GB676606A - Process for the purification of spent sulphuric acid - Google Patents

Process for the purification of spent sulphuric acid

Info

Publication number
GB676606A
GB676606A GB397451A GB397451A GB676606A GB 676606 A GB676606 A GB 676606A GB 397451 A GB397451 A GB 397451A GB 397451 A GB397451 A GB 397451A GB 676606 A GB676606 A GB 676606A
Authority
GB
United Kingdom
Prior art keywords
acid
sludge
per cent
sulphuric acid
alkyl
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
GB397451A
Inventor
George Charles Eltenton
William Alfred John Preece
Stanley Hope
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.)
Shell Refining and Marketing Co Ltd
Original Assignee
Shell Refining and Marketing Co Ltd
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 Shell Refining and Marketing Co Ltd filed Critical Shell Refining and Marketing Co Ltd
Priority to GB397451A priority Critical patent/GB676606A/en
Publication of GB676606A publication Critical patent/GB676606A/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
    • C01B17/90Separation; Purification
    • C01B17/92Recovery from acid tar or the like, e.g. alkylation acids
    • C01B17/925Recovery from acid tar or the like, e.g. alkylation acids by processes involving a liquid-liquid extraction

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Carbon and carbonaceous material are removed from spent sulphuric acid, e.g. that derived from a process for producttion of alcohols from olefins, by mixing with not more than 15 per cent by weight of a water-soluble anionic surface-active agent, blowing a non-reactive gas, e.g. air, nitrogen, carbon dioxide, or furnace gases, through the resulting mixture, allowing the acid to settle and separating the lower layer of cleaned acid from the upper layer of carbonaceous sludge. Surface-active agents, usually present to about 0.2 per cent by weight, may be longchain alkyl acid esters of inorganic oxygen-containing polybasic acids, particularly secondary alkyl acid esters of sulphuric acid described in Specifications 459,078, 459,079, 459,080, and 459,117, [all in Group IV], or salts therof, alkyl aryl sulphonic acids or salts thereof such as dodecyl cumene and dodecyl benzene sulphonic acids, sulphonic acids or salts thereof, produced in the treatment of hydrocarbon oils with sulphuric acid or oleum, soaps such as alkalic metal stearates, oleates, or naphthenates, and sulphonated fatty acids, fatty acid esters and glycerides. About 1 per cent of an oleophilic organic liquid, e.g. liquid hydrocarbons such as a spindle oil or aromatic extract from refining mineral lubricating oils, an alcohol or ester, by-product polymers which separate on diluting or neutralizing alkyl sulphuric acid ester crude products, residues from distillation of methyl-isobutyl ketone, diisobutyl ketone, hexylene glycol, mesityl oxide, and amyl and higher alcohols, may be added to coalesce the carbon particles. The acid should be of strength 45-50 per cent by weight and treatment temperatures up to 100 DEG C may be used. Sludge from previous batches may be added to subsequent batches or in a continuous process some sludge may be recycled. Before the sludge is discarded it is diluted with water, allowed to settle, and cleaned diluted acid separated which is either used to dilute spent acid to the required strength or passed to a concentrator.
GB397451A 1951-02-19 1951-02-19 Process for the purification of spent sulphuric acid Expired GB676606A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB397451A GB676606A (en) 1951-02-19 1951-02-19 Process for the purification of spent sulphuric acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB397451A GB676606A (en) 1951-02-19 1951-02-19 Process for the purification of spent sulphuric acid

Publications (1)

Publication Number Publication Date
GB676606A true GB676606A (en) 1952-07-30

Family

ID=9768414

Family Applications (1)

Application Number Title Priority Date Filing Date
GB397451A Expired GB676606A (en) 1951-02-19 1951-02-19 Process for the purification of spent sulphuric acid

Country Status (1)

Country Link
GB (1) GB676606A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1129141B (en) * 1958-06-13 1962-05-10 Shell Int Research Process for the purification of dilute sulfuric acid from acid sludge
US4194952A (en) * 1976-12-11 1980-03-25 Hoechst Aktiengesellschaft Process for regenerating waste sulfuric acid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1129141B (en) * 1958-06-13 1962-05-10 Shell Int Research Process for the purification of dilute sulfuric acid from acid sludge
US4194952A (en) * 1976-12-11 1980-03-25 Hoechst Aktiengesellschaft Process for regenerating waste sulfuric acid

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