Modified ceramsite packing useful for biomembrane trickling filter and a process for removing SO2 from flue gas using the trickling filter

Patent metadata

Field	Value
Publication number	US-9833740-B2
Application number	US-201414307976-A
Country	US
Kind code	B2
Filing date	Jun 18, 2014
Priority date	Jun 18, 2013
Publication date	Dec 5, 2017
Grant date	Dec 5, 2017

Abstract

A process of removing SO 2 from a flue gas with a trickling filter using modified ceramsite packing is described. The biological flue gas desulfurization process includes: feeding the flue gas containing sulfur dioxide through the column bottom into the biomembrane trickling filter at certain temperature, contacting with the modified ceramsite biomembrane packing and purifying, which purified flue gas is discharged via the column top; and spraying the nutrient fluid rich in high concentration of the desulfurization strain through the top to the modified ceramsite biomembrane packing, thereby the sulfur-bearing pollution source in the flue gas is degraded, so as to discharge a purified flue gas satisfying the environmental requirements.

First claim

The invention claimed is:

1. A process of removing SO 2 from flue gas comprising utilizing a biomembrane trickling filter comprising a packing, in which the biomembrane trickling filter has a principle section of a packed column and further comprises a liquid circulation system and a gas circulation system, wherein the packing is a modified ceramsite obtained from chemically modifying a ceramsite, wherein the modified ceramsite has performance parameters of: a density of about 2.1-about 2.5 g/cm 3 , a specific surface area of about 0.4-about 0.8 m 2 /g, a porosity of about 0.5-about 0.7, a pH at isoelectric point of about 7.5-about 9.0, and a surface pH of about 5.0-about 6.0.

2. The process according to claim 1 , wherein a desulfurization strain is introduced into a nutrient fluid after the chemical modification of the packing, so as to carry out a biomembrane colonization for the packing in the column, and to form a biomembrane of the desulfurization strain on a packing surface.

3. The process according to claim 2 , comprising a counter-current operation manner in the column, wherein the flue gas containing SO 2 is fed through the column bottom into the biomembrane trickling filter, contacted with the modified ceramsite biomembrane packing and purified, which purified flue gas is discharged via the column top; and the nutrient fluid rich of the desulfurization strain is sprayed through the column top to the modified ceramsite biomembrane packing, passed through the packing layer and discharged via the column bottom, wherein a ratio of nutrient fluid:bacteria-containing fluid is 50-100:1.

4. The process according to claim 1 , wherein the process for chemically modifying the ceramsite packing comprises: drying a cleaned ceramsite; impregnating with a solution of an acid, and washing with water to be neutral; ultrasonic impregnating the neutral ceramsite obtained into an aqueous solution of modifier and baking; calcinating at a temperature of 300 degrees C. to 700 degrees C., cooling to room temperature, washing with water, and baking, so as to obtain the modified ceramsite packing.

5. The process according to claim 1 , comprising a membrane-forming step, wherein the membrane-forming step in the column comprises: introducing the desulfurization strain into the nutrient fluid, and spraying the nutrient fluid containing the desulfurization strain in the biomembrane trickling filter downward to the packing, so as to immobilize the desulfurization strain to the packing, and adding dominant bacteria periodically, wherein a ratio of nutrient fluid:bacteria-containing fluid is 50-100:1.

6. The process according to claim 1 , wherein the nutrient fluid consists of an aqueous mixture of two or more of ammonium sulfate, potassium chloride, potassium hydrogen phosphate, magnesium sulfate heptahydrate, calcium nitrate, ammonium chloride, ammonium dihydrogen phosphate, calcium chloride and iron(II) sulfate heptahydrate.

7. The process according to claim 2 , wherein the desulfurization strain is one or more selected from the group consisting of Thiobacillus ferroxidans, Thiobacillus thioparus, thiobacillus denitrificans, desulfovibrio, Leptospirillums ferrooxidans, thiobacillus thiooxidans and Thiothrix.

8. The process according to claim 1 , wherein the biomembrane trickling filter is constructed as a multi-stage packing column.

9. The process according to claim 1 , wherein the temperature during the desulfurization in the biomembrane trickling filter is controlled to be 20-40 degrees C.

10. The process according to claim 4 , wherein the modifier is an aqueous solution of iron chloride, ferric nitrate, aluminum sulfate or aluminum chloride.

11. The process according to claim 9 , wherein the temperature during the desulfurization in the biomembrane trickling filter is controlled to be 25-35 degrees C.

Assignees

• China Petroleum & Chem Corp
• Res Institute Of Nanjing Chemical Industrial Group

Inventors

• Hao Aixiang
• Mao Songbai
• Kong Jing

Classifications

• B01D53/78

  with gas-liquid contact · CPC title

• B01D2258/0283

  Flue gases · CPC title

• B01D53/84 Primary

  Biological processes · CPC title

• B01D53/228

  characterised by specific membranes · CPC title

• B01D53/18

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title