Apparatus and method for performing electrolysis

Patent metadata

Field	Value
Publication number	US-2023349059-A1
Application number	US-202118016965-A
Country	US
Kind code	A1
Filing date	Aug 24, 2021
Priority date	Aug 24, 2020
Publication date	Nov 2, 2023
Grant date	—

Abstract

The invention relates to an apparatus and a method for performing electrolysis with an originally oxygen-containing alkali hydroxide solution as an electrolyte precursor, wherein the pressure and temperature of the alkali hydroxide solution and the O 2 content thereof are set.

First claim

1 . A process for operating an electrolysis apparatus, the process comprising introducing an electrolyte into an electrolysis cell of the electrolysis apparatus and discharging the electrolyte from the electrolysis cell, wherein gaseous oxygen is introduced into the electrolyte in contact with at least one electrode of the electrolysis cell as a result of an electrochemical process occurring at the at least one electrode, wherein the electrolyte to be introduced into the electrolysis cell is an alkaline, aqueous electrolyte containing alkali metal hydroxide and at an absolute pressure of 1 bar and a temperature of 20° C. and an O 2 amount between 0 and 25 mg/L, wherein before introduction into the electrolysis cell the absolute pressure of the electrolyte for introduction is in the range from 1.2 bar to 3.5 bar and the temperature of the electrolyte for introduction is greater than 40° C.

2 . The process as claimed in claim 1 , wherein said electrolyte for introduction has a smaller O 2 amount than the discharged electrolyte.

3 . The process as claimed in claim 1 , wherein said discharged electrolyte has an O 2 amount of at least 25 mg/L at an absolute pressure of 1 bar and a temperature of 20° C.

4 . The process as claimed in claim 1 , wherein said electrolyte for introduction has a temperature in the range from 60° C. to 85° C.

5 . The process as claimed in claim 1 , wherein said electrolyte flows through the electrolysis cell, wherein said electrolyte is continuously introduced into the electrolysis cell and discharged therefrom again.

6 . The process as claimed in claim 1 , wherein said at least one electrode consumes oxygen gas or evolves oxygen as a result of the electrochemical process occurring at said at least one electrode.

7 . The process as claimed in claim 1 , wherein said electrolyte for introduction is at the-feed conduits and/or the an inlet into the electrolysis cell in contact with at least one thermoplastic material.

8 . The process as claimed in claim 1 , wherein the electrolyte is subjected to a step of reducing the O 2 amount and then introduced into the electrolysis cell as said electrolyte for introduction.

9 . The process as claimed in claim 1 , wherein discharged electrolyte is subjected to at least one step of reducing the O 2 amount and subsequently reused for providing electrolyte to be introduced into the electrolysis cell.

10 . The process as claimed in claim 9 , wherein discharged electrolyte is mixed with at least water to lower the alkalinity before the step of reducing the O 2 amount.

11 . The process as claimed in claim 8 , wherein an inert gas is employed to reduce the O 2 amount.

12 . An electrolysis apparatus comprising
(a) at least one electrolyzer, comprising
at least one electrolysis cell comprising at least one electrode suitable for an electrochemical process where oxygen gas is introduced into the electrolyte of the electrolyzer which is in contact with said electrode,
at least one inlet for introducing electrolyte for introduction with feeding at least into said at least one electrolysis cell, wherein the electrolyte for introduction contains an O 2 amount of between 0 and 25 mg/L and has an absolute pressure in the range from 1.2 bar to 3.5 bar and a temperature of greater than 40° C.,
at least one apparatus for pressurizing,
at least one outlet for discharging discharged electrolyte,
and (b) at least one apparatus for reducing the O 2 amount of aqueous, alkaline liquids for providing the electrolyte for introduction which is in fluid communication with the at least one inlet for introducing electrolyte for introduction.

13 . The electrolysis apparatus as claimed in claim 12 , wherein said electrode is an oxygen depolarized cathode.

14 . The electrolysis apparatus as claimed in claim 12 , wherein the electrolysis apparatus contains electrolyte for introduction, wherein the electrolyte for introduction is an alkaline, aqueous electrolyte containing alkali metal hydroxide and an O 2 amount of between 0 and 25 mg/L.

15 . The electrolysis apparatus as claimed in claim 12 , wherein the electrolysis apparatus additionally contains a storage vessel for electrolytes, the storage vessel comprising at least one feed which is in fluid communication with the apparatus for reducing the O 2 amount, wherein the apparatus for reducing the O 2 amount is in fluid communication with the outlet for discharging discharged electrolyte.

16 . The process as claimed in claim 3 , wherein said discharged electrolyte has an O 2 amount of at least 35 mg/L at an absolute pressure of 1 bar and a temperature of 20° C.

17 . The process as claimed in claim 7 , wherein the at least one thermoplastic material is selected from polypropylene (PP), polyvinyl chloride (PVC), or polytetrafluoroethylene (PTFE).

18 . The process as claimed in claim 11 , wherein the inert gas comprises nitrogen, argon, or a mixture thereof.

19 . The electrolysis apparatus as claimed in claim 12 , wherein the at least one apparatus for pressurizing comprises a pump.

Assignees

• Covestro Deutschland Ag

Inventors

• Goltz Oliver
• Sieben Rainer
• Bulan Andreas
• Grossholz Michael

Classifications

• C25B15/029 Primary

  Concentration · CPC title

• C25B9/15

  Flow-through cells · CPC title

• C25B15/027

  Temperature · CPC title

• C25B15/087

  Recycling of electrolyte to electrochemical cell · CPC title

• C25B1/04 Primary

  by electrolysis of water · CPC title