;
wherein said metal filler is in the form of dispersed powder or dispersed flakes, or of a thin sheet incorporated in the polymer.
2. The electrochemical cell according to claim 1 , wherein said metal filler when present results in a different electrochemical potential for the two lateral sectors of the polymer membrane, said sectors acting as a cathode and as an anode, respectively, of the electrochemical cell in the presence of a conductive solution which connects them electrically.
3. The electrochemical cell according to claim 2 , wherein when said first cathode sector and said third anode sector are electrically connected to each other by means of a conductive solution which touches them simultaneously acting as an electrolytic solution, a voltage is produced between said cathode and anode, the intensity of which depends on the concentration of ions in the conductive solution.
4. The electrochemical cell according to claim 2 , wherein the polymer material is polyvinylidene fluoride.
5. The electrochemical cell according to claim 4 , wherein said metal filler with negative standard reduction potential is Nickel or Aluminum.
6. The electrochemical cell according to claim 5 , wherein said polymer membrane is self-standing, light, flexible and maneuverable, washable and reusable.
7. The electrochemical cell according to claim 1 , wherein when said first cathode sector and said third anode sector are electrically connected to each other by means of a conductive solution which touches them simultaneously acting as an electrolytic solution, a voltage is produced between said cathode and anode, the intensity of which depends on the concentration of ions in the conductive solution.
8. The electrochemical cell according to claim 1 , wherein the polymer material is polyvinylidene fluoride.
9. The electrochemical cell according to claim 1 , wherein said metal filler with negative standard reduction potential is Nickel or Aluminum.
10. The electrochemical cell according to claim 1 , wherein said polymer membrane is self-standing, light, flexible and maneuverable, washable and reusable.
11. A process of producing an electrolytic cell with polymer membrane wherein it includes using at least the following reagents, chemicals, and products:
polyvinylidene fluoride,
N, N-dimethylformamide,
commercial metal powders or thin sheets,
graphite intercalation compound,
and wherein it comprises the following steps:
(a) producing worm-like exfoliated graphite, or WEG, through thermal expansion of graphite intercalation compounds, said GIC compounds being subjected to a thermal shock at a temperature above 1000° C. for a time between 4 and 8 seconds, thus causing an increase in volume of about 200 times and complete reduction;
(b) dissolving a film of polyvinylidene fluoride PVDF in N, N-dimethylformamide by magnetic stirring, for a time period up to 4 hours, at a controlled temperature between 55° C. and 75° C.;
(c) partitioning the PVDF and DMF solution obtained from the previous step into two containers: a first container and a second container;
(d) adding the worm-like exfoliated graphite prepared in step (a), to the first container;
(e) homogenizing, through sonication, the compound resulting from the previous step, using an ultrasound processor set with a pulsed cycle (typically 1 sec on and 1 sec off) and for an execution time of at least fifteen minutes, thus ensuring the exfoliation of the WEGs and obtaining a suspension of GNP;
(f) obtaining, after sonication, two distinct mixtures: one consisting of PVDF+DMF only in the second container, the other of PVDF+DMF loaded with GNP in the first container;
(g) separating part of the mixture of PVDF and GNP from the first container in a third container and adding commercial metal powders or metal flakes thereto, mixed by stirring and/or ultrasonic bath, depending on the metal powders chosen;
(h) casting the three mixtures thus obtained: one consisting of PVDF only, another of PVDF with GNP, and a third one consisting of PVDF, GNP, and metal powders, on a mask appropriately provided to obtain a polymer membrane having three different adjacent sectors;
(i) treating the mask with the cast mixtures from the previous step, in an oven at 160° C. for a time period from 1 to 6 hours.
12. The process according to claim 11 , wherein the dissolution step (b) occurs at the temperature of 65° C. for 2 hours.