NO814455L - PROCEDURES FOR OPERATING AND MANAGING GAS - Google Patents
PROCEDURES FOR OPERATING AND MANAGING GASInfo
- Publication number
- NO814455L NO814455L NO814455A NO814455A NO814455L NO 814455 L NO814455 L NO 814455L NO 814455 A NO814455 A NO 814455A NO 814455 A NO814455 A NO 814455A NO 814455 L NO814455 L NO 814455L
- Authority
- NO
- Norway
- Prior art keywords
- pipe
- venturi
- air
- burner
- heat exchanger
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 10
- 238000002485 combustion reaction Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000003245 coal Substances 0.000 claims description 9
- 238000007664 blowing Methods 0.000 claims description 3
- 238000010348 incorporation Methods 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 description 13
- 239000002956 ash Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 239000003208 petroleum Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- -1 residues Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 239000010883 coal ash Substances 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 230000001965 increasing effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23B—METHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
- F23B90/00—Combustion methods not related to a particular type of apparatus
- F23B90/04—Combustion methods not related to a particular type of apparatus including secondary combustion
- F23B90/06—Combustion methods not related to a particular type of apparatus including secondary combustion the primary combustion being a gasification or pyrolysis in a reductive atmosphere
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/34—Grates; Mechanical ash-removing devices
- C10J3/36—Fixed grates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/74—Construction of shells or jackets
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/093—Coal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0956—Air or oxygen enriched air
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0973—Water
- C10J2300/0976—Water as steam
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
- C10J2300/1807—Recycle loops, e.g. gas, solids, heating medium, water
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
- C10J2300/1861—Heat exchange between at least two process streams
- C10J2300/1869—Heat exchange between at least two process streams with one stream being air, oxygen or ozone
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
- C10J2300/1861—Heat exchange between at least two process streams
- C10J2300/1884—Heat exchange between at least two process streams with one stream being synthesis gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
- C10J2300/1861—Heat exchange between at least two process streams
- C10J2300/1892—Heat exchange between at least two process streams with one stream being water/steam
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Solid-Fuel Combustion (AREA)
Description
-L-L
For å bidra til å løse det problem som mange land To help solve the problem that many countries
■står overfor, nemlig avhengigheten av petroleum for energi-formål, har søkeren utviklet en anordning som omfatter en forgasser for å danne brennbar gass ved brenning av kull; for således å gi en gass som har meget høy brennverdi, sCm er fri for forurensninger, og som har en høy flammetempera-tur, slik at kullet kan benyttes meget effektivt og erstatte eller supplere brenselolje utvunnet av petroleum. ■faced, namely the dependence on petroleum for energy purposes, the applicant has developed a device comprising a gasifier to form combustible gas by burning coal; to thus give a gas which has a very high calorific value, sCm is free of contaminants, and which has a high flame temperature, so that the coal can be used very efficiently and replace or supplement fuel oil extracted from petroleum.
<1>Slikt utstyr, som er gjenstand for søkerens norskj patentsøknad nr. 81 2750, utgjøres av en kompakt forgasser som har et nedre luftinnløp under en rist hvor kull forbrennes, som oventil er forsynt med rør for utløp av den dannede gass, hvilket rør fører til et syklonfilter hvor forurensninger, rester og aske som stammer fra f orbrennirigs-prosessen, sentrifugeres og avsettes ved bunnen av en vann- <1>Such equipment, which is the subject of the applicant's Norwegian patent application no. 81 2750, consists of a compact carburettor which has a lower air inlet under a grate where coal is burned, which is provided with a pipe above for the outlet of the formed gas, which pipe leads to a cyclone filter where pollutants, residues and ash originating from the incinerator process are centrifuged and deposited at the bottom of a water
beholder.container.
i in
i Den filtrerte gass føres til en brennertupp, som i i The filtered gas is led to a burner tip, as i
i in
sin tur er koblet til rør som tilfører primærluft for j spredning og brenning av oljen. Brenneren er videre for-j- in turn is connected to pipes that supply primary air for spreading and burning the oil. The burner is further for-j-
synt med et primærluftinnløp for forbrenning av gassen og for sekundær oljeforbrenning. I provided with a primary air inlet for combustion of the gas and for secondary oil combustion. IN
Denne forgasser er senere blitt forbedret ved hjelp av tilleggsutstyr som danner én sone som er i stand til å bevirke forbrenning av kullpulver, rester, aske og luft,;somj tidligere ble sentrifugert ut av filteret og avsatt på i bunnen av vannreservoaret, for således a danne en gass-prosent som sendes til ovnen hvor den forbrennes sammen mi ed This carburettor has later been improved by means of additional equipment which forms one zone capable of effecting the combustion of coal powder, residues, ash and air, which was previously centrifuged out of the filter and deposited on the bottom of the water reservoir, thus a form a gas percentage which is sent to the furnace where it is combusted together with mi ed
asken som avsettes ved bunnen av ovnen for således å skapethe ash that is deposited at the bottom of the furnace to thus create
; I ; IN
en mer effektiv temperatur ved utnyttelse av de elementer ; som tidligere ble ansett for å være ubrukelige (pulver, i rester, forurensninger og aske), som medføres av trykkluft j opp til en venturi hvor det dannes en brennsone hvor for-brenningen skjer. Denne forbedring er beskrevet i søkerens , norske patentsøknad nr. 81 2968. a more effective temperature when utilizing the elements; which were previously considered to be unusable (powder, residues, contaminants and ash), which are carried by compressed air j up to a venturi where a combustion zone is formed where the combustion takes place. This improvement is described in the applicant's Norwegian patent application no. 81 2968.
Den foreliggende oppfinnelse vedrører en drift- og styringsprosess for forgasseren, som utgjøres av nye og j viktige forbedringer som gir utstyret så godt som optimal funksjon og således gjør forgasseren mer effektiv, praktisk, økonomisk og meget fordelaktig. Disse forbedringer er båide.. The present invention relates to an operating and control process for the carburettor, which consists of new and important improvements which give the equipment almost optimal function and thus make the carburettor more efficient, practical, economical and very advantageous. These improvements are both..
nye og oppfinneriske.new and inventive.
Den nevnte fremgangsmåte drives av trykkluft og venturier (forøkningseffekt), gir enklere regulering (mindre rør) og eliminerer bevegelige deler, såsom vifter som vanlig-vis benyttes til å befordre luft. The aforementioned method is powered by compressed air and venturis (increasing effect), provides simpler regulation (smaller pipes) and eliminates moving parts, such as fans which are usually used to convey air.
Den tillater oppvarmning av trykkluften for således å øke volumet ved oppvarmning og forbedre., venturienes virkningsgrad. Den forbedrer forgasserens og brennerens respons i forbrenningsprosessen. It allows heating of the compressed air to thus increase the volume during heating and improve the efficiency of the venturi. It improves the response of the carburettor and the burner in the combustion process.
Bruk av to venturier for forgassingen, én for blåsingj og den annen for inhalering, gjør forgasseren isobarisk, sliki at den kan åpnes og fylles mens den er i funksjon. Using two venturis for the gasification, one for blowing and the other for inhalation, makes the gasifier isobaric, so that it can be opened and filled while in operation.
Bruk av en spesielt konstruert kompressor tillater energireduksjon og matning av flere funksjonssektorer i utstyret. Sammen med forvarmning av luften ved utløpet kan 1/3 av den mekaniske energi spares. The use of a specially designed compressor allows energy reduction and the feeding of several functional sectors in the equipment. Together with preheating the air at the outlet, 1/3 of the mechanical energy can be saved.
Forgasserens drift- og styreprosess ifølge oppfinnelsen medfører derfor en rekke fordeler. The carburettor's operating and control process according to the invention therefore entails a number of advantages.
Til bedre forståelse av oppfinnelsen skal den be- j skrives nærmere under henvisning til det utførelseseksempel i på oppfinnelsen som er vist på vedføyede tegning. j <' For a better understanding of the invention, it shall be described in more detail with reference to the embodiment of the invention shown in the attached drawing. j <'
Tegningen viser skjematisk og i snitt en trekull-forgasser og utstyr for forbrenning av den resulterende gass i med alternativ for oljeforbrenning, og omfatter drift- og styreutstyr ifølge oppfinnelsen. j På tegningen angir henvisningstall 1 en ovn med i ! The drawing shows schematically and in section a charcoal gasifier and equipment for burning the resulting gas with an alternative for oil combustion, and includes operating and control equipment according to the invention. j In the drawing, reference number 1 denotes an oven with i !
i i hengslet deksel 2, hvilken ovn nedentil har et kammer forsynt med et luftinnløp 4 og over dette en rist 5 hvor det in the hinged cover 2, which oven below has a chamber provided with an air inlet 4 and above this a grate 5 where the
i skjer en forbrenning av pulverisert eller granulert kull.! in a combustion of pulverized or granulated coal takes place.!
Som det vil kunne ses av tegningen, tillater fore-<:>liggende fremgangsmåte at det rom som tidligere ble opptatt av den ildfaste utmuring 6 blir redusert til det halve, idet ildfast utmuring nå kun benyttes i den nedre del hvor for- . brenningen skjer, slik at det blir større plass i den øvre. J del for chargering. i As can be seen from the drawing, the present method allows the space that was previously occupied by the refractory masonry 6 to be reduced to half, as refractory masonry is now only used in the lower part where the the burning takes place, so that there is more space in the upper one. J part for charging. in
Henvisningstallet 7 betegner et rør som fører fra I en<i1>'inntaksanordning 8 i ovnen til et syklonfilter 9.. Gassen; som genereres i ovnen føres gjennom dette rør til filtereI t !i hvor den filtreres. I utløpet fra filteret befinner det- seg et grenrør 10 for installasjon av et trykkluftrør 11 som er anbragt inntil en venturi 12. Venturien fortsetter i en kanal 13 som er forbundet med den nedre del av ovnen, hvor luftkammeret og askerommet befinner seg.. .Dette arrangement utgjør ikke noen del av den foreliggende oppfinnelse, men er gjort til gjenstand for en tidligere søknad på forbedringer ved forgasseren. En av fordelene ved den foreliggende oppfinnelse består i innlemmelse av en varmeveksler 14 i forgasserutstyret, hvilken varmeveksler er installert mellom syklonfilteret 9 og brenneren 15. Røret 16, som fører filtrert gass fra I syklonfilteret er forbundet med varmeveksleren 14, som igjen er forbundet med tilførselsrøret 17 til brenneren 15, og | som danner en venturi 18. The reference number 7 denotes a pipe leading from an inlet device 8 in the oven to a cyclone filter 9. The gas; which is generated in the furnace is led through this pipe to the filtereI t !i where it is filtered. In the outlet from the filter there is a branch pipe 10 for the installation of a compressed air pipe 11 which is placed next to a venturi 12. The venturi continues in a channel 13 which is connected to the lower part of the oven, where the air chamber and ash chamber are located.. . This arrangement does not form any part of the present invention, but has been made the subject of an earlier application for improvements to the carburettor. One of the advantages of the present invention consists in the incorporation of a heat exchanger 14 in the carburettor equipment, which heat exchanger is installed between the cyclone filter 9 and the burner 15. The pipe 16, which carries filtered gas from the cyclone filter is connected to the heat exchanger 14, which in turn is connected to the supply pipe 17 to the burner 15, and | which forms a venturi 18.
Brenneren 15 er også koblet til rør 19 som tilfører luft for gassforbrenningen. (På den skjematiske tegning Jer systemet for alternativ fyring med olje utelatt fordi det ikke utgjør noen del av den foreliggende oppfinnelse). The burner 15 is also connected to pipe 19 which supplies air for the gas combustion. (On the schematic drawing, the system for alternative heating with oil is omitted because it does not form any part of the present invention).
En annen fordel ved den foreliggende oppfinnelse vedrører innlemmelse av en kompressor 20 som er spesielt ><i>| konstruert og av liten størrelse, som tilfører trykkluft til Another advantage of the present invention relates to the incorporation of a compressor 20 which is particularly ><i>| designed and of small size, which supplies compressed air to
i ovnskammeret 3, til brenneren 15, til brennerens gasstil-j førsel, til venturien 12, hvor forbrenningssonen dannes, bg in the furnace chamber 3, to the burner 15, to the burner's gas supply, to the venturi 12, where the combustion zone is formed, bg
i også til. et rør hvor luft/vann omformes til damp. i in also to. a pipe where air/water is transformed into steam. in
Gjennom rørene 21 og 22, som danner en slags spiral ! inne i varmeveksleren 14, blir trykkluft oppvarmet før den j føres til blåseventurien 23, inhaleringsventurien 18 og for- j brenningsluftventurien 25, for således å øke trykkluftvolumet og forbedre venturienes virkningsgrad, i tillegg til å for- i bedre virkningen av forgasseren og brenneren. Through pipes 21 and 22, which form a kind of spiral! inside the heat exchanger 14, compressed air is heated before it is led to the blowing venturi 23, the inhalation venturi 18 and the combustion air venturi 25, in order to thus increase the compressed air volume and improve the efficiency of the venturis, in addition to improving the effectiveness of the carburettor and the burner.
Gjennom den samme kompressor og ved hjelp av rør 31 blir trykkluft tilført venturien 12, som resirkulerer kull-støv og aske under risten. Through the same compressor and by means of pipe 31, compressed air is supplied to the venturi 12, which recycles coal dust and ash under the grate.
I varmeveksleren 14 er det innsatt et rør 26. Med''.In the heat exchanger 14, a pipe 26 is inserted. With''.
i dette er det forbundet et sprøytemunnstykke som via et rør 27 er forbundet med et vanntilførselsrør 28. Således vil, vann kunne sprøytes inn i luften i røret 26, og blandingenI av luft og- vann omdannes til damp etter oppvarmning av de j hete gasser. Dampen føres gjennom røret 29 til-kammeret-3 for connected to this is a spray nozzle which is connected via a pipe 27 to a water supply pipe 28. Thus, water can be sprayed into the air in the pipe 26, and the mixture I of air and water is converted into steam after heating the j hot gases. The steam is led through the pipe 29 to the chamber 3 for
, I , I
'■ å i tørke kullet. '■ to in dry the coal.
Kompressoren mater også en sylinder 3 0 som benyttes The compressor also feeds a cylinder 30 which is used
■ ltiil -å åpne ovnens deksel 2. ' i Alle trykkluftledninger er forsynt med ventiler som muliggjør regulering av matningstrykket til de forskjellige funksjonssektorer i forgasseren. j 1 ! Drift- og styreprosessen ifølge oppfinnelsen for forgasseren vil forbedre forgasserens ytelse og kapasitet, ■ ltiil -to open the stove's cover 2. ' i All compressed air lines are equipped with valves that enable regulation of the supply pressure to the different functional sectors in the carburettor. j 1 ! The operation and control process according to the invention for the carburettor will improve the performance and capacity of the carburettor,
både teknisk og økonomisk, i betydelig grad og representerer 1 o I således et teknisk fremskritt. Oppfinnelsen tilveiebringer both technically and economically, to a considerable extent and thus represents 1 o I a technical advance. The invention provides
i in
også utstyr som bidrar effektivt til å løse det verdensom-spennende problem som avhengigheten av petroleum utgjør.; also equipment that contributes effectively to solving the worldwide problem posed by dependence on petroleum.;
Kull benyttes som råmateriale og som en alternativ energikilde, Coal is used as a raw material and as an alternative energy source,
idet det ved brenning av kullet dannes en gass med høy brenn<1->since when the coal is burned, a gas with a high burn<1-> is formed
t verdi som benyttes som brensel for å erstatte eller supplere brenselolje utvunnet av petroleum. t value used as fuel to replace or supplement fuel oil extracted from petroleum.
i in
I IN
Claims (3)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BR8008640A BR8008640A (en) | 1980-12-29 | 1980-12-29 | DRIVING AND CONTROL DEGASIFICATION PROCESS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| NO814455L true NO814455L (en) | 1982-06-30 |
Family
ID=4024638
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO814455A NO814455L (en) | 1980-12-29 | 1981-12-28 | PROCEDURES FOR OPERATING AND MANAGING GAS |
Country Status (6)
| Country | Link |
|---|---|
| JP (1) | JPS57134602A (en) |
| BR (1) | BR8008640A (en) |
| DE (1) | DE3145410A1 (en) |
| IT (1) | IT1143417B (en) |
| NO (1) | NO814455L (en) |
| SE (1) | SE8107804L (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102011010071B4 (en) * | 2011-02-01 | 2014-10-02 | Wolfgang Penc | Color fixing system |
| CN104329670A (en) * | 2014-10-17 | 2015-02-04 | 济南联星石油化工有限公司 | Biomass combustion system |
-
1980
- 1980-12-29 BR BR8008640A patent/BR8008640A/en unknown
-
1981
- 1981-08-21 IT IT49151/81A patent/IT1143417B/en active
- 1981-11-16 DE DE19813145410 patent/DE3145410A1/en not_active Withdrawn
- 1981-12-28 NO NO814455A patent/NO814455L/en unknown
- 1981-12-28 SE SE8107804A patent/SE8107804L/en not_active Application Discontinuation
- 1981-12-29 JP JP56216035A patent/JPS57134602A/en active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| DE3145410A1 (en) | 1982-09-16 |
| SE8107804L (en) | 1982-06-30 |
| IT1143417B (en) | 1986-10-22 |
| IT8149151A0 (en) | 1981-08-21 |
| BR8008640A (en) | 1981-05-26 |
| JPS57134602A (en) | 1982-08-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS6023709A (en) | Heat generator | |
| CN109735371A (en) | A kind of biomass circulating fluidized bed direct-combustion boiler and its with gasification furnace coupled electricity-generation co-producing active carbon system | |
| US4646713A (en) | Smoke-incinerating woodstove | |
| CN106322362B (en) | A kind of combustion method of biomass combustion machine and biomass fuel | |
| GB2032080A (en) | Starting a fluidised bed combustion chamber | |
| NO814455L (en) | PROCEDURES FOR OPERATING AND MANAGING GAS | |
| CN2525093Y (en) | Gas generating furnace | |
| CN1133036C (en) | High efficiency coal burner without pollution | |
| CN101608799B (en) | Straw briquette gasification dual-swirl burning furnace | |
| CN113803725A (en) | Small garbage incinerator with additional bypass garbage preheating channel | |
| CN201513930U (en) | Straw block gasification dual-swirl combustion furnace | |
| CN201059534Y (en) | Boiler for chemical industry producing | |
| RU2218520C2 (en) | Boiler for burning clinkering coal | |
| CN206709083U (en) | A kind of garbage pyrolysis gasification incinerator | |
| GB2117876A (en) | Boilers | |
| RU56560U1 (en) | INSTALLATION FOR JOINT GASIFICATION AND BURNING OF SOLID FUELS AND BIOMASS | |
| CN2417374Y (en) | Multi-functional stove or range with pit coal gasifing and smoke-less combustion | |
| SU1698565A1 (en) | Stoker | |
| SU77694A1 (en) | Dual-zone gas generator with Schwellschacht | |
| US1487297A (en) | Heating | |
| US1716676A (en) | Process of making mixed water gas and oil gas | |
| US1488701A (en) | Heating system and plant therefor | |
| Puzyrev et al. | Tornado Technology for Power Boilers | |
| US1840688A (en) | Furnace operation | |
| US1650498A (en) | Gas-heated furnace |