Method for recycling sulfur dioxide from sulfite pulping liquors

• US 5,096,540 A
• Filed: 04/06/1990
• Issued: 03/17/1992
• Est. Priority Date: 04/06/1990
• Status: Expired due to Fees

• Current Assignee: Jack C. Norman, Nancy J. Sell
• Original Assignee: Jack C. Norman, Nancy J. Sell
• Inventors: Sell, Nancy J., Norman, Jack C.
• Primary Examiner(s): Hastings, Karen M.
• Assistant Examiner(s): FRIEDMAN, CHARLES
• Application Number:
  US07/505,422
• Time in Patent Office: 711 Days
• Field of Search: 162/16, 162/36, 162/42, 162/45
• US Class Current: 162/16
• CPC Class Codes: D21C 11/0085 Introduction of auxiliary substances into the regenerating system in order to improve the performance of certain steps of the latter, the presence of these substances being confined to the regeneration cycle introduction of compounds in order to make up for the losses of pulping agents D21C11/0035; conventional causticizing of green liquors D21C11/0064; fractionating of spent liquors D21C11/0042
• CPC Class Codes: D21C 11/02 of acid, neutral or alkaline sulfite lye
• CPC Class Codes: D21C 11/10 Concentrating spent liquor by evaporation evaporators B01D

Abstract

Combined acidification and evaporative concentration of sulfite based chemical and sulfite based semichemical spent liquors expel massive amounts of gaseous sulfur dioxide and water vapor from the spent liquor.

The concentration of the expelled sulfur dioxide is sufficiently high so that the sulfur dioxide and water vapor can be recycled directly, without further separation, to produce fresh sulfite pulping liquor.

Claims

1. In a method for recycling sulfur dioxide from spent chemical and semi-chemical sulfite pulping liquor, the steps consisting of:

a. acidifying the spent liquor;

b. then evaporating the acidified spent liquor to expel sulfur dioxide and water vapor and;

c. collecting the expelled sulfur dioxide and water vapor for recycling as pulping liquor.

2. In a method for recycling sulfur dioxide from spent chemical and semichemical sulfite pulping liquor, the steps consisting of:

a. acidifying the spent liquor by adding a minimum of 0.024 mmol hydrogen ion per mg total sulfur content of the untreated spent liquor to a maximum of 0.75 mmol hydrogen ion per mg total sulfur content of the untreated spent liquor;

then evaporating the acidified spent liquor at or near the boiling point of the spent liquor to a minimum of 5% moisture by weight of the spent liquor;

c. collecting the sulfur dioxide and water vapor expelled from the acidified and evaporated spent liquor for recycling as pulping liquor.

3. In a method for recycling sulfur dioxide from spent chemical and semichemical sulfite pulping liquor the steps consisting of:

a. acidifying the spent liquor by adding a minimum of 0.024 mmol hydrogen ion per mg total sulfur content of the untreated spent liquor to a maximum of 0.75 mmol hydrogen ion per mg total sulfur content of the untreated spent liquor;

b. then evaporating the acidified spent liquor at or near the boiling point of the spent liquor to a minimum of 5% moisture by weight, to a maximum of 50% moisture by weight of the spent liquor;

c. collecting the sulfur dioxide and water vapor expelled from the acidifed and evaporated spent liquor for recycling as pulping liquor.