AU3160393A - Method to purify gases - Google Patents
Method to purify gasesInfo
- Publication number
- AU3160393A AU3160393A AU31603/93A AU3160393A AU3160393A AU 3160393 A AU3160393 A AU 3160393A AU 31603/93 A AU31603/93 A AU 31603/93A AU 3160393 A AU3160393 A AU 3160393A AU 3160393 A AU3160393 A AU 3160393A
- Authority
- AU
- Australia
- Prior art keywords
- collection
- electron beam
- sheets
- accordance
- field
- Prior art date
- 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.)
- Abandoned
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/0892—Electric or magnetic treatment, e.g. dissociation of noxious components
-
- 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
- B01D53/007—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 by irradiation
-
- 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
- B01D53/32—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 by electrical effects other than those provided for in group B01D61/00
-
- 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
- B01D53/60—Simultaneously removing sulfur oxides and nitrogen oxides
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Environmental & Geological Engineering (AREA)
- Biomedical Technology (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Treating Waste Gases (AREA)
- Electrostatic Separation (AREA)
- Separation By Low-Temperature Treatments (AREA)
Description
METHOD TO PURIFY GASES
The object of the invention is a method to purify gases, such as combustion gases, in which method oxides of nitrogen and sulphur are converted into solid particles by an electron beam coming from an electron source, with the aid of added alkaline.
The mostly used method to purify combustion gases these days is a method, in which an electric filter is used to remove the solid particles, and slaked lime, which binds to itself part of the sulphur oxide formed during the burning process, is fed into the furnace of the boiler. This slaked lime dust is then filtered off in the electric filter with all the other solid particles. Usually nitrogen oxides are not even attempted to be removed, but the burning process is designed such that the temperature is low all the time, which reduces the amount of nitrogen oxides produced. In principle the lowered temperature does not reduce the amount of heath produced, but, because power plants generally produce electricity, according to the theoretical Carnot's machine the efficiency of electricity production is reduced as the temperature difference used by the machine is reduced. The efficiency of the Carnot's machine is (T2 - i)/T2 (T2 > Tx), that is, the temperature of the boiler can not be lowered very much without a significant reduction in efficiency. Power plants have also been designed, in which the combustion gases would be in such a high temperature that they would already be so strongly ionized, that electricity could be formed directly from these charge carriers by separating them into collection surfaces of opposite charge with the aid of a magnetic field. Then, if there is nitrogen present, it certainly burns into oxide. By adding washing methods of combustion gases, of which wet washing is most general, to the above described primary purification methods, 80 % of sulphur can usually be removed. Even with these washing methods nitrogen oxides can not be removed
without expensive special chemicals. A great disadvantage of the wet washing methods is also a huge amount of dirty water which is usually cleaned and recycled.
Today electric filters are good in removing solid material sufficiently. Perhaps their greatest disadvantages are the duration age of the wires used in the corona discharge, and keeping the corona discharge voltage at the breakdown level.
The aim of the invention is to achieve a method to purify gases, which in addition to removing solid material also efficiently removes S02 and most of NO.
The aim of the invention is achieved by a method which is characterized in the claims.
In the method of this invention, particles in the gas, that have been charged by an electron beam, are guided to gather on a collection surface with the aid of an external electromagnetic field, and this collection surface is cleaned at desired time intervals. In this method dust-like lime or some similar material, which removes part of the sulphur oxides directly and, together with the moisture in the combustion gases or added water, neutralizes nitrogen acid and sulphuric acid formed in the electron beam of NO and S02 ( NO + electron-beam -> N02 + H20 -> HN03; S02 + electron-beam -> S03 + H20 -> H2S04 ) , is added into the furnace of the boiler. In addition to lime, also ammonium added into the combustion gases can act as a neutralizer. In other words, the electron beam converts the weakly reacting
•NO and S02 to effectively reacting nitrogen acid and sulphuric acid, which are neutralized with bases into salts that form solid particles. This is known technology, which has not yet been used, mainly because inexpensive, effective electron beam devices with a good efficiency have not been available. According to earlier methods, burned nitrogen and sulphur, after they have been converted into solid material.
have been removed with electric filters. In this invention the charge of the particles is exploited, because immediately after the electron beam all solid particles have been charged with a strong negative charge by the electron beam. With the charge and an external electromagnetic field the particles can be guided to wanted positions. The currents of the electron beams are very high, for example in a 100 MW power plant with electron energy of 330 keV, the electron beam current is 300 A. In a coal power plant of egual size, the current needed by the electric filter is (the amount of combustion gases per second : 200 m3) 100 m2/m3 0,1 mA = 2 A. That is, when calculated without the ionization effect the current in the electron beam is more than hundredfold. In other words, it can be shown that ionization is apparently much more effective in the electron beam than in the gas discharge, taking into account also the fact that the voltage in the electron beam is about five times higher than in the gas discharge. So the power put to the ionization in the electron beam device is about 1000 times greater when compared to the power in the electric filter based on gas discharge. This means that distances between the collection sheets can be longer and collection areas can be smaller.
In the following the invention is explained in more detail with reference to the appended drawings, where figure 1 presents one embodiment the method, and figure 2 presents another embodiment of the method.
In figure 1 the electron beam source 1 has been installed beside the combustion channel 9 in such a way that the electron beam 3 is injected by it into the gas flow 2 in the combustion channel 9. After going through the electron beam the gas is ionized and the previously mentioned reactions take place so that most of the nitrogen and sulphur oxides are converted into solid particles in the area 4, which particles are charged negatively by the electron beam. When
the gases have gone a little further, the negative particles are guided between the collection sheets 5 by the electro¬ magnetic field 8. In this embodiment the electromagnetic field is produced economically by an organ shaped like a ring. Between the collection sheets 5 there is a separate electric field 6 from one sheet to the other perpendicular to the gas flow. The electromagnetic field which acts as a collection field 6 forces the solid material into the surface of the other collection sheet 7, from where it is removed for example with a mechanical impact or with a fast electrical counter impulse.
In figure 2 , the charged particles are collected into successive collection sheets 5 with collection guidance electric fields 10, 11. The collection sheets are in a positive potential referred to the body. There is also a separate collection field 6 in the collection sheets. There can be two or more successive sets of collection sheets and the collection guidance electric field 11 can be controlled with separate controllers 12, which are in different potentials, and for example shaped like a ring. The collection sheets can also be in several layers, in which case each of them is charged to a higher potential than the previous one, or every other sheet is charged to a higher potential. The figures are schematic diagrams which can in reality of course be more complicated and for example in different positions for the removal of solid material.
The invention is not restricted to the presented embodiments, but it can be altered according to the claims and applied also to purify other than combustion gases.
Claims (5)
1. Method to purify gases, such as combustion gases, in which method oxides of nitrogen and sulphur are converted into solid particles by an electron beam (3) coming from an electron source (1) with the aid of added base, c h a r a c¬ t e r i z e d in that particles charged in the electron beam are guided with an external electric field to gather on a collection sheet (5) into a layer (7) which can be cleaned at desired time periods.
2. Method in accordance with claim 1, c h a r a c t e r i ¬ z e d in that the particles charged by the electron beam (3) are guided with a spesific collection guidance field (10, 11) between the collection sheets (5) which there can be two or more successive sets.
3. Method in accordance with claim 2, c h a r a c t e r i ¬ z e d in that, for shaping the collection field, organs (12) which are in different potential than the collection sheets are used between the collection sheets and the wall of the combustion channel.
4. Method in accordance to some of claims 1-3, c h a r a c- t e r i z e d in that there are several collection sheets
(5) in layers so that every other layer has a higher potential.
5. Method in accordance to some of claims 1-3, c h a r a c- t e r i z e d in that the solid material collected on the collection sheets (5) is removed with a fast electric impulse which has opposite polarity than the voltage of the collection field.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI915921A FI915921A0 (en) | 1991-12-17 | 1991-12-17 | FOERFARANDE FOER RENING AV ROEKGASER. |
FI915921 | 1991-12-17 |
Publications (1)
Publication Number | Publication Date |
---|---|
AU3160393A true AU3160393A (en) | 1993-07-19 |
Family
ID=8533675
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU31603/93A Abandoned AU3160393A (en) | 1991-12-17 | 1992-12-16 | Method to purify gases |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0642379A1 (en) |
JP (1) | JPH07506759A (en) |
AU (1) | AU3160393A (en) |
CA (1) | CA2126073A1 (en) |
FI (2) | FI915921A0 (en) |
WO (1) | WO1993011855A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994017899A1 (en) * | 1993-02-05 | 1994-08-18 | Massachusetts Institute Of Technology | Tunable compact electron beam generated plasma system for the destruction of gaseous toxic compounds |
JP3431731B2 (en) * | 1994-08-16 | 2003-07-28 | 株式会社荏原製作所 | Electron beam irradiation exhaust gas treatment equipment |
US7704460B2 (en) | 2003-02-03 | 2010-04-27 | Advanced Electron Beams, Inc. | Gas separation device |
JP2006218360A (en) * | 2005-02-08 | 2006-08-24 | Japan Atomic Energy Agency | Removal method and its apparatus of organic compound using electron beam (eb) |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0640945B2 (en) * | 1987-12-10 | 1994-06-01 | 株式会社荏原製作所 | Radiation irradiation exhaust gas treatment method |
FI83481C (en) * | 1989-08-25 | 1993-10-25 | Airtunnel Ltd Oy | REFERENCE FOUNDATION FOR LENGTH, ROEKGASER ELLER MOTSVARANDE |
-
1991
- 1991-12-17 FI FI915921A patent/FI915921A0/en unknown
-
1992
- 1992-12-16 JP JP5510652A patent/JPH07506759A/en active Pending
- 1992-12-16 CA CA 2126073 patent/CA2126073A1/en not_active Abandoned
- 1992-12-16 AU AU31603/93A patent/AU3160393A/en not_active Abandoned
- 1992-12-16 WO PCT/FI1992/000343 patent/WO1993011855A1/en not_active Application Discontinuation
- 1992-12-16 EP EP93900194A patent/EP0642379A1/en not_active Withdrawn
-
1994
- 1994-06-15 FI FI942834A patent/FI942834A/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
CA2126073A1 (en) | 1993-06-24 |
FI915921A0 (en) | 1991-12-17 |
EP0642379A1 (en) | 1995-03-15 |
JPH07506759A (en) | 1995-07-27 |
WO1993011855A1 (en) | 1993-06-24 |
FI942834A0 (en) | 1994-06-15 |
FI942834A (en) | 1994-06-15 |
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