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 alg

Info

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
Application number
MXPA/A/1996/000261A
Other languages
Spanish (es)
Inventor
Alberto Sanchez Y De La Camara Felipe
Original Assignee
Grupo Purecorn Sa De Cv
Filing date
Publication date
Application filed by Grupo Purecorn Sa De Cv filed Critical Grupo Purecorn Sa De Cv
Priority to ZA9705957A priority Critical patent/ZA975957B/en
Priority to BR9711000-0A priority patent/BR9711000A/en
Priority to AU35475/97A priority patent/AU3547597A/en
Priority to DE69703185T priority patent/DE69703185D1/en
Priority to AT97401610T priority patent/ATE196696T1/en
Priority to PCT/FR1997/001209 priority patent/WO1998001836A1/en
Priority to RU99102178/09A priority patent/RU99102178A/en
Priority to CA002259528A priority patent/CA2259528A1/en
Priority to EP97401610A priority patent/EP0817144B1/en
Priority to CN97197398.9A priority patent/CN1228861A/en
Priority to ARP970103020A priority patent/AR007817A1/en
Publication of MXPA96000261A publication Critical patent/MXPA96000261A/en

Links

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)

  1. 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. 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. ANY
    0. 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.
MXPA/A/1996/000261A 1996-07-05 1996-01-17 Rotating reactor for precise nixtamalization demaiz that does not break the grain, does not produce naxayoteni genera contaminante alg MXPA96000261A (en)

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