MXPA96000261A - Rotating reactor for precise nixtamalization demaiz that does not break the grain, does not produce naxayoteni genera contaminante alg - Google Patents
Rotating reactor for precise nixtamalization demaiz that does not break the grain, does not produce naxayoteni genera contaminante algInfo
- Publication number
- MXPA96000261A MXPA96000261A MXPA/A/1996/000261A MX9600261A MXPA96000261A MX PA96000261 A MXPA96000261 A MX PA96000261A MX 9600261 A MX9600261 A MX 9600261A MX PA96000261 A MXPA96000261 A MX PA96000261A
- Authority
- MX
- Mexico
- Prior art keywords
- grain
- nixtamalization
- reaction chamber
- jacket
- reaction
- Prior art date
Links
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 239000000356 contaminant Substances 0.000 claims abstract description 8
- 230000005540 biological transmission Effects 0.000 claims abstract description 7
- 238000004064 recycling Methods 0.000 claims abstract description 6
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims abstract description 5
- 235000005822 corn Nutrition 0.000 claims abstract description 4
- 235000005824 corn Nutrition 0.000 claims abstract description 4
- 240000008042 Zea mays Species 0.000 claims description 3
- 235000013339 cereals Nutrition 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- 235000015097 nutrients Nutrition 0.000 claims description 3
- 235000012184 tortilla Nutrition 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 claims description 2
- 238000005461 lubrication Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 239000011490 mineral wool Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 241000863929 Naxa Species 0.000 claims 1
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 239000002131 composite material Substances 0.000 claims 1
- 229910052500 inorganic mineral Inorganic materials 0.000 claims 1
- 235000009973 maize Nutrition 0.000 claims 1
- 239000011707 mineral Substances 0.000 claims 1
- 235000016709 nutrition Nutrition 0.000 claims 1
- 230000003449 preventive Effects 0.000 claims 1
- 241000894007 species Species 0.000 claims 1
- 230000002459 sustained Effects 0.000 claims 1
- 229920002456 HOTAIR Polymers 0.000 abstract description 4
- 238000010411 cooking Methods 0.000 abstract description 3
- 241000209149 Zea Species 0.000 abstract 2
- 239000002699 waste material Substances 0.000 abstract 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000000292 calcium oxide Substances 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 1
- 229940029983 VITAMINS Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 230000001066 destructive Effects 0.000 description 1
- 235000019621 digestibility Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000003301 hydrolyzing Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 230000000737 periodic Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 230000003381 solubilizing Effects 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 238000004326 stimulated echo acquisition mode for imaging Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229930003231 vitamins Natural products 0.000 description 1
Abstract
The present invention refers to a rotating reactor for nixtamalization of corn that does not break the grain, does not produce naxayote, does not generate contaminants, has a reaction chamber or container heated by thermal oil heated in turn by hot air produced by a gas oven LP, equipped with a pressure eliminator system and hot gas recycler characterized in that, a reaction chamber is surrounded by a first thermal oil jacket connected to a pressure eliminator system, a second hot air jacket produced by a gas oven LP, involves the oil and the reaction chamber, having a hot gas recycling system, all arranged in such a way that we will obtain a new system to transmit exact temperature for a definite time to a reaction chamber or precise cooking using oil thermal and hot air as a means of heat transmission all this equipped with a transmission system variable rotation as appropriate, which allows an exact and stoichiometric reaction in the nixtamalization of corn to avoid waste or contaminants.
Description
ROTATING REACTOR FOR PRECISE NIXTAMALIZATION OF MAIZE THAT DOES NOT
BANK THE GRAIN, DOES NOT PRODUCE NAXAYOTE NOR GENERATE CONTAMINANT SOME
D ES CR IP CI ON
BACKGROUND OF THE INVENTION. ALREADY ILLESCAS IN 1943, IN THE MAGAZINE OF THE MEXICAN SOCIETY OF NATURAL HISTORY, WROTE THEIR "CHEMICAL THEORY OF THE FORMATION OF NIXTAMAL", WHERE EXPRESSED: "WHEN THE TIME OF COOKING THAT IS GIVEN TO MAIZE DURING NIXTAMALIZATION IS VERY SHORT, VERY LOOSE MASSES ARE OBTAINED, WHICH CAN NOT BE MOLDED WITHOUT UNBLOCKING, THIS IS BECAUSE THEY DO NOT HAVE STRIPS, OR THAT ARE MISSING WHAT CAN BE CALLED SUFFICIENT REACTION GIVEN BY A MIXTURE OF ZEINE AND GLUTELINE, WHICH, AS A MATTER OF LEAGUE, DAN THE COHESION BETWEEN THE CELLULOSIC RESIDUES AND STARCH, IF THE TIME WAS VERY LONG, YOU GET CHEETOUS MASSES THAT CAN NOT BE TORNED, (FORM THE TORTILLA) FOR BEING STICKY AND ADHERING TO ANY SURFACE WITH WHICH YOU GET IN CONTACT. THE CALACING OF CALLE ACTS ON THE AMYLOURONIDS (HEMILCELULOSAS), HYDROLYZING
APPROXIMATELY 50% .- ON LIPIDS HAS A SOLUBILIZING ACTION, THERE IS A LOSS OF 12 TO 15% OF THE ETHERIC EXTRACT WHEN THE CORN IS TRANSFORMED IN NIXTAMAL. ON THE PROTEINS, THERE IS A HYDROLYZATION WITH VERY SMALL SOLUBILIZATION. ABOUT THE COLORANTS, BY THEIR ALKALINITY, INTENSIFIES THE COLOR OF THE FLAVONIC DERIVATIVES BY ALSO VARYING THE ANTHOCYANINE ON THE HYDROSOLUBE VITAMINS, HAS A DESTRUCTIVE ACTION.
DESPITE THE ALMOST FIFTY YEARS THAT HAVE HAPPENED FROM THIS THEORY, THE EQUIPMENT OF THE NIXTAMALIZATION INDUSTRY, ESPECIALLY THE ONE DEDICATED TO THE ALKALINE COOKING IN ITSELF, HAS HAD VARIATIONS ONLY LOOKING FOR OPTIMUM USE OF THE HEAT AND AN EASE OF USE FOOD AND DISCHARGE. THERE ARE EQUIPMENTS IN WHICH THE HEATING IS DIRECT FIRE, HEATING UP TO WATER THE WATER WITH THE LIME FOR ADDING THE MAIZE AND REVOLVE EVERYTHING, REMOVING THE FIRE IMMEDIATELY, AND LEAVING TO REST WITH PERIODIC MANUAL MOVEMENTS TO AVOID THE SETTING OF THE CAL. THIS TYPE OF REACTORS ARE SIMPLE AND CONSIST ONLY IN A METAL CONTAINER. THE LOAD AND DISCHARGE IS COMPLETELY MANUAL AND REQUIRES AN ADDITIONAL CONTAINER TO SEPARATE THE GRAIN OF THE NAXAYOTE OR RESIDUAL BROWN, WHICH CONSTITUTES AN EFFLUENT OF HIGHER CAPACITY POLLUTANT OF THE ENVIRONMENT FOR HIGH CONTENT OF CAL.
THERE ARE ALSO REACTORS IN WHICH THE REQUIRED HEAT IS PROVIDED THROUGH A STEAM JACKET, THIS IS THE ONLY STRUCTURAL DIFFERENCE WITH RESPECT TO PREVIOUSLY USED REACTORS
IN ALL THESE REACTORS TWO BASIC PROBLEMS ARE PRESENTED, ONE RELATED TO SOLUBILITY OF THE CALCIUM OXIDE AND THE OTHER RELATED TO THE TRANSFER OF HEAT FROM THE CONTAINER TO THE BOTTOM OF THE MAIZ-AGUA-CAL SYSTEM AND THE
, MORE EXTERIOR LAYERS OF THE SYSTEM TO THE MOST INTERIOR OF THE SAME. THE CALCIUM OXIDE, HAS A VERY LOW SOLUBILITY AND THE MAJOR PART IS PRECIPITATIVE ORIGINATING PARTS OF THE SYSTEM WITH EXCESS OF OXIDE AND PART OF THE SAME WITH A VERY WEAK CONCENTRATION.
. WITH REFERENCE OF THE TRANSFER OF THE HEAT, THIS IS CARRIED OUT IN TWO WAYS, SINCE THE RADIATION CAN BE DESPISED, ONE BY DRIVING (BETWEEN THE WALLS OF THE REACTOR AND THE OUTER LAYERS OF THE WATER-MAIZE SYSTEM- CAL) THE OTHER BY CONVECTION , THE ONE THAT IS ESTABLISHED BETWEEN THE. MORE FOREIGN LAYERS AND THE MORE INTERNAL. THE TRANSMISSION OF THE HEAT BY CONVECTION IS ENOUGH SMALL IN THE CURRENT REACTORS.
SUBSEQUENTLY WITH RECORD NUMBER 01982, ON NINE DAY OF APRIL ONE THOUSAND NINE HUNDRED NINETY TWO AND TWO, I PROVIDE A MORE MODERN TYPE OF REACTOR EXPLICITLY DESCRIBED IN THE BODY OF THE APPLICATION OF THAT DATE, SAME AS I WORKED IN THE ARCHIVE OF THAT H. INSTITUTE AND CURRENTLY CONSIDERED AS ABANDONED.
NOW, IN THIS NEW AND MORE EFFICIENT REACTOR, A BETTER DISTRIBUTION AND USE OF THE ENERGY THROUGH A THERMAL SPECIFICATION OIL JACKET IS AVAILABLE AROUND ALL THE REACTOR IN ADDITION TO A HOT AIR FREE TRANSIT JACKET INTENDED TO DELIVER THE CONTROLLED TEMPERATURE, WITHOUT HAVING TO DO IT DIRECTLY FROM THE OVEN IN ADDITION TO HAVING IT PROVIDED OF A SYSTEM TO ELIMINATE GASES THAT GENERATE PRESSURE BY OBTAINING A CONSTANT TEMPERATURE WITHOUT VARIATION OF ANY NATURE. IN THE SAME WAY, EVERY INTERNAL ELEMENT HAS BEEN ELIMINATED IN THE REACTOR REACTION CHAMBER, SUCH AS ALAVES, ELEVATORS, SPIRALS, ETC. WITH THE PURPOSE OF PREVENTING THE GRAIN FROM BREAKING BY THE EFFECT OF THE FRICTION, SINCE WE KNOW THAT THE BROKEN GRAIN IS NOT NIXTAMALIZABLE AND ORIGINS BIG LOSSES IN BIRDS BY EXCESS OF NIXTAMALIZATION, WHENEVER THE BROKEN GRAIN COMES IN IMMEDIATE REACTION BY THE STARCHES EXPOSED ORIGINATING A PREMATURE NIXTAMALIZATION WITH RESPECT TO THE REST OF THE MATERIAL PRESENT IN THE REACTION.
IN THIS WAY THE EQUIPMENT HAS REMAINED WITH A MEDIUM CAPACITY BETWEEN 2.5 TO 3.0 TONS OF MAIZE BY TANDA OR BACHE, WORKING AT A HALF TEMPERATURE BETWEEN 70 AND 100 ° CA WILL IN THE REACTION CHAMBER (1), THERMAL OIL JACKET THAT PREVENTS ANY VARIATION (DESCENT OR ELEVATION) OF THE TEMPERATURE TO HAVE A HOMOGENEOUS REACTION (2), HOT AIR JACKET FOR FREE TRANSIT WITH OVEN RECYCLING FOR VERY IMPORTANT FUEL SAVING (3), MINERAL WOOL ENVELOPE FOR, TEMPERATURE CONSERVATION (4), PRESSURE ELIMINATION SYSTEM TO ACHIEVE AN OPEN SYSTEM (14), ENGINE AND TRANSMISSION SYSTEM (5), BEARING TRACK (6), DRIP FOR CONSTANT TRANSMISSION LUBRICATION (7), CHARGING GATE (8) ), GASKET WITH ANTI-TOOTHING SEAL FOR
. DISCHARGE (9), DUCT FOR RECYCLING HOT AIR (10),
INJECTION OF OXYGEN TO THE FLAME (11), BURNER FOR GAS L.P. (12), COMBUSTION OVEN FOR AIR HEATING (13), ASSEMBLY CHASSIS (15) AND SUPPORT BALL (16).
OF VERY SPECIAL ATTENTION RESULTS THE FACT THAT THIS. ^ REACTOR EQUIPMENT FOR NIXTAMALIZATION OF CORN, FOR THE TECHNICAL ADVANCES THAT HAVE BEEN INCORPORATED, IN NO EVENT BANKRUPTCY OR ELIMINATES THE FIBER CONSTITUTIVE OF THE PERCHARP ENVELOPE OF THE GRAIN, ALLOWS A REACTION ESTRYOMETRICALLY CALCULATED THAT DOES NOT PRODUCE ANY 'MERMA AND OBTAINS A NIXTAMALIZED GRAIN TO EXACT NEED WITH ALL NUTRIENTS OF CORN PRESENT WITHOUT ANY LOSS, WHICH IS TRANSLATED INTO AN INTEGRALLY NIXTAMALIZED CORN THAT CONTAINS ALL OF ITS INTACT NUTRIENTS, PASSING THEM 100% TO THE MASS AND FINALLY TO THE TORTILLA, WHICH IS ENRICHED NUTRITIONALLY WITH FIBER DE VERY HIGH DIGESTIBILITY AND LOW IN LIGNINA, ELEVATION OF THE BELT AND MUCH MORE ADVANTAGEOUS FEATURES IN CONSERVATION, TASTE AND ODOR FOR THE FINAL CONSUMER, DOES NOT PRODUCE CONTAMINANT OF ANY KIND, DOES NOT RELEASE EFFLUENTS, DO NOT FREE GASES AND ONLY USE 30% OF THE WATER CURRENTLY USED IN THIS PROCESS.
HAVING DESCRIBED THE INVENTION IS CONSIDERED AS A NOVELTY AND IT IS CLAIMED BY BOTH AS PROPERTY WHICH IS CONTAINED IN THE FOLLOWING:
Claims (2)
- R EI VIND I CA CI ONES L- ROTATING REACTOR FOR PRECISE NIXTAMALIZATION OF MAIZE THAT DOES NOT BREAK THE GRAIN, DOES NOT PRODUCE NAXAYOTE NOR GENERATE ANY CONTAMINANT, CHARACTERIZED BY HAVING A CHAMBER OF ROTATING REACTION WITHOUT WAVE, SPIRALS, CONVEYORS, ELEVATORS, FIXED BODIES OR, INTERNAL MOBILE DESIGNED TO MOVE THE GRAIN DURING THE REACTION; A FIRST TEMPERATURE TEMPERATURE THERMAL OIL JACKET CONNECTED TO A PRESSURE ELIMINATING SYSTEM AND INVOLVING THE ENTIRE REACTION CHAMBER; A SECOND HOT AIR JACKET WITH RECYCLING TO THE OVEN GENERATOR OF THE AIR MIXTURE AND HOT GASES, WHICH INVOLVES THE THERMAL OIL JACKET PLUS THE REACTION CHAMBER AND FINALLY, A THERMAL WOOL COAT , ALUMINUM LINED MINERAL, PLACED AS FINAL ENVOL VENTE TO ALL THE TEAM BODY.
- 2. - ROTATING REACTOR FOR PRECISE NIXTAMALIZATION OF MAIZE THAT DOES NOT BREAK THE GRAIN, DOES NOT PRODUCE NAXAYOTE NOR GENERATE ANY CONTAMINANT, WHICH IS CHARACTERIZED BECAUSE SUCH AS IT WAS CLAIMED IN. THE PREVIOUS CLAUSE, THE REACTION CHAMBER IS ROTATING WITHOUT INTERNAL ELEMENTS AS IT CAN BE WIRELESS, SPIRALS, CONVEYORS, ELEVATORS OR FIXED OR MOBILE BODIES INTENDED TO MOVE THE GRAIN DURING THE REACTION 0. THE REACTION CHAMBER IS TOTALLY WRAPPED BY A FIRST JACKET THAT CONTAINS THERMAL SPECIFIED OIL, OF UNIVERSAL SPECIFICATIONS, SUSTAINED AT A TEMPERATURE BETWEEN 200 AND 210 5. CENTRAL GRADES AND CONNECTED TO A PRESSURE ELIMINATING SYSTEM THAT DOES NOT ALLOW ANY COLLAPSE OR INTERNAL PRESSURE TO OCCUR AT ANY TIME. or THE OBJECT OF THIS FIRST JACKET IS TO KEEP THE REACTION CHAMBER AT A TEMPERATURE BETWEEN 80 AND 100 CENTRAL CONGRESSED DEGREES. SUMMARY A SPECIFIC MECHANICAL STRUCTURE FOR THE PRECISE NIXTAMALIZATION OF MAIZE, CONTROLLED, IS DESCRIBED 5 < BY MEANS OF MECHANICAL MOVEMENT WITH FREE REACTION CHAMBER OF INTERNAL MECHANICAL ELEMENTS WRAPPED AND HEATED BY A FIRST THERMAL OIL JACKET, HEATED IN TIME BY A SECOND HOT AIR JACKET GENERATED IN? n A OVEN WITH RECYCLING AND IS PROVIDED WITH A PREVENTIVE PRESSURE ELIMINATING SYSTEM OF OVER INTERNAL PRESSURES IN THE EQUIPMENT, MAKE THE MOST OF THE MATERIALS SUBJECTED TO REACTION UNTIL POSSIBILITIES OF PRECISION BY CALCULATION 15, ESTEQUIOMETRIC, DOES NOT PRODUCE CONTAMINANTS OF ANY NATURE, DOES NOT BREAK THE GRAIN IN ABSOLUTE, THEREFORE NOT CAUSE MERMA OF ANY SPECIES, DO NOT DETACH THE PERICARPIO OF CORN ALLOWING A NIXTAMALIZATION OR 100% REACTION, 20, WHAT IS TRANSLATED IN A PERFECTLY COMPOSITE NIXTAMALIZED GRAIN THAT ALLOWS TO OBTAIN A NUTRITIONAL COEFFICIENT MUCH HIGHER THAN THE KNUNTIL TODAY FOR CONTAINING ALL THE NATURAL NUTRIENTS OF THE MAIZE BEING USED IN THE MASS AND FINALLY IN THE 25, TORTILLA. ROTATING REACTOR FOR PRECISE NIXTAMALIZATION OF MAIZE THAT DO NOT BREAK THE GRAIN, DO NOT PRODUCE NAXA YOTE NOR GENERATE CONTAMINANT. ANY0. L- REACTION CHAMBER 2.- THERMAL OIL JACKET (2") 3. - HOT AIR JACKET (2") 4. - MINERAL WOOL WIND ENVELOPE (2") 5.- ENGINE AND TRANSMISSION SYSTEM 5. 6 .- TRACK 7.- DRILL FOR TRANSMISSION LUBRICATION 8.- LOADING 9.- DISCHARGE 10.- HOT AIR RECYCLING DUCT OR 1L- OXYGEN INJECTOR 12.- BURNER 13.- COMBUSTION OVEN 14.- BREATHER REMOVAL OF PRESSURE 15.- CHASSIS 5.
Priority Applications (11)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ZA9705957A ZA975957B (en) | 1996-07-05 | 1997-07-03 | Method to control the use of a pager, pager working according to this method and chip card for conditional access to a pager. |
BR9711000-0A BR9711000A (en) | 1996-07-05 | 1997-07-04 | Method for controlling the use of pager, pager operating with this method and card for restricted access to a pager |
AU35475/97A AU3547597A (en) | 1996-07-05 | 1997-07-04 | Method for controlling the use of a pager, pager operating with this method and chip card for conditioned access to pager |
DE69703185T DE69703185D1 (en) | 1996-07-05 | 1997-07-04 | Method for controlling the use of a pager, pager working according to this method and chip card for conditional access of a pager |
AT97401610T ATE196696T1 (en) | 1996-07-05 | 1997-07-04 | METHOD FOR CONTROLLING THE USE OF A PALLER, PALLER OPERATING ACCORDING TO THIS METHOD AND CHIP CARD FOR CONDITIONAL ACCESS TO A PALLER |
PCT/FR1997/001209 WO1998001836A1 (en) | 1996-07-05 | 1997-07-04 | Method for controlling the use of a pager, pager operating with this method and chip card for conditioned access to a pager |
RU99102178/09A RU99102178A (en) | 1996-07-05 | 1997-07-04 | METHOD FOR CONTROLLING USE OF A MESSAGE TRANSMISSION DEVICE (PAGER), A MESSAGE TRANSMISSION DEVICE AND A CARD WITH AN INTEGRATED IC FOR ACCESS TO A MESSAGE TRANSMISSION DEVICE |
CA002259528A CA2259528A1 (en) | 1996-07-05 | 1997-07-04 | Method for controlling the use of a pager, pager operating with this method and chip card for conditioned access to a pager |
EP97401610A EP0817144B1 (en) | 1996-07-05 | 1997-07-04 | Method to control the use of a pager, pager functioning with this method and ic card for conditional access to a pager |
CN97197398.9A CN1228861A (en) | 1996-07-05 | 1997-07-04 | Method for controlling use of pager, pager operating with this method and chip card for conditioned access to pager |
ARP970103020A AR007817A1 (en) | 1996-07-05 | 1997-07-07 | A METHOD FOR CONTROLLING THE USE OF A CALLER FOR MOBILE PERSONAL COMMUNICATIONS, A CALLER FOR TAKING PRACTICE OF SUCH METHOD AND A CARD FOR ACCESS TO SUCH CALLER |
Publications (1)
Publication Number | Publication Date |
---|---|
MXPA96000261A true MXPA96000261A (en) | 1997-12-01 |
Family
ID=
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201964423U (en) | Pyrolysis and pyrolysis gas secondary combustion integral burning equipment | |
CN201322307Y (en) | Multifunctional incinerator | |
TWI439604B (en) | Method and apparatus for burning and working of solid fuel powder into open combustion gas turbine burner. | |
MXPA96000261A (en) | Rotating reactor for precise nixtamalization demaiz that does not break the grain, does not produce naxayoteni genera contaminante alg | |
CN104654311B (en) | A kind of marine incinerator processing system | |
US4270466A (en) | Method and apparatus for rendering an ignitable fuel-oxygen mixture inert | |
RU2477819C2 (en) | Rotor furnace for pyrolysis of solid domestic wastes | |
US4892560A (en) | Fuels | |
GB2060848A (en) | Wood burning system and method | |
CN207405125U (en) | A kind of horizontal biomass reacting furnace | |
DE3572528D1 (en) | Apparatus for direct firing | |
CN109210546A (en) | A kind of incineration plants material hole refuse processing method | |
AU2855601A (en) | Method and device for the autocombustion of oily organic waste, comprising a tangential heating furnace | |
US5353720A (en) | Refuse incinerator | |
CN107726300A (en) | A kind of energy-saving combustion boiler | |
CN208169797U (en) | A kind of production wellhead pipe heating device | |
SE8207193D0 (en) | DEVICE FOR COMBUSTION OF GRANULATED MATERIAL | |
CN207006173U (en) | Flammable solid waste pyrolytic gasification-swirl flow combustion system | |
CN102278204A (en) | Powdery solid fuel combustion and work application method and device | |
CN215446474U (en) | Internal heating type converter linkage state secondary combustion chamber for hazardous waste disposal | |
WO1996036472A1 (en) | Method of reprocessing rubber waste materials | |
CN104501200A (en) | Biomass micron fuel high temperature clean combustion method based on adiabatic combustion condition | |
CN204853449U (en) | Aluminium liquid that uses biofuel dissolves stove | |
CN220062569U (en) | Heating and reducing treatment pry for oil-containing solid waste by utilizing waste heat | |
CN202303405U (en) | Novel horizontal combustion furnace |