Patent US4590049A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4590049A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for dry desulfurization of exhaust gas

Assignee: Individual
•
Filing: 1984-08-14
•
Granted: 1986-05-20
•
Expires: 2004-08-14
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A method for desulfurizing exhaust gases such as flue gases from steam generators that have been charged with brown coal, in which powdered lime is charged into the furnace and then removed or precipitated from the flowing exhaust gases after a certain reaction time. The dust or particulate matter which has been removed from the flowing exhaust gas stream, and which is at least partially charged with noxious substances along the surfaces thereof, is pulverized and then subjected to dry stream hydration, followed by recycling into the flue gas stream which has been cooled to a lower temperature. During the dry steam treatment, the points of fracture or exposure of the pulverized particulate additive are activated so that Ca(OH) 2 formation takes place, which has a high affinity for sulfur dioxide at low temperature. An apparatus for pulverizing and hydrating the particulate matter is also provided.

Inventors

  • 👤 Gernot Staudinger

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 12:41
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; B01D53/501; C; C01; C01F; C01F11/00; C01F11/46; C01F11/464

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 182 words
Method for the desulfurization of ash-containing exhaust gas of a sulfur-containing coal in a coal burning, steam generating furnace, which comprises: charging the furnace with powdered limestone which during the burning of the coal is split into CaO particles and CO 2 , the CaO particles absorbing SO 2 resulting from the burning of the sulfur-containing coal and forming particles with CaSO 3 or CaSO 4 on at least the surfaces thereof; separating particulate matter, including CaO without and CaO with CaSO 3 or CaSO 4 on at least the surfaces thereof, from the exhaust gas; mechanically crushing the thus-separated particulate matter, whereby CaO of the particles becomes exposed; classifying the particulate matter into larger and smaller particles; subjecting the thus-separated and crushed particulate matter to dry steam which reacts with the exposed CaO to hydrate the same and convert the CaO into Ca(OH) 2 ; and recycling particles of the thus-obtained Ca(OH) 2 , CaSO 3 , and CaSO 4 to the exhaust gas at an exhaust gas temperature which has been cooled to substantially the outlet temperature of the gas.
Claim 2
Dependent Claim 182 words
Method for the desulfurization of ash-containing exhaust gas of a sulfur-containing coal in a coal burning, steam generating furnace, which comprises: charging the furnace with powdered limestone which during the burning of the coal is split into CaO particles and CO 2 , the CaO particles absorbing SO 2 resulting from the burning of the sulfur-containing coal and forming particles with CaSO 3 or CaSO 4 on at least the surfaces thereof; separating particulate matter, including CaO without and CaO with CaSO 3 or CaSO 4 on at least the surfaces thereof, from the exhaust gas; mechanically crushing the thus-separated particulate matter, whereby CaO of the particles becomes exposed; classifying the particulate matter into larger and smaller particles; subjecting the thus-separated and crushed particulate matter to dry steam which reacts with the exposed CaO to hydrate the same and convert the CaO into Ca(OH) 2 ; and recycling particles of the thus-obtained Ca(OH) 2 , CaSO 3 , and CaSO 4 to the exhaust gas at an exhaust gas temperature which has been cooled to substantially the outlet temperature of the gas.
Claim 3
Dependent Claim 39 words
The method of claim 1, wherein the particulate matter is classified by sifting the thus-separated and crushed particulate matter after the mechanical crushing thereof; and removing the particles of particulate matter retained on the sieve after the sifting thereof.
Claim 4
Dependent Claim 27 words
The method of claim 1, comprising subjecting the thus-separated and crushed particulate matter to dry steam hydration for a period of time from 2 to 24 hours.
Claim 5
Dependent Claim 25 words
The method of claim 3, comprising subjecting the thus-separated and crushed particulate matter to dry steam hydration at a pressure slightly greater than atmospheric pressure.
Claim 6
Dependent Claim 17 words
The method of claim 1, wherein the thus-obtained particles are recycled by application of dry steam thereto.
Claim 7
Dependent Claim 34 words
The method of claim 1, wherein the thus-separated particulate matter is mechanically crushed in a ball mill, and the thus-separated and crushed particulate matter is subjected to the dry steam hydration in a damper.
Claim 8
Dependent Claim 31 words
The method of claim 1, wherein the particles are recyeled to the exhaust gas downstream of the furnace and upstream of the separation of the particulate matter from the exhaust gas.
Claim 9
Dependent Claim 23 words
The method of claim 7, wherein the particles are recycled to the exhaust gas at an exhaust gas temperature below about 300° C.
Claim 10
Dependent Claim 189 words
Method for the desulfurization of ash ccontaining exhaust gas of a sulfur-containing coal in a coal burning, steam generating furnace, which comprises charging the furnace with powdered limestone which during the burning of the coal is split into CaO particles and CO 2 , the CaO particles absorbing SO 2 resulting from the burning of the sulfur-containing coal and forming particles with CaSO 3 or CaSO 4 on at least the surfaces thereof; separating particulate matter, including CaO without and CaO with CaSO 3 or CaSO 4 on at least the surfaces thereof, from the exhaust gas; crushing the thus-separated particulate matter, whereby CaO of the particles becomes exposed; subjecting the thus-separated and crushed particulate matter to dry steam which reacts with the exposed CaO to hydrate the same and convert the CaO to Ca(OH) 2; classifying the particulate matter into larger and smaller particles after subjecting the same to the dry steam hydration; and recycling particles of the thus-obtained Ca(OH) 2 , CaSO 3 and CaSO 4 to the exhaust gas at an exhaust gas temperature which has been cooled to substantially the outlet temperature of the gas.
Claim 11
Dependent Claim 189 words
Method for the desulfurization of ash ccontaining exhaust gas of a sulfur-containing coal in a coal burning, steam generating furnace, which comprises charging the furnace with powdered limestone which during the burning of the coal is split into CaO particles and CO 2 , the CaO particles absorbing SO 2 resulting from the burning of the sulfur-containing coal and forming particles with CaSO 3 or CaSO 4 on at least the surfaces thereof; separating particulate matter, including CaO without and CaO with CaSO 3 or CaSO 4 on at least the surfaces thereof, from the exhaust gas; crushing the thus-separated particulate matter, whereby CaO of the particles becomes exposed; subjecting the thus-separated and crushed particulate matter to dry steam which reacts with the exposed CaO to hydrate the same and convert the CaO to Ca(OH) 2; classifying the particulate matter into larger and smaller particles after subjecting the same to the dry steam hydration; and recycling particles of the thus-obtained Ca(OH) 2 , CaSO 3 and CaSO 4 to the exhaust gas at an exhaust gas temperature which has been cooled to substantially the outlet temperature of the gas.
Claim 12
Dependent Claim 42 words
The method of claim 9, wherein the thus-separated and crushed particulate matter is subjected to dry steam hydration in a base portion of a fluidized bed provided with at least one nozzle means for introducing the dry steam into the fluidized bed.
Claim 13
Dependent Claim 37 words
The method of claim 9, wherein the particulate matter is classified by sifting the thus-obtained particles after subjecting the same to the dry steam hydration; and removing the particles retained on the sieve after the sifting thereof.
Claim 14
Dependent Claim 17 words
The method of claim 11, wherein the thus-obtained particles are recycled by application of dry steam thereto.

References Cited (Backward Citations)

US3481289A Cited
US4185080A Cited
US4329324A Cited
US4387078A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-05-19 1989-11-18 1990-05-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-05-19 1993-11-18 1994-05-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-05-19 1997-11-18 1998-05-20 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag