GB1568929A – Treating facility for sintering waste gas
– Google Patents
GB1568929A – Treating facility for sintering waste gas
– Google Patents
Treating facility for sintering waste gas
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Publication number
GB1568929A
GB1568929A
GB9916/78A
GB991678A
GB1568929A
GB 1568929 A
GB1568929 A
GB 1568929A
GB 9916/78 A
GB9916/78 A
GB 9916/78A
GB 991678 A
GB991678 A
GB 991678A
GB 1568929 A
GB1568929 A
GB 1568929A
Authority
GB
United Kingdom
Prior art keywords
waste gas
pressure
gas
main blower
heat exchanger
Prior art date
1977-03-29
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB9916/78A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Engineering Corp
Original Assignee
Nippon Kokan Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
1977-03-29
Filing date
1978-03-13
Publication date
1980-06-11
1978-03-13
Application filed by Nippon Kokan Ltd
filed
Critical
Nippon Kokan Ltd
1980-06-11
Publication of GB1568929A
publication
Critical
patent/GB1568929A/en
Status
Expired
legal-status
Critical
Current
Links
Espacenet
Global Dossier
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Classifications
F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
F23J15/00—Arrangements of devices for treating smoke or fumes
F23J15/006—Layout of treatment plant
B—PERFORMING OPERATIONS; TRANSPORTING
B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
B01D—SEPARATION
B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
B—PERFORMING OPERATIONS; TRANSPORTING
B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
B01D—SEPARATION
B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
B01D53/34—Chemical or biological purification of waste gases
B—PERFORMING OPERATIONS; TRANSPORTING
B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
B01D—SEPARATION
B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
B01D53/34—Chemical or biological purification of waste gases
B01D53/46—Removing components of defined structure
B01D53/48—Sulfur compounds
Description
PATENT SPECIFICATION
( 11) 1 568 929 ( 21) Application No 9916/78 ( 22) Filed 13 March 1978 ( 19) ( 31) Convention Application No.
52/033969 ( 32) Filed 29 March 1977 in ( 33) Japan (JP) ( 44) Complete Specification published 11 June 1980 11 ( 51) INT CL 3 BO 1 J 19/00 ( 52) Index at acceptance Bl W AX ( 54) A TREATING FACILITY FOR SINTERING WASTE GAS ( 71) We, NIPPON KOKAN KABUSHIKI KAISHA, a corporation organised and existing under the laws of Japan, of No 1-2, 2-chome, Marunouchi, Chiyoda-ku, Tokyo, Japan, do hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement: The invention relates to an improved purifying apparatus for waste gas exhausted from a sintering furnace.
The sintering process is widely employed as a pre-treatment for ores This process burns raw materials in a sintering furnace, whose exhaust vents are connected to a main duct, exhaust gases being sucked from the exhaust vents by a main blower provided in the main duct In general, these gases exhausted through the main duct, bear much dust which is removed by an electrostatic dust precipitator installed upstream of the main blower More recently, demands have been raised for regulation of air pollution caused by N Os and SO contained in the waste gas Therefore, it has been necessary to provide a desulfurizing means, or a means for removing nitrogen oxide, in a subsequent line downstream of the main blower for purifying the total amount of the waste gas Consequently, several means for the treatment of the waste gas to reduce air pollution have been practised, but there still remain some apprehensions for the safety of the apparatus.
For example, when the pressure loss of the waste gas suddenly drops for any cause on the sucking side of the main blower, there will be a very high pressure on the opposite exhaust side, and if this pressure is too great, there may be damage to the purifying means and the other facilities e g the desulfurizing means arranged in the subsequent line.
Similarly, in a system provided with a compressor if the pressure of the waste gas suddenly drops for any reason on ths suction side of the compressor, the purify 50 ing device and other incidental facilities will experience a high negative pressure, and they will possibly be broken Such accidents may also happen through imbalance of opening angles of the respective 55 suction dampers at start up of the main blower and the compressor.
Apart from damage caused to the apparatus by abnormal pressure, there is also the danger of damage by waste gas of 60 abnormally high temperature flowing through the apparatus For instance, the desulfurizing means will often have a reinforcing plastics lining on an inner surface of the steel plate from which it is made 65 Therefore, for example, if a cooling liquid pump for SO, absorption in the desulfurizing means should stop, the high temperature waste gas from the main blower may pass into the desulfurizing equipment and 70 other subsequent apparatus, and the lining material may be damaged with resulting failure of the installed machinery Such dangers would probably result from stoppage of the electric current supplied to the 75 apparatus If this happens, the cooling liquid pump will instantly stop, but the main blower will continue to rotate because of its inertia, and therefore the high temperature waste gas will pass directly 80 into the desulfurizing apparatus from the main blower, to create the same danger as mentioned above.
The present invention provides a treating apparatus for waste gas from a sin 85 tering furnace which comprises a gaspurifying line connecting a main blower downstream of a dust collector for the waste gas from a sintering furnace, and downstream of the main blower, a heat ex 90 x 1 Ch 00 \ O in 1 568 929 changer for inderect heat exchange between unpurified high temperature waste gas and purified low temperature waste gas, followed in succession by a waste gas purifying device, and electrostatic dust precipitator and a compressor, wherein a pressure-adjusting valve is provided in a duct leading from the gas-purifying line downstream of the main blower.
This invention will be further described with reference to the accompanying Drawing which shows a flow sheet of one embodiment of an apparatus for purifying waste gas from a sintering furnace according to the invention.
In the Drawing, reference numeral 1 indicates a sintering furnace, 2 indicates a main electrostatic dust precipitator, 3 indicates a main blower, and 13 indicates a main duct Waste gas from the sintering furnace 1 is drawn through the main electrostatic dust precipiator 2 by the main blower 3 via the main duct 13 to remove the dust The waste gas from the blower 3 is sent subsequently into a heat exchanger 5 It is preferred to arrange a silencer 4 before the heat exchanger to reduce noise.
The heat exchanger 5 can be for example a metallic rotary exchanger, e g a Jungstrom heat exchanger For example, the high temperature waste gas from blower 3 passes into a semi-circular side of the metallic rotary element, and the low temperature gas is passed into another half side thereof for indirect heat exchange.
The low temperature waste gas will have been purified as mentioned later.
According to the invention, a waste gas purifying device, e g a wet desulfurizing apparatus 6, follows the heat exchanger 5.
The actual structure of the wet desulfurizing apparatus 6 need not to be especially discussed Since it is well known and conventional The wet desulfurizing apparatus 6 may be replaced by another desulfurizing apparatus, a denitrifying apparatus or other purifying device.
The waste gas from the wet desulfurizing apparatus 6 will generally contain a mist of ammonium sulfate, ammonium sulfite, or other salts, and therefore according to the invention, the wet desulfurizing apparatus 6 is followed by a wet electrostatic dust precipitator 7 to remove the mist A compressor 8 is positioned after the wet electrostatic dust precipitator 7 in order to overcome the pressure loss of the waste gas as it flows through the heat exchanger 5, the desulfurizing apparatus 6 and the wet electrostatic dust precipitator 7 The pressure of the waste gas is increased by the compressor 8 to drive it into the heat exchanger 5 The heat exchange takes place between unpurified high temperature waste gas and the desulfurized low temperature waste gas, and said low temperature waste gas will be heated to the desired temperature for exhausting it from a chimney 10 into the atmosphere The tem 70 perature of the waste gas to be exhausted from the chimney 10 should in general be at least 120 ‘C, to avoid air pollution.
Therefore, if the waste gas does not reach this temperature, it should be heated by 75 a re-heater 9 positioned before the chimney 10.
A characteristic feature of the invention is the provision of a pressure-adjusting valve 11 in the duct 13 at the exhaust side 8 G of the main blower 3 This valve 11 is ordinarily closed during operation Now, if the pressure loss of the waste gas at the sucking side of the main blower 3 suddenly drops for any reason to create a pressure 85 exceeding the designed maximum pressure of the apparatus after the main blower 3, the pressure-adjusting valve 11 will open, and concurrently the inlet dampers of the main blower 3 and the compressor 8 will go close in order partially to exhaust the waste gas from the sintering furnace 1 directly into the atmosphere, or to lead it to the chimney 10 via a by-pass 16.
When starting the compressor 8 and in 95 creasing the opening angle of the damper, if the resistance before the main blower 3 is high, a negative pressure will be created by the sucking strength of the compressor 8 in the sucking tower and other 100 portions of the desulfurizing apparatus 6, which pressure may exceed the design limits (e g + 750 mm Aq) In this case, the pressure-adjusting valve 11 will open and concurrently if necessary the inlet 105 dampers of the main blower 3 and the compressor 8 will close, and air will be drawn in through the valve 11 For example, if the resistance at the head of the sintering furnace increases and the negative pressure 110 of the gas in the main duct 13 exceeds the determined value (e g up to -2000 mm Aq), the pressure-adjusting valve 11 will open and concurrently the inlet dampers of the main blower 3 and the compressor 115 8 will close for protecting the electrostatic dust precipitator, ducts and other portions of the apparatus If the pressure exceeds the predetermined limits for the main duct or the sucking tower of the desulfurizing 120 apparatus 6 though depending upon the above said means (e g the negative pressure of the main duct becomes -2200 mm Aq, or the pressure of the sucking tower reaches up to + 90 Omm Aq), then the 125 main blower 3 and the compressor 8 are stopped to protect the whole of the system.
Abnormal pressures of the waste gas are measured, according to the invention, by means of a pressure gauge 14 installed near 130 1 568 929 the heat exchanger 5 When the pressure gauge 14 detects an abnormal pressure, the pressure-adjusting valve 11 can be opened automatically or manually For automatic operation, for example, preselected values are set for the pressure in the main duct 13, the wet desulfurizing device 6 and other portions of the apparatus and when the pressure of the waste gas reaches these values the pressure valve 11 will open, and if necessary to the inlet dampers of the main blower 3 and the compressor 8 will be closed A control system for this purpose does not need special instruments, 7; 15 and conventional systems can be employed Therefore, details are omitted.
A preferred feature of the invention is the provision of an emergency cut-off valve 12 following the pressure-adjusting valve 11 in the duct 13 on the exhaust side of the main blower 3 This emergency cut-off valve 12 is always open when the apparatus is properly working If, however, the heat exchanger 5 and/or the cooling liquid pump of the desulfurizing apparatus 6 were to stop, the high temperature waste gas would be directly fed into the machinery installed in the subsequent line In order to prevent this happening, the main blower 3 and the compressor 8 can be stopped, and concurrently the emergency cut-off valve 12 can be closed to interrupt the flow of the high temperature waste gas into the following instruments, and concurrently the pressure-adjusting valve 11 can be opened to exhaust the gas into the atmosphere, directly from the valve or from the chimney 10 through the by-pass 16.
Abnormal temperatures can be measured by a thermometer 15 provided near the desulfurizing apparatus 6 When the thermometer 15 detects an abnormal temperature above a predetermined temperature (e.g if the temperature at the cooling parts of the desulfurizing apparatus rises to 700 C) the pressure-adjusting valve 11 and the emergency cut-off valve 12 can be operated automatically or manually For automatic operaion, the heat resistance, temperatures of the desulfurizing device 6 and the electrostatic dust precipitator 7 will determine the predetermined value, and if the temperature of the waste gas reaches to this value, the valve 11 and 12 will be opened or closed automatically or manually No special instruments are needed and conventional systems can be employed.
It should be noted that the attaching Drawing shows the pressure gauge 14 posi 60 tioned after the heat exchanger 5 and the thermometer 16 positioned after the wet desulfurizing device 6, but the present invention is not limited to these indicated positions, since these devices 14 and 16 65 may be placed before the heat exchanger 5.
From the above statement, the usefulness of the pressure-adjusting valve 11 and the emergency cut-off valve 12 will be ap 70 parent, since breakage of the instruments owing to abnormal pressure and temperature conditions may be exactly avoided, thus improving the safety of the operation.
Even if electric power were to fail over 75 the whole system, the high temperature gas will be prevented from flowing into the sucking tower by automatically opening the pressure-adjusting valve and automatically closing the emergency cut-off valve 80
Claims (8)
WHAT WE CLAIM IS: –
1 A treating apparatus for waste gas from a sintering furnace which comprises a gas-purifying line connecting a main blower downstream of a dust collector for 85 the waste gas from a sintering furnace, and downstream of the main blower, a heat exchanger for indirect heat exchange between unpurified high temperature waste gas and purified low temperature waste 90 gas, followed in succession by a waste gas purifying device, an electrostatic dust precipitator and a compressor, wherein a pressure-adjusting valve is provided in a duct leading from the gas-purifying line 95 downstream of the main blower.
2 An apparatus as claimed in claim 1 wherein a cut-off valve is provided downstream of the duct.
3 An apparatus as claimed in claim 1 100 or 2 which comprises a pressure-sensitive gauge in the gas purifying line for detecting abnormal pressures.
4 An apparatus as claimed in any preceding claim which comprises a thermo 105 meter in the gas purifying line for detecting temperature variations of the waste gas.
An apparatus as claimed in any of the preceding claims wherein the duct is a 110 1 568 929 by-pass leading from the pressure-adjusting valve to a chimney for exhausting the waste gas.
6 An apparatus as claimed in any of the preceding claims which comprises a re-heater before the chimney for further heating the waste gas which has been heated in the heat exchanger.
7 An apparatus as claimed in any of the preceding claims which comprises a silencer upstream of the heat exchanger.
8 An apparatus as claimed in claim 1 and substantally as hereinbefore described with reference to the accompanying Drawing.
MICHAEL BURNSIDE & PARTNERS, Chartered Patent Agents, Hancock House, 87 Vincent Square, London SW 1 P 2 PH.
Printed for Her Majesty’s Stationery Office by The Tweeddale Press Ltd, Berwick-upon-Tweed, 1980 Published at the Patent Office, 25 Southampton Buildings, London, WC 2 A l AY, from which copies may be obtained
GB9916/78A
1977-03-29
1978-03-13
Treating facility for sintering waste gas
Expired
GB1568929A
(en)
Applications Claiming Priority (1)
Application Number
Priority Date
Filing Date
Title
JP3396977A
JPS53119203A
(en)
1977-03-29
1977-03-29
Treating equipment for exhaust gas of sintering
Publications (1)
Publication Number
Publication Date
GB1568929A
true
GB1568929A
(en)
1980-06-11
Family
ID=12401305
Family Applications (1)
Application Number
Title
Priority Date
Filing Date
GB9916/78A
Expired
GB1568929A
(en)
1977-03-29
1978-03-13
Treating facility for sintering waste gas
Country Status (6)
Country
Link
US
(1)
US4187085A
(en)
JP
(1)
JPS53119203A
(en)
BE
(1)
BE864948A
(en)
DE
(1)
DE2813572C2
(en)
FR
(1)
FR2385983A1
(en)
GB
(1)
GB1568929A
(en)
Cited By (1)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
CN111701380A
(en)
*
2020-07-28
2020-09-25
贵溪三元金属有限公司
Flue gas dust removal equipment for reverberatory furnace
Families Citing this family (9)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
DE3111074A1
(en)
*
1981-03-20
1982-09-30
Metallgesellschaft Ag, 6000 Frankfurt
Steam-generating plant with an exhaust-gas purification apparatus
DE3236905C2
(en)
*
1982-10-06
1986-01-02
Gottfried Bischoff Bau kompl. Gasreinigungs- und Wasserrückkühlanlagen GmbH & Co KG, 4300 Essen
Process for desulphurization of flue gases and device for carrying out the process
DE3721451C1
(en)
*
1987-06-30
1988-12-08
Asea Brown Boveri
Process for operating a pyrolysis plant
CN102809208A
(en)
*
2012-07-18
2012-12-05
桐乡市辛普森热能设备有限公司
High-temperature waste gas afterheat recycling and peculiar smell treating equipment and method
CN104197730B
(en)
*
2014-09-05
2016-03-02
秦冶工程技术(北京)有限责任公司
A kind of sintered discharge gas waste heat recycling system and method
CN104923021B
(en)
*
2015-06-24
2017-06-16
武汉纺织大学
The purification method and its device of a kind of heat setting machine high temperature oil-containing waste gas
CN106801884A
(en)
*
2016-11-22
2017-06-06
浙江巨化热电有限公司
A kind of smoke comprehensive processing unit and its method
CN111203083B
(en)
*
2020-02-25
2021-05-07
钢铁研究总院
Sintering flue gas desulfurization and denitrification process
CN115301065A
(en)
*
2022-07-22
2022-11-08
圣戈班管道系统有限公司
Method for removing bypass by sintering SDA (Stratagene-sulfate-sodium) semi-dry desulfurization
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1911-03-15
1911-08-03
Heinrich Zschocke
Device for the purification and cooling of hot gases and gas mixtures
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1914-07-23
1920-02-03
Research Corp
Apparatus for electrical treatment of gases
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1953-03-19
1956-01-03
Grindle Corp
Cupola waste gas heat exchange and purifying system
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1953-11-12
1956-04-10
Sueddeutsche Kalkstickstoff
Apparatus for the removal of solid matter from gases
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1955-06-10
1959-03-10
Metallgesellschaft Ag
Separation of dust from sinter waste gas
US3377058A
(en)
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1965-09-21
1968-04-09
Ajem Lab Inc
Cupola furnace installations having a safety bypass
JPS517610B2
(en)
*
1972-09-09
1976-03-09
SE373114B
(en)
*
1973-05-02
1975-01-27
Boliden Ab
DE2631444A1
(en)
*
1975-08-12
1977-02-24
Lee Joseph Duvall
METHOD AND APPARATUS FOR THE REMOVAL AND RECOVERY OF SULFUR DIOXIDE FROM EXHAUST GASES
1977
1977-03-29
JP
JP3396977A
patent/JPS53119203A/en
active
Granted
1978
1978-03-03
US
US05/883,202
patent/US4187085A/en
not_active
Expired – Lifetime
1978-03-13
GB
GB9916/78A
patent/GB1568929A/en
not_active
Expired
1978-03-16
BE
BE2056765A
patent/BE864948A/en
not_active
IP Right Cessation
1978-03-28
FR
FR7808956A
patent/FR2385983A1/en
active
Granted
1978-03-29
DE
DE2813572A
patent/DE2813572C2/en
not_active
Expired
Cited By (1)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
CN111701380A
(en)
*
2020-07-28
2020-09-25
贵溪三元金属有限公司
Flue gas dust removal equipment for reverberatory furnace
Also Published As
Publication number
Publication date
DE2813572C2
(en)
1982-09-16
BE864948A
(en)
1978-07-17
US4187085A
(en)
1980-02-05
JPS53119203A
(en)
1978-10-18
FR2385983B1
(en)
1980-06-20
DE2813572A1
(en)
1978-10-05
FR2385983A1
(en)
1978-10-27
JPS5636758B2
(en)
1981-08-26
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Legal Events
Date
Code
Title
Description
1980-09-24
PS
Patent sealed [section 19, patents act 1949]
1993-11-10
PCNP
Patent ceased through non-payment of renewal fee
Effective date:
19930313
