Recovery of heat and chemical values from spent pulping liquors

• US 4,526,760 A
• Filed: 02/16/1984
• Issued: 07/02/1985
• Est. Priority Date: 07/21/1982
• Status: Expired due to Term

• Current Assignee: International Paper Company
• Original Assignee: International Paper Company
• Inventors: Empie, Howard L. Jr.
• Primary Examiner(s): Smith, William
• Assistant Examiner(s): Hastings, K. M.
• Application Number:
  US06/580,918
• Time in Patent Office: 502 Days
• Field of Search: 162/30.1, 162/30.11, 423/207, 423/DIG. 3, 110/346, 110/210, 422/185
• US Class Current: 422/185
• CPC Class Codes: D21C 11/066 Separation of solid compounds from these gases; further treatment of recovered products
• CPC Class Codes: D21C 11/12 Combustion of pulp liquors
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

An integrated apparatus and process for recovery of heat and chemical values from spent pulping liquors are disclosed. Novel means for recovering heat values and residual entrained solids from the combustion gases are provided.

Claims

1. An integrated apparatus for the recovery of energy and chemical values from spent pulping liquors comprising:

(a) an initial fluidized bed reaction chamber provided with means for combusting concentrated spent pulping liquor with air and a plurality of solid particulate materials, at least one of which is of finer particle size than another;

(b) means for separating the finer particle size inert particulate material from the gaseous and solid combustion products communicating with the top portion of said initial fluidized bed reaction chamber;

(c) a fluidized bed heat exchanger means external to said initial fluidized bed reaction chamber communicating with said means for separating the finer particle size inert particulate material;

(d) means for returning separated finer particle size inert particulate material to the initial fluidized bed reaction chamber communicating with the fluidized bed heat exchanger means;

(e) oxidation reactor means for further combusting said gaseous combustion products at a temperature greater than the melting point of the solid combustion products;

(f) means for carrying gaseous and solid combustion products of the initial combustion step to the oxidation reactor means, said means for carrying gaseous and solid combustion products communicating with the means for separating finer particle size inert particulate material from the gaseous and solid combustion products;

(g) reducer means for reducing at least a portion of the solid combustion products by action of a reducing agent in a molten inorganic salt mass and recovering a smelt; and

(h) means for recovering and conveying to the reducer means, molten salts produced in the oxidation reactor means communicating with both the reducer means and the oxidation reactor means.

2. Apparatus as defined in claim 1 wherein means for introducing exhaust gases from the reduction of at least a portion of the solid combustion products into the means carrying gaseous and solid combustion products of the initial combustion step immediately prior to the reactor means for further combustion of said gaseous combustion products are provided.