OA20011A

OA20011A - Water- And Energy-Saving Systems And Methods For Producing Lime-Cooked Masa.

Info

Publication number: OA20011A
Application number: OA1202100066
Authority: OA
Inventors: Felipe A. Rubio; Roberto Contreras
Original assignee: Gruma S.A.B. De C.V.
Priority date: 2018-08-17
Filing date: 2019-08-06
Publication date: 2021-08-31

Abstract

Water- and energy-saving systems and methods for producing lime-cooked masa are described. Such methods generally include adding water to maize kernel in a first predetermined proportion, the maize kernel having endosperm, germ, pericarp, and tip cap components. Using a first conditioner, the maize kernel is conditioned for a first predetermined amount of time to cause moisture absorption to within a first predetermined range. The maize kernel is limed. The maize kernel is cooked, using a cooker, in an environment of steam. After the maize kernel is cooked, water is added to the maize kernel in a second predetermined proportion and, using a second conditioner, the maize kernel is conditioned for a second predetermined amount of time to cause moisture absorption to within a second predetermined range. The maize kernel is milled using one or more mills.

Description

Cross-Reference to Related Applications

[0001] This application claims the benefit of the filing date of, and priority to, U.S. Application No. 62/765,075, filed August 17, 2018, the entire disclosure of which is hereby incorporated herein by reference.

[0002] This application claims the benefit of the filing date of, and priority to, U.S. Application No. 16/531,553, filed August 5, 2019, the entire disclosure of which is hereby incorporated herein by reference.

Technical Field

[0003] The présent disclosure relates generally to lime-cooked masa production and, more particularly, to water- and energy-saving Systems and methods for producing lime-cooked masa for the préparation of tortilla, snack, and other maize-based foods.

Background

[0004] Maize, or corn, is a cereal grain. A maize kernel has five separable components, namely tip cap, pericarp (or hull), aleurone, endosperm, and germ components. Two industrial processes can be employed for transforming maize into food products, namely wet milling and dry milling. In wet milling processes, maize is separated into relatively pure Chemical compound classes of starch, protein, oil, and fiber. In dry milling processes, a réduction in the particle size of clean maize occurs with or without separators (for degerming) or aspirators (for dehulling) so that ail or some of the original germ and fiber (pericarp/hull) are retained. One type of wet milling process is nixtamal milling (or nixtamalization) in which whole maize kernels are soaked in a lime solution, cooked, steeped in cooking liquor, drained, and rinsed to yield nejayote (or alkaline steepwater). The process of nixtamal milling partially removes some of the germ and most of the pericarp. The partially-cooked maize (nixtamal) is then either ground to make a wet dough (masa) from which tortillas or snack foods can be formed, or is allowed to dry before being milled into masa flour.

[0005] The traditional or household préparation of cooking maize with lime at the rural level requires hard labor and is time consuming (around 14 to 20 hours). Most of this time is taken by cooking and steeping/washing operations; this time can be decreased to 6-12 hours at the urban or cottage level (with 5% to 17% wastewater solid loss). C. Duran-de Bazua et al., Use ofAnaerobicAerobic Treatment Systems for Maize Processing Installation: Applied Microbiology In Action, Communicating Current Research and Educational Topics and Trends in Applied Microbiology 3-12 (A. Mendez ed., Formatex 2007); Kurt A. Rosentrater et al., Economie Simulation Modeling of Reprocessing Alternatives for Corn Masa Byproducts, 39 Resources, Conservation and Recycling, 341-367 (2003); Ricardo Bressani et al., Fortification of Corn Masa Flour with Iron and/or Other Nutrients: A Literature and Industry Expérience Review 4-85 (SUSTAIN 1997). In modem processes, lime (0.5% to 1.5% based on grain) is mixed with 1 to 1.5 parts of water for each part of maize. The mixture/suspension is cooked by boiling or steam injection and, while the hull/tip cap is partially removed during cooking/washing, there is still fiber left. After steeping, the alkaline steepwater, which contains dissolved hull/aleurone and germ, along with undissolved lime, is discarded. Further, the maize kernels are washed thoroughly of remaining liquid, so that the residual hulls can be removed manually (for small-scale (< 4 tons/day) processes) or mechanically (for large-scale (>10 tons/day) nixtamal mills). At the industrial scale (100-500 tons/day), this déhydration step is a major cost factor.

[0006] The human food supply chain contributes to 30% of carbon dioxide émissions, but this environmental burden can decrease with clean energy technology that créâtes products and services sustainably. Elevated prices of fossil fuels, such as fuel oil and natural gas (55 kg of CO₂/MMBTU), allow compétition from maize as biofuel (e.g., biomass: 110 kg CO2/MMBTU or éthanol: 70 kg CO2/MMBTU), which can increase compétition for food supply and aggravate malnutrition around the world. In addition, costs associated with water usage and its environmental treatment affect sustainability in expanding nixtamal mills, especially in areas where water is scarce due to increasing climate change (e.g., >2°C above the pre-industrial average) from CO2 émissions (e.g., >380ppmv). It would therefore be désirable to provide a low or zero-carbon energy process for producing lime-cooked masa that would contribute to the stabilization of greenhouse gas concentration by reducing or avoiding energy-related émissions. Moreover, in contrast to the above-described processes, it would be désirable to provide a process for the continuous production of lime-cooked masa that produces no (or negligible) wastewater.

[0007] Therefore, what is needed is an apparatus, System, and/or method that addresses one or more of the foregoing issues, and/or one or more other issues.

Brief Description of the Drawings

[0008] Figure 1 is a diagrammatic illustration of a System adapted to make lime-cooked masa, according to one or more embodiments of the présent disclosure.

[0009] Figure 2 is a flow diagram of a method of making lime-cooked masa using the System of Figure 1, according to one or more embodiments of the présent disclosure.

[0010] Figure 3 is a table showing nutritional average compositions for lime-cooked masa 10 (LCM) prepared by the method of Figure 2 as compared to traditional nixtamal masa (NM) and whole grain maize (WM), according to one or more embodiments of the présent disclosure.

[0011] Figure 4 is a table showing the physicochemical content of the lime-cooked masa (LCM) prepared by the method of Figure 2 as compared to traditional nixtamal masa and whole maize dough (WM), according to one or more embodiments of the présent disclosure.

[0012] Figure 5 is a diagrammatic illustration of another System adapted to make lime-cooked masa, according to one or more embodiments of the présent disclosure.

[0013] Figure 6 is a flow diagram of a method of making lime-cooked masa using the System of Figure 5, according to one or more embodiments of the présent disclosure.

[0014] Figure 7 is a table showing nutritional average compositions for lime-cooked masa 20 (LCM) prepared by the method of Figure 6 as compared to traditional nixtamal masa and whole maize (WM), according to one or more embodiments of the présent disclosure.

[0015] Figure 8 is a table showing the physicochemical content of the lime-cooked masa (LCM) prepared by the method of Figure 6 as compared to nixtamal maize and whole maize dough, according to one or more embodiments of the présent disclosure.

[0016] Figure 9 is a diagrammatic illustration of yet another System adapted to make limecooked masa, according to one or more embodiments of the présent disclosure.

[0017] Figure 10 is a flow diagram of a method of making lime-cooked masa using the System of Figure 9, according to one or more embodiments of the présent disclosure.

[0018] Figure 11 is a table comparing water and energy consumption, as well as solid waste and 30 wastewater, between traditional masa production and lime-cooked masa prepared using one or more embodiments of the présent disclosure.

[0019] Figure 12 is a diagrammatic illustration of a computing node for implementing one or more embodiments of the présent disclosure.

Detailed Description

[0020] The présent disclosure provides a process that départs from existing nixtamalization processes for whole cereal grains such as, for example, maize, to produce lime-cooked masa. This process involves a thermo-alkaline treatment that produces no (or negligible) wastewater with reduced steam heating consumption, while producing a high yield of the desired food product. In some embodiments, one objective is to employ an industrial process with an atmospheric steamer to continuously produce cooked coarse-sized and fine-sized dough fractions and also to yield a wasteless or a reduced waste lime-cooked masa. In some embodiments, another objective is to provide a lime-cooked masa for tortillas and snacks that is uniform and improved in its nutritional and physico-chemical properties.

[0021] In an embodiment, as illustrated in Figure 1, a system adapted to make lime-cooked masa is generally referred to by the reference numéral 100. The system 100 includes a moisturizer such as, for example, a mixer 105. A conditioner 110 is operably coupled to the mixer 105. A blower 115 is operably coupled to a boiler 120. A cooker such as, for example, a steamer 125, is operably coupled to the boiler 120. The steamer 125 is also operably coupled to the conditioner 110. A conditioner such as, for example, a quencher 130, is operably coupled to the steamer 125. Mills 135 and 140 are each operably coupled to the quencher 130. A cooler 145 is operably coupled to each of the mills 135 and 140. A kneader 150 is operably coupled to the cooler 145. A sheet cutter 155 is operably coupled to the kneader 150. An oven 160 is operably coupled to the sheet cutter 155. A cooler such as, for example, a homogenizer cooler 165, is operably coupled to the oven 160. A toaster/fryer 170 is operably coupled to the homogenizer cooler 165. In some embodiments, the toaster/fryer 170 includes a fryer and a cooling section (not shown) located downstream of the fryer; in some embodiments, the cooling section of the toaster/fryer 170 is, or includes, one or more clean air fans. A packer 175 is operably coupled to each of the homogenizer cooler 165 and the toaster/fryer 170.

[0022] In operation, with continuing reference to Figure 1, the mixer 105 receives clean maize kernel, as indicated by arrow 180, receives a lime solution containing water and lime, as indicated by arrow 185, limes the received clean maize by mixing the received clean maize kernel with the received lime solution, and discharges the mixture, as indicated by arrow 190. In some embodiments, the mixture of the received clean maize kernel and the received lime solution contains 0.1-0.3% by weight lime to maize kernel. On a dry weight basis, the maize kernel has tip cap (e.g., 0.8-1.1% by weight), pericarp/hull (e.g., 5.1-5.7% by weight), aleurone (2% by weight), endosperm (e.g., 81.1-83.5% by weight), and germ (e.g., 10.2-11.9% by weight). The pericarp contains 90% insoluble fiber (e.g., 67% hemicellulose-heteroxylans, 23% cellulose, 5-7% glucuronic acid, and 0.1% lignin). Stanley A. Watson, Description, Development, Structure and Composition of the Corn Kernel, Corn: Chemistry and Technology 69—106 (Pamela J. White & Lawrence A. Johnson eds., American Association of Cereal Chemists, Inc. 2nd ed. 2003); F. R. Earle et al., Composition of the Components Parts of the Maize Kernel, 23 Cereal Chemistry, 504511 (1946).

[0023] The conditioner 110 receives the mixture discharged from the mixer 105, as indicated by the arrow 190, tempers the mixture causing additional moisture absorption, and discharges the tempered mixture, as indicated by arrow 195. In some embodiments, the conditioner 110 includes a feeder adapted to receive the mixture discharged from the mixer 105. In some embodiments, as in Figure 1, water is added to the mixture discharged from the mixer 105, as indicated by arrow 200, before, during, or after the discharged mixture is received by the conditioner 110.

[0024] The blower 115 blows clean air to the boiler 120, as indicated by arrows 205 and 210, and the boiler 120, in tum, receives water, as indicated by arrow 215, receives the clean air from the blower 115, as indicated by the arrow 210, receives fuel (e.g., natural gas), as indicated by arrow 220, boils the received water by burning the received fuel and clean air, vents exhaust from the burnt fuel, as indicated by arrow 225, and discharges steam produced by the boiled water, as indicated by arrow 230.

[0025] The steamer 125 receives the tempered mixture discharged from the conditioner 110, as indicated by the arrow 195, receives the steam discharged from the boiler 120, as indicated by the arrow 230, precooks the received mixture with the received steam, and discharges the precooked mixture, as indicated by arrow 235. In some embodiments, the steamer 125 is or includes a rotary cylinder chamber and/or a heat-transfer screw conveyer. In some embodiments, the steamer 125 includes a feeder adapted to receive the tempered mixture from the conditioner 110. As described herein, steaming is a thermal process by which food is heated for the purpose of inactivating enzymes, modifying texture, and/or preserving color, flavor, and nutritional value. Hot water and steam can be used as heating media, but hot gas (dry-heat) can also be used. Steam infusion heating is a direct-contact process where condensation occurs on the surface of a flowable food, under atmospheric pressure. This process requires atmospheric steam, pumpable food and mechanical device to facilitate steam heating/condensation.

[0026] The quencher 130 receives the precooked mixture discharged from the steamer 125, as indicated by the arrow 235, tempers the precooked mixture causing cooling and additional moisture absorption, and discharges the tempered mixture, as indicated by arrows 240a and 240b. In some embodiments, the quencher 130 includes a feeder adapted to receive the precooked mixture discharged from the steamer 125. In some embodiments, as in Figure 1, water is added to 10 the precooked mixture discharged from the steamer 125, as indicated by arrow 245, before, during, or after the precooked mixture is received by the quencher 130.

[0027] The mill 135 receives at least a first portion of the tempered mixture discharged from the quencher 130, as indicated by the arrow 240a, grinds the first portion into the fine-ground dough material, and discharges the fine-ground dough material, as indicated by arrow 250a. In some 15 embodiments, the mill 135 includes a feeder adapted to receive the first portion of the tempered mixture discharged from the quencher 130. In some embodiments, the mill 135 is a gravity-fed attrition mill (e.g., a stone mill or gap mill). In some embodiments, a stone gap in the mill 135 measures 1,000 microns. Similarly, the mill 140 receives at least a second portion of the tempered mixture discharged from the quencher 130, as indicated by the arrow 240b, grinds the second 20 portion into the coarse-ground dough material, and discharges the coarse-ground dough material, as indicated by arrow 250b. In some embodiments, the mill 140 includes a feeder adapted to receive the second portion of the tempered mixture discharged from the quencher 130. In some embodiments, the mill 140 is a gravity-fed attrition mill (e.g., a stone mill or gap mill). In some embodiments, a stone gap in the mill 140 measures 2,000 microns. In some embodiments, as in 25 Figure 1, water is added to the tempered mixture discharged from the quencher, as indicated by arrow 255, before, during, or after the tempered mixture is received by the mill 135 or the mill 140.

[0028] The cooler 145 receives the fine-ground dough material from the mill 135, as indicated by the arrow 250a, receives the coarse-ground dough material from the mill 140, as indicated by 30 the arrow 250b, receives clean air (e.g., discharged from the blower 115), as indicated by arrow 260, cools the received dough materials with the received clean air, and discharges the cooled dough materials, as indicated by arrow 265. In some embodiments, the cooler 145 includes a belt conveyor adapted to receive the fine-ground dough material from the mill 135, and to receive the coarse-ground dough material from the mill 140.

[0029] The kneader 150 receives the cooled dough materials discharged from the cooler 145, as 5 indicated by the arrow 265, mixes the cooled dough materials into a lime-cooked masa, and discharges the lime-cooked masa, as indicated by arrow 270.

[0030] The sheet cutter 155 receives the lime-cooked masa from the kneader 150, as indicated by the arrow 270, forms the lime-cooked masa into sheets, cuts individual pièces from the sheets, and discharges the individual pièces, as indicated by arrow 275.

[0031] The oven 160 receives the individual pièces discharged from the sheet cutter 155, as indicated by the arrow 275, bakes the received individual pièces, and discharges the baked individual pièces, as indicated by arrow 280. In some embodiments, the oven 160 is a three-tiered, gas-fired oven.

[0032] The homogenizer cooler 165 receives the baked individual pièces discharged from the 15 oven, as indicated by the arrow 280, cools and homogenizes moisture of the baked individual pièces, and discharges the cooled individual pièces, as indicated by arrow 285. In some embodiments, the homogenizer cooler 165 includes a sériés of open tiers.

[0033] In some embodiments, the packer 175 receives the cooled individual pièces discharged from the homogenizer cooler 165, as indicated by the arrow 285, packages the cooled individual 20 pièces in snack- or tortilla-sized portions, and discharges the packaged portions, as indicate by arrows 290a and/or 290b. In addition, or instead, the toaster/fryer 170 may receive at least a portion of the cooled individual pièces discharged from the homogenizer cooler 165, as indicated by arrow 295, fry the cooled individual pièces and cool them again in the cooling section of the toaster/fryer 170, and discharge the fried individual pièces, as indicated by arrow 300. In such 25 instances, the packer 175 receives the fried individual pièces discharged from the toaster/fryer 170, as indicated by the arrow 300, packages the fried individual pièces in snack- or tortilla-sized portions, and discharges the packaged portions, as indicated by the arrows 290a and/or 290b.

[0034] In an embodiment, as illustrated in Figure 2, a method of making lime-cooked masa using the System 100 is generally referred to by the reference numéral 305. The method 305 includes at 30 a step 310, mixing, using the mixer 105, maize kernel with lime solution to lime the maize kernel.

In some embodiments, the mixture contains 0.1-0.3% by weight lime to maize kernel. In some embodiments, the maize kernel is dry-cleaned prior to mixing with the lime solution. The maize kernel may be a maize grain such as, for example, 7.ea Mays subspecies Parviglumis or Mexicana (e.g., white maize, yellow maize, blue maize, quality-protein maize, waxy maize, and/or highamylose maize) or another cereal grain. The lime solution may contain 1% to 5% lime by weight; for example, the lime solution may contain 2% to 3% lime by weight. The cleaned maize kernel is thoroughly sprayed with the lime solution for 5 to 10 minutes to uniformly wet the kernel surface. In some embodiments, a solid to water ratio from 1:0.04 to 1:0.07 is maintained in the mixer 105 during the step 310. As a resuit, the moisture content of the maize kernel is adjusted from 12% or 13% to 17% or 18% during the step 310.

[0035] At a step 315, the conditioner 110 tempers the mixture to cause additional moisture absorption. In some embodiments, the mixture is tempered for 20 to 40 minutes at températures from 25°C to 30°C. Water is added to the mixture before and/or during the tempering of the mixture by the conditioner 110. More particularly, in some embodiments, a solid to water ratio from 1:0.13 to 1:0.19 is maintained in the conditioner 110 during the step 315. As a resuit, the moisture content of the maize kernel is adjusted to 25% to 30% during the step 315; for example, the moisture content of the maize kernel may be adjusted to 28% to 30%.

[0036] At a step 320, the steamer 125 precooks the tempered mixture with steam (e.g., saturated steam). In some embodiments, the tempered mixture is precooked for 5 to 10 minutes at températures from 80°C to 95°C and at steam pressures from 90 kPa to 110 kPa (or 13.1-16.0 psi); for example, the tempered mixture may be precooked at a steam pressure of 101 kPa (or 14.7 psi) for a desired time to control température. As a resuit, the tempered mixture is heated and rehydrated (i.e., from steam condensate), and the moisture content of the maize kernel is adjusted to 30% to 42%; for example, the moisture content of the maize kernel may be adjusted to 32% to 38%; for another example, the moisture content of the maize kernel may be adjusted to 34% to 36%. In some embodiments, execution of the step 320 causes hydrolysis of the extemal-most layers of the maize kernel (i.e., the pericarp, the tip cap, and the aleurone) and partial hydrolysis or gelatinization of the internal-most layers of the maize kernel (i.e., the endosperm and the germ). As a resuit, the bran (i.e., the pericarp and the tip cap) is preserved so that the calcium bound in the resulting lime-cooked masa is increased for human nutrition (as compared to nixtamal masa and whole maize).

[0037] At a step 325, the quencher 130 tempers the precooked mixture to cause cooling and additional moisture absorption through the bran (i.e., the pericarp and tip cap). In some embodiments, the precooked mixture is tempered for 30 to 60 minutes at températures from 65°C to 80°C. Water is added to the precooked mixture before and/or during tempering of the precooked mixture by the quencher 130. More particularly, in some embodiments, a solid to water ratio from 1:0.06 to 1:0.24 is maintained in the quencher 130 during the step 325. As a resuit, the moisture content of the maize kernel is adjusted to 35% to 47% during the step 325; for example, the moisture content of the maize kernel may be adjusted to 39% to 41%. Once tempered, the kernel is hard enough to be milled more efficiently than higher moisture and more elastic grains, while maintaining sufficient elasticity to avoid overheating during milling (which can cause starch damage in masa products).

[0038] At a step 330, the mill 135 grinds a first portion of the tempered mixture into a fineground dough material. Similarly, at a step 335, the mill 140 grinds a second portion of the tempered mixture into a coarse-ground dough material. Water is added to the tempered mixture before and/or during the grinding ofthe first and second portions by the respective mills 135 and 140. More particularly, in some embodiments, a solid to water ratio from 1:0.12 to 1:0.27 is maintained in the respective mills 135 and 140 during the steps 330 and 335. As a resuit, the moisture content of the maize kernel is adjusted to 40% to 52% during the steps 330 and 335; for example, the moisture content of the maize kernel may be adjusted to 44% to 46%. In addition, the added water cools the grinding stones of the respective mills 135 and 140 to températures from 45°C to 60°C. During the steps 330 and 335, the mills 135 and 140 grind and abrade the first and second portions of the tempered mixture into a coarse-ground (larger-sized) fraction and a fineground (smaller-sized) fraction. The coarse-ground fraction (e.g., 14-35 mesh) may be used to produce snacks. The fine-ground fraction (e.g., 45-100 mesh) may be used to produce lime-cooked tortilla. Bimodal particle size distribution of the coarse-ground and fine-ground fractions is directly related to the respective sizes of the stone gaps in the mills 135 and 140, the pressure between the respective rotor and stator stones of the mills 135 and 140, the relative surface velocities of the respective rotor and stator stones of the mills 135 and 140, and/or the apparent viscosity of the desired end product.

[0039] At a step 340, the cooler 145 cools the fine-ground and coarse-ground dough materials with clean air (e.g., supplied from the blower 115). In some embodiments, the dough materials are cooled for 5 minutes. As a resuit, the moisture content of the dough materials is adjusted to 38% to 50% during the step 340; for example, the moisture content of the dough materials may be adjusted to 42% to 45%.

[0040] At a step 345, the kneader 150 mixes the cooled dough materials together to form a lime5 cooked masa. In some embodiments, the lime-cooked masa is uniformly mixed, plastic (elastic), and cohesive (viscous).

[0041] At a step 350, the sheet cutter 155 forms the lime-cooked masa into sheets and cuts individual pièces (e.g., disk- or triangular-shaped) from the sheets. In some embodiments, the sheets are eut into the individual pièces by a rotating cutter.

[0042] At a step 355, the oven 160 bakes the individual pièces. In some embodiments, the individual pièces are baked for 20 to 40 seconds at températures from 280°C to 300°C.

[0043] At a step 360, the homogenizer cooler 165 cools the baked individual pièces (e.g., with clean air supplied from the blower 115).

[0044] At a step 365, the packer 175 packages the cooled individual pièces in snack- or tortilla15 sized portions. In some embodiments, the cooled individual pièces are packaged in the tortillasized portions with a moisture content 40% to 50%. In other embodiments, the toaster/fryer 170 bakes or fries the cooled individual pièces before the packer 175 packages the baked or fried individual pièces in the snack-sized portions. For example, the cooled individual pièces may be baked for 35 to 50 seconds at températures from 260°C to 290°C, or fried (e.g., in vegetable oil) 20 for 50 to 80 seconds at températures from 170°C to 190°C. The baked or fried individual pièces are then packaged (e.g., laminated in plastic bags) in the snack-sized portions (e.g., as whole snacks) with a moisture content of less than 1.5%.

[0045] Turning to Figure 3, a table showing nutritional average compositions for lime-cooked masa prepared by the method 305 (“LCM1”), nixtamal masa (“NM”), and whole maize (“WM”) 25 is illustrated; composition values shown in the table are based on a moisture content of 10%. The LCM1 and the NM each include a network of solubilized starch and non-starch polymers (continuous phase) supporting dispersed, uncooked, and swollen protein-starch granules, fiber cell fragments, and lipids (dispersed phase). Both the LCM1 and the NM contain particles from the endosperm and the germ; however, the LCM1 and the NM contain different content from the bran 30 (i.e., the pericarp and the tip cap). Consequently, as shown in Figure 3, the LCM1 contains 10.4% dietary fiber and .15% calcium. Moreover, the LCM1 has, on average, a higher nutritional value as compared to the NM, with more protein (at ~9%), ~25% more fat, ~30% more dietary fiber, —100% more crude fiber, and ~25% more résistant starch. Dietary fiber may be described as a carbohydrate polymer with ten or more monomeric units (which are not hydrolyzed by the endogenous amylases in the small intestine) belonging to one of three categories: (i) naturally occurring edible carbohydrates in consumed food; (ii) carbohydrates obtained from raw food by physical, Chemical, or enzymatic treatments and which hâve been shown to physiologically benefit health; and (iii) synthetic carbohydrates with a (claimed) health benefit. Prebiotic résistant starch (RS3: retrograded after heat-cool cycles) is included in this définition because it is obtained from maize and partially fermented by colonie bacteria.

[0046] In some embodiments, due to the inclusion of, or similarities to, other minimal processing techniques in the production of the LCM 1 (e.g., cracking, crushing, rolling, lightly pearling, and/or steaming), the LCM1 is considered “whole grain”. Other benefits associated with the LCM1 include, but are not limited to, organoleptic benefits (e.g., improved flavor and texture for tortillas) and other nutritional benefits (e.g., unbound niacin for pellagra prévention, bound calcium for osteoporosis, etc.). For example, the functional gum-Iike dispersion of the LCM1 (from .3% to .4% acidic soluble fiber) may impart not only a high water-binding capacity and viscosity, but also yields a biofunctional treatment for osteoporosis. Moreover, the LCM1 has improved tortilla texture and higher calcium availability (associated with bran acidic groups).

[0047] Turning to Figure 4, a table showing the physico-chemical content of the LCM1 (i.e., prepared by the method 305), the NM, and the WM (i.e., dry-milled dough) is illustrated. On a percentage-by-weight basis, both the LCM1 and the NM hâve bimodal distributions containing a smaller- and a larger-sized group of particles as described by their modes. More particularly, the LCM1 yields a larger-sized mode (i.e., 18 mesh or 1,000 microns with 15% weight) and a smallersized mode (i.e., 60 mesh or 250 microns and 35% weight) appropriate for tortilla and snack making. The NM also yields a larger-sized mode (i.e., 35 mesh or 500 microns and 30% weight) and a smaller-sized mode (i.e., 80 mesh or 180 microns and 20% weight). However, as compared to the NM dough (at ~60%), the LCM1 dough has a lower weight fraction (-33%) above 45 mesh or 355 microns. The différence in size and weight between the larger-sized mode of the LCM1 and the larger-sized mode of the NM causes the apparent peak viscosity of the LCM1 (-2,760 centipoise) (at 95°C) to be lower than the apparent peak viscosity of the NM (-3,470 centipoise). This différence in apparent peak viscosity may be (at least partially) attributable to: free starch particles increasing the viscosity of the NM during pasting (i.e., at 14% solids content); and slower water diffusion into, and swelling of, the LCMl’s coarser particles. Finally, the WM contains smaller and finer particles (i.e., 355 microns) than both the LCM1 and the NM; as a resuit, the WM has an even higher apparent peak viscosity (-5,600 centipoise).

[0048] In an embodiment, as illustrated in Figure 5, another System adapted to make limecooked masa is generally referred to by the reference numéral 370. The System 370 includes several components substantially identical to corresponding components ofthe System 100, which substantially identical components are given the same reference numerals. However, the System 370 also includes several components that are different from components of the System 100; more 10 particularly, the System 370 does not include the mills 135 and 140, but instead includes a crusher 375, a separator 380, and a mill 385. Accordingly, as shown in Figure 5, the System 370 includes the mixer 105, to which the conditioner 110 is operably coupled. The steamer 125 is operably coupled to the conditioner 110. The boiler 120 is operably coupled to the steamer 125. The blower 115 is operably coupled to the boiler 120. The quencher 130 is operably coupled to the steamer 15 125. The crusher 375 is operably coupled to the quencher 130. The separator 380 is operably coupled to the crusher 375. The mill 385 is operably coupled to the separator 380. The cooler 145 is operably coupled to the mill 385. The kneader 150 is operably coupled to the cooler 145. The sheet cutter 155 is operably coupled to the kneader 150. The oven 160 is operably coupled to the sheet cutter 155. The homogenizer cooler 165 is operably coupled to the oven 160. The 20 toaster/fryer 170 is operably coupled to the homogenizer cooler 165. As noted above, in some embodiments, the toaster/fryer 170 includes a fryer and a cooling section (not shown) located downstream of the fryer; in some embodiments, the cooling section of the toaster/fryer 170 is, or includes, one or more clean air fans. The packer 175 is operably coupled to each of the homogenizer cooler 165 and the toaster/fryer 170.

[0049] In operation, with continuing reference to Figure 5, the mixer 105 receives the clean maize kernel, as indicated by arrow 390, receives the lime solution containing the water and lime, as indicated by arrow 395, limes the received clean maize kernel by mixing the received clean maize kernel with the received lime solution, and discharges the mixture, as indicated by arrow 400. In some embodiments, the mixture of the received clean maize kernel and the received lime 30 solution contains 0.1-0.3% by weight lime to maize kernel.

[0050] The conditioner 110 receives the mixture discharged from the mixer 105, as indicated by the arrow 400, tempers the mixture causing additional moisture absorption, and discharges the tempered mixture, as indicated by arrow 405. In some embodiments, as in Figure 5, water is added to the mixture discharged from the mixer 105, as indicated by arrow 410, before, during, or after the discharged mixture is received by the conditioner 110.

[0051] The blower 115 blows clean air to the boiler 120, as indicated by arrows 415 and 420, which boiler 120, in turn, receives water, as indicated by arrow 425, receives the clean air from the blower 115, as indicated by the arrow 420, receives fuel (e.g., natural gas), as indicated by arrow 430, boils the received water by burning the received fuel and clean air, vents exhaust from the burnt fuel, as indicated by arrow 435, and discharges steam produced by the boiled water, as indicated by arrow 440.

[0052] The steamer 125 receives the tempered mixture discharged from the conditioner 110, as indicated by the arrow 405, receives the steam discharged from the boiler 120, as indicated by the arrow 440, precooks the received mixture with the received steam, and discharges the precooked mixture, as indicated by arrow 445.

[0053] The quencher 130 receives the precooked mixture discharged from the steamer 125, as indicated by the arrow 445, tempers the precooked mixture causing cooling and additional moisture absorption, and discharges the tempered mixture, as indicated by arrow 450. In some embodiments, as in Figure 5, water is added to the precooked mixture discharged from the steamer 125, as indicated by arrow 455, before, during, or after the precooked mixture is received by the quencher130.

[0054] The crusher 375 receives the tempered mixture discharged from the quencher 130, as indicated by the arrow 450, crushes the tempered mixture into a coarse-ground kernel portion and a hull (or pericarp) portion, and discharges the coarse-ground kernel portion and the hull portion, as indicated by arrow 460. In some embodiments, the crusher 375 includes a feeder adapted to receive the tempered mixture discharged from the quencher 130. In some embodiments, the crusher 375 is a gravity-fed attrition mill (e.g., a jaw or rotary crusher). In some embodiments, a stone gap in the crusher 375 measures from 3,000 microns to 4,000 microns.

[0055] The separator 380 receives the coarse-ground kernel portion and the hull portion discharged from the separator 380, as indicated by the arrow 460, séparâtes the coarse-ground kernel portion from the hull portion, and discharges the separated coarse-ground kernel portion, as indicated by arrow 465, and the separated hull portion, as indicated by arrow 470. In some embodiments, the separator 380 at least partially séparâtes the coarse-ground kernel portion from the hull portion by receiving clean air (e.g., discharged from the blower 115), as indicated by arrow 475, aspirating the received hull portion with the received clean air, and venting the aspirated air from the hull portion, as indicated by arrow 480. In addition, or instead, the separator 380 may include a sieve adapted to at least partially separate the coarse-ground kernel portion from the hull portion.

[0056] The mill 385 receives the separated coarse-ground kernel portion discharged from the separator 380, as indicated by the arrow 465, grinds the separated coarse-ground kernel portion into dough materials, and discharges the dough materials, as indicated by arrow 485. In some embodiments, the mill 385 includes a feeder adapted to receive the separated coarse-ground kernel portion discharged from the separator 380. In some embodiments, as in Figure 5, water is added to the separated coarse-ground kernel portion discharged from the separator 380, as indicated by arrow 486, before, during, or after the separated coarse-ground kernel portion is received by the mill 385. In some embodiments, the mill 385 is a gravity-fed attrition mill (e.g., a stone mill or gap mill). In some embodiments, a stone gap in the mill 385 measures from 300 microns to 1,500 microns.

[0057] The cooler 145 receives the dough materials from the mill 385, as indicated by the arrow 485, receives clean air (e.g., discharged from the blower 115), as indicated by arrow 490, cools the received dough materials with the received clean air, and discharges the cooled dough materials, as indicated by arrow 495. In some embodiments, the cooler 145 includes a band conveyer adapted to receive the dough materials discharged from the mill 385.

[0058] The kneader 150 receives the cooled dough materials discharged from the cooler 145, as indicated by the arrow 495, mixes the cooled dough materials into a lime-cooked masa, and discharges the lime-cooked masa, as indicated by arrow 500.

[0059] The sheet cutter 155 receives the lime-cooked masa from the kneader 150, as indicated by the arrow 500, forms the lime-cooked masa into sheets, cuts individual pièces from the sheets, and discharges the individual pièces, as indicated by arrow 505.

[0060] The oven 160 receives the individual pièces discharged from the sheet cutter 155, as indicated by the arrow 505, bakes the received individual pièces, and discharges the baked individual pièces, as indicated by arrow 510.

[0061] The homogenizer cooler 165 receives the baked individual pièces discharged from the oven, as indicated by the arrow 510, homogenizes moisture and cools the baked individual pièces, and discharges the cooled individual pièces, as indicated by arrow 515.

[0062] In some embodiments, the packer 175 receives the cooled individual pièces discharged 5 from the homogenizer cooler 165, as indicated by the arrow 515, packages the cooled individual pièces in snack- or tortilla-sized portions, and discharges the packaged portions, as indicate by arrows 520a and/or 520b. In addition, or instead, the toaster/fryer 170 may receive at least a portion of the cooled individual pièces discharged from the homogenizer cooler 165, as indicated by arrow 525, fry the cooled individual pièces, cool the individual pièces again in the cooling 10 section of the toaster/fryer 170, and discharge the fried individual pièces, as indicated by arrow

530. In such instances, the packer 175 receives the fried individual pièces discharged from the toaster/fryer 170, as indicated by the arrow 530, packages the fried individual pièces in snack- or tortilla-sized portions, and discharges the packaged portions, as indicated by the arrows 520a and/or 520b.

[0063] In an embodiment, as illustrated in Figure 6, a method of making lime-cooked masa using the System 100 is generally referred to by the reference numéral 535. The method 535 includes at a step 540, mixing, using the mixer 105, maize kernel with lime solution to lime the maize kernel. In some embodiments, the mixture contains 0.1-0.3% by weight lime to maize kernel. In some embodiments, the maize kernel is dry-cleaned prior to mixing with the lime solution. The maize kernel may be a maize grain such as, for example, Z.ea Mays subspecies Parviglumis or Mexicana (e.g., white maize, yellow maize, blue maize, quality-protein maize, waxy maize, and/or highamylose maize) or another cereal grain. The lime solution may contain 1% to 5% lime by weight; for example, the lime solution may contain 2% to 3% lime by weight. The cleaned maize kernel is thoroughly sprayed with the lime solution for 5 to 10 minutes to uniformly wet the kernel surface. In some embodiments, a solid to water ratio from 1:0.04 to 1:0.07 is maintained in the mixer 105 during the step 540. As a resuit, the moisture content of the maize kernel is adjusted from 12% or 13% to 17% or 18% during the step 540.

[0064] At a step 545, the conditioner 110 tempers the mixture to cause additional moisture absorption. In some embodiments, the mixture is tempered for 20 to 40 minutes at températures 30 from 25°C to 30°C. Water is added to the mixture before and/or during the tempering of the mixture by the conditioner 110. More particularly, in some embodiments, a solid to water ratio from 1:0.10 to 1:0.18 is maintained in the conditioner 110 during the step 545. As a resuit, the moisture content of the maize kernel is adjusted to 25% to 30% during the step 545; for example, the moisture content of the maize kernel may be adjusted to 28% to 30%.

[0065] At a step 550, the steamer 125 precooks the tempered mixture with steam (e.g., saturated steam). In some embodiments, the tempered mixture is precooked for 5 to 10 minutes at températures from 80°C to 95°C and at steam pressures from 90 kPa to 110 kPa (or 13.1-16.0 psi); for example, the tempered mixture may be precooked at a steam pressure of 101 kPa (or 14.7 psi) for a desired time to control température. As a resuit, the tempered mixture is heated and rehydrated (i.e., from steam condensate), and the moisture content of the maize kernel is adjusted to 30% to 42%; for example, the moisture content of the maize kernel may be adjusted to 32% to 38%; for another example, the moisture content of the maize kernel may be adjusted to 34% to 36%. In some embodiments, execution of the step 550 causes hydrolysis of the extemal-most layers of the maize kernel (i.e., the pericarp, the tip cap, and the aleurone) and partial hydrolysis or gelatinization of the intemal-most layers of the maize kernel (i.e., the endosperm and the germ). As a resuit, the bran (i.e., the pericarp and the tip cap) is preserved so that the calcium bound in the resulting lime-cooked masa is increased for human nutrition (as compared to nixtamal masa and whole maize).

[0066] At a step 555, the quencher 130 tempers the precooked mixture to cause cooling and additional moisture absorption through the bran (i.e., the pericarp and tip cap). In some embodiments, the precooked mixture is tempered for 30 to 60 minutes at températures from 65°C to 80°C. Water is added to the precooked mixture before and/or during tempering ofthe precooked mixture by the quencher 130. More particularly, in some embodiments, a solid to water ratio from 1:0.11 to 1:0.16 is maintained in the quencher 130 during the step 555. As a resuit, the moisture content of the maize kernel is adjusted to 35% to 47% during the step 555; for example, the moisture content of the maize kernel may be adjusted to 39% to 41%. Once tempered, the kernel is hard enough to be milled more efficiently than higher moisture and more elastic grains, while maintaining sufficient elasticity to avoid overheating during milling (which can cause starch damage in masa products).

[0067] At a step 560, the crusher 375 crushes the tempered mixture into a coarse-ground kernel portion and a hull portion.

[0068] At a step 565, the separator 380 séparâtes the coarse-ground kernel portion from the hull portion. In some embodiments, the separated hull portion makes up between 5% to 6% by weight of the coarse-ground kernel portion and the hull portion, taken together.

[0069] At a step 570, the mill 385 grinds the separated coarse-ground kernel portion into dough materials. Water is added to the separated coarse-ground kernel portion before and/or during the grinding of the separated coarse-ground kernel portion by the mill 385. More particularly, in some embodiments, a solid to water ratio from 1:0.14 to 1:0.20 is maintained in the mill 385 during the step 570. As a resuit, the moisture content of the maize kernel is adjusted to 40% to 52% during the step 570; for example, the moisture content of the maize kernel may be adjusted to 44% to 46%. In addition, the added water cools the grinding stones of the mill 385 to températures from 45°C to 60°C. During the step 570, the mill 385 grinds and abrades the coarse-ground kernel portion into a coarse-ground (larger-sized) fraction and a fme-ground (smaller-sized) fraction. The coarse-ground fraction (e.g., 14-35 mesh) may be used to produce snacks. The fine-ground fraction (e.g., 45-100 mesh) may be used to produce lime-cooked tortilla. Bimodal particle size distribution of the coarse-ground and fine-ground fractions is directly related to the size of the stone gap in the mill 385, the pressure between the respective rotor and stator stones of the mill 385, and/or the relative surface velocities of the respective rotor and stator stones of the mill 385. In addition, or instead, the bimodal particle size distribution of the coarse-ground and fine-ground fractions may be directly related to the size of the stone gap in the crusher 375, the pressure between the respective rotor and stator stones of the crusher 375, and/or the relative surface velocities of the respective rotor and stator stones of the crusher 375.

[0070] At a step 575, the cooler 145 cools the fine-ground and coarse-ground fractions with clean air (e.g., supplied from the blower 115). In some embodiments, the dough materials are cooled for 5 minutes. As a resuit, the moisture content of the dough materials is adjusted to 38% to 50% during the step 575; for example, the moisture content of the dough materials may be adjusted to 42% to 45%.

[0071] At a step 580, the kneader 150 mixes the cooled dough materials together to form a limecooked masa. In some embodiments, the lime-cooked masa is uniformly mixed, plastic (elastic), and cohesive (viscous).

[0072] At a step 585, the sheet cutter 155 forms the lime-cooked masa into sheets and cuts individual pièces (e.g., disk- or triangular-shaped) from the sheets. In some embodiments, the sheets are eut into the individual pièces by a rotating cutter.

[0073] At a step 590, the oven 160 bakes the individual pièces. In some embodiments, the 5 individual pièces are baked for 20 to 40 seconds at températures from 280°C to 300°C.

[0074] At a step 595, the homogenizer cooler 165 cools the baked individual pièces (e.g., with clean air to homogenize and balance moisture).

[0075] At a step 600, the packer 175 packages the cooled individual pièces in snack- or tortillasized portions. In some embodiments, the cooled moisture equilibrated individual pièces are 10 packaged in the tortilla-sized portions with a moisture content 40% to 50%. In other embodiments, the toaster/fryer 170 fries the cooled moisture equilibrated individual pièces and then cools the hot fried individual pièces before the packer 175 packages the fried individual pièces in the snacksized portions. For example, the moisture equilibrated cooled individual pièces may be fried (e.g., in vegetable oil) for 50 to 80 seconds at températures from 170°C to 190°C. The hot fried 15 individual pièces are then cooled in the cooling section of the toaster/fryer 170, and then are packaged (e.g., laminated in plastic bags) in the snack-sized portions (e.g., as whole snacks) with a moisture content of less than l .5%.

[0076] Turning to Figure 7, a table showing nutritional average compositions for lime-cooked masa prepared by the method 535 (“LCM2”), nixtamal masa (“NM”), and whole maize (“WM”) 20 is illustrated; composition values shown in the table are based on a moisture content of 10%. The

LCM2 and the NM each include a network of solubilized starch and non-starch polymers (continuous phase) supporting dispersed, uncooked, and swollen protein-starch granules, fiber cell fragments, and lipids (dispersed phase). Both the LCM2 and the NM contain particles from the endosperm and the germ; however, the LCM2 and the NM contain different content from the bran 25 (i.e., the pericarp and the tip cap). Consequently, as shown in Figure 7, the LCM2 contains 8.5% dietary fiber and . 1% calcium. Moreover, the LCM2 has, on average, a higher nutritional value as compared to the NM, with more protein (at ~9%), ~25% more fat, and -25% more résistant starch. [0077] In some embodiments, due to the inclusion of, or similarities to, other minimal processing techniques in the production of the LCM2 (e.g., cracking, crushing, rolling, 1 ightly pearling, and/or 30 steaming), the LCM2 is considered “whole grain”. Other benefits associated with the LCM2 include, but are not limited to, organoleptic benefits (e.g., improved flavor and texture for tortillas) and other nutritional benefits (e.g., unbound niacin for pellagra prévention, bound calcium for osteoporosis, etc.). For example, the functional gum-like dispersion of the LCM2 (from .2% to .3% acidic soluble fiber) may impart not only a high water-binding capacity and viscosity, but also yields a biofunctional treatment for osteoporosis. Moreover, the LCM2 has improved tortilla 5 texture and higher calcium availability (associated with bran acidic groups).

[0078] Turning to Figure 8, a table showing the physico-chemical content of the LCM2 (i.e., prepared by the method 535), the NM, and the WM (i.e., dry-milled dough) is illustrated. On a percentage-by-weight basis, both the LCM2 and the NM hâve bimodal distributions containing a smaller- and a larger-sized group of particles as described by their modes. More particularly, the 10 LCM2 yields a larger-sized mode (i.e., 25 mesh or 710 microns with 13% weight) and a smallersized mode (i.e., 60 mesh or 250 microns and 35% weight) appropriate for tortilla and snack making. The NM also yields a larger-sized mode (i.e., 35 mesh or 500 microns and 30% weight) and a smaller-sized mode (i.e., 80 mesh or 180 microns and 20% weight). However, as compared to the NM dough (at -60%), the LCM2 dough has a lower weight fraction (-30%) above 45 mesh 15 or 355 microns. The différence in size and weight between the larger-sized mode of the LCM2 and the larger-sized mode of the NM causes the apparent peak viscosity of the LCM2 (-3,000 centipoise) (at 95°C) to be lower than the apparent peak viscosity of the NM (-3,470 centipoise). This différence in apparent peak viscosity may be (at least partially) attributable to: free starch particles increasing the viscosity of the NM during pasting (i.e., at 14% solids content); and slower 20 water diffusion into, and swelling of, the LCM2’s coarser particles. Finally, the WM contains smaller and finer particles (i.e., 355 microns) than both the LCM2 and the NM; as a resuit, the WM has an even higher apparent peak viscosity (-5,600 centipoise). After two separate heatingcooling processes (i.e., steamer 125-quencher 130 and mill 385-cooler 145), a partial gelatinization of the starchy endosperm induces résistant starch (RS3) formation (at 2.5%) along with particle25 size aggregation but does not destroy granule structure.

[0079] In an embodiment, as illustrated in Figure 9, yet another system adapted to make limecooked masa is generally referred to by the reference numéral 605. The system 605 includes a moisturizer 610, a conditioner 615, a polisher/dehuller 620, a separator 625, a screener 630, a separator 635, a moisturizer 640, a conditioner 645, a cooker 650, a conditioner such as, for 30 example, a conditioner bin 655, a mill 660, and a cooler 665. As shown in Figure 9, the conditioner

615 is operably coupled to the moisturizer 610. The polisher/dehuller 620 is operably coupled to the conditioner 615. The separator 625 is operably coupled to the polisher/dehuller 620. The screener 630 is also operably coupled to the polisher/dehuller 620. The separator 635 is operably coupled to the screener 630. The moisturizer 640 is operably coupled to each of the separator 625 and the separator 635. The conditioner 645 is operably coupled to the moisturizer 640. The cooker 5 650 is operably coupled to each ofthe conditioner 645 and the screener 630. The conditioner bin

655 is operably coupled to the cooker 650. The mill 660 is operably coupled to the conditioner bin 655. The cooler 665 is operably coupled to the mill 660.

[0080] In operation, with continuing reference to Figure 9, the moisturizer 610 receives clean maize kernel, as indicated by arrow 670, receives water, as indicated by arrow 675, moisturizes 10 the received clean maize kernel with the received water, and discharges the moisturized maize kernel, as indicated by arrow 680. The clean maize kernel includes endosperm, germ, pericarp, and tip cap components.

[0081] The conditioner 615 receives the moisturized maize kernel discharged from the moisturizer 610, as indicated by the arrow 680, tempers the moisturized maize kemel, and 15 discharges the tempered maize kernel, as indicated by arrow 685. In some embodiments, the conditioner 615 includes a feeder adapted to receive the moisturized maize kernel discharged from the moisturizer 610.

[0082] The polisher/dehuller 620 receives the tempered maize kernel discharged from the conditioner 615, as indicated by the arrow 685, at least partially breaks and at least partially loosens 20 the pericarp of the tempered maize kernel, discharges a coarse maize fraction including most of the pericarp, as indicated by arrow 690, and discharges a fine maize fraction, as indicated by arrow 695. In some embodiments, the polisher/dehuller 620 includes a feeder adapted to receive the tempered mixture from the conditioner 615.

[0083] The separator 625 receives the coarse maize fraction discharged from the 25 polisher/dehuller 620, as indicated by the arrow 690, receives clean air, as indicated by arrow 691, removes the pericarp component from the coarse maize fraction using the clean air, discharges the pericarp component, as indicated by arrow 700, and discharges the purified coarse maize fraction, as indicated by arrow 705. In some embodiments, as in Figure 9, the separator 625 is or includes an air separator. In some embodiments, in addition, or instead, the separator 625 is or includes 30 another type of separator.

[0084] The screener 630 receives the fine maize fraction discharged from the polisher/dehuller 620, as indicated by the arrow 695, receives the pericarp component discharged from the separator 625, as indicated by the arrow 700, screens the received maize particles to yield first, second, and third streams, discharges the first stream as a byproduct, as indicated by arrow 710, discharges the second stream, as indicated by arrow 715, and discharges the third stream, as indicated by arrow 720. The first stream includes large size pericarp. The second stream includes residual fines, the tip cap component, and small size or fine pericarp. The third stream includes purified fines.

[0085] The separator 635 receives the second stream discharged from the screener 630, as indicated by the arrow 715, receives clean air, as indicated by arrow 725, removes the residual fines and small size or fine pericarp components from the second stream using the clean air, discharges the removed residual fines and small size or fine pericarp components as a byproduct, as indicated by arrow 730, and discharges the purified second stream, which includes the tip cap component, as indicated by arrow 735.

[0086] The moisturizer 640 receives the purified coarse maize fraction discharged from the separator 625, as indicated by the arrow 705, receives the purified second stream discharged from the separator 635, as indicated by the arrow 735, receives water, as indicated by arrow 740, moisturizes the received maize particles with the received water, and discharges the moisturized maize particles, as indicated by arrow 745.

[0087] The conditioner 645 receives the moisturized maize particles discharged from the moisturizer 640, as indicated by the arrow 745, tempers the moisturized maize particles, and discharges the tempered maize particles, as indicated by arrow 750.

[0088] The cooker 650 receives the third stream discharged from the screener 630, as indicated by the arrow 720, receives the tempered maize particles discharged from the conditioner 645, as indicated by the arrow 750, receives water, as indicated by arrow 755, receives clean steam, as indicated by arrow 760, cooks the received maize particles with the received water and clean steam, and discharges the cooked maize particles, as indicated by arrow 765. In some embodiments, as shown in Figure 9, the maize kernel, in the form of tempered maize particles discharged from the conditioner 645, is limed by adding lime to the tempered maize particles discharged from the conditioner 645, as indicated by arrow 770, before, during, or after the discharged tempered maize particles are received by the cooker 650; in some embodiments, the maize particles are limed by adding lime powder in a range of 0.1 % to 0.3% based on maize kernel;

in some embodiments, the maize particles are limed before they are received by the cooker 650; in some embodiments, before the maize particles are received by the cooker 650, the maize particles are limed by adding lime powder in a range of 0.1% to 0.3% based on maize kernel. In some embodiments, the cooker 650 steams the received maize particles, the received lime, and the received water to an absolute pressure of at least, for example, 90 kPa.

[0089] The conditioner bin 655 receives the cooked maize particles discharged from the cooker 650, as indicated by the arrow 765, tempers the cooked maize particles, and discharges the tempered maize particles, as indicated by arrow 775. In some embodiments, as in Figure 9, water is added to the cooked maize particles discharged from the cooker 650, as indicated by arrow 780, before, during, or after the discharged cooked maize particles are received by the conditioner bin 655; the added water lowers the température of the cooked maize particles.

[0090] The mill 660 receives the tempered maize particles from the conditioner bin 655, as indicated by the arrow 775, mills the tempered maize particles into lime-cooked masa, and discharges the lime-cooked masa, as indicated by arrow 785. In some embodiments, as in Figure 9, water is added to the tempered maize particles discharged from the conditioner bin 655, as indicated by arrow 790, before, during, or after the discharged tempered maize particles are received by the mill 660. In some embodiments, the mill 660 is or includes a stone mill having milling stone(s) that are adjustable to various gap widths depending upon the desired characteristics of the lime-cooked masa.

[0091] The cooler 665 receives the lime-cooked masa discharged from the mill 660, as indicated by the arrow 785, receives clean air, as indicated by arrow 795, cools the lime-cooked masa with the clean air, and discharges the cooled lime-cooked masa, as indicated by arrow 800. The discharged lime-cooked masa can then be used in the manufacture of food products such as, for example, snacks (e.g., chips) and tortillas.

[0092] In an embodiment, as illustrated in Figure 10, a method of making lime-cooked masa (“LCM3”) using the System 605 is generally referred to by the reference numéral 805. In some embodiments, execution of the method 805 results in: water consumption of from 0.52 to 0.60 parts water per one part maize kernel by weight for chip production and 0.76 parts water per one part maize kernel by weight for tortilla production; negligible wastewater discharge; negligible solid waste; energy consumption of less than 0.5 gigajoule(GJ)/ton of the provided maize kernel for chip production; or any combination thereof. In an embodiment, as illustrated in Figure 10, a method of making lime-cooked masa (“LCM3”) using the System 605 is generally referred to by the reference numéral 805. In some embodiments, execution of the method 805 results in: water consumption of no more than 0.60 parts water per one part maize kernel by weight for chip production; no more than 0.76 parts water per one part maize kernel by weight for tortilla 5 production; negligible wastewater discharge; negligible solid waste; energy consumption of less than 0.5 gigajoule(GJ)/ton of the provided maize kernel for chip production; or any combination thereof. The method 805 includes at a step 810, moisturizing, using the moisturizer 610, maize kernel by adding water to the maize kernel in a first predetermined proportion, the maize kernel having endosperm, germ, pericarp, and tip cap components. In some embodiments ofthe step 810, 10 the first predetermined proportion ranges from .07 to .12 parts water for every 1 part of solids (i.e., maize kernel).

[0093] At a step 815, the maize kernel is conditioned, using the conditioner 615, for a first predetermined amount of time to cause moisture absorption to within a first predetermined range. In some embodiments of the step 815, the first predetermined amount of time is at least 10 minutes. 15 In some embodiments of the step 815, the first predetermined range is from 17% to 21%.

[0094] At a step 820, the maize kernel is polished/dehulled, using the polisher/dehuller 620, to yield a fine fraction and a coarse fraction.

[0095] At a step 825, the coarse fraction is separated, using the separator 625, to yield a purified coarse fraction and pericarp.

[0096] At a step 830, the fine fraction and the pericarp separated from the coarse fraction are screened, using the screener 630, to yield first, second, and third streams, the first stream including pericarp, the second stream including residual fines, tip cap, and fine pericarp, and the third stream including purified fines.

[0097] At a step 835, the second stream is separated, using the separator 635, to yield tip cap 25 and a residual second stream.

[0098] At a step 840, the purified coarse fraction and the tip cap separated from the second stream are moisturized, using the moisturizer 640, by adding water in a second predetermined proportion. In some embodiments of the step 840, the second predetermined proportion ranges from 0.2 to 0.26 parts water for every 1 part of solids.

[0099] At a step 845, the purified coarse fraction and the tip cap separated from the second stream are conditioned, using the conditioner 645, for a second predetermined amount of time to cause moisture absorption to within a second predetermined range. In some embodiments of the step 845, the second predetermined amount of time is at least 3 hours. In some embodiments of the step 845, the second predetermined moisture range is from 30% to 34%.

[0100] At a step 850, the purified coarse fraction, the tip cap separated from the second stream, and the third stream are cooked, using the cooker 650, in an environment of steam. In some embodiments, before or during the step 850, the maize particles are limed by adding lime powder in a range of 0.1% to 0.3% based on maize kernel. In some embodiments, before or during the step 850, the maize particles are moisturized by adding water in a proportion ranging from 0.20 to 0.26 parts water for every 1 part of solids. In some embodiments of the step 850, the maize particles are steamed and hydrated to an absolute pressure of at least 90 kPa for an amount of time ranging from 4 minutes to 12 minutes. During this time, the cooker 650 reaches a température from 72°C to 96°C; as a resuit, the cooked maize particles reach a moisture content from 42% to 51% and a température from 71°C to 89°C.

[0101] At a step 855, the maize kernel is conditioned, using the conditioner bin 655, for a third predetermined amount of time to cause moisture absorption to within a third predetermined range. In some embodiments of the step 855, the third predetermined amount of time ranges from at least 3 hours to 4 hours. In some embodiments, before or during the step 855, water is added to the maize kernel in a third predetermined proportion; for example, the third predetermined proportion may range from .1 to .2 parts water for every 1 part of solids. In some embodiments, execution of the step 855 lowers the température of the maize particles to between 60°C and 70°C. In some embodiments, execution of the step 855 results in the cooked maize particles reaching a moisture content from 43% to 53%.

[0102] At a step 860, the maize kernel is milled using the mill 660. In some embodiments, before or during the step 860, the method 805 further includes adding water to the maize kernel in a fourth predetermined proportion; for example, the fourth predetermined proportion may range from .01 to .05 parts water for every 1 part of solids. In some embodiments, after the step 860, the method 805 further includes cooling, using the cooler 665, the milled maize kernel. In some embodiments, execution of the step 860 causes the maize particles to reach a température of between 55°C and 72°C. The cooler 665 may subsequently be utilized to cool the maize particles to a température of between 25°C and 35°C.

[0103] Referring to Figure 11, a table comparing water and energy consumption between traditional masa production and lime-cooked masa prepared using one embodiment of a System of the présent disclosure (e.g., LCM1 prepared using the system 100, LCM2 prepared using the system 370, or LCM3 prepared using the system 605), and/or using one embodiment of a method of the présent disclosure (e.g., LCM1 prepared by the method 305, LCM2 prepared by the method 535, or LCM3 prepared by the method 805) is illustrated. As shown in Figure 11, it is possible to manufacture lime-cooked masa with steam heating and without wastewater (or very little wastewater, or negligible amounts of wastewater), and with negligible solid waste, which is more energy and water efficient, wherein some of the nutrient, water and energy losses that would hâve been présent but for the features of the présent method(s) are prevented. In some embodiments, the steps of the method(s) 305, 535, and/or 805 are: continuously and repeatedly performed; continuously and repeatedly performed for a predetermined amount of time; and/or continuously and repeatedly performed over a time period. In some embodiments, the operation of the system 100, 370, or 605, and/or the execution of the method 305, 535, or 805: saves water usage; éliminâtes wastewater discharge; results in very little wastewater discharge; results in negligible wastewater discharge; results in savings of 91% to 93% in water consumption (e.g., to between 4.5 and 5.5 cubic meters of water per ton of maize kernel) as compared to a traditional NM wetmill; results in savings of 20% to 40% in energy consumption (e.g., to between 0.1 and 0.2 MMBTU/ton of maize kernel) as compared to a traditional NM wet-mill; and/or reduces carbon dioxide émission (e.g., to between 60 and 84 kg of CO2/ ton of maize kernel). In some embodiments, the term “ton” may refer to “metric ton,” a unit of weight equal to 1,000 kg (about 2,200 1b).

[0104] Referring to Figure 12, in an embodiment, a computing node 1000 for implementing one or more embodiments of one or more of the above-described éléments, Systems (e.g., 100, 370, and/or 605), methods (e.g., 305, 535, and/or 805) and/or steps (e.g., 310, 315, 320, 325, 330, 335, 340, 345, 350, 355, 360, 365, 540, 545, 550, 555, 560, 565, 570, 575, 580, 585, 590, 595, 600, 810, 815, 820, 825, 830, 835, 840, 845, 850, 855, and/or 860), or any combination thereof, is depicted. The node 1000 includes a processor or microprocessor 1000a, an input device 1000b, a storage device 1000c, a controller lOOOd, a system memory 1000e, a display lOOOf, and a communication device 1000g ail interconnected by one or more buses lOOOh. In several embodiments, the storage device 1000c may include a floppy drive, hard drive, CD-ROM, optical drive, any other form of storage device or any combination thereof. In several embodiments, the storage device 1000c may include, and/or be capable of receiving, a floppy disk, CD-ROM, DVDROM, or any other form of computer-readable medium that may contain exécutable instructions. In several embodiments, the communication device 1000g may include a modem, network card, or any other device to enable the node 1000 to communicate with other nodes. In several embodiments, any node represents a plurality of interconnected (whether by intranet or Internet) computer Systems, including without limitation, personal computers, mainframes, PDAs, smartphones and cell phones.

[0105] In several embodiments, one or more of the components of any of the above-described Systems include at least the node 1000 and/or components thereof, and/or one or more nodes that are substantially similar to the node 1000 and/or components thereof. In several embodiments, one or more of the above-described components of the node 1000 and/or the above-described Systems include respective pluralities of same components.

[0106] In several embodiments, a computer System typically includes at least hardware capable of executing machine readable instructions, as well as the software for executing acts (typically machine-readable instructions) that produce a desired resuit. In several embodiments, a computer System may include hybrids of hardware and software, as well as computer sub-systems.

[0107] In several embodiments, hardware generally includes at least processor-capable platforms, such as client-machines (also known as personal computers or servers), and hand-held processing devices (such as smart phones, tablet computers, personal digital assistants (PDAs), or personal computing devices (PCDs), for example). In several embodiments, hardware may include any physical device that is capable of storing machine-readable instructions, such as memory or other data storage devices. In several embodiments, other forms of hardware include hardware sub-systems, including transfer devices such as modems, modem cards, ports, and port cards, for example.

[0108] In several embodiments, software includes any machine code stored in any memory medium, such as RAM or ROM, and machine code stored on other devices (such as floppy disks, flash memory, or a CD ROM, for example). In several embodiments, software may include source or object code. In several embodiments, software encompasses any set of instructions capable of being executed on a node such as, for example, on a client machine or server.

[0109] In several embodiments, combinations of software and hardware could also be used for providing enhanced functionality and performance for certain embodiments of the présent disclosure. In an embodiment, software functions may be directly manufactured into a Silicon chip. Accordingly, it should be understood that combinations of hardware and software are also included within the définition of a computer System and are thus envisioned by the présent disclosure as possible équivalent structures and équivalent methods.

[0110] In several embodiments, computer readable médiums include, for example, passive data storage, such as a random-access memory (RAM) as well as semi-permanent data storage such as a compact disk read only memory (CD-ROM). One or more embodiments of the présent disclosure may be embodied in the RAM of a computer to transform a standard computer into a new spécifie computing machine. In several embodiments, data structures are defined organizations of data that may enable an embodiment of the présent disclosure. In an embodiment, data structure may provide an organization of data, or an organization of exécutable code.

[0111] In several embodiments, any networks and/or one or more portions thereof, may be designed to work on any spécifie architecture. In an embodiment, one or more portions of any networks may be executed on a single computer, local area networks, client-server networks, wide area networks, internets, hand-held and other portable and wireless devices and networks.

[0112] In several embodiments, a database may be any standard or proprietary database software. In several embodiments, the database may hâve fields, records, data, and other database éléments that may be associated through database spécifie software. In several embodiments, data may be mapped. In several embodiments, mapping is the process of associating one data entry with another data entry. In an embodiment, the data contained in the location of a character file can be mapped to a field in a second table. In several embodiments, the physical location of the database is not limiting, and the database may be distributed. In an embodiment, the database may exist remotely from the server, and run on a separate platform. In an embodiment, the database may be accessible across the Internet. In several embodiments, more than one database may be implemented.

[0113] In several embodiments, a plurality of instructions stored on a non-transitory computer readable medium may be executed by one or more processors to cause the one or more processors to carry out or implement in whole or in part the above-described operation of each of the abovedescribed éléments, Systems (e.g., 100, 370, and/or 605), methods (e.g., 305, 535, and/or 805), steps (e.g., 310, 315, 320, 325, 330, 335, 340, 345, 350, 355, 360, 365, 540, 545, 550, 555, 560, 565, 570, 575, 580, 585, 590, 595, 600, 810, 815, 820, 825, 830, 835, 840, 845, 850, 855, and/or 860), or any combination thereof. In several embodiments, such a processor may include one or more of the microprocessor 1000a, any processor(s) that are part of the components of the abovedescribed Systems, and/or any combination thereof, and such a computer readable medium may be distributed among one or more components of the above-described Systems. In several embodiments, such a processor may execute the plurality of instructions in connection with a Virtual computer System. In several embodiments, such a plurality of instructions may communicate directly with the one or more processors, and/or may interact with one or more operating Systems, middleware, firmware, other applications, and/or any combination thereof, to cause the one or more processors to execute the instructions. In several embodiments, such a nontransitory computer readable medium may be part of one or more controllers; in several embodiments, the System 100, 370, or 605 may include such one or more controllers, in several embodiments, one or more components of the System 100, 370, or 605 may include such one or more controllers.

[0114] In some embodiments, objects and advantages of the présent disclosure can be achieved through a continuous processing technique applied to the production of whole lime-cooked masa, in which heating and cooling steps increase the résistant starch, and the lime cooked hull yields a soluble fiber that can bind calcium. Embodiments of this process include providing a clean maize kernel by mixing and conditioning with lime solution, steaming the tempered kernel with saturated steam to effect a partial cooking without wastewater and reduced energy usage, conditioning and cooling the blanched kernel for efficient grinding, milling and adding water to the tempered kernel so as to produce a coarse-ground and fine-ground dough material in order to yield a wasteless limecooked masa, forming the masa into the desired product form, such as tortilla or snack, baking and cooling the food product, and packaging the tortilla, or further baking or frying the food for snack and maize-based foods.

[0115] In some embodiments, objects and advantages of the présent disclosure can be achieved through a continuous processing technique applied to the production of partially whole limecooked masa, in which the hull is separated while leaving the tip cap. Embodiments of this process include providing a clean maize kernel by mixing and conditioning with lime solution, steaming the tempered kernel with saturated steam to effect a partial cooking without wastewater and reduced energy usage, conditioning and cooling the steamed kernel for efficient grinding, crushing the kernel, separating a hull fraction from the ground kernel, milling and adding water to the separated fraction so as to produce a coarse-ground and fine-ground dough material in order to yield a wasteless lime-cooked masa, forming the masa into the desired product form, such as tortilla or snack, baking and cooling the food product, and packaging the tortilla or further baking or frying the food for snack and maize-based foods.

[0116] The présent disclosure introduces a method of making lime-cooked masa. The method generally includes: providing maize kernel having endosperm, germ, pericarp, and tip cap components; after providing the maize kernel, adding water to the maize kernel in a first predetermined proportion, and conditioning, using a first conditioner, the maize kernel for a first predetermined amount of time to cause moisture absorption to within a first predetermined range; liming the maize kernel; cooking, using a cooker, the maize kernel in an environment of steam; after cooking the maize kernel, adding water to the maize kernel in a second predetermined proportion, and conditioning, using a second conditioner, the maize kernel for a second predetermined amount of time to cause moisture absorption to within a second predetermined range; and milling, using one or more mills, the maize kernel.

[0117] The foregoing method embodiment may include one or more of the following éléments, either alone or in combination with one another:

[0118] Execution of the method results in: water consumption of no more than 0.6 parts of water per one part of maize kernel by weight for chip production; water consumption of no more than 0.76 parts of water per one part of maize kernel by weight for tortilla production; negligible wastewater discharge; negligible solid waste; energy consumption of less than 0.5 GJ/ton of the provided maize kernel for chip production; or any combination thereof.

[0119] The method further includes: after milling the maize kernel, cooling, using a cooler, the milled maize kernel; and after cooling the milled maize kernel, kneading, using a kneader, the cooled milled maize kernel into the lime-cooked masa.

[0120] The method further includes: before or during milling the maize kernel, adding water to the maize kernel in a third predetermined proportion.

[0121] The method further includes: after conditioning the maize kernel for the first predetermined amount of time and before cooking the maize kernel, polishing/dehulling, using a pohsher/dehuller, the maize kernel to yield a fine fraction and a coarse fraction, separating, using a first separator, the coarse fraction to yield a purified coarse fraction and pericarp, screening, using a screener, the fine fraction and the pericarp separated from the coarse fraction to yield first, second, and third streams, the first stream including pericarp, the second stream including residual fines, tip cap, and fine pericarp, and the third stream including purified fines, and separating, using a second separator, the second stream to yield tip cap and a residual second stream.

[0122] The method further includes: adding water to the purified coarse fraction and the tip cap separated from the second stream in a third predetermined proportion; and conditioning, using a third conditioner, the purified coarse fraction and the tip cap separated from the second stream for a third predetermined amount of time to cause moisture absorption to within a third predetermined range.

[0123] Cooking, using the cooker, the maize kernel in the environment of steam includes: after conditioning the purified coarse fraction and the tip cap separated from the second stream for the third predetermined amount of time, cooking, using the cooker, the purified coarse fraction, the tip cap separated from the second stream, and the third stream in the environment of steam; and liming the maize kernel includes: adding lime powder to the purified coarse fraction and the tip cap separated from the second stream.

[0124] The method further includes: after conditioning the maize kernel for the second predetermined amount of time and before milling the maize kernel, crushing, using a crusher, the maize kernel into coarse-ground kernel and pericarp, and separating, using a separator, the crushed maize kernel to yield the coarse-ground kernel and the pericarp.

[0125] Milling, using the one or more mills, the maize kernel includes: after separating the crushed maize kernel to yield the coarse-ground kernel and the pericarp, milling, using the one or more mills, the coarse-ground kernel.

[0126] Milling, using the one or more mills, the maize kernel includes: milling a first portion ofthe maize kernel with a first mill to yield fine-ground dough material; and milling a second portion of the maize kernel with a second mill to yield coarse-ground dough material.

[0127] The présent disclosure also introduces a System adapted to make lime-cooked masa. The System generally includes: a first conditioner to which water and maize kernel are adapted to be provided in a first predetermined proportion, the maize kernel having endosperm, germ, pericarp, and tip cap components, wherein the first conditioner is adapted to condition the maize kernel for a first predetermined amount of time to cause moisture absorption to within a first predetermined range; a cooker adapted to cook the maize kernel together with lime in an environment of steam; a second conditioner to which water and the cooked maize kernel are adapted to be provided in a second predetermined proportion, wherein the second conditioner is adapted to condition the cooked maize kernel for a second predetermined amount of time to cause moisture absorption within a second predetermined range; and one or more mills adapted to mill the maize kernel.

[0128] The foregoing System embodiment may include one or more of the following éléments, either alone or in combination with one another:

[0129] Using the System to make lime-cooked masa results in: water consumption of no more than 0.6 parts of water per one part of maize kernel by weight for chip production; water consumption of no more than 0.76 parts of water per one part of maize kernel by weight for tortilla production; negligible wastewater discharge; negligible solid waste; energy consumption of less than 0.5 GJ/ton of the provided maize kernel for chip production; or any combination thereof.

[0130] The System further includes: a cooler adapted to cool the milled maize kernel; and a kneader adapted to knead the cooled maize kernel into the lime-cooked masa.

[0131] Water and the maize kernel are adapted to be provided to the one or more mills in a third predetermined proportion.

[0132] The System further includes: a polisher/dehuller adapted to polish/dehull the maize kernel to yield a fine fraction and a coarse fraction; a first separator adapted to separate the coarse fraction to yield a purified coarse fraction and pericarp; a screener adapted to screen the fine fraction and the pericarp separated from the coarse fraction to yield first, second, and third streams, the first stream including pericarp, the second stream including residual fines, tip cap, and fine pericarp, and the third stream including purified fines; and a second separator adapted to separate the second stream to yield tip cap and a residual second stream.

[0133] Water, the purified coarse fraction, and the tip cap separated from the second stream are adapted to be provided to a third conditioner in a third predetermined proportion; and the System further includes the third conditioner adapted to condition the purified coarse fraction and the tip cap separated from the second stream for a third predetermined amount of time to cause moisture absorption to within a third predetermined range.

[0134] The cooker is adapted to cook the purified coarse fraction, the tip cap separated from the second stream, and the third stream in the environment of steam.

[0135] The System further includes: a crusher adapted to crush the maize kernel into coarse-ground kernel and pericarp; and a separator adapted to separate the crushed maize kernel to yield the coarse-ground kernel and the pericarp.

[0136] The one or more mills are adapted to mill the coarse-ground kernel.

[0137] The one or more mills include: a first mill adapted to mill a first portion of the maize kernel to yield fine-ground dough material; and a second mill adapted to mill a second portion of the maize kernel to yield coarse-ground dough material.

[0138] The présent disclosure also introduces an apparatus, which generally includes: a nontransitory computer readable medium; and a plurality of instructions stored on the non-transitory computer readable medium, wherein the instructions are executed with one or more processors so that the following steps are executed: adding water to maize kernel in a first predetermined proportion, the maize kernel having endosperm, germ, pericarp, and tip cap components; conditioning, using a first conditioner, the maize kernel for a first predetermined amount of time to cause moisture absorption to within a first predetermined range; liming the maize kernel; cooking, using a cooker, the maize kernel in an environment of steam; after cooking the maize kernel, adding water to the maize kernel in a second predetermined proportion, and conditioning, using a second conditioner, the maize kernel for a second predetermined amount of time to cause moisture absorption to within a second predetermined range; and milling, using one or more mills, the maize kernel.

[0139] The foregoing apparatus embodiment may include one or more of the following éléments, either alone or in combination with one another:

[0140] Execution of the instructions with the one or more processors results in: water consumption of no more than 0.6 parts of water per one part of maize kernel by weight for chip production; water consumption of no more than 0.76 parts of water per one part of maize kernel by weight for tortilla production; negligible wastewater discharge; negligible solid waste; energy consumption of less than 0.5 GJ/ton of the provided maize kernel for chip production; or any combination thereof.

[0141] The instructions are executed with the one or more processors so that the following additional steps are executed: after milling the maize kernel, cooling, using a cooler, the milled maize kernel; and after cooling the maize kernel, kneading, using a kneader, the cooled maize kernel into the lime-cooked masa.

[0142] The instructions are executed with the one or more processors so that the following additional step is executed: before or during milling the maize kernel, adding water to the maize kernel in a third predetermined proportion.

[0143] The instructions are executed with the one or more processors so that the following additional steps are executed: after conditioning the maize kernel for the first predetermined amount of time and before cooking the maize kernel, polishing/dehulling, using a polisher/dehuller, the maize kernel to yield a fine fraction and a coarse fraction, separating, using a first separator, the coarse fraction to yield a purified coarse fraction and pericarp, screening, using a screener, the fine fraction and the pericarp separated from the coarse fraction to yield first, second, and third streams, the first stream including pericarp, the second stream including residual fines, tip cap, and fine pericarp, and the third stream including purified fines, and separating, using a second separator, the second stream to yield tip cap and a residual second stream.

[0144] The instructions are executed with the one or more processors so that the following additional steps are executed: adding water to the purified coarse fraction and the tip cap separated from the second stream in a third predetermined proportion; and conditioning, using a third conditioner, the purified coarse fraction and the tip cap separated from the second stream for a third predetermined amount of time to cause moisture absorption to within a third predetermined range.

[0145] Cooking, using the cooker, the maize kernel in the environment of steam includes: after conditioning the purified coarse fraction and the tip cap separated from the second stream for the third predetermined amount of time, cooking, using the cooker, the purified coarse fraction, the tip cap separated from the second stream, and the third stream in the environment of steam; and liming the maize kernel includes: adding lime powder to the purified coarse fraction and the tip cap separated from the second stream.

[0146] The instructions are executed with the one or more processors so that the following additional steps are executed: after conditioning the maize kernel for the second predetermined amount of time and before milling the maize kernel, crushing, using a crusher, the maize kernel into coarse-ground kernel and pericarp, and separating, using a separator, the crushed maize kernel to yield the coarse-ground kernel and the pericarp.

[0147] Milling, using the one or more mills, the maize kernel includes: after separating the crushed maize kernel to yield the coarse-ground kernel and the pericarp, milling, using the one or more mills, the coarse-ground kernel.

[0148] Milling, using the one or more mills, the maize kernel includes: milling a first portion of the maize kernel with a first mill to yield fine-ground dough material; and milling a second portion of the maize kernel with a second mill to yield coarse-ground dough material.

[0149] It is understood that variations may be made in the foregoing without departing from the scope of the présent disclosure.

[0150] In some embodiments, the éléments and teachings of the various embodiments may be combined in whole or in part in some or ail of the embodiments. In addition, one or more of the éléments and teachings of the various embodiments may be omitted, at least in part, and/or combined, at least in part, with one or more of the other éléments and teachings of the various embodiments.

[0151] Any spatial references, such as, for example, “upper,” “lower,” “above,” “below,” “between,” “bottom,” “vertical,” “horizontal,” “angular,” “upwards,” “downwards,” “side-toside,” “left-to-right,” “right-to-left,” “top-to-bottom,” “bottom-to-top,” “top,” “bottom,” “bottomup,” “top-down,” etc., are for the purpose of illustration only and do not limit the spécifie orientation or location of the structure described above.

[0152] In some embodiments, while different steps, processes, and procedures are described as appearing as distinct acts, one or more of the steps, one or more of the processes, and/or one or more of the procedures may also be performed in different orders, simultaneously and/or sequentially. In some embodiments, the steps, processes, and/or procedures may be merged into one or more steps, processes and/or procedures.

[0153] In some embodiments, one or more of the operational steps in each embodiment may be omitted. Moreover, in some instances, some features of the présent disclosure may be employed without a corresponding use of the other features. Moreover, one or more of the above-described embodiments and/or variations may be combined in whole or in part with any one or more of the other above-described embodiments and/or variations.

[0154] Although some embodiments hâve been described in detail above, the embodiments described are illustrative only and are not limiting, and those skilled in the art will readily 5 appreciate that many other modifications, changes and/or substitutions are possible in the embodiments without materially departing from the novel teachings and advantages of the present disclosure. Accordingly, ail such modifications, changes, and/or substitutions are intended to be included within the scope of this disclosure as defined in the following claims. Moreover, it is the express intention of the applicant not to invoke 35 U.S.C. § 112, paragraph 6, for any limitations 10 of any of the claims herein, except for those in which the claim expressly uses the word “means” together with an associated function.

Claims

What is claimed is:

Claims

What is claimed is:

1. A method of making lime-cooked masa, the method comprising:

adding water to maize kernel in a first predetermined proportion, the maize kernel having endosperm, germ, pericarp, and tip cap components;

conditioning, using a first conditioner, the maize kernel for a first predetermined amount of time to cause moisture absorption to within a first predetermined range;

liming the maize kernel;

cooking, using a cooker, the maize kernel in an environment of steam;

after cooking the maize kernel:

adding water to the maize kernel in a second predetermined proportion;

conditioning, using a second conditioner, the maize kernel for a second predetermined amount of time to cause moisture absorption to within a second predetermined range; and milling, using one or more mills, the maize kernel.
2. The method of claim 1, wherein execution of the method results in:

water consumption of no more than 0.6 parts of water per one part of maize kernel by weight for chip production;

water consumption of no more than 0.76 parts of water per one part of maize kernel by weight for tortilla production;

negligible wastewater discharge;

negligible solid waste;

energy consumption of less than 0.5 GJ/ton of the provided maize kernel for chip production; or any combination thereof.
3. The method of claim 1, further comprising:

after milling the maize kernel, cooling, using a cooler, the milled maize kernel;

and after cooling the milled maize kernel, kneading, using a kneader, the cooled milled maize kernel into the lime-cooked masa.
4. The method of claim 1, further comprising:

before or during milling the maize kernel, adding water to the maize kernel in a third predetermined proportion.
5. The method of claim 1, further comprising:

after conditioning the maize kernel for the first predetermined amount of time and before cooking the maize kernel, polishing/dehulling, using a polisher/dehuller, the maize kernel to yield a fine fraction and a coarse fraction, separating, using a first separator, the coarse fraction to yield a purified coarse fraction and pericarp, screening, using a screener, the fine fraction and the pericarp separated from the coarse fraction to yield first, second, and third streams, the first stream including pericarp, the second stream including residual fines, tip cap, and fine pericarp, and the third stream including purified fines, and separating, using a second separator, the second stream to yield tip cap and a residual second stream.
6. The method of claim 5, further comprising:

adding water to the purified coarse fraction and the tip cap separated from the second stream in a third predetermined proportion; and conditioning, using a third conditioner, the purified coarse fraction and the tip cap separated from the second stream for a third predetermined amount of time to cause moisture absorption to within a third predetermined range.
7. The method of claim 6, wherein cooking, using the cooker, the maize kernel in the environment of steam comprises:

after conditioning the purified coarse fraction and the tip cap separated from the second stream for the third predetermined amount of time, cooking, using the cooker, the purified coarse fraction, the tip cap separated from the second stream, and the third stream in the environment of steam;

and wherein liming the maize kernel comprises adding lime powder to the purified coarse fraction and the tip cap separated from the second stream.
8. The method of claim 1, further comprising:

after conditioning the maize kernel for the second predetermined amount of time and before milling the maize kernel, crushing, using a crusher, the maize kernel into coarse-ground kernel and pericarp, and separating, using a separator, the crushed maize kernel to yield the coarse-ground kernel and the pericarp.
9. The method of claim 8, wherein milling, using the one or more mills, the maize kernel comprises:

after separating the crushed maize kernel to yield the coarse-ground kernel and the pericarp, milling, using the one or more mills, the coarse-ground kernel.
10. The method of claim 1, wherein milling, using the one or more mills, the maize kernel comprises:

milling a first portion of the maize kernel with a first mill to yield fine-ground dough material; and milling a second portion of the maize kernel with a second mill to yield coarse-ground dough material.
11. A System adapted to make lime-cooked masa, the System comprising:

a first conditioner to which water and maize kernel are adapted to be provided in a first predetermined proportion, the maize kernel having endosperm, germ, pericarp, and tip cap components, wherein the first conditioner is adapted to condition the maize kernel for a first predetermined amount of time to cause moisture absorption to within a first predetermined range;

a cooker adapted to cook the maize kernel together with lime in an environment of steam; a second conditioner to which water and the cooked maize kernel are adapted to be provided in a second predetermined proportion, wherein the second conditioner is adapted to condition the cooked maize kernel for a second predetermined amount of time to cause moisture absorption within a second predetermined range;

and one or more mills adapted to mill the maize kernel.
12. The System of claim 11, wherein using the System to make lime-cooked masa results in: water consumption of no more than 0.6 parts of water per one part of maize kernel by weight for chip production;

water consumption of no more than 0.76 parts of water per one part of maize kernel by weight for tortilla production;

negligible wastewater discharge;

negligible solid waste;

energy consumption of less than 0.5 GJ/ton of the provided maize kernel for chip production; or any combination thereof.
13. The System of claim 11, further comprising:

a cooler adapted to cool the milled maize kernel; and a kneader adapted to knead the cooled maize kernel into the lime-cooked masa.
14. The System of claim 11, wherein water and the maize kernel are adapted to be provided to the one or more mills in a third predetermined proportion.
15. The System of claim 11, further comprising:

a polisher/dehuller adapted to polish/dehull the maize kernel to yield a fine fraction and a coarse fraction;

a first separator adapted to separate the coarse fraction to yield a purified coarse fraction and pericarp;

a screener adapted to screen the fine fraction and the pericarp separated from the coarse fraction to yield first, second, and third streams, the first stream including pericarp, the second stream including residual fines, tip cap, and fine pericarp, and the third stream including purified fines; and a second separator adapted to separate the second stream to yield tip cap and a residual second stream.
16. The System of claim 15, wherein water, the purified coarse fraction, and the tip cap separated from the second stream are adapted to be provided to a third conditioner in a third predetermined proportion; and wherein the System further comprises the third conditioner adapted to condition the purified coarse fraction and the tip cap separated from the second stream for a third predetermined amount of time to cause moisture absorption to within a third predetermined range.
17. The System of claim 16, wherein the cooker is adapted to cook the purified coarse fraction, the tip cap separated from the second stream, and the third stream in the environment of steam.
18. The System of claim 11, further comprising:

a crusher adapted to crush the maize kernel into coarse-ground kernel and pericarp; and a separator adapted to separate the crushed maize kernel to yield the coarse-ground kernel and the pericarp.
19. The System of claim 18, wherein the one or more mills are adapted to mill the coarseground kernel.
20. The system of claim 11, wherein the one or more mills comprise:

a first mill adapted to mill a first portion of the maize kernel to yield fine-ground dough material; and a second mill adapted to mill a second portion of the maize kernel to yield coarse-ground dough material.
21. An apparatus, comprising: a non-transitory computer readable medium; and a plurality of instructions stored on the non-transitory computer readable medium, wherein the instructions are executed with one or more processors so that the following steps are executed:

adding water to maize kernel in a first predetermined proportion, the maize kernel having endosperm, germ, pericarp, and tip cap components;

conditioning, using a first conditioner, the maize kernel for a first predetermined amount of time to cause moisture absorption to within a first predetermined range;

liming the maize kernel;

cooking, using a cooker, the maize kernel in an environment of steam;

after cooking the maize kernel:

adding water to the maize kernel in a second predetermined proportion, conditioning, using a second conditioner, the maize kernel for a second predetermined amount of time to cause moisture absorption to within a second predetermined range; and milling, using one or more mills, the maize kernel.
22. The apparatus of claim 21, wherein execution of the instructions with the one or more processors results in:

water consumption of no more than 0.6 parts of water per one part of maize kernel by weight for chip production;

water consumption of no more than 0.76 parts of water per one part of maize kernel by weight for tortilla production;

negligible wastewater discharge;

negligible solid waste;

energy consumption of less than 0.5 GJ/ton of the provided maize kernel for chip production; or any combination thereof.
23. The apparatus of claim 21, wherein the instructions are executed with the one or more processors so that the following additional steps are executed:

after milling the maize kernel, cooling, using a cooler, the milled maize kernel; and after cooling the maize kernel, kneading, using a kneader, the cooled maize kernel into the lime-cooked masa.
24. The apparatus of claim 21, wherein the instructions are executed with the one or more processors so that the following additional step is executed:

before or during milling the maize kernel, adding water to the maize kernel in a third predetermined proportion.
25. The apparatus of claim 21, wherein the instructions are executed with the one or more processors so that the following additional steps are executed:

after conditioning the maize kernel for the first predetermined amount of time and before cooking the maize kernel, polishing/dehulling, using a polisher/dehuller, the maize kernel to yield a fine fraction and a coarse fraction, separating, using a first separator, the coarse fraction to yield a purified coarse fraction and pericarp, screening, using a screener, the fine fraction and the pericarp separated from the coarse fraction to yield first, second, and third streams, the first stream including pericarp, the second stream including residual fines, tip cap, and fine pericarp, and the third stream including purified fines, and separating, using a second separator, the second stream to yield tip cap and a residual second stream.
26. The apparatus of claim 25, wherein the instructions are executed with the one or more processors so that the following additional steps are executed:

adding water to the purified coarse fraction and the tip cap separated from the second stream in a third predetermined proportion; and conditioning, using a third conditioner, the purified coarse fraction and the tip cap separated from the second stream for a third predetermined amount of time to cause moisture absorption to within a third predetermined range.
27. The apparatus of claim 26, wherein cooking, using the cooker, the maize kernel in the environment of steam comprises:

after conditioning the purified coarse fraction and the tip cap separated from the second stream for the third predetermined amount of time, cooking, using the cooker, the purified coarse fraction, the tip cap separated from the second stream, and the third stream in the environment of steam;

and wherein liming the maize kernel comprises adding lime powder to the purified coarse fraction and the tip cap separated from the second stream.
28. The apparatus of claim 21, wherein the instructions are executed with the one or more processors so that the following additional steps are executed:

after conditioning the maize kernel for the second predetermined amount of time and before milling the maize kernel, crushing, using a crusher, the maize kernel into coarse-ground kernel and pericarp, and separating, using a separator, the crushed maize kernel to yield the coarse-ground kernel and the pericarp.
29. The apparatus of claim 28, wherein milling, using the one or more mills, the maize kernel comprises:

after separating the crushed maize kernel to yield the coarse-ground kernel and the

5 pericarp, milling, using the one or more mills, the coarse-ground kernel.
30. The apparatus of claim 21, wherein milling, using the one or more mills, the maize kernel comprises:

milling a first portion of the maize kernel with a first mill to yield fine-ground dough

10 material; and milling a second portion of the maize kernel with a second mill to yield coarse-ground dough material.