GB687160A - Manufacture of sulphuric acid - Google Patents

Manufacture of sulphuric acid

Info

Publication number
GB687160A
GB687160A GB13623/50A GB1362350A GB687160A GB 687160 A GB687160 A GB 687160A GB 13623/50 A GB13623/50 A GB 13623/50A GB 1362350 A GB1362350 A GB 1362350A GB 687160 A GB687160 A GB 687160A
Authority
GB
United Kingdom
Prior art keywords
acid
sulphur trioxide
cooler
sulphuric
sulphuric acid
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
Application number
GB13623/50A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bayer AG
Original Assignee
Bayer AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Bayer AG filed Critical Bayer AG
Publication of GB687160A publication Critical patent/GB687160A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00Sulfur; Compounds thereof
    • C01B17/69Sulfur trioxide; Sulfuric acid
    • C01B17/74Preparation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Drying Of Gases (AREA)

Abstract

Sulphuric acid is produced by contacting a gas comprising sulphur trioxide with an aqueous fluid under such conditions that the resulting sulphuric acid reaches a temperature of at least 150 DEG C, the acid then being cooled by contact with air and the air after effecting cooling being contacted <PICT:0687160/III/1> with water or dilute sulphuric acid to effect heat and material exchange. The resulting heated dilute acid may be employed as the aqueous fluid which is contacted with the sulphur trioxide. In the Figure, sulphur trioxide enters an adsorber 2 at 1 and is washed with boiling sulphuric acid, the heat-concentrated acid then passing through pipe 3 to an air cooler 4. Air enters at 5 and after cooling the acid and entraining acid vapours, passes through pipe 6 to a heat and material-exchanger 10 irrigated partly by the acid pumped from the cooler 4 via line 9 and partly by dilute acid added to the system at 11. The cooled gases, freed from sulphur trioxide and acid vapours, are evacuated at 13 and may be recycled to the cooler 4 to avoid the introduction of water vapour to the cooler. Product acid is withdrawn at 8. The aqueous fluid used to absorb the sulphur trioxide may be diluted acid resulting from drying and heating gases with concentrated sulphuric acid, the absorbed water being partly reacted with the sulphuric trioxide and partly evaporated by the heat of the reaction, thereby reconcentrating the acid. Alternatively, the dilute acid supply may be that from a refrigeration device where water evaporated under low pressure is absorbed in concentrated sulphuric acid.
GB13623/50A 1949-05-31 1950-05-31 Manufacture of sulphuric acid Expired GB687160A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR687160X 1949-05-31

Publications (1)

Publication Number Publication Date
GB687160A true GB687160A (en) 1953-02-11

Family

ID=9025967

Family Applications (1)

Application Number Title Priority Date Filing Date
GB13623/50A Expired GB687160A (en) 1949-05-31 1950-05-31 Manufacture of sulphuric acid

Country Status (1)

Country Link
GB (1) GB687160A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4547353A (en) * 1984-01-27 1985-10-15 C-I-L Inc. Apparatus and processes for the concentration of sulphuric acid
US4576813A (en) * 1983-07-05 1986-03-18 Monsanto Company Heat recovery from concentrated sulfuric acid
US4670242A (en) * 1984-11-09 1987-06-02 Monsanto Company Heat recovery from concentrated sulfuric acid
EP0224340A1 (en) * 1985-11-21 1987-06-03 C-I-L Inc. Sulphur trioxide absorption tower and process

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4576813A (en) * 1983-07-05 1986-03-18 Monsanto Company Heat recovery from concentrated sulfuric acid
US4547353A (en) * 1984-01-27 1985-10-15 C-I-L Inc. Apparatus and processes for the concentration of sulphuric acid
US4670242A (en) * 1984-11-09 1987-06-02 Monsanto Company Heat recovery from concentrated sulfuric acid
EP0224340A1 (en) * 1985-11-21 1987-06-03 C-I-L Inc. Sulphur trioxide absorption tower and process

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