WO1986007602A1 - A powder additive for use in the combustion of solid materials, and the use of the powder additive - Google Patents
A powder additive for use in the combustion of solid materials, and the use of the powder additive Download PDFInfo
- Publication number
- WO1986007602A1 WO1986007602A1 PCT/DK1986/000064 DK8600064W WO8607602A1 WO 1986007602 A1 WO1986007602 A1 WO 1986007602A1 DK 8600064 W DK8600064 W DK 8600064W WO 8607602 A1 WO8607602 A1 WO 8607602A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- weight
- additive
- combustion
- powder
- powder additive
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/10—Treating solid fuels to improve their combustion by using additives
Definitions
- the present invention relates to a powder additive for use in the combustion of solid materials.
- the invention further relates to the use of the powder additive for counteracting the formation of deposits in furnaces, boilers and filters as well as reduction of environmental contaminating discharges during combustion.
- a conventional combustion system or plant consists in principle of three main elements, viz. furnace, boiler and filter.
- a satisfactory operation of the system requires a combustion, which is so complete that no interruptions of operation arise due to sediments and deposits in the individual parts or clogging of filters. It must furthermore be avoided that the operation has to be stopped on account of discharges exceeding the permissible limits.
- the furnace part is in most cases provided with a refractory lining, which has to be kept intact and reasonably clean.
- deposits are deposited, which have to be removed intermittenly.
- the removal of such deposits has previously been very difficult, as hard-handed cleaning methods, such as pneumatic chiseling and shootings, must be applied; these methods will often result in damages to the refractory lining.
- Repair of the refractory lining is expensive, time consuming and difficult and may involve a sanitary risk to the repairer.
- the boiler part may be of different constructions, e.g. either with horizontal or with vertical tubes.
- Deposits in boilers are usually formed quickly and to a great extent.
- the deposits reduce the heat transfer through the tube walls to the thermal medium and consequently reduce the efficiency of the boiler.
- the deposits in the boiler have reached an unacceptable level, they should be removed to ensure a satisfactory operation of the system.
- the necessary removal of the deposits in boilers is the usual reason for interruptions in operation.
- the filter part serves to prevent discharge of particulate impurities, such as flyash, soot, loose deposits and other substances which would otherwise pass out into the atmosphere from the combustion system.
- Danish Patent Specification No. 147,407 discloses the use of dicalcium phosphate to reduce the thickness of surface deposits in oil-fired systems affected by exhaust gases. This process has, however, in practice turned out to result in a completely unsatisfactory effect.
- Danish Patent Specification No. 140,343 describes a process of complete or partial neutralization of the acid combustion products formed by combustion of sulphurous fuel by continuous and simultaneous injection of the following compounds: alkali-metal nitrate, ammonium nitrate, magnesium carbonate, carbon and ammonium carbonate. It is stated that the ammonium carbonate ingredient is of considerable importance for the achievement of an efficient neutralization.
- the agent used by said process is particularly developed for use in oil-fired systems and is primarily intended to neutralize the acid products, especially sulphur dioxide, formed by the combustion of the sulphur.
- the above known agent is in practice dosed to the boiler. The addition presents corrosive problems in the boiler and does not prevent the formation of deposits.
- the object of the present invention is to remedy the drawbacks of the prior art stated above and is described In detail below.
- the inventive powder additive can advantageously be used in the way described in the characterising clause of claim 4.
- the powder additive according to the invention is characterised by containing the following ingredients:
- perborate such as sodium perborate and potassium perborate
- a manganese compound e.g. manganese salt such as manganese sulphate
- saltpetre such as NaNO 3 and KNO 3
- a mixture of the two compulsory ingredients as well as perborate may e.g. be used for the combustion of straw.
- the optimum mixture by using the two compulsory ingredients as well as perborate is 75% by weight of dicalcium phosphate + 5% by weight of perborate and 20% by weight of ammonium chloride.
- this mixture will normally be used in an amount of 100-150 g/ton of fired waste (industrial waste mixed with domestic garbage).
- 100 g/ton of fired straw is used in the combustion of straw.
- a mixture of dicalcium phosphate, sodium phosphate and ammonium chloride may e.g. be used for the combustion of coal and coke.
- the combustion of coal and coke is, however, improved considerably if manganese sulphate and calcium nitrate are also added to the additive.
- this additive mixture for the combustion of coal and coke the furnace is kept clean, fewer clinkers and less flyash being formed.
- an additive mixture according to the invention for combustion in crematories may reduce discharge of toxic substances, such as dioxines. It is normally difficult to avoid toxic discharges of this type in connection with combustion tasks with frequent cold starts, which renders the achievement of sufficiently high temperatures for complete combustion of e.g. poisonous substances difficult.
- the additive contains ingredients of each of the above eight types, this yielding the optimum ensurance against noxious discharges.
- the various ingredients may be mixed in the following ratio:
- dicalcium phosphate 45-93% by weight, preferably 75% by weight
- ammonium chloride 5-50% by weight, preferably 20% by weight
- saltpetre 0-10% by weight
- 75-300 g, preferably 100-150 g of additive of the chosen composition may be used for the combustion of 1000 kilogram of solid material.
- the powder additive according to the invention has surprising advantages when used in combustion systems, such as systems for the combustion of
- waste or garbage including plastics containing waste
- solid fuel such as coal and coke
- straw d) as well as cremation.
- the combustion is supported by the use of the powder additive according to the invention.
- the powder additive further ensures a limitation of the formation of flyash, and the powder keeps the boiler dry and leads to a loosening of any deposit, which may already be present.
- the powder When using of the powder additive, the powder Is fed continuously Into the furnace in such a manner that the powder reaches the flames in the form of a mist. By adding the powder directly to the flames it gets into direct contact with the ingredients which would later result in deposits. The powder also gets into contact with the toxic ingredients which have to be removed before the exhaust gas is let out into the atmosphere.
- the powder additive ensures a complete combustion of the materials which would otherwise form deposits as well as of the toxic substances by converting them into non-toxic materials. A utilization of the calorific value of these substances is furthermore obtained by the removal of technically and sanitarily noxious substances.
- Oxide scales may be formed if the combustion temperature is too high, and if the temperature is too low deposits are formed in the form of a moist mass containing toxic substances. Such deposits may be deposited in furnaces, boilers and filters. The Incomplete combustion at low combustion temperatures may moreover lead to discharge of toxic substances.
- the inventive powder additive has a highly drying effect. A considerable reduction of the extent of deposits is obtained by means of the combined effect of a considerable improvement of the combustion and a reduction of the content of moist ingredients In the exhaust gas. These deposits are furthermore dried and loosened so that they are easily removed.
- a considerable reduction of the formation of deposits is effected in the furnace.
- a considerable reduction of the damages arising in the refractory lining during cleaning is obtained, and the cleaning can take place at greater intervals than previously.
- the cleaning may furthermore be performed quickly and convenientlywithout the previously mentioned sanitary risk to the cleaner.
- the cleaning of the furnace part after use of the additive according to the invention has thus been reduced to a quite small task, as there are no serious deposits to remove.
- the boiler part is kept completely dry and substantially free of deposits by using the inventive powder additive.
- the only deposits, which may occur, will be in the form of dry, easily removable deposits.
- the toxic substances will be burned before the exhaust gas reaches the boiler part.
- the environment around the boiler Is thus improved drastically, the known inconveniences of smell being removed. This is a great advantage in the daily, work around the boiler and particulary In connection with the cleaning of the boiler.
- the additive according to the invention may of course be used as desooting agent, the main object is, however, to ensure a combustion of the solid fuel to such a complete extent that damaging deposits and environmental problems in the form of discharge of toxic and malodorous gases and particles to the surroundings are avoided.
- a boiler increases of course the utilization of heat to a considerable extent, no insulating deposits preventing transfer of heat to the heat transferring medium (e.g. water) being present.
- the heat transferring medium e.g. water
- the content of solid particles in the exhaust gas has been reduced to such a considerable extent that the filter will no longer be a limiting factor for the operation of the combustion system.
- This circumstance can be illustrated by an example from practical life in connection with a new straw furnace.
- the furnace could only function for 8 or 10 days before the need of a thorough cleaning performed by a chimney sweeper arose.
- the filters were moreover clogged even before, so that the system was completely inoperative after a short period, unless the filters were disconnected.
- the inventive additive the filters could be connected and the system was operative without the chimney sweeper being called.
- the system in question how operates for 8 weeks without cleaning.
- the powder additive according to the invention presents considerable savings.
- the costs of the powder are thus only one fourth of the costs for the work to be performed by a skilled chimney sweeper.
- the inventive powder to this should be added the other far more important advantages obtained by using the inventive powder, such as a reduction of the damages to the system, better utilization of the calorific value of the burned material as well as an improvement of the environment.
- composition of the powder additive according to the invention varies with the material burned. Consequently it is advantageous to add dyestuff to the powder additive, in order to facilitate the distinction of the various types of utilization of the inventive powder additive from each other.
- the reaction mechanism causing the effects of the powder additive are not yet fully elucidated, but the obtained effect exceeds the additive effect of the individual components of the additive.
- 100 g of additive consisting of 75% by weight of dicalcium phosphate, 5% by weight of sodium perborate, 15% by weight of ammonium chloride + 5% by weight of manganese sulphate per ton of coal resulted after three or four days use not only in fulfilment of the environmental, requirements since measurements showed that the pollution was only one fourth of the permissible.
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NO870676A NO870676L (en) | 1985-06-20 | 1987-02-19 | POWDER ADDITIVE FOR USE IN COMBUSTION OF SOLID MATERIALS AND APPLICATION OF POWDER ADDITIVE |
FI870692A FI81375C (en) | 1985-06-20 | 1987-02-19 | Finely divided additive for use in the combustion of solids n |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK280385A DK151194C (en) | 1985-06-20 | 1985-06-20 | POWDER ADDITIVE TO USE IN COMBUSTION OF SOLID MATERIAL, AND USE OF POWDER ADDITIVE |
DK2803/85 | 1985-06-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1986007602A1 true WO1986007602A1 (en) | 1986-12-31 |
Family
ID=8115933
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DK1986/000064 WO1986007602A1 (en) | 1985-06-20 | 1986-06-11 | A powder additive for use in the combustion of solid materials, and the use of the powder additive |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0229090A1 (en) |
AU (1) | AU5963386A (en) |
DK (1) | DK151194C (en) |
FI (1) | FI81375C (en) |
WO (1) | WO1986007602A1 (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0258708A2 (en) * | 1986-08-15 | 1988-03-09 | Toa Nekken Corp., Ltd. | Method of controlling generation of clinker ash from exhaust gas dust of coal |
WO1989003241A1 (en) * | 1987-10-16 | 1989-04-20 | Reinhard Fischer | Process for disposal of waste by combustion with oxygen |
WO1994028091A1 (en) * | 1993-05-28 | 1994-12-08 | Gb Therma-Chem Limited | Method of removing deposits from heating apparatus |
US5376354A (en) * | 1987-10-16 | 1994-12-27 | Noell Abfall-Und Energietechnik Gmbh | Process for disposal of waste by combustion with oxygen |
WO2001005911A2 (en) * | 1999-07-16 | 2001-01-25 | Reatech | A method for reducing agglomeration, sintering and deposit formation |
EP1411108A1 (en) * | 2002-10-16 | 2004-04-21 | Ethyl Corporation | Method of enhancing the operation of a diesel fuel combustion after treatment system |
WO2008034437A1 (en) | 2006-09-22 | 2008-03-27 | Herbert Georg Nopper | Compressed fuel composed of renewable organic residues and/or raw materials and production thereof |
US8079845B2 (en) * | 2005-05-10 | 2011-12-20 | Environmental Energy Services, Inc. | Processes for operating a utility boiler and methods therefor |
DE202011108946U1 (en) | 2011-12-13 | 2012-02-13 | Georg Dohmen | Additive for the improvement of ash and slag properties during the combustion of biogenic masses |
CN104164269A (en) * | 2014-08-26 | 2014-11-26 | 山东大学 | Biomass solid formation fuel additive and doping method thereof |
KR102129396B1 (en) * | 2020-03-31 | 2020-07-02 | (주)에이치에스에너지 | Combusition additive for solide fuel and method for preparing the same |
CN116734265A (en) * | 2023-07-17 | 2023-09-12 | 中国环境科学研究院 | In-furnace control method for acidic pollutants in household garbage co-combustion industrial organic solid waste process |
CN116734265B (en) * | 2023-07-17 | 2024-05-14 | 中国环境科学研究院 | In-furnace control method for acidic pollutants in household garbage co-combustion industrial organic solid waste process |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102212405A (en) * | 2010-04-01 | 2011-10-12 | 马中胜 | Coal-saving catalytic synergistic agent |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1493403A (en) * | 1923-04-26 | 1924-05-06 | Joseph Russell | Composition for treating fuel |
US2777761A (en) * | 1954-06-03 | 1957-01-15 | Chemical & Engineering Company | Composition for eliminating slag, soot, and fly ash |
US3630696A (en) * | 1969-10-27 | 1971-12-28 | Trimex Corp | Combustion adjuvant |
US4190421A (en) * | 1978-07-17 | 1980-02-26 | Chemed Corporation | Fireside treating compositions |
DE2413520B2 (en) * | 1974-03-21 | 1980-05-08 | C.H. Boehringer Sohn, 6507 Ingelheim | |
SE418302B (en) * | 1979-11-07 | 1981-05-18 | Kjell Steenberg | Process for reducing the thickness of deposit on the surfaces of a heating plant that come into contact with flue gases |
-
1985
- 1985-06-20 DK DK280385A patent/DK151194C/en not_active IP Right Cessation
-
1986
- 1986-06-11 WO PCT/DK1986/000064 patent/WO1986007602A1/en active IP Right Grant
- 1986-06-11 EP EP19860903277 patent/EP0229090A1/en not_active Withdrawn
- 1986-06-11 AU AU59633/86A patent/AU5963386A/en not_active Abandoned
-
1987
- 1987-02-19 FI FI870692A patent/FI81375C/en not_active IP Right Cessation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1493403A (en) * | 1923-04-26 | 1924-05-06 | Joseph Russell | Composition for treating fuel |
US2777761A (en) * | 1954-06-03 | 1957-01-15 | Chemical & Engineering Company | Composition for eliminating slag, soot, and fly ash |
US3630696A (en) * | 1969-10-27 | 1971-12-28 | Trimex Corp | Combustion adjuvant |
DE2413520B2 (en) * | 1974-03-21 | 1980-05-08 | C.H. Boehringer Sohn, 6507 Ingelheim | |
US4190421A (en) * | 1978-07-17 | 1980-02-26 | Chemed Corporation | Fireside treating compositions |
SE418302B (en) * | 1979-11-07 | 1981-05-18 | Kjell Steenberg | Process for reducing the thickness of deposit on the surfaces of a heating plant that come into contact with flue gases |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0258708A2 (en) * | 1986-08-15 | 1988-03-09 | Toa Nekken Corp., Ltd. | Method of controlling generation of clinker ash from exhaust gas dust of coal |
EP0258708B1 (en) * | 1986-08-15 | 1993-07-14 | Toa Nekken Corp., Ltd. | Method of controlling generation of clinker ash from exhaust gas dust of coal |
WO1989003241A1 (en) * | 1987-10-16 | 1989-04-20 | Reinhard Fischer | Process for disposal of waste by combustion with oxygen |
US5376354A (en) * | 1987-10-16 | 1994-12-27 | Noell Abfall-Und Energietechnik Gmbh | Process for disposal of waste by combustion with oxygen |
WO1994028091A1 (en) * | 1993-05-28 | 1994-12-08 | Gb Therma-Chem Limited | Method of removing deposits from heating apparatus |
WO2001005911A2 (en) * | 1999-07-16 | 2001-01-25 | Reatech | A method for reducing agglomeration, sintering and deposit formation |
WO2001005911A3 (en) * | 1999-07-16 | 2001-08-09 | Reatech | A method for reducing agglomeration, sintering and deposit formation |
US6615751B1 (en) | 1999-07-16 | 2003-09-09 | Raetech | Method for reducing agglomeration, sintering and deposit formation in gasification and combustion of biomass |
EP1411108A1 (en) * | 2002-10-16 | 2004-04-21 | Ethyl Corporation | Method of enhancing the operation of a diesel fuel combustion after treatment system |
US8079845B2 (en) * | 2005-05-10 | 2011-12-20 | Environmental Energy Services, Inc. | Processes for operating a utility boiler and methods therefor |
WO2008034437A1 (en) | 2006-09-22 | 2008-03-27 | Herbert Georg Nopper | Compressed fuel composed of renewable organic residues and/or raw materials and production thereof |
DE202011108946U1 (en) | 2011-12-13 | 2012-02-13 | Georg Dohmen | Additive for the improvement of ash and slag properties during the combustion of biogenic masses |
CN104164269A (en) * | 2014-08-26 | 2014-11-26 | 山东大学 | Biomass solid formation fuel additive and doping method thereof |
KR102129396B1 (en) * | 2020-03-31 | 2020-07-02 | (주)에이치에스에너지 | Combusition additive for solide fuel and method for preparing the same |
CN116734265A (en) * | 2023-07-17 | 2023-09-12 | 中国环境科学研究院 | In-furnace control method for acidic pollutants in household garbage co-combustion industrial organic solid waste process |
CN116734265B (en) * | 2023-07-17 | 2024-05-14 | 中国环境科学研究院 | In-furnace control method for acidic pollutants in household garbage co-combustion industrial organic solid waste process |
Also Published As
Publication number | Publication date |
---|---|
DK151194B (en) | 1987-11-09 |
FI81375B (en) | 1990-06-29 |
DK280385A (en) | 1986-12-21 |
AU5963386A (en) | 1987-01-13 |
FI870692A0 (en) | 1987-02-19 |
FI81375C (en) | 1990-10-10 |
FI870692A (en) | 1987-02-19 |
DK280385D0 (en) | 1985-06-20 |
DK151194C (en) | 1988-04-25 |
EP0229090A1 (en) | 1987-07-22 |
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