Patent US3844879A successfully refreshed from Google Patents.
US3844879A
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System for removing sodium chloride contaminants from a magnesium base pulping process
Assignee: Babcock International Ltd
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Filing: 1972-10-30
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Granted: 1974-10-29
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Expires: 1992-10-30
Abstract
Abstract A chemical absorption system for removing hydrogen chloride from gases resulting from the combustion of magnesium base pulp residual liquor containing sodium chloride.
Inventors
- 👤 L Flais
- 👤 R Mcilroy
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 16:15
CPC Classifications
D; D21; D21C; D21C11/00; D21C11/06; D21C11/063; Y; Y10; Y10S; Y10S162/00; Y10S162/08; Y10S55/00; Y10S55/07
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
289 words
IN A CHEMICAL RECOVERY SYSTEM WHEREIN CELLULOSIC MATERIALS CONTAINING SODIUM CHLORIDE ARE PULPED IN A MAGNESIUM BASE COOKING LIQUID, AND THE RESIDUAL LIQUOR FROM THE PULPING PROCESS CONTAINS THE SODIUM CHLORIDE FROM THE CELLULOSIC MATERIALS, THE RESIDUAL LIQUOR IS CONCENTRATED BY EVAPORATION AND BURNED TO PRODUCE HOT FLUE GASES CONTAINING SULPHUR DIOXIDE AND HYDROGEN CHLORIDE AND ENTRAINED SOLIDS INCLUDING SODIUM SULPHATE AND MAGNESIUM OXIDE, THE STEP OF REMOVING ENTRAINED SOLIDS FROM THE GASES, TREATING THE SOLIDS TO FORM A SLURRY OF MAGNESIUM OXIDE AND TO DISCARD THE SODIUM SULPHATE, PASSING THE FLUE GASES THROUGH A SULPHUR DIOXIDE ABSORBING ZONE IN CONTACT WITH THE MAGNESIUM OXIDE CONTAINING SLURRY TO FORM MAGNESIUM SULPHUR COMPOUNDS, THE IMPROVED STEP OF WASHING THE FLUE GASES BEFORE THEY ARE PASSED TO THE SULPHUR DIOXIDE ABSORBING ZONE TO SELECTIVELY REMOVE THE HYDROGEN CHLORIDE GASES BY ABSORPTION IN A MAGNESIUM CONTAINING LIQUID, THE MAGNESIUM CONTAINING LIQUID BEING FORMED BY SOME OF THE ENTRAINED MAGNESIUM OXIDE SOLIDS PASSING WITH THE FLUE GASES TO THE HYDROGEN CHLORIDE WASHING STEP AND COMBINING WITH THE WASHING LIQUID TO FORM MAGNESIUM CHLORIDE AND SOME OF THE GASEOUS SULPHUR OXIDES COMBINES TO FORM A SOLUTION OF MAGNESIUM BISULPHITE IN THE LIQUID, RECIRCULATING A MAJOR PORTION OF THE LIQUID TO THE WASHING STEP TO ABSORB HYDROGEN CHLORIDE, DISCARDING A PORTION OF THE LIQUID, ADDING MAKE UP WATER TO CONTROL THE CONCENTRATION OF MAGNESIUM CHLORIDE AND MAGNESIUM BISULPHITE IN THE RECIRCULATED LIQUID, REMOVING SOME OF THE LIQUID FROM THE WASHING STEP TO BE REACTED WITH MAGNESIUM HYDROXIDE TO PRECIPITATE MAGNESIUM SULPHITE, THE REACTED LIQUID IS SEPARATED FROM THE PRECIPITATE WITH THE LIQUID RECYCLED TO THE WASHING STEP, AND THE PRECIPITATE SOLID MAGNESIUM SULPHITE SUBSEQUENTLY UTILIZED IN THE SULPHUR DIOXIDE ABSORBING STEP IN FORMING COOKING LIQUOR.
Claim 2
Dependent Claim
289 words
IN A CHEMICAL RECOVERY SYSTEM WHEREIN CELLULOSIC MATERIALS CONTAINING SODIUM CHLORIDE ARE PULPED IN A MAGNESIUM BASE COOKING LIQUID, AND THE RESIDUAL LIQUOR FROM THE PULPING PROCESS CONTAINS THE SODIUM CHLORIDE FROM THE CELLULOSIC MATERIALS, THE RESIDUAL LIQUOR IS CONCENTRATED BY EVAPORATION AND BURNED TO PRODUCE HOT FLUE GASES CONTAINING SULPHUR DIOXIDE AND HYDROGEN CHLORIDE AND ENTRAINED SOLIDS INCLUDING SODIUM SULPHATE AND MAGNESIUM OXIDE, THE STEP OF REMOVING ENTRAINED SOLIDS FROM THE GASES, TREATING THE SOLIDS TO FORM A SLURRY OF MAGNESIUM OXIDE AND TO DISCARD THE SODIUM SULPHATE, PASSING THE FLUE GASES THROUGH A SULPHUR DIOXIDE ABSORBING ZONE IN CONTACT WITH THE MAGNESIUM OXIDE CONTAINING SLURRY TO FORM MAGNESIUM SULPHUR COMPOUNDS, THE IMPROVED STEP OF WASHING THE FLUE GASES BEFORE THEY ARE PASSED TO THE SULPHUR DIOXIDE ABSORBING ZONE TO SELECTIVELY REMOVE THE HYDROGEN CHLORIDE GASES BY ABSORPTION IN A MAGNESIUM CONTAINING LIQUID, THE MAGNESIUM CONTAINING LIQUID BEING FORMED BY SOME OF THE ENTRAINED MAGNESIUM OXIDE SOLIDS PASSING WITH THE FLUE GASES TO THE HYDROGEN CHLORIDE WASHING STEP AND COMBINING WITH THE WASHING LIQUID TO FORM MAGNESIUM CHLORIDE AND SOME OF THE GASEOUS SULPHUR OXIDES COMBINES TO FORM A SOLUTION OF MAGNESIUM BISULPHITE IN THE LIQUID, RECIRCULATING A MAJOR PORTION OF THE LIQUID TO THE WASHING STEP TO ABSORB HYDROGEN CHLORIDE, DISCARDING A PORTION OF THE LIQUID, ADDING MAKE UP WATER TO CONTROL THE CONCENTRATION OF MAGNESIUM CHLORIDE AND MAGNESIUM BISULPHITE IN THE RECIRCULATED LIQUID, REMOVING SOME OF THE LIQUID FROM THE WASHING STEP TO BE REACTED WITH MAGNESIUM HYDROXIDE TO PRECIPITATE MAGNESIUM SULPHITE, THE REACTED LIQUID IS SEPARATED FROM THE PRECIPITATE WITH THE LIQUID RECYCLED TO THE WASHING STEP, AND THE PRECIPITATE SOLID MAGNESIUM SULPHITE SUBSEQUENTLY UTILIZED IN THE SULPHUR DIOXIDE ABSORBING STEP IN FORMING COOKING LIQUOR.
Claim 3
Dependent Claim
189 words
In a chemical recovery system wherein cellulosic materials containing sodium chloride are pulped in a magnesium base cooking liquor, and the residual liquor from the pulping process contains the sodium chloride from the cellulosic materials, the residual liquor is concentrated by evaporation and burned to produce hot flue gases containing sulphur dioxide and hydrogen chloride and entrained solids including sodium sulphate and magnesium oxide, the step of removing over 97 percent of the entrained solids from the gases, treating the solids to form a slurry of magnesium oxide and to discard the sodium sulphate, passing the flue gases through a sulphur dioxide absorbing zone in contact with a magnesium oxide containing slurry to form magnesium sulphur compounds, the improved step of washing the flue gases before they are passed to the sulphur dioxide absorbing zone to remove the hydrogen chloride gases by absorption in a magnesium chloride liquid, recycling the liquid containing magnesium chloride and regulating the rate Of discard of magnesium chloride from the washing step to control the pH of the recirculated liquid to improve hydrogen chloride absorption and minimize SO2 absorption in the liquid washing step.
Claim 4
Dependent Claim
189 words
In a chemical recovery system wherein cellulosic materials containing sodium chloride are pulped in a magnesium base cooking liquor, and the residual liquor from the pulping process contains the sodium chloride from the cellulosic materials, the residual liquor is concentrated by evaporation and burned to produce hot flue gases containing sulphur dioxide and hydrogen chloride and entrained solids including sodium sulphate and magnesium oxide, the step of removing over 97 percent of the entrained solids from the gases, treating the solids to form a slurry of magnesium oxide and to discard the sodium sulphate, passing the flue gases through a sulphur dioxide absorbing zone in contact with a magnesium oxide containing slurry to form magnesium sulphur compounds, the improved step of washing the flue gases before they are passed to the sulphur dioxide absorbing zone to remove the hydrogen chloride gases by absorption in a magnesium chloride liquid, recycling the liquid containing magnesium chloride and regulating the rate Of discard of magnesium chloride from the washing step to control the pH of the recirculated liquid to improve hydrogen chloride absorption and minimize SO2 absorption in the liquid washing step.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1977-10-28 | 1978-04-29 | 1978-10-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1981-10-28 | 1982-04-29 | 1982-10-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1985-10-28 | 1986-04-29 | 1986-10-29 | $7700.00 | Window Closed / Lapsed |