Method and system of thermal recovery relating to the operation of a dissolver of a chemical recovery boiler

• US 10,487,449 B2
• Filed: 12/11/2017
• Issued: 11/26/2019
• Est. Priority Date: 01/20/2017
• Status: Active Grant

• Current Assignee: Valmet Technologies OY (Valmet Oyj)
• Original Assignee: Valmet Technologies OY (Valmet Oyj)
• Inventors: Mansikkasalo, Jarmo
• Primary Examiner(s): Calandra, Anthony
• Assistant Examiner(s): Vera, Elisa
• Application Number:
  US15/837,486
• Publication Number:
  US 20180209095A1
• Time in Patent Office: 715 Days
• CPC Class Codes: D21C 11/0064 Aspects concerning the production and the treatment of green and white liquors, e.g. causticizing green liquor
• CPC Class Codes: D21C 11/12 Combustion of pulp liquors
• CPC Class Codes: D21C 11/122 Treatment, e.g. dissolution, of the smelt
• 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

The disclosed solution relates to recovering thermal energy from the operation of a dissolver of a chemical recovery boiler used in pulp manufacturing. According to the solution, a primary fluid circuit conveys green liquor from the dissolver to an external process such as causticizing and solvent such as weak white liquor back to the dissolver, and from this circuit solvent is diverted into a secondary fluid passageway comprising a heat exchanger which cools the solvent by recovering heat from it and transfers the heat to a heat-consuming process. After heat recovery, solvent may be used for further processes before it is at least partly conveyed back to the dissolver.

Claims

1. A method of recovering heat from the operation of a dissolver of a chemical recovery boiler, the method comprising the steps of:

dissolving smelt in weak white liquor in the dissolver, resulting in green liquor;

conveying green liquor from the dissolver through a primary fluid circuit into an external process;

conveying weak white liquor from the external process through the primary fluid circuit to the dissolver;

diverting part of the weak white liquor from the primary fluid circuit into a secondary fluid passageway;

conveying weak white liquor via the secondary fluid passageway at least partly into the dissolver;

recovering heat from weak white liquor with a heat exchanger in the secondary fluid passageway and thereby cooling the weak white liquor diverted from the primary fluid circuit and running through the secondary fluid passageway; and

transferring heat with a transfer medium from the heat exchanger to a heat-consuming process,

wherein;

the primary fluid circuit comprises;

a first fluid passageway configured to alternate between i) conveying green liquor from the dissolver into the external process and ii) conveying weak white liquor from the external process to the dissolver; and

a second fluid passageway configured to alternate between i) conveying green liquor from the dissolver into the external process and ii) conveying weak white liquor from the external process to the dissolver,

in a first state of the primary fluid circuit the first fluid passageway is configured to convey green liquor from the dissolver into the external process while the second fluid passageway is conveying weak white liquor from the external process to the dissolver,

in a second state of the primary fluid circuit the second fluid passageway is configured to convey green liquor from the dissolver into the external process while the first fluid passageway is conveying weak white liquor from the external process to the dissolver, and

a valve arrangement is provided for connecting the primary fluid circuit to the secondary fluid passageway, the valve arrangement being configured to controllably divert weak white liquor from the primary fluid circuit to the secondary fluid passageway, the valve arrangement being further configured to alternate between i) diverting, in the second state, weak white liquor from the first fluid passageway of the primary fluid circuit to the secondary fluid passageway and ii) diverting, in the first state, weak white liquor from the second fluid passageway of the primary fluid circuit to the secondary fluid passageway.

2. The method according to claim 1, the method further comprising the step of conveying weak white liquor from the secondary fluid passageway to one or more of the following processes connected downstream from the heat exchanger:

a vent duct through which excess gases are expelled from the dissolver;

a smelt feed line via which smelt from the chemical recovery boiler is conveyed into the dissolver;

a solution-stirring agitator or agitators of the dissolver; and

a vent gas scrubber configured to scrub excess gases expelled from the dissolver.

3. The method according to claim 1, wherein the heat-consuming process is an air heating system of a chemical recovery boiler building.

4. The method according to claim 1, wherein the external process is causticizing.

5. The method according to claim 3, wherein the heat exchanger is configured to transfer heat to a circulating heat transfer medium circuit, and wherein the air heating system of a chemical recovery boiler building is configured to use the heat of the circulating heat transfer medium circuit to heat the air of the chemical recovery boiler building.

6. The method according to claim 1, wherein the dissolver is connected downstream from the heat exchanger in the direction of weak white liquor flow.