Method for controlling a recovery boiler
US-2018363900-A1 · Dec 20, 2018 · US
US11512428B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11512428-B2 |
| Application number | US-201916374463-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 3, 2019 |
| Priority date | Apr 4, 2018 |
| Publication date | Nov 29, 2022 |
| Grant date | Nov 29, 2022 |
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Various techniques are described for enhanced combustion of hot water extraction (HWE) derived liquor. For example, the HWE derived liquor can be pre-treated prior to introduction into a combustion chamber. The pre-treatment can include subjecting HWE derived liquor to filtration to remove suspended solids, evaporation to produce a first stage concentrated HWE liquor; additional concentration to produce a second stage concentrated HWE liquor; additional filtration to remove additional suspended solids; and pre-heating to produce a preheated HWE liquor. The preheated HWE liquor can be atomized and combined with pre-heated combustion air supplied into a combustion chamber to effect combustion of the HWE derived liquor.
Opening claim text (preview).
The invention claimed is: 1. A process for combusting hot water extraction (HWE) derived liquor, comprising: subjecting HWE derived liquor to filtration to remove suspended solids and produce a solids-depleted HWE derived liquor; supplying the solids-depleted HWE derived liquor to an evaporator system to produce a first stage concentrated HWE derived liquor; supplying the first stage concentrated HWE derived liquor to a concentrator or evaporator to produce a second stage concentrated HWE derived liquor; subjecting the second stage concentrated HWE derived liquor to additional filtration to remove additional suspended solids and produce a filtered concentrated HWE derived liquor; pre-heating the filtered concentrated HWE derived liquor to produce a preheated HWE derived liquor; subjecting the preheated HWE derived liquor to atomization to produce an atomized HWE derived liquor; pre-heating air to produce heated combustion air; and supplying the atomized HWE derived liquor and the heated combustion air into a combustion chamber to effect combustion of the HWE derived liquor. 2. The process of claim 1 , wherein the filtration and/or the additional filtration is performed using a strainer type separator, a basket separator, a belt filter and/or a drum filter. 3. The process of claim 1 , wherein the atomization is performed by injecting pressurized air, steam and/or a light hydrocarbon into the pre-heated HWE derived liquor. 4. The process of claim 1 , wherein the pre-heating of the filtered concentrated HWE derived liquor is performed in at least one indirect heat exchanger that receives a heating fluid. 5. The process of claim 4 , wherein the heating fluid is steam or hot flue gas. 6. The process of claim 1 , wherein the pre-heating of the filtered concentrated HWE derived liquor is performed in an electric pre-heater. 7. The process of claim 1 , further comprising adding a co-combustion fuel into the combustion chamber. 8. The process of claim 7 , wherein the co-combustion fuel is added to the HWE derived liquor prior to introduction into the combustion chamber, or wherein the co-combustion fuel is added into the combustion chamber simultaneously and into a same inlet as the HWE derived liquor. 9. The process of claim 7 , wherein the co-combustion fuel comprises propane or natural gas. 10. The process of claim 7 , wherein the co-combustion fuel is added to the combustion chamber at an independent entry point compared to that of the HWE derived liquor. 11. The process of claim 10 , wherein the co-combustion fuel comprises wood residues. 12. The process of claim 1 , wherein the HWE derived liquor has an initial concentration of dissolved solids between 2 wt % and 10 wt %. 13. The process of claim 12 , wherein the evaporator system is operated so that the first stage concentrated HWE derived liquor has a concentration of dissolved solids between 25 wt % and 35 wt %, and the concentrator or evaporator is operated so that the second stage concentrated HWE derived liquor has a concentration of dissolved solids of at least about 45 wt %. 14. The process of claim 13 , wherein the second stage concentrated HWE derived liquor has a concentration of dissolved solids of at least about 55 wt %. 15. The process of claim 1 , wherein the preheating is performed so that the preheated HWE derived liquor has a temperature above about 55° C., or has a temperature up to but below a boiling point of the HWE derived liquor at operating pressures upstream of combustion. 16. A process for combusting hot water extraction (HWE) derived liquor, comprising: producing HWE derived liquor by: subjecting wood material to HWE to produce a mixture comprising fibres, water, dissolved solids and suspended solids; separating the mixture into a fibre-enriched stream and a fibre-depleted stream; filtering the fibre-depleted stream to produce the HWE derived liquor having a dissolved solids concentration of about 2 wt % to about 10 wt %; concentrating the HWE derived liquor to produce a concentrated HWE liquor having a dissolved solids concentration of at least 45 wt %; and supplying the HWE derived liquor and air into a combustion chamber to effect combustion of the HWE derived liquor. 17. The process of claim 16 , wherein the concentrating is performed in an evaporator system; and wherein the process further comprises filtering the concentrated HWE liquor to remove additional suspended solids therefrom and pre-heating the concentrated HWE derived liquor to produce a preheated HWE derived liquor prior to combustion, and subjecting the pre-heated HWE derived liquor to atomization to produce an atomized HWE derived liquor that combusted. 18. A process for combusting hot water extraction (HWE) derived liquor, comprising: filtering suspended solids from the HWE derived liquor; concentrating the HWE derived liquor to increase dissolved solids concentration therein; pre-heating the HWE derived liquor to a temperature above about 55° C.; and atomizing the HWE derived liquor during introduction into a combustion chamber. 19. A process for producing paperboard, comprising: subjecting biomass to a hot water extraction (HWE) operation to produce a slurry that comprises pulp and an HWE liquor; separating the pulp from the HWE liquor to produce a pulp-depleted HWE liquor; subjecting the pulp to pulp processing to produce a paperboard product; subjecting the pulp-depleted HWE liquor to a pre-treatment prior to combustion to produce energy, the pre-treatment comprising solids removal, concentration, and pre-heating; and utilizing at least some of the energy in the pulp processing, the HWE operation or a combination thereof. 20. The process of claim 19 , wherein the pre-treatment of the pulp-depleted HWE liquor comprises the steps as follows: separating the pulp-depleted HWE liquor into a fibre-enriched stream and a fibre-depleted stream; filtering the fibre-depleted stream to produce a filtered HWE derived liquor having a dissolved solids concentration of about 2 wt % to about 10 wt %; and concentrating the filtered HWE derived liquor to produce a concentrated HWE liquor having a dissolved solids concentration of at least 45 wt %. 21. The process of claim 19 , wherein the pulp-depleted HWE liquor is co-combusted with wood residues during combustion thereof to produce the energy.
Concentrating spent liquor by evaporation (evaporators B01D) · CPC title
Combustion of pulp liquors · CPC title
of waste liquors, e.g. sulfite liquors · CPC title
Preheating processes other than drying or pyrolysis · CPC title
Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for (volatile compounds obtained by decomposition of spent liquors in order to regenerate them D21C11/125; compounds obtained by fractionating the liquors in order to regenerate them D21C11/0042) · CPC title
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