GB1267262A - - Google Patents
Info
- Publication number
- GB1267262A GB1267262A GB1267262DA GB1267262A GB 1267262 A GB1267262 A GB 1267262A GB 1267262D A GB1267262D A GB 1267262DA GB 1267262 A GB1267262 A GB 1267262A
- Authority
- GB
- United Kingdom
- Prior art keywords
- temperature
- sulphuric acid
- acid
- plate column
- condensation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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
- C01B17/74—Preparation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Treating Waste Gases (AREA)
Abstract
1,267,262. Manufacture of sulphuric acid. STICKSTOFFWERK PIESTERITZ VEB. 5 Jan., 1970, No. 456/70. Heading C1A. Sulphuric acid is manufactured by treating SO 3 containing gases with water vapour at a temperature above the dew point of sulphuric acid and condensing the sulphuric acid in a plate column down which cone. H 2 SO 4 is passed in counter-current flow to the gas mixture resulting in the formation of foam layers in which the condensation of sulphuric acid from the gas mixture takes place under conditions such that no formation of mists occurs and the condensation and absorption of H 2 SO 4 are optimized. The SO 3 containing gas is used at a temperature between 300‹ and 380‹ C., the water vapour as saturated or superheated steam at a temperature between 125‹ C. and the temperature of the SO 3 containing gas, and the temperature of the feed acid to the plate column is between 155‹ and 240‹ C. The optimum condensation and absorption conditions in the plate column are achieved by virtue of the large surface area of the foam layer which is produced therein. The feed acid concentration is between 94 and 98À3% and the temperature of the plate column is maintained by variation of the sprinkling density of the cooled circulated acid.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB45670 | 1970-01-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1267262A true GB1267262A (en) | 1972-03-15 |
Family
ID=9704665
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1267262D Expired GB1267262A (en) | 1970-01-05 | 1970-01-05 |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1267262A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2479172A1 (en) * | 1980-03-25 | 1981-10-02 | Haldor Topsoe As | PROCESS FOR PRODUCING SULFURIC ACID |
US4368183A (en) * | 1979-11-08 | 1983-01-11 | Metallgesellschaft Aktiengesellschaft | Process of producing concentrated sulfuric acid |
US5538707A (en) * | 1994-03-01 | 1996-07-23 | Monsanto Company | Acid concentration control in SO3 absorption |
-
1970
- 1970-01-05 GB GB1267262D patent/GB1267262A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4368183A (en) * | 1979-11-08 | 1983-01-11 | Metallgesellschaft Aktiengesellschaft | Process of producing concentrated sulfuric acid |
FR2479172A1 (en) * | 1980-03-25 | 1981-10-02 | Haldor Topsoe As | PROCESS FOR PRODUCING SULFURIC ACID |
US5538707A (en) * | 1994-03-01 | 1996-07-23 | Monsanto Company | Acid concentration control in SO3 absorption |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
CSNS | Application of which complete specification have been accepted and published, but patent is not sealed |