WO2005111510A2 - Procede de transfert thermique et de filtrage d'air - Google Patents

Procede de transfert thermique et de filtrage d'air Download PDF

Info

Publication number
WO2005111510A2
WO2005111510A2 PCT/TR2005/000023 TR2005000023W WO2005111510A2 WO 2005111510 A2 WO2005111510 A2 WO 2005111510A2 TR 2005000023 W TR2005000023 W TR 2005000023W WO 2005111510 A2 WO2005111510 A2 WO 2005111510A2
Authority
WO
WIPO (PCT)
Prior art keywords
water
tank
order
air
refinement
Prior art date
Application number
PCT/TR2005/000023
Other languages
English (en)
Other versions
WO2005111510A3 (fr
Inventor
Seydi Bakirci
Original Assignee
Seydi Bakirci
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.)
Filing date
Publication date
Application filed by Seydi Bakirci filed Critical Seydi Bakirci
Publication of WO2005111510A2 publication Critical patent/WO2005111510A2/fr
Publication of WO2005111510A3 publication Critical patent/WO2005111510A3/fr

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D11/00—Central heating systems using heat accumulated in storage masses
    • F24D11/002—Central heating systems using heat accumulated in storage masses water heating system
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D10/00—District heating systems
    • 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
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/17—District heating
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/14—Combined heat and power generation [CHP]

Definitions

  • This invention is related to the methods comprising the protection of the atmosphere and nature, the establishment of a plant outside the settlement in order to provide the comfort of the people and cheap heating in a secure and healthy environment, by carrying the boiled water (at 110 degrees C) with tankers to the regional heating centers within the settlement, the prevention of air and environmental pollution, the use of an air filter washing system (refinement) in order to provide cheap production, the prevention of the emission loss of the fluid and its pollution of the atmosphere, the drying of the air with a system similar to that of the cyclone method in order to provide that effective combustion is performed at humid weather and providing for the drying of the humid coal products without polluting the air and the prevention of the ashes spreading into the air and the environment.
  • Chimneys thro ⁇ gh which the combustion products of solid, fluid and gas fuels, which are used in domestic heating and the industry for the production of water or steam or electricity (thermal power plants) are discharged into the atmosphere, are the most important air and environment pollution sources.
  • th ⁇ old heating technique of stoves used for domestic heating is still valid today. This system uses firewood and coal and there is close contact to the fuel and the chimney. Carrying the fuel, setting it up on fire and discharging and carrying the ashes causes pollution and problems at home.
  • lignites used in industrial facilities and thermal power plants, etc. include a high amount of N and in order to avoid pollutants such as
  • Waters are polluted through factors such as organic wastes resulting from garbage and pollutions within the settlements, rain water and winds and thus gases (H 2 S, etc.) are discharged into the air as a result of unaerobic degradation.
  • gases H 2 S, etc.
  • the main element of the plastic materials burnt at garbage dumps are petrochemical materials including ethylene and this is another factor for air and environmental pollution.
  • Coal, quality lignite, briquette coke and washed coal include less sulphur than lignites.
  • Briquettes produced of ground lignites, have a high concentration of volatile elements and thus a risk of sudden ignition. They also discharge toxic chimney gases.
  • coke is decomposed from flammable gases (CH 4 ,CO,S), its calorie is low, but the cost increases and the C factor is again another important pollution source.
  • CH 4 ,CO,S flammable gases
  • the S rate in the coal decreases by 20% the element loss causes waste and waste water causes pollution.
  • Another energy source which may be used in future is nuclear energy.
  • This energy is a risk in itself, because it has dangers which may destroy the world in a moment's time.
  • the negative impacts of the Chernobyl calamity experienced in the recent past on human health and nature is worldwide known.
  • Another drawback is that atomic industry materials are constantly radioactive. Because actually not only the uranium, but also its reactor, tools used, leftovers of the disintegration (a big reactor leaves tons of leftovers) radiates. It seems that the deuterium energy is difficult to be attained. And since the electricity energy has multi-purpose uses and is scarce it is not used much for heating. Since electrical energy is produced mainly from thermal power plants it is again a great pollutant source. However since wind energy is a natural source (non-pollutant) it is the best electricity energy production method to be used.
  • the said pollutions are experienced because of the combustion of biomass, coal, petroleum and natural gases because of the said reasons.
  • the impact of air pollution on the environment is global, regional and local. Globally, it is estimated that effects such as the greenhouse effect caused by the increase of CO 2 , the holes in the ozone stratum may lead to important climatologically events in the atmosphere and thus on the globe. Regionally, acid rains cause the destruction of the rain forests, harming the chemical balance of the soil and the ecological balance as a result of acidization of the lakes.
  • Locally air pollutants such as SO 2 particulates, CO, Ozone, NO ⁇ create negative impacts on human health, flora, structures and materials.
  • the said negative impacts increasing based on the population increase shall further increase.
  • the CO2 concentration in the atmosphere was about 200 - 250 ppm until 200 years ago; since 200 years this rate has reached 3J35 ppm through the combustion of fossil fuels. Measurements show that this rate shall reach 400-600 ppm within the coming 50 years.
  • the said pollution will cause that the CO 2 rate in the atmosphere shall reach enormous dimension in the coming few centuries.
  • CO 2 and its increase is a great danger to the said climate of the world. It is accepted that this feature of CO2 permeates the sun radiation at short wavelength and absorbs the long wavelength infrared radiation reflected from the earth and its increase in concentration causes the increase of the average temperature of the world climate.
  • Ethylene is the only organic gas which has a direct negative impact on plants. It has been medically proven that air pollution causes great negative impacts on human health. Especially the active toxicity of CO, the transformation of SO2 in the throat -into sulphuric acid; especially acute respiration insufficiency in children, direct effects of particles respiratory ways and direct impacts to lungs, carcinogenic effect and damage in the brain, asthma patients having a difficult life, caner risks, etc. may be listed. With the excessive increase of the pollution levels even comas and fatal cases are experienced.
  • Adirondack (New York) lakes the pH value was 6.5 in the 1930s it dropped below 5 in 1975. In Pitlochry, Scotland the pH value was measured as 2.4 in one rainfall. Over settlements very high concentrated nitric acid rains are observed. Besides the waster water heated as a result of the cooling performed with water at thermal power plants in order to protect the materials cause great negative effects on the aquatic life.
  • limestone is used as raw SO 2 absorbable material.
  • SO 2 washed with the formed lime solution is added to the calcium sulphite/sulphate mixture and is transformed to gypsum plaster through oxidation. Since there was no area for use for this product there is a great waste problem.
  • the compound Fe-EDTA (Ethylendiamine Tetraasidic Acid) method is based on the method of washing with lime. SO 2 and NO ⁇ are refined together and gypsum plaster is obtained. From the refined material iron based EDTA elements are placed into the fluid and the SO 2 and NO ⁇ is decomposed in the polluted gas and through the assistance of NO, sulphite ions the elements are transformed into nitrogen and sulphates are formed.
  • active carbon becomes again active after the carbon is loaded with SO 2 .by absorbing it from the polluted gas, and by discharging the SO 2 load
  • SO 2 refining products are formed and at the second surface holder NO ⁇ s are held with ammonia.
  • NO ⁇ may be refined with the dry wet NO ⁇ , compound SO 2 and NO ⁇ methods.
  • the dry NO ⁇ refining method uses reduction methods with selected or unselected catalysts in dry methods with catalysts. ' :
  • NH3 is injected into the chimney gas and together with oxygen the ammonia, nitrogen oxide reduced to nitrogen.
  • NOX refinement productivity increases up to 80%.
  • wet NO ⁇ refinement method the NO component is transformed into NO 2 by gas phase oxidation and refined through absorption by the refining solution.
  • the compound wet SO 2 /NO ⁇ refinement methods are divided into two main groups such as oxidation-absorption and adsorption reduction methods.
  • the most known oxidation- absorption method is the Walther process.
  • the absorption-reduction process is the EDTA process.
  • Trifunctional closed circuit exhaust gas refinement system In order to provide combustion conditions in this system the fuel mixture, exhaust gas O2 content are measured at the entry of the catalyst with the electrochemical method and the carburetor or the electronic fuel spraying system are adjusted so that cytochiometric operation conditions are provided. This multifunctional compound refinement system is accepted as the most appropriate and effective refinement system.
  • Inventions which aim to wholly remove all these negative impacts are: Heat transfer, air filter (chimney gases refinement), evaluation of the chimney temperature, emission protection, effective combustion with dry air and fuel mixture and control of ashes methods.
  • the heat transfer aims at removing all said problems in settlement heating; the feature of this method is that is related to carrying the water, which is boiled in the central facility to be established in the affinity of the settlements (city, towns, small villages), from there through tankers to the regional heating (apartment blocks, apartment, streets, schools, etc.) centers of boiler rooms. Houses constructed unsystematically (especially detached houses) are grouped together and central heating systems may be furnished, and the network volume can be charged by calculations. Thus this can be achieved without smoking chimneys, without machines being noisy, without polluting the air and environment and without experiencing all the said negative impacts and the cost can be further decreased by decreasing the said negative impacts.
  • the houses can be heated by using geothermal energies. Besides with the said method hot water can be transferred to industrial use.
  • the amount of the water to be heated is calculated and its transfer performed. For example, hot water of 60.000 kg at 100 degrees shall be transferred to a block where a daily amount of 1000 kg 6000 Cal is burnt. Considering meteorology reports the needed amount of water shall be carried. The water which cools down up to 20 degrees through circulation shall be reheated by carrying it to the central facility. Hot water transfer to the city centers shall be performed only at night. The tankers shall not enter the traffic at school hours, at the rush hours in the mornings and evenings. Since the distances are not very long the transportation expense should not be high. Since filling and discharging shall be quick there will be no time loss, the tankers shall not work and be noisy during the emptying and filling procedures, (at systems not appropriate, discharging shall be made with a dynamo.)
  • thermometers to be placed on each department of the tanker shall openly show this. All systems regarding the 0 heat transfers shall be firmly isolated, filling and emptying shall be performed together with the emission prevention method evidenced in the attached. Therefore heat loss shall be negligible.
  • the aim is to provide for maximum productivity and minimum pollution.
  • Humid air is passed through a 100 degree environment and is greatly dried by taking its steam with a method similar to the cycloning method (wide mouthed cyclone 1 system). Combustion is realized by adding maximum extra air into the excessively ground coal after a pre heating to 110 degrees, [the methods of dry air and dry fuel (coal dust) is explained on the attached Figure 4.] Since a maximum combustion reaction shall be realized with fine coal and dry air which have been sent to the combustion room by dehumidifying there will be almost no chimney gas components such as CO, C and S.
  • the ashes causing pollution shall be sent to the ash storing system after wet without being spread into the environment and silolized.
  • the polluted (acidic, ashy, particulated) water formed from the refinement of the chimney gases shall be destroyed by mixing with the ashes.
  • the wastes useful for industry shall be cleaned.
  • Figure 1 shows on the one hand some of the blocks which have been furnished into the tank which provides the heat transfer in the boiler room and on the other hand is a schematic illustration showing the lateral cross section of a tanker which performs filling and discharging. Besides a cross section from above of a block can also be seen. (The emission method is shown with a tanker discharging.)
  • FIG. 1 shows on the one hand some of the blocks which have been furnished into the tank which provides the heat transfer in the boiler room and on the other hand is a schematic illustration showing the lateral cross section of a tanker which performs filling and discharging. Besides a cross section from above of a block can also be seen. (The emission method is shown with a tanker discharging.)
  • FIG. 1 shows on the one hand some of the blocks which have been furnished into the tank which provides the heat transfer in the boiler room and on the other hand is a schematic illustration showing the lateral cross section of a tanker which performs filling and discharging. Besides a cross section from above
  • the X circulation main input pipe are mounted to the 2 no blocks through 1 no pipes, 2 no blocks are mounted to 4 no parallel blocks with 3 no pipes. And the 4 no blocks are connected to the Y circulation return main pipe with 5 no pipes. 2 no blocks are fixed with 6 no bolts at their lower corners and 4 no blocks at their upper corners.
  • the 8 no water hose (fireproof rubber) is connected to the 7 no mouth at the lower part of the tank.
  • 9 no dynamo is mounted to the 8 no water drainage hose, between the 9 no dynamo and the 7 no mouth (to the 8 no hose) 10 no valve is mounted.
  • 8 no hose is attached to the filling mouth of the 12 no tanker with the 11 no plug.
  • 8 no hose which prevents the heat loss to arise with kinetic pressure, is mounted to the emission mouth of the 14 no tank and with the 11 no plug to the emission mouth of the 13 no tank.
  • 8 no hose is mounted to the 15 no mouth of tank and the 16 no mouth of the tank with the 11 no plug.
  • the said plugs are used to mount 10 no valves in between of each of the tanker mouths and tank mouths.
  • the central heating system water (having transferred its heat to the houses) coming from the x circulation main pipe is distributed over 1 pipes (three in number until the Y return of the system as shown in the example figure) at equal pressures according to the volume of the blocks and pass the 2 blocks through 3 pipes to 4 blocks. (The tank is full with hot water at 100 degrees).
  • the system water which is heated to a degree close to the hot water temperature in the tank has returned to heat the house through 5 no pipes to the Y circulation main pipe.
  • the heat is transferred until the water in the tank decreases to 20 degrees and the room temperature is maintained at 26-30 degrees.
  • the circulation pump which is connected to the time relay opens and closes at intervals and with savings on electricity and since the room temperature does not exceed 30 degrees the rapid loss of heat caused by kinetic pressure has decreased.
  • the water is cooled down to 20 degrees and the 10 valve on the 8 hose connected to 7 mouth, is opened and the 9 dynamo is operated.
  • the water is filled to the tanker through the 8 hose and 12 tanker filling mouth and carried to the central facility. Before the hot water carried from the central facility is transferred to the tank, the 10 valve after the emptying mouth of the 7 tank is closed and thus both heat loss and damage to the 9 dynamo is prevented.
  • the 8 emission hose connected to the 14 emission mouth is attached to the 12 emission mouth of the tanker with the 11 plug.
  • the method of protecting the said emission facilities the emptying of all fluids in the central facility and prevents material loss and pollution to arise with kinetic pressure.
  • This method can be used in commercial type industrial facilities, organic chemistry (refineries, tanker filling and emptying, etc.) and inorganic chemistry, etc. facilities.
  • the chimney gases are absorbed by the fan and pumped into the water by distributing to slim pipes.
  • chimney gases contacting at maximum with water are controlled as a result of decomposition and absorption by precipitating chimney gases components (COx,SOx,NOx,H2S,HF,HC, etc.) into acids and particles (Sb, As, Cd, Cr, Cu, Bp, Hg, Ni, Se, Ag, Zn, Tn, U, etc.) and ashes suspending in water and rising to water surface.
  • Chimney gases whose heat has been used at most by passing them through chimney heat tanks are fairly cooled down with the parallel air conditioning system.
  • the air heated as a result of the cooling procedure is passed through the humid air drying system mentioned in the appendix and is sent to the combustion room in order to create effective combustion reaction and its heat is utilized and the extra air need is removed. Since the chimney gases which have been absorbed by the fan and sent into the water is low and since the water 0 continuously flows acid steam formation is prevented.
  • a small cytochiometric acid steam is passed through a second and, if necessary, a third procedure and thus controlled. This effective combustion method has decreased chimney gases and the load of the refinement is reduced.
  • the said refinement method with washing system may be used at vehicles. However stagnant water instead of moving water. Water is passed through the thin pipes (connected to the radiator system) furnished into the stagnant water and cooled down. Since the fans to operate in the refinement system at the vehicles require fixed revolution (so that toxic gases can effective contact water) they take their movement from the electronic system.
  • the dirty ⁇ Q water shall during fueling at the fuel station by the staff sent to the dirt water tank through an automatic fitting hose without losing time.
  • the emptied stagnant water tank will be filled with clean water.
  • the acidic dirty water at the station shall be carried with special tankers to the said heat transfer centers and destroyed by mixing with the ashes.
  • vehicle pollution will be reduced to minimum.
  • a small amount of cytochiometric acid steam is negligible.
  • the use of the said process in planes shall reduce the said negative 45 , impacts of NO on ozone to a minimum. Even its use in ships prevents the said pollution.
  • Another advantage of this process is that it reduces the exhaust noise to a minimum and requires cheap technology.
  • Figure-2 shows the method's evaluation of the chimney heat and shows the graphic of the refinement method.
  • 17 no thin cupper pipes have been inserted into the mass chimney heat boilers and these pipes have the same dimension and amount and have been welded with 18 no plate. Because 17 no pipes are subject to corrosion and need cleaning the boilers were installed distanced and this distance was completed and fixed with 19 no plates and 6 no bolts to the boilers. Similar 17 and 18 no pipes and plate blocks are inserted with 6 no bolts into the 21 no climate block. 20 no fan is located through 25 no pipe on the 21 no climate block and system.
  • 25 no pipe which provides that the gases remaining as a result of the refinement are sent to a second 20 no fan system, is mounted on the 27 no refinement water tank with the 20 no fan.
  • 25 no chimney which provides that the remaining gases are left into the atmosphere after the second and third refinement system which repeat the same refinement procedure, is mounted on the third 27 no refinement system.
  • the chimney gases are passed through the 17 no cupper pipes in the chimney heat boilers and the chimney gases heat is transferred through isolation to the water in the chimney heat boilers.
  • Water cooled down to 30-40 degrees is passed through 17 no thin cupper pipes within the 21 climate blocks and its heat is further decreased by climatizing through the 20 no fan.
  • Water warming up after climatizing is sent to the furnace by the 20 no climate fan through the 25 pipe as extra air.
  • the extra air given in order to realize effective combustion the heat lost with the chimney is reduced to minimum with the hydrogen in the fuel and air and the humidity rate in the air (especially in winter).
  • the chimney gases are absorbed by the 20 no chimney gas absorbing fan installed at the exit of the 17 no pipes within the 21 no climate block and is then pumped into the water at equal pressure through the 17 no thin pipes which are installed as said with the 18 no plate included in the water and the chimney gases components are contacted at maximum with water and thus the said reactions are realized and the Claimed refinement is completed. Clean water coming from the 22 no pipe further decreases the chimney gases, whose heat is dropped, and the overflow of the dirty water is caused. Thus there are no more acid steams and toxic chimney gas components. The said steam and components are refined at minimum with the second and third (illustrated in graphics) repetition of the said refinement method. At the end of the refinement gases such as 2 , H > N 2 are released into the atmosphere through the 25 chimney pipe.
  • the dirty water is transferred to the 26 no dirty water tank through the 23 no dirty water pipe.
  • the dirty water is released from the 24 mouth of the 30 no spiral at the immediate exit of the 29 furnace to the 30 no horizontal spiral with the 23 dirty water pipe which is located between the 24 ash spiral mouth (horizontal spiral providing the ash discharge procedure by taking the ashes falling under the room) and the 23 dirty water pipe and thus the ashes are wet.
  • Wet ashes are filled into the 32 no ash silo through the 31 no inclined spiral. 50
  • the transfer of the ashes from the 10 no valve of the 32 no ash silo which is mounted in the air to special trucks is facilitated and they are carried to the ash storing center by preventing their spreading into the environment.
  • the application of the refinement method at exhausts uses stagnant water in the dirty water tank.
  • the exhaust gases cooled down by the air conditioner are absorbed by the fan and pumped into the stagnant water.
  • the heated water is cooled down by the thin pipes which are connected to the radiator and which are inserted into the said water tank.
  • the dirty water is transferred during fueling at the fuel station into the special tank and exchanged with clean water. Collected waste water is carried to the said heat transfer thermal power plants and destroyed through the said methods. This method is explained in detail in the attached drawings.
  • FIG. 3 The illustration of the vehicle exhaust gases refinement system ancf wetting of the ashes with waste waters.
  • Figure-3 The illustration of the vehicle exhaust gases refinement system ancf wetting of the ashes with waste waters.
  • Stagnant water is filled into the 27 no dirty water tank.
  • the block consisting of the said 17 no thin pipes and 18 no plates.
  • 25A no cold water pipe is inserted. 25 no pipe is furnished between the exit of
  • the exhaust gases in the 21 climate block are climatized entering through the 25 no pipe and the heated air is released to the atmosphere by the 20 no fan.
  • the heat of the stagnant refinement water, which is heated with the exhaust gases are cooled down by isolating through the cold water passing from the said 17 no thin pipe block in the stagnant water filled into the 27 no water tank to the block from the 25A cold water pipe connected to the radiator return and pumping it to the radiator from the 25 pipe connected to the block exit and the radiator.
  • Hot water which returns through the 25 no pipe at the end of the said system is cooled by the radiator and the procedure is completed.
  • the said procedure O is performed continuously as long as the engine of the motor operates.
  • the pipe Q height which discharges the gases remaining after the 25 no refinement procedure is arranged according to appropriate standards.
  • the good quality of the vehicle fuels and reduced exhaust gases the refinement load is low. Therefore the said refinement mass shall be small. Therefore the volume of the said refinement system, deformations at the vehicles and its weight do not create any loading problems.
  • the clean water filling procedure at the station shall be performed according to the amount of the 27 no stagnant water tank which is determined as standard (automobile, truck, bus, etc. standard 27 no stagnant water tank).
  • This method sends the coal by removing the humidity after:the coal, which is crushed into dust in order to remove the humidity of the coal products, is heated to 110 degrees and its feature is that the coal heated through a horizontal spiral is sent into the environment, which is cleared of steam.
  • a block is mounted on the horizontal spiral and a fan and the said chimney gas refinement system is mounted on the block.
  • a harmful cytochiometric emission which may arise with the humidity of the dried coal is made harmless through the said refinement method.
  • dry coal is obtained for the Claimed effective combustion reaction. This method is explained in detail in the attached drawings.
  • no fan is mounted between the Q no cell and the 28 no cyclone with 25 no pipes.
  • a 14 no emission mouth at appropriate standards is opened.
  • a second 20 no fan smaller than the first 20 no fan is mounted with 25 no pipes.
  • the humid air is passed via the first 20 no fan through the Q cell and heated up to 110 degrees.
  • the said heated air is passed through 25 no pipes, on which the 20 no mounted fan is mounted, and sent to the 28 no cycloning tank.
  • the steam of the humid hot air which gets the possibility of expansion in the said tank it rises with kinetic pressure to the 14 no emission of the 28 no tank and released to the atmosphere through the said mouth.
  • the hot air which is formed as a result of the cooling procedure by climatizing the chimney gases is decomposed from its humidity with the said method. Besides the hydrogen in the air can be partially controlled and thus the negative impact of the transformation of the hydrogen into water steam in the ' combustion room is prevented.
  • the 25 no pipe is mounted between the heating environment and the 30 no horizontal spiral and the 21 no cycloning block is mounted on the 30 no horizontal spiral.
  • the washing system refinement system and the 20 no fan is mounted on the said block.
  • the said horizontal spiral is mounted on the 25 pipe, which is mounted between the 21 no block and the 28 cycloning and the 20 no 2. fan.
  • the coal dust heated to 110 degrees is sent in the closed system from the 25 no pipe to the 30 no horizontal spiral, the humid of the heated fuel spreads over to the 21 block (it is open after having entered the block on the horizontal spiral), which is mounted on the said spiral and is absorbed (without damaging the coal dust) by the 20 no refinement fan, which is mounted on the said block and thus the refinement is facilitated. And a thin cytochiometric coal emission which may be formed together with the humidity is refined with the said washing system refinement method is increased and thus prevents pollution.
  • Dried dust coal is sent to the combustion room together with the dried air mixture through the 20 no fan which is mounted between the 28 cycloning tank and the 29 combustion room by the 30 horizontal spiral and thus effective combustion reaction is realized.
  • This method may be used at appropriate standardized sized vehicles.
  • said washing system refinement method by cycloning and drying the hot water which is obtained through the cooling of the exhaust gases as said and by burning it as a mixture of fuel and dried air the said negative impacts can be prevented.
  • the atmosphere and nature shall be freed from the big negative impacts caused by the said pollution and the atmosphere and nature shall return gradually to its natural condition before the industrial revolution.
  • the soil shall return to its chemical balance, which will cause increase in productivity, with the decrease in artificial fertilizers the formation of diazotoxics the said negative impacts will be minimized.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Drying Of Solid Materials (AREA)
  • Treating Waste Gases (AREA)

Abstract

La présente invention a pour objet de supprimer les besoins d'apport de chaleur dans des systèmes de chauffage, dans le cadre d'un procédé de transfert de chaleur, afin de réaliser un chauffage par acheminement d'eau chaude avec des systèmes de réservoirs, d'une installation centrale à l'extérieur de l'établissement, à des réservoirs dans un centre à systèmes de chauffage régional, l'eau de réseau de chauffage central provenant de flux d'entrée de circulation (X) et étant chauffée jusqu'à des blocs d'entrée (2) via des conduites d'entrée (1), des blocs d'entrée (2) à des blocs de retour (4) avec conduites (3), et des blocs de retour (4) à une conduite de retour de circulation (Y) via des conduites de retour (5). Afin d'éviter les pertes de chaleur par émission au cours du remplissage et du vidage d'eau chaude, une gaine inflammable (8) est disposée entre les ouvertures d'émission du réservoir (14) et du réservoir (13). Dans des systèmes de raffinage de cheminée, afin de limiter les gaz de cheminée sur le système de filtrage d'air de système de lavage, les gaz de cheminée provenant du système de sortie des conduites (17) de bloc de climatisation (21) de ventilateur (20), sont absorbés par le ventilateur (20) et pompés par les conduites (17) dans l'eau dans un réservoir d'eau de raffinage (27). Lesdites conduites sont fixées au ventilateur (20), à l'extrémité de conduite (25) avec une plaque (18). Des eaux usées ainsi produites, sont détruites par mélange dans les cendres d'une spirale de cendres horizontale (30). Ainsi, les cendres ne sont pas dispersées dans l'environnement et dans l'air. Dans le cadre du procédé pour éviter les pertes de chaleur avec de l'air humide, et pour réaliser une combustion efficace, de l'air humide est chauffé dans une cellule (Q) et alimente un réservoir de cyclonage (28). L'air en circulation dans ledit réservoir sous l'effet de la pression cinétique, est séché par décomposition avec une ouverture d'émission (14). L'air alimente alors une chambre de combustion (29) avec le mélange de poussière de charbon séché avec un procédé similaire. Comme de la lignite de qualité peut être brûlée, la production s'avère économique.
PCT/TR2005/000023 2004-05-17 2005-05-11 Procede de transfert thermique et de filtrage d'air WO2005111510A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
TR2004/01168 2004-05-17
TR200401168 2004-05-17

Publications (2)

Publication Number Publication Date
WO2005111510A2 true WO2005111510A2 (fr) 2005-11-24
WO2005111510A3 WO2005111510A3 (fr) 2006-08-03

Family

ID=34969269

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/TR2005/000023 WO2005111510A2 (fr) 2004-05-17 2005-05-11 Procede de transfert thermique et de filtrage d'air

Country Status (1)

Country Link
WO (1) WO2005111510A2 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113144762A (zh) * 2021-03-29 2021-07-23 宁夏淼漫游泳有限公司 一种防排气管进水水箱式净化器
CN114719902A (zh) * 2022-03-25 2022-07-08 河北邯峰发电有限责任公司 智能型风量风压测量试验方法

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3906874A (en) * 1973-08-30 1975-09-23 Nutmeg Sanitation Inc Mobile furnace vehicle
DE3130165A1 (de) * 1981-07-30 1983-02-24 Jakob 7954 Bad Wurzach Altvater Verfahren zur fernuebertragung von waermeenergie
DE3519087A1 (de) * 1985-05-28 1986-12-04 Jakob 7954 Bad Wurzach Altvater Verfahren sowie anordnung zum be- oder entladen eines luftempfindlichen mediums
EP0328990A2 (fr) * 1988-02-18 1989-08-23 Siemens Aktiengesellschaft Dispositif et procédé de purification de matières granuleuses ou pâteuses, notamment de sols
EP0464285A1 (fr) * 1990-07-02 1992-01-08 Chun-Teh Chen Dispositif pour la purification de gaz
GB2252817A (en) * 1990-12-14 1992-08-19 George Michael Ettinger Heat transport apparatus
FR2742218A1 (fr) * 1995-12-08 1997-06-13 Bernier Jacques Dispositif de stockage mobile de chaleur ou de froid
WO2001083955A1 (fr) * 2000-05-02 2001-11-08 Yukio Toyama Epurateur pour les gaz d'echappement d'un moteur diesel

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59125350A (ja) * 1982-12-29 1984-07-19 Matsushita Electric Ind Co Ltd 湯沸装置

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3906874A (en) * 1973-08-30 1975-09-23 Nutmeg Sanitation Inc Mobile furnace vehicle
DE3130165A1 (de) * 1981-07-30 1983-02-24 Jakob 7954 Bad Wurzach Altvater Verfahren zur fernuebertragung von waermeenergie
DE3519087A1 (de) * 1985-05-28 1986-12-04 Jakob 7954 Bad Wurzach Altvater Verfahren sowie anordnung zum be- oder entladen eines luftempfindlichen mediums
EP0328990A2 (fr) * 1988-02-18 1989-08-23 Siemens Aktiengesellschaft Dispositif et procédé de purification de matières granuleuses ou pâteuses, notamment de sols
EP0464285A1 (fr) * 1990-07-02 1992-01-08 Chun-Teh Chen Dispositif pour la purification de gaz
GB2252817A (en) * 1990-12-14 1992-08-19 George Michael Ettinger Heat transport apparatus
FR2742218A1 (fr) * 1995-12-08 1997-06-13 Bernier Jacques Dispositif de stockage mobile de chaleur ou de froid
WO2001083955A1 (fr) * 2000-05-02 2001-11-08 Yukio Toyama Epurateur pour les gaz d'echappement d'un moteur diesel

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN vol. 008, no. 249 (M-338), 15 November 1984 (1984-11-15) & JP 59 125350 A (MATSUSHITA DENKI SANGYO KK), 19 July 1984 (1984-07-19) *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113144762A (zh) * 2021-03-29 2021-07-23 宁夏淼漫游泳有限公司 一种防排气管进水水箱式净化器
CN114719902A (zh) * 2022-03-25 2022-07-08 河北邯峰发电有限责任公司 智能型风量风压测量试验方法

Also Published As

Publication number Publication date
WO2005111510A3 (fr) 2006-08-03

Similar Documents

Publication Publication Date Title
Harrison Understanding our environment: an introduction to environmental chemistry and pollution
Dincer Energy and environmental impacts: present and future perspectives
Dara et al. A textbook of environmental chemistry and pollution control
Cheremisinoff Pollution control handbook for oil and gas engineering
Byrne et al. Energy and environment: The policy challenge
WO2005111510A2 (fr) Procede de transfert thermique et de filtrage d'air
Curley New thinking about pollution
Al-Taai et al. Air Pollution: A Study of Its Concept, Causes, Sources and Effects
Flower Environmental pollution-especially air pollution-and public health
Butenova et al. The impact of waste from thermal power plants on the natural environment
Dincer et al. Current and future perspectives on energy use and environmental impact
de las Heras Air Pollution and Anthropogenic Climate Change
Ning PREVENT AND ELIMINATE ENVIRONMENTAL DAMAGE
Golomb et al. Atmospheric impact of the fossil fuel cycle
Ying Study on building a good ecological environment by controlling urban air pollution
Kaushika et al. Energy Environment Interactions
Gerson The environmental effects of air pollution from the energy sector in South Africa
Winkler et al. Weathering agents
Nowicki Air quality protection
Veliu et al. Air pollution with particulate matter and heavy metals of Kosova Thermal power plant
Ioana-Alina et al. Monitoring the Best Available Techniques Implementation at the Ash and Slug Landfill Utvin, Timis County, Romania
Blasing et al. Potential effects of clean coal technologies on acid precipitation, greenhouse gases, and solid waste disposal
James Coal, Environment and Health
Medved Applied Energy and Resource Management in the Urban Environment
Biasing et al. Potential consequences of the clean coal program for air and waste issues

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A2

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KM KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NG NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A2

Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase in:

Ref country code: DE

WWW Wipo information: withdrawn in national office

Country of ref document: DE

122 Ep: pct application non-entry in european phase