MX9707397A - Conversion en fase liquida de una fuente de dioxido de azufre en acido sulfurico. - Google Patents
Conversion en fase liquida de una fuente de dioxido de azufre en acido sulfurico.Info
- Publication number
- MX9707397A MX9707397A MX9707397A MX9707397A MX9707397A MX 9707397 A MX9707397 A MX 9707397A MX 9707397 A MX9707397 A MX 9707397A MX 9707397 A MX9707397 A MX 9707397A MX 9707397 A MX9707397 A MX 9707397A
- Authority
- MX
- Mexico
- Prior art keywords
- sulfuric acid
- sulfur dioxide
- source
- liquid phase
- conversion
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/69—Sulfur trioxide; Sulfuric acid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/507—Sulfur oxides by treating the gases with other liquids
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/69—Sulfur trioxide; Sulfuric acid
- C01B17/74—Preparation
- C01B17/76—Preparation by contact processes
- C01B17/775—Liquid phase contacting processes or wet catalysis processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/50—Inorganic acids
- B01D2251/504—Nitric acid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/50—Inorganic acids
- B01D2251/506—Sulfuric acid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/304—Hydrogen sulfide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/306—Organic sulfur compounds, e.g. mercaptans
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
Se describe un procedimiento para producir ácido sulfurico concentrado en una fase líquida a partir de una fuente de dioxido de azufre; el procedimiento comprende convertir la fuente de dioxido de azufre de ácido sulfurico; la fase líquida comprende: ácido nítrico a una concentracion suficiente para comenzar la conversion de dioxido de azufre en ácido sulfurico en presencia de oxígeno y en ausencia inicial de ácido sulfurico; ácido nítrico a una concentracion suficiente para mantener la conversion de dioxido de azufre en presencia deácido sulfurico, ya se generado por dicha conversion o presente al comienzo de dicha conversion; y concentracion combinada de ácido nítrico y ácido sulfurico que varía de 5M a 16M, en donde la concentracion de ácido nítrico es de por lo menos 5M en ausencia inicial de ácido sulfurico, y se introduce una fuente de oxígeno a la fase acuosa a una concentracion suficiente para proveer dicha conversion catalítica de SO2 y H2SO4.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US41095795A | 1995-03-27 | 1995-03-27 | |
US410957 | 1995-03-27 |
Publications (2)
Publication Number | Publication Date |
---|---|
MX9707397A true MX9707397A (es) | 1998-06-28 |
MXPA97007397A MXPA97007397A (es) | 1998-10-30 |
Family
ID=
Also Published As
Publication number | Publication date |
---|---|
CZ302997A3 (cs) | 1998-05-13 |
AU704392B2 (en) | 1999-04-22 |
EP0839117A2 (en) | 1998-05-06 |
KR19980703355A (ko) | 1998-10-15 |
PL322447A1 (en) | 1998-02-02 |
AU5140696A (en) | 1996-10-23 |
WO1996031262A3 (en) | 1996-12-12 |
JPH11503105A (ja) | 1999-03-23 |
CA2216432A1 (en) | 1996-10-10 |
BR9607990A (pt) | 2000-04-18 |
CA2216432C (en) | 2003-12-02 |
WO1996031262A2 (en) | 1996-10-10 |
US5788949A (en) | 1998-08-04 |
NO974468D0 (no) | 1997-09-26 |
NO974468L (no) | 1997-11-26 |
CN1181743A (zh) | 1998-05-13 |
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