Process for the production of hydrogen peroxide
View Patent ↗The anthraquinone process for producing hydrogen peroxide, including a hydrogenation step, an oxidation step and an extraction step. The oxidation waste gas leaving the oxidation reactor at an excess pressure is passed as a propellant jet to one or more gas jets and whereby a vacuum is produced for auxiliary processes, such as drying of the working solution, distillation of the aqueous hydrogen peroxide solution and drawing off of ventilator gases from solvent storage tanks.
1. A process for the production of hydrogen peroxide by the anthraquinone process in a continuously operated production plant, comprising:
(i) in a hydrogenation step, hydrogenating an organic working solution containing one or more anthraquinone derivatives in the presence of a heterogeneous catalyst, to form a hydrogenated working solution,
(ii) in an oxidation step, oxidizing the hydrogenated working solution to form an oxidized working solution, with the formation of hydrogen peroxide, by introducing an oxygen-containing oxidizing gas, at an excess pressure P i of at least 1 bar into an oxidation reactor and contacting it with the working solution from step (i), withdrawing oxidation waste gas from the oxidation reactor and optionally purifying it in a waste-gas purification plant, and
(iii) recovering the hydrogen peroxide from the oxidized working solution,
wherein the oxidation waste gas has an excess pressure P a which is less than P i but greater than atmospheric pressure P 0 , and passing the oxidation waste gas as a flow of propellant gas to at least one gas jet and thereby producing a vacuum for auxiliary processes required in the anthraquinone process.
2. The process according to claim 1 further comprising using said vacuum for at least one of the following process steps:
drying extracted working solution from extraction prior to return of said extracted working solution to the hydrogenation step,
for distilling resulting aqueous hydrogen peroxide solution,
for drawing in ventilator gases at emission points of solvent vapours within the production plant.
3. The process according to claim 2 wherein said solvent vapours are from solvent storage tanks.
4. The process according to claim 1 , wherein air or oxygen-enriched air as oxidizing gas is introduced into the oxidation reactor at an excess pressure P i within the range of 2 to 15 bar.
5. The process according to claim 1 , wherein the oxidizing gas leaving the oxidation reactor at an excess pressure P a within the range of 1 to 10 bar is passed, in the form of a propellant jet, to a gas jet.
6. The process according to claim 4 , wherein the oxidizing gas leaving the oxidation reactor at an excess pressure P a within the range of 1 to 10 bar is passed, in the form of a propellant jet, to a gas jet.
7. The process according to claim 1 , further comprising in a dryer for drying extracted working solution, producing a dryer vacuum within the range of 10 to 300 mbar absolute, by a gas jet operated by oxidation waste gas and passing a mixture of propellant gas and vapours drawn to a waste-gas purification plant.
8. The process according to claim 4 , further comprising in a dryer for drying extracted working solution, producing a dryer vacuum within the range of 10 to 300 mbar absolute, by a gas jet operated by oxidation waste gas and passing a mixture of propellant gas and vapours drawn to a waste-gas purification plant.
9. The process according to claim 5 , further comprising in a dryer for drying extracted working solution, producing a dryer vacuum within the range of 10 to 300 mbar absolute, by a gas jet operated by oxidation waste gas and passing a mixture of propellant gas and vapours drawn to a waste-gas purification plant.
10. The process according to claim 1 , further comprising at a head of a distillation device for concentrating aqueous hydrogen peroxide solution, forming a distillation vacuum within the range of 20 to 200 mbar absolute by a gas jet operated by oxidation waste gas and passing a mixture of propellant gas and of previously at least partially condensed vapours to a waste-gas purification plant.
11. The process according to claim 4 , further comprising at a head of a distillation device for concentrating aqueous hydrogen peroxide solution, forming a distillation vacuum within the range of 20 to 200 mbar absolute by a gas jet operated by oxidation waste gas and passing a mixture of propellant gas and of previously at least partially condensed vapours to a waste-gas purification plant.
12. The process according to claim 5 , further comprising at a head of a distillation device for concentrating aqueous hydrogen peroxide solution, forming a distillation vacuum within the range of 20 to 200 mbar absolute by a gas jet operated by oxidation waste gas and passing a mixture of propellant gas and of previously at least partially condensed vapours to a waste-gas purification plant.
13. The process according to claim 1 , further comprising in order to prevent emissions of solvent from storage tanks containing organic solvents or working solution, drawing off ventilator gases by a gas jet operated by oxidation waste gas and having a suction pressure within the range of less than atmospheric pressure up to 400 mbar absolute and passing a mixture of propellant gas and gases drawn in to a waste-gas purification plant.
14. The process according to claim 4 , further comprising in order to prevent emissions of solvent from storage tanks containing organic solvents or working solution, drawing off ventilator gases by a gas jet operated by oxidation waste gas and having a suction pressure within the range of less than atmospheric pressure up to 400 mbar absolute and passing a mixture of propellant gas and gases drawn in to a waste-gas purification plant.
15. The process according to claim 5 , further comprising in order to prevent emissions of solvent from storage tanks containing organic solvents or working solution, drawing off ventilator gases by a gas jet operated by oxidation waste gas and having a suction pressure within the range of less than atmospheric pressure up to 400 mbar absolute and passing a mixture of propellant gas and gases drawn in to a waste-gas purification plant.
16. The process according to claim 1 , further comprising passing a mixture of propellant gas and withdrawn gases through a bed of an adsorbent material, in an adsorption plant and freeing said mixture from organic constituents.
17. The process according to claim 16 wherein said bed of absorbent material is activated carbon or a zeolite.
18. The process according to claim 1 further comprising passing the oxidation waste gas to a first gas jet for the purpose of drawing off solvent vapours from storage tanks, and passing at least another gas jet to a dryer for producing the vacuum for the drying of the working solution and/or to a distillation column to operate a distillation column.