Patent US4640205A successfully refreshed from Google Patents.
US4640205A
Expired / Lapsed
US
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Method of drying granular fuel in a fluidized bed combustion plant and a combustion plant with a drying device
Assignee: ABB Stal AB
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Filing: 1985-07-02
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Granted: 1987-02-03
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Expires: 2005-07-02
Abstract
Abstract The conveying properties of a particulate fuel during pneumatic transportation to a fluidized bed in a combustion plant, are improved by at least surface drying of the fuel. A calcium-containing bed material is withdrawn from the bed under such conditions that the bed material is calcined to form CaO. This withdrawn bed material is crushed and mixed with fuel, whereby the CaO absorbs water from the fuel in an exothermic reaction forming calcium hydroxide, Ca(OH) 2 , the released heat evaporating moisture from the fuel. The fuel particles will have reduced surface moisture which reduces the risk of clogging during pneumatic feeding of fuel to a combustion chamber. Due to the intimate contact between the fuel particles and the crushed bed material, the tendency towards reaction between sulfer in the fuel and the bed material increases.
Inventors
- 👤 Roine Brannstrom
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 16:58
CPC Classifications
F; F23; F23C; F23C10/00; F23C10/16; F23K; F23K1/00; F23K3/00; F23K3/02
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
204 words
A method of improving the pneumatic conveying properties of a particulate fuel fed to a pneumatically fluidized combustion bed in a combustion chamber, the fuel particles prior to feeding containing moisture and the fluidized combustion bed containing particulate bed material comprising calcium carbonate, said method comprising withdrawing a fluidized portion of said bed material directly from said pneumatically fluidized combustion bed in the combustion chamber, subjecting said withdrawn portion to calcining conditions to at least partially calcine said bed material to provide calcium oxide in said withdrawn portion, crushing said withdrawn bed material to expose said calcium oxide, mixing said crushed bed material with said fuel particles containing moisture to dry the particulate fuel by reacting said calcium oxide with said moisture at the surface of said fuel particles, contacting said mixture of crushed bed material and moist particulate fuel with a supply of drying gas to aid in the drying of said fuel, and supplying said mixture of crushed bed material and dried particulate fuel to the combustion chamber via a pneumatic conveying means, the drying provided by said crushed bed material and said drying gas reducing the moisture content of said particulate fuel sufficiently to prevent clogging of said pneumatic conveying means.
Claim 2
Independent Claim
204 words
A method of improving the pneumatic conveying properties of a particulate fuel fed to a pneumatically fluidized combustion bed in a combustion chamber, the fuel particles prior to feeding containing moisture and the fluidized combustion bed containing particulate bed material comprising calcium carbonate, said method comprising withdrawing a fluidized portion of said bed material directly from said pneumatically fluidized combustion bed in the combustion chamber, subjecting said withdrawn portion to calcining conditions to at least partially calcine said bed material to provide calcium oxide in said withdrawn portion, crushing said withdrawn bed material to expose said calcium oxide, mixing said crushed bed material with said fuel particles containing moisture to dry the particulate fuel by reacting said calcium oxide with said moisture at the surface of said fuel particles, contacting said mixture of crushed bed material and moist particulate fuel with a supply of drying gas to aid in the drying of said fuel, and supplying said mixture of crushed bed material and dried particulate fuel to the combustion chamber via a pneumatic conveying means, the drying provided by said crushed bed material and said drying gas reducing the moisture content of said particulate fuel sufficiently to prevent clogging of said pneumatic conveying means.
Claim 3
Dependent Claim
26 words
A method according to claim 1, in which the withdrawn bed material is passed through a zone with a low CO 2 content during said calcining.
Claim 4
Dependent Claim
24 words
A method according to claim 2, in which the temperature in the low CO 2 content zone is between 700° C. and 800° C.
Claim 5
Dependent Claim
32 words
A method according to claim 1, in which combustion air is fed into a discharge device for withdrawing said portion of the bed material to cool the bed material during its withdrawal.
Claim 6
Dependent Claim
53 words
A method according to claim 1, which further comprises drying said mixture of crushed bed material and fuel with a drying gas, and in which said particulate fuel is crushed coal and said crushed coal is mixed with finely crushed bed material in a rotary mixer which is transversed by said drying gas.
Claim 7
Dependent Claim
25 words
A method according to claim 1, in which at least 90% of the crushed bed material has a grain size of less than 0.1 mm.
Claim 8
Dependent Claim
25 words
A method according to claim 1, which further comprises drying said mixture of crushed bed material and fuel with exhaust gases from the combustion chamber.
Claim 9
Dependent Claim
31 words
A method according to claim 1, which further comprises drying said mixture of crushed bed material and fuel with transport gas from an ash discharge system connected to the combustion chamber.
Claim 10
Dependent Claim
25 words
A method according to claim 1, in which said withdrawn bed material and said particulate fuel are mixed and crushed together in a common mill.
Claim 11
Dependent Claim
24 words
A method according to claim 1, in which said calcining conditions are such tht substantially complete calcination of said withdrawn bed material is obtained.
Claim 12
Dependent Claim
41 words
A method according to claim 1, in which at least 90% of the crushed bed material has a grain size of less than 0.1 mm and substantially all of said particulate fuel has a grain size of less than 5 mm.
Claim 13
Independent Claim
204 words
An apparatus for improving the pneumatic conveying properties of a particulate fuel fed to a pneumatically fluidized combustion bed in a combustion chamber, the fuel particles prior to feeding containing moisture and the fluidized combustion bed containing particulate bed material comprising calcium carbonate, said apparatus comprising means for withdrawing a fluidized portion of said bed material directly from said pneumatically fluidized combustion bed in the combustion chamber, means for subjecting said withdrawn portion to calcining conditions to at least partially calcine said bed material to provide calcium oxide in said withdrawn portion, means for crushing said withdrawn bed material to expose said calcium oxide, mixing means for mixing said crushed material with said fuel particles containing moisture to dry the particulate fuel by reacting said calcium oxide with said moisture at the surface of said fuel particles, means for supplying a drying gas to said mixing means to aid in the drying of said particulate fuel, and pneumatic conveying means for supplying said mixture of crushed bed material and dried fuel to the combustion chamber, the drying provided by said crushed bed material and said drying gas reducing the moisture content of said particulate fuel sufficiently to prevent clogging of said pneumatic conveying means.
Claim 14
Independent Claim
204 words
An apparatus for improving the pneumatic conveying properties of a particulate fuel fed to a pneumatically fluidized combustion bed in a combustion chamber, the fuel particles prior to feeding containing moisture and the fluidized combustion bed containing particulate bed material comprising calcium carbonate, said apparatus comprising means for withdrawing a fluidized portion of said bed material directly from said pneumatically fluidized combustion bed in the combustion chamber, means for subjecting said withdrawn portion to calcining conditions to at least partially calcine said bed material to provide calcium oxide in said withdrawn portion, means for crushing said withdrawn bed material to expose said calcium oxide, mixing means for mixing said crushed material with said fuel particles containing moisture to dry the particulate fuel by reacting said calcium oxide with said moisture at the surface of said fuel particles, means for supplying a drying gas to said mixing means to aid in the drying of said particulate fuel, and pneumatic conveying means for supplying said mixture of crushed bed material and dried fuel to the combustion chamber, the drying provided by said crushed bed material and said drying gas reducing the moisture content of said particulate fuel sufficiently to prevent clogging of said pneumatic conveying means.
Claim 15
Dependent Claim
100 words
An appartus according to claim 12, in which said particulate fuel comprises a sulphur and moisture containing coal, in which said fluidized bed material comprises a sulphur absorbent particulate material comprising calcuim carbonate, and in which said apparatus further comprises means for generating calcining conditions for the sulphur absorbent material within a calcining portion of said combustion chamber below said combustion bed to provide calcium oxide in the sulfur absorbent material within said calcining portion of the combustion chamber, and means for supplying said calcined sulfur absorbent material from said calcining portion of the combustion chamber to said crushing means.
Claim 16
Dependent Claim
17 words
An apparatus according to claim 12, including means for mixing together crushed fuel and crushed bed material.
Claim 17
Dependent Claim
29 words
An apparatus according to claim 12, including means for mixing uncrushed fuel and uncrushed bed material and a crushing device for crushing the mixture of fuel and bed material.
Claim 18
Dependent Claim
23 words
An apparatus according to claim 12, further including an inclined, rotary cylinder which is supplied with coal, bed material and a drying gas.
References Cited (Backward Citations)
DE292541C
Cited
US2849968A
Cited
US3833943A
Cited
US4059060A
Cited
US4159682A
Cited
US4159682B1
Cited
US4153411A
Cited
US4270279A
Cited
US4274836A
Cited
US4476790A
Cited
US4361100A
Cited
US4387654A
Cited
US4421036A
Cited
SE434087B
Cited
US4397248A
Cited
US4411879A
Cited
US4355601A
Cited
US4411204A
Cited
US4416418A
Cited
US4446799A
Cited
WO1984000976A1
Cited
US4424766A
Cited
US4434726A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-02-02 | 1990-08-04 | 1991-02-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-02-02 | 1994-08-04 | 1995-02-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-02-02 | 1998-08-04 | 1999-02-03 | $7700.00 | Window Closed / Lapsed |