Process for energy recovery in carbon black production

Patent metadata

Field	Value
Publication number	US-10723964-B2
Application number	US-201615759558-A
Country	US
Kind code	B2
Filing date	Sep 9, 2016
Priority date	Sep 28, 2015
Publication date	Jul 28, 2020
Grant date	Jul 28, 2020

Abstract

A combustible gas from carbon black production is utilized in a gas engine by adding an oxygen-containing gas to the combustible gas, passing said mixed gas over a selective catalyst, which is active for oxidizing H2S to SO2 but substantially inactive for oxidation of CO, H2 and other hydrocarbons with less than 4 C-atoms, passing the converted gas through an SO2 removal step, and passing the cleaned gas to a gas engine or to an energy recovery boiler. This way, the tail gas from carbon black production, which is normally combusted in a CO boiler or incinerated, can be utilized to good effect.

First claim

The invention claimed is:

1. A method for utilization of a combustible gas from carbon black production in a gas engine, said method comprising the steps of
(a) adding an oxygen-containing gas to the combustible gas in an amount corresponding to an O 2 content of 0.5-5% in an outlet of a carbon black production facility,
(b) passing said mixed gas over a selective catalyst, which is active for oxidizing H 2 S to SO 2 but substantially inactive for oxidation of CO, H 2 and other hydrocarbons with less than 4 C-atoms,
(c) passing the converted gas from step (b) through an SO 2 removal step, and
(d) passing the cleaned gas from step (c) to a gas engine.

2. The method according to claim 1 , wherein the cleaned gas from step (c) is passed to an energy recovery boiler.

3. The method according to claim 1 , wherein the selective catalyst consists of one or more metal oxides, in which the metal is selected from the group consisting of V, W, Ce, Mo, Fe, Ca and Mg, and one or more supports taken from the group consisting of Al 2 O 3 , SiO 2 , SiC and TiO 2 , optionally in the presence of other elements in a concentration below 1 wt %.

4. The method according to claim 3 , wherein the selective catalyst comprises from 1 wt % to 50 wt % V 2 O 5 .

5. The method according to claim 1 , wherein a monolithic type catalyst is used with the further purpose of avoiding plugging in the system.

6. The method according to claim 1 , wherein the selective catalyst is integrated inside the wall of a ceramic candle dust filter.

7. The method according to claim 1 , wherein the selective catalyst is integrated inside the wall of a fabric dust filter bag.

8. The method according to claim 1 , wherein said SO 2 removal step is carried out by using a wet scrubber and an alkaline reagent, an oxidative reagent, or combinations thereof.

9. The method according to claim 8 , wherein said SO 2 removal step is carried out by using a dry scrubber and an alkaline sorbent.

10. The method according to claim 1 ,
wherein said SO 2 removal step is carried out by using a wet scrubber and an alkaline reagent, an oxidative reagent, or combinations thereof, or
wherein said SO 2 removal step is carried out by using a dry scrubber and an alkaline sorbent.

Assignees

• Haldor Topsoe As

Inventors

• Jakobsson Niklas Bengt
• Christensen Kurt Agerbaek

Classifications

• B01J35/56

  Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title

• B01D53/508 Primary

  by treating the gases with solids · CPC title

• Y02P20/10

  Process efficiency · CPC title

• B01D2255/2047

  Magnesium · CPC title

• B01D2251/604

  Hydroxides · CPC title