Patent Publication Number: US-2021188664-A1

Title: Humic and fulvic black water based beverage for human consumption

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
     This Patent Application is a Continuation-in part and claims priority to United States Patent Application entitled: “HUMIC AND FULVIC BLACK WATER BASED BEVERAGE FOR HUMAN CONSUMPTION”, U.S. Ser. No. 16/124,128 filed on Sep. 6, 2018, the U.S. Patent Application being incorporated herein by reference. 
    
    
     BACKGROUND 
     Humic and fulvic acids are extracted using a number of chemical processes that add chemicals which are not suitable for human consumption or use. Those extracted humus sourced acids are used in fertilizers for agricultural use and in some cases added to animal feeds. Some of the chemicals used in the processes and some of the processes introduce chemicals borne in water that can produce chemical reactions or leave residual amounts that are known carcinogens. An extraction method to extract both humic and fulvic acids for human consumption and use should not include the use of those or similar types of chemicals and eliminate any added chemicals that could be present in any mixing water. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  shows a block diagram of an overview of black water humic and fulvic acids extraction for human consumption and use method and devices of one embodiment. 
         FIG. 2  shows for illustrative purposes only an example of black water humic and fulvic acids extraction for human consumption and use method and devices of one embodiment. 
         FIG. 3A  shows for illustrative purposes only an example humic and fulvic acids extraction and separation of one embodiment. 
         FIG. 3B  shows for illustrative purposes only an example humic and fulvic acids extraction particulate waste separation of one embodiment. 
         FIG. 3C  shows for illustrative purposes only an example humic and fulvic acids extraction sterilization of one embodiment. 
         FIG. 4  shows a block diagram of an overview of extraction for human consumption and use processing of one embodiment. 
         FIG. 5  shows a block diagram of an overview of humic and fulvic acids extraction devices and processes of one embodiment. 
         FIG. 6  shows for illustrative purposes only an example of first stage humate-treated water mixture particulate filtration of one embodiment. 
         FIG. 7  shows for illustrative purposes only an example of chopped/pulverized humate—treated water mixture constituents of one embodiment. 
         FIG. 8  shows for illustrative purposes only an example of first stage particulate filter of one embodiment. 
         FIG. 9  shows for illustrative purposes only an example of second stage particulate filter of one embodiment. 
         FIG. 10  shows for illustrative purposes only an example of third stage particulate filter of one embodiment. 
         FIG. 11  shows for illustrative purposes only an example of fourth stage particulate filter of one embodiment. 
         FIG. 12  shows for illustrative purposes only an example of fifth stage particulate filter of one embodiment. 
         FIG. 13  shows for illustrative purposes only an example of second UV light treatment process sterilization and dechlorination of one embodiment. 
         FIG. 14  shows for illustrative purposes only an example of a particulate filter settling tank of one embodiment. 
         FIG. 15  shows for illustrative purposes only an example of ultraviolet light exposure channels of one embodiment. 
         FIG. 16A  shows for illustrative purposes only an example of UV light dechlorination of one embodiment. 
         FIG. 16B  shows for illustrative purposes only an example of UV light sterilization of one embodiment. 
         FIG. 17A  shows for illustrative purposes only an example of a humic acid and fulvic acid separation and segregation process overview of one embodiment. 
         FIG. 17B  shows for illustrative purposes only an example of a humic-fulvic acid separation chamber of one embodiment. 
         FIG. 17C  shows for illustrative purposes only an example of fulvic acid separation and segregation of one embodiment. 
         FIG. 17D  shows for illustrative purposes only an example of humic acid separation and segregation of one embodiment. 
         FIG. 18A  shows for illustrative purposes only an example of a pH scale of one embodiment. 
         FIG. 18B  shows a block diagram of an overview flow chart of titration curve of one embodiment. 
         FIG. 19A  shows a block diagram of an overview flow chart of treating water processes of one embodiment. 
         FIG. 19B  shows a block diagram of an overview flow chart of treating water additional processes of one embodiment. 
         FIG. 20  shows a block diagram of an overview flow chart of extraction and segregation of humic and fulvic acids of one embodiment. 
         FIG. 21  shows a block diagram of an overview flow chart of creating products for human consumption and use with humic and fulvic acids of one embodiment. 
         FIG. 22  shows a block diagram of an overview flow chart of a continuation of creating products for human consumption and use with humic and fulvic acids of one embodiment. 
         FIG. 23A  shows a block diagram of an overview of artificial sweetener ingredients of one embodiment. 
         FIG. 23B  shows a block diagram of an overview of natural sweetener ingredients of one embodiment. 
         FIG. 24  shows for illustrative purposes only an example of a black water bottling process of one embodiment. 
         FIG. 25  shows for illustrative purposes only an example of a bottling electronic monitoring and control network of one embodiment. 
         FIG. 26  shows for illustrative purposes only an example of a black water bottling quality control process of one embodiment. 
         FIG. 27  shows a block diagram of an overview of product labeling of one embodiment. 
     
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     In a following description, reference is made to the accompanying drawings, which form a part hereof, and in which is shown by way of illustration a specific example in which the invention may be practiced. It is to be understood that other embodiments may be utilized and structural changes may be made without departing from the scope of the embodiments. 
     General Overview: 
     It should be noted that the descriptions that follow, for example, in terms of a black water beverage method and devices is described for illustrative purposes and the underlying system can apply to any number and multiple types of apparatuses and processes. In one embodiment of the present invention, the black water beverage method and devices for using at least one or more humate sources to extract humic and fulvic acids of one embodiment. The black water beverage method and devices includes at least one or more beverage product and includes black water, soft drinks and alcoholic beverages using the embodiments. 
     In one embodiment, the fulvic and humic water solution is used as a base for soda beverages, including cola and root beer. In another embodiment, the fulvic and humic water solution is used as a base for coffee and tea. In another embodiment, the black colored water is used as a base for carbonated water, distilled water, sparkling water, spring water and purified water. In another embodiment, the black colored water is used as a base for alcoholic beverages, such as for mixed alcoholic drinks. 
       FIG. 1  shows a block diagram of an overview of black water humic and fulvic acids extraction for human consumption method and use and devices of one embodiment.  FIG. 1  shows humate sources  100  including humus soil  110 , coal  120 , ocean water  130 , inland stream  140 , degradated plants  150  and composted plants  155 . Treated water storage  165  contains a water source purified with various processes including filtration, ultrafiltration, purification, ultra-purification and sterilization that produce potable water. The treated water is mixed with at least one of the humate sources  100  that have been processed using a humate materials chopper  160  and chopped humate materials pulverizer  161  in a mixing tank  171 . 
     The humate and treated water mixture filtration, dechlorination, defluoridation, sterilization, pH adjustment and temperature control devices and processes  170  is followed by humic and fulvic acid molecules separation and segregated storage suspended in purified water  180 . The black water humic and fulvic acids extraction for human consumption and use method and devices processes and devices are controlled using digital processors, digital servers, digital computers, digital sensors, digital analyzers, digital valves, digital pumps, and other digitally controlled devices including wireless digital devices for automating individual process steps and operations. These processes produce humic and fulvic acids that are suitable for human consumption in for example a black colored water beverage, and other black colored water beverages including flavored beverages including a fruit flavored beverage, tea, coffee, soft drinks, alcoholic beverages, and products for human use including supplements, cosmetics, pharmaceuticals and food additives. 
     The humic and fulvic acids that are suitable for cosmetic products including for example skin moisturizers, perfumes, lipsticks, fingernail polishes, eye and facial makeup preparations, cleansing shampoos, permanent waves, hair colors and deodorants and other components used in cosmetic products. Hemp and medicinal legalized CBD and medicinal legalized cannabis are used in the solution for the human consumption beverages and the human use topical products for medicinal reasons. The humic and fulvic acids that are suitable for pharmacological products including for example fulvic sunscreen creams and lotions, fulvic first aid topical creams including fulvic topical agents to enhance healing of wounds infected with drug-resistant pathogens; and incorporating malacidins to attack and kill many types of super bugs, such as methicillin-resistant Staphylococcus aureus (MRSA) of one embodiment. 
     Composting a Humate Source: 
     Humus refers to decomposed organic matter. Humus is found on the forest floor where leaves and plant material decompose naturally. Humus can also result as a product of composting organic materials including vegetation. One humate source is degradated plants  150  of  FIG. 1 . Composting provides benefits in the supplying of composted plants  155  of  FIG. 1  as a humate source as it is done in an organized and well managed process at virtually any location. 
     Decomposition of vegetative organic materials using composting is controlled to produce desired variants in a humate source. For example different vegetation selections are highly aromatic. On average 35% of the humic acid (HA) molecules are aromatic. Humate used for extracting humic and fulvic acids sourced from composting highly aromatic vegetation including flowers will retain the aromaticity of the selected vegetation. Products for human use and consumption including the aromatic humic acids ingredients can include the aromatic characteristics of the selected vegetation. 
     Selective composting can increase the production of humic and fulvic acids independently. For example, a composting environment that is acidic tends to produce plant debris with a greater percentage of fulvic acids. In a neutral and alkaline composting environment a large percentage of the organic matter is present in the form of humic acids and humin. 
     Organic matter is composed of minerals and trace elements required by plants. Different plants have varying amounts of certain minerals and trace elements. Composting of vegetation selected by the amounts of certain minerals and trace elements in the vegetation can result in the humic and fulvic acids extracted having greater concentrations of those certain minerals and trace elements for providing a desired purpose of one embodiment. 
     Fulvic and Humic Minerals: 
     Minerals and trace elements present in extracted humic and fulvic acids will vary by those present in the humate source materials. Some of the more common minerals present include iron (Fe), copper (Cu), zinc (Zn), magnesium (Mg), manganese (Mn), and calcium (Ca). Many scientific studies have shown that humic substances [humic acids (HAs) and fulvic acids (FAs)] present in the root zone of the organic vegetation of the humate material reduce the toxicity of metal cations. 
     Fulvic and Humic Minerals Supplements: 
     Supplements are a convenient way for a consumer to add additional vitamins, minerals and other beneficial elements to augment their dietary intake. Humic and fulvic acids in an aqueous solution is one preparation wherein the consumer can take a suggested dosage orally or put a suggested dosage into a familiar beverage or liquid containing food product for example a soup. Another preparation can include a powdered form wherein the humic and fulvic acids are mixed with for example a fruit for flavoring, the mixture liquefied and then dehydrated and pulverized into a powder. The pulverized powder is pressed into a tablet or filled into a suitable capsule container of one embodiment. 
     Fulvic and Humic Minerals Food Additives: 
     Food additives are prevalent in processed foods. Food additive can include for example essential vitamins to provide at least a portion of a recommended daily diet intake. Humic and fulvic acids in an aqueous solution is one preparation wherein a food digital processor can include a predetermined dosage into an ingredient mixture during processing for example a breakfast cereal, cookie batter, soup mixture or other processed food products. Another preparation can include a powdered form wherein an aqueous solution of humic and fulvic acids are mixed with for example other ingredients and dried or baked during the processing to form a powder or formed solid for example a baking mixture or a nutrient bar of one embodiment. 
     DETAILED DESCRIPTION 
       FIG. 2  shows for illustrative purposes only an example of black water humic and fulvic acids extraction for human consumption and use method and devices of one embodiment.  FIG. 2  shows a process wherein at least one of the humate sources  100  of  FIG. 1  is processed in the humate materials chopper  160  and chopped humate materials pulverizer  161  then collected in a chopped-pulverized humate material storage  200  and deposited in the mixing tank  171  with a quantity of treated water from the treated water storage  165 . A humate-treated water mixture supply piping  201  conveys the mixture to a first stage humate-treated water mixture particulate filtration  202 . The first stage humate-treated water mixture particulate filtration  202  can include ultrafiltration. Ultrafiltration involves the filtration of water through a semi-permeable membrane to remove suspended particles. Ultrafiltration is a physical filtration process typically used as a pretreatment method to separate solids from water used for industrial processes, such as food and beverage processing, semiconductor manufacturing, pharmaceutical production and power generation. A filtered humate-treated water mixture supply  203  is processed through a second stage humate-treated water mixture particulate filtration settling tank  210 . The particulates filtered out of the mixture are accumulated in a particulate disposal container  211  of one embodiment. 
     UV light dechlorination  220  is performed on the mixture before it is processed to an adsorption defluoridation device  230  with granular activated carbon (GAC). The fluoride molecules adsorb to surfaces of the granular activated carbon (GAC). A fresh treated water storage tank  240  with a fresh treated water temperature control device and a pH control device  241  is used to supply additional water and control the desired pH level. The pH level is regulated to be greater than or equal than 8.5 and less than 10. A fresh treated water supply pipe  242  is used to convey treated water to a humic-fulvic acid separation chamber  250  with a bed of activated carbon material, a separation vacuum device, temperature regulating device and pH control device  241 . The fulvic acid separation vacuum device and temperature regulating device process the separated fulvic acid molecules that have concentrated in the humic-fulvic acid separation chamber  250 . The separation vacuum device uses a vacuum pressure to draw the concentrated fulvic acid molecules into a fulvic acid storage tank  252  with temperature and pH control device  241  of one embodiment. 
     A first humic acid separation chamber  260  with a humic acid separation vacuum device and temperature regulating device  263  in a second humic acid separation chamber  261  is used to draw separated humic acid molecules that have concentrated in the second humic acid separation chamber  262  into a humic acid storage tank  264  with temperature and pH control device  241 . The segregated fulvic and humic acid molecules suspended in the treated water are stored for use in products of one embodiment. 
     Humic and Fulvic Acids Extraction and Separation: 
       FIG. 3A  shows for illustrative purposes only an example of humic and fulvic acids extraction and separation of one embodiment.  FIG. 3A  shows the humate-treated water mixture supply piping  201  conveying the mixture to the first stage humate-treated water mixture particulate filtration  202 . The humate-treated water mixture particulate filtration process  202  includes removable filter elements  300  including semi-permeable membrane filter elements. The filtered humate-treated water mixture supply  203  is processed through the second stage humate-treated water mixture particulate filtration settling tank  210 . Particulates filtered out of the mixture are conveyed to the particulate waste disposal container  211  and second stage particulate disposal container  212  of one embodiment. 
     The UV light dechlorination  220  processes is followed by conveying the mixture to the adsorption defluoridation device  230 . Chlorine and fluoride are found in water and found in humate sources through run-off of municipal water used domestically and by irrigation. These are harmful to humans at differing concentrations. After defluoridation settled ha-fa suspended mixture is stored in a settled ha-fa suspended mixture  232  settled ha-fa suspended mixture storage tank  231 . Supplemental water  241  during the process is supplied from the fresh treated water storage tank  240  with the fresh treated water temperature control device through the fresh treated water supply pipe  242  of one embodiment. 
     Humic and Fulvic Acids Extraction Particulate Waste Separation: 
       FIG. 3B  shows for illustrative purposes only an example of humic and fulvic acids extraction particulate waste separation of one embodiment.  FIG. 3B  shows a particulate waste accumulator funnel  311  used to accumulate the particulate waste at the particulate waste disposal discharge pipe  312  that includes a butterfly valve  313 . The butterfly valve  313  is opened to pass the particulate waste to the particulate waste disposal container  211  from the particulate waste accumulator funnel  311 . The particulate waste disposal container  211  includes a particulate waste water dehydrator  314  to dry the particulate waste for dry disposal and wet disposal of any liquid residue of one embodiment. 
     Humic and Fulvic Acids Extraction Sterilization: 
       FIG. 3C  shows for illustrative purposes only an example of humic and fulvic acids extraction sterilization of one embodiment.  FIG. 3C  shows the UV light dechlorination  220  processor that includes UV light high intensity bulbs  320  and UV light ballast  321 . The high intensity wave length UV light beams pass through the aqueous mixtures as it flows through a filtered humate-treated water mixture supply serpentine channel  322 . The serpentine channel  322  is fabricated to allow a predetermined amount of UV light exposure to the aqueous mixture to kill microorganisms of one embodiment. 
     Extraction for Human Consumption and Use Processing: 
       FIG. 4  shows a block diagram of an overview of extraction for human consumption and use processing of one embodiment.  FIG. 4  shows using black water humic and fulvic acids extraction for human consumption and use method and devices using at least one humate source  400 . A process is used for chopping and pulverizing the at least one humate source  410 . Processing includes treating and sterilizing a water source to create a purified potable water source supply for mixing including adjusting the pH level, dechlorinating, defluoridating, filtering particulates, and desalinating  420 . The processed humate source and treated and sterilized water are deposited into a mixing tank for mixing the purified aqueous ingredient with chopped and pulverized humate materials  430 . The mixture ingredients are processed by treating the purified aqueous ingredient with chopped and pulverized humate materials mixture including sterilizing, adjusting the pH level, dechlorinating, defluoridating, filtering particulates, and desalinating  440 . Processing continues for segregating and storing the fulvic acid molecules from mixture  450  and segregating and storing the humic acid molecules from mixture  460 . The humic and fulvic acids extracted, segregated and suspended in an aqueous solution are used for creating a black colored water beverage, flavored beverages, soft drinks, alcoholic beverages, supplements and food additives using a mixture of segregated humic and fulvic molecules ingredients  470  of one embodiment. 
     The beverage is processed and treated with the extracted humic acid and fulvic acid molecules for creating a mixed solution, wherein the fulvic acid and humic acid molecules are sufficiently suspended within water molecules to create a black colored water. 
     Fulvic Cosmetic Products: 
     The humic and fulvic acids that are suitable for cosmetic products including for example skin moisturizers, perfumes, lipsticks, fingernail polishes, eye and facial makeup preparations, cleansing shampoos, permanent waves, hair colors and deodorants and other components used in cosmetic products. Fulvic cosmetic products can include pharmacological components for example incorporating malacidins and other antibiotic agents to enhance healing of wounds, skin irritants and infections of one embodiment. 
     Fulvic Pharmacological Products: 
     The humic and fulvic acids that are suitable for pharmacological products including for example fulvic sunscreen creams and lotions, fulvic first aid topical creams including fulvic topical agents to enhance healing of wounds infected with drug-resistant pathogens; and incorporating malacidins to attack and kill many types of super bugs, such as methicillin-resistant Staphylococcus aureus (MRSA) and other antibiotic agents to enhance healing of wounds, skin irritants and infections of one embodiment. 
     Humic and Fulvic Acids Extraction Devices and Processes: 
       FIG. 5  shows a block diagram of an overview of humic and fulvic acids extraction devices and processes of one embodiment.  FIG. 5  shows humate sources  100  including humus soil  110 , coal  120 , ocean water  130 , inland stream water  140 , degradated plants  150  and composted plants  155 . Treated water purification processes  500  are used to create potable water for human consumption and is stored in treated water storage temperature and pH control tanks  501 . The treated water processes  500  can include creating oxygenated water using electrolysis and distilled water for human consumption and use. Treated water discharge piping to mixing and bottling processes  502  is used to deposit treated water to the mixing tank  171 . Humate sources chopping and pulverizing processes  510  prepare the humate sources for deposition into the mixing tank  171  with the treated water. 
     Humic and fulvic acids extraction devices and processes  520  are used to separate humic acid molecules suspended in treated water  530  which are stored in humic acid concentrate suspended in treated water storage tank including temperature and pH control apparatuses and processes  540 . The processed humic acid concentrate is conveyed through a humic acid discharge piping to mixing and bottling processes  550 . Fulvic acid molecules suspended in treated water  560  are stored in fulvic acid concentrate suspended in treated water storage tank including temperature and pH control apparatuses and processes  570 . The processed fulvic acid concentrate is conveyed through fulvic acid discharge piping to mixing and bottling processes  580 . 
     The bottling processes include a filling control station where amounts of humic acid, fulvic acid and/or ulmic acid concentrates are added in predetermined quantities according to the beverage being bottled. For example ulmic acids are soluble in alcohol and may be added to the filling process for alcoholic beverages. Selective aromatic humic acids may be added to flavored or fruit beverages in a greater percentage than fulvic acids. Aromatic humic acids alone may be added to cosmetic products being bottled for example perfumes. The bottling processes include temperature regulating devices to assure the bottled mixtures do not exceed temperature thresholds both high and low established for the various types of beverages and to prevent clouding. The bottling processes also include pH level measurement devices to check and adjust the pH levels as the various beverage ingredients are added to prevent precipitation of the humic acid in an over acidic pH level of one embodiment. 
     First Stage Humate-Treated Water Mixture Particulate Filtration: 
       FIG. 6  shows for illustrative purposes only an example of first stage humate-treated water mixture particulate filtration of one embodiment.  FIG. 6  shows the humate-treated water mixture supply piping  201  conveying a humate-treated water mixture supply  610  to a process. The humate-treated water mixture supply  610  is processed using pH sensors and pH level adjustment devices  602  to adjust the pH to a desired level. The pH level is adjusted to maintain a pH in which humic acid molecules are soluble in water. The first stage humate-treated water mixture particulate filtration  202  conveys an unfiltered humate-treated water mixture  620  through a first stage particulate filter  621 . The first stage particulate filter  621  is a mesh at a predetermined size to block particulates of a size greater than the mesh openings. A first stage particulate filter treated water flush supply pipe  622  supplies first stage particulate filter flush treated water  623  to flush the blocked particulates off of the first stage particulate filter  621  to prevent clogging of mesh openings and allow the remaining fluid to pass through. The first stage particulate filter flush treated water  623  exits the first stage particulate filter  621  through a first stage particulate filter treated water flush discharge pipe  624  and first stage particulate filter flush treated water discharge  625  is conveyed to the particulate disposal container  211  of one embodiment. 
     A first stage particulate filtered humate-treated water mixture  630  is passed through a second stage particulate filter  631  mesh at a predetermined size to block particulates of a size greater than the mesh openings. A second stage particulate filter treated water flush supply pipe  632  conveys second stage particulate filter flush treated water  633  to clean the second stage particulate filter  631 . The flush water exits through a second stage particulate filter treated water flush discharge pipe  634  wherein second stage particulate filter flush treated water discharge  635  is conveyed to the particulate disposal container  211  of one embodiment. 
     A second stage particulate filtered humate-treated water mixture  640  is passed through a third stage particulate filter  641  with a predetermined sized mesh to block particulates of a size greater than the mesh openings. A third stage particulate filter treated water flush supply pipe  642  conveys third stage particulate filter flush treated water  643  used to flush blocked particulates off of the third stage particulate filter  641 . A third stage particulate filter treated water flush discharge pipe  644  conveys third stage particulate filter flush treated water discharge  645  to the particulate disposal container  211  of one embodiment. 
     A third stage particulate filtered humate-treated water mixture  650  passes through a fourth stage particulate filter  651  with a particulate blocking mesh of a predetermined size to block particulates larger than the mesh openings. Fourth stage particulate filter flush treated water  653  passes through a fourth stage particulate filter treated water flush supply pipe  652  to clean the fourth stage particulate filter  651 . A fourth stage particulate filter treated water flush discharge pipe  654  passes fourth stage particulate filter flush treated water discharge  655  to the particulate disposal container  211  of one embodiment. 
     A fourth stage particulate filtered humate-treated water mixture  660  flows through a fifth stage particulate filter  661  with a mesh of a predetermined size to block particulates larger than the predetermined size. A fifth stage particulate filter treated water flush supply pipe  662  supplies fifth stage particulate filter flush treated water  663  to clean the fifth stage particulate filter  661  of blocked particulate which pass out of the filter through a fifth stage particulate filter treated water flush discharge pipe  664 . Fifth stage particulate filter flush treated water discharge  665  is conveyed to the particulate disposal container  211 . The fifth stage particulate filtered humate-treated water mixture  670  passes through piping to the next processes of one embodiment. 
     The fifth stage particulate filtered humate-treated water mixture  670  flows through a sixth stage particulate filter wherein UV light treatment devices  666  provide a treatment to kill bacteria and microorganisms and wherein a plurality of anodes  672  connected to a power circuit  677 , not shown, and cathodes  671  connected to a power circuit  673 , not shown, are energized to create an electrical charge  676  between an anode  672  and a corresponding cathode  671 . The electrical charge  676  kills any bacteria and microorganisms, not shown, remaining in the fifth stage particulate filtered humate-treated water mixture  670 . 
     Sixth stage particulate accumulation discharge  675  is conveyed to the particulate disposal container  211  through a sixth stage particulate accumulation discharge pipe  674 . The sixth stage particulate filtered water  679  then flows out through a post filtration valve  681  and pipe  680  to the second stage humate-treated water mixture particulate filtration settling tank  210  of  FIG. 2  of one embodiment. 
     Chopped/Pulverized Humate—Treated Water Mixture Constituents: 
       FIG. 7  shows for illustrative purposes only an example of chopped/pulverized humate—treated water mixture constituents of one embodiment.  FIG. 7  shows chopped/pulverized humate—treated water mixture constituents  700  in the humate-treated water mixture supply piping  201 . The mixture flow  701  is treated by injecting soda ash to raise pH  710  above the pH level of humic acid solubility. The chopped/pulverized humate—treated water mixture constituents  700  include s+ soda ash molecule  720 , p 2  particulate size  2   752 , protozoa microorganism  760 , p 1  particulate size  1   751 , p 3  particulate size  3   753 , p 4  particulate size  4   754 , ha humic acid molecule  730 , bact. bacteria microorganism  762 , cl chlorine molecule  770 , fa fulvic acid molecule  740  of one embodiment. Descriptions of further processing are shown in  FIG. 8 . 
     First Stage Particulate Filter: 
       FIG. 8  shows for illustrative purposes only an example of first stage particulate filter of one embodiment.  FIG. 8  shows continuing from  FIG. 7  the humate-treated water mixture supply piping  201  conveys the mixture to the first stage particulate filter  621  flow  701  where p 1  particulate size  1  are blocked  810  from the chopped/pulverized humate—treated water mixture  700 . The first stage particulate filter treated water flush supply pipe  622  supplies first stage particulate filter flush treated water  623  to flush the blocked particulates off of the first stage particulate filter  621  to prevent clogging. The first stage particulate filter treated water flush discharge pipe  624  conveys the first stage particulate filter flush treated water discharge  625  of one embodiment. The description of the process continues on  FIG. 9 . 
     Second Stage Particulate Filter: 
       FIG. 9  shows for illustrative purposes only an example of second stage particulate filter of one embodiment.  FIG. 9  shows continuing from  FIG. 8  the humate-treated water mixture supply piping  201  continue the flow  701  of the mixture through the second stage particulate filter  631  where p 2  particulate size  2  are blocked  910  out of the chopped/pulverized humate—treated water mixture  700 . The second stage particulate filter treated water flush supply pipe  632  conveys second stage particulate filter flush treated water  633  to clean the second stage particulate filter  631 . The flush water exits through a second stage particulate filter treated water flush discharge pipe  634  wherein the second stage particulate filter flush treated water discharge  635  is conveyed of one embodiment. The description of the process continues on  FIG. 10 . 
     Third Stage Particulate Filter: 
       FIG. 10  shows for illustrative purposes only an example of third stage particulate filter of one embodiment.  FIG. 10  shows continuing from  FIG. 9  the flow  701  through the humate-treated water mixture supply piping  201  through the third stage particulate filter  641  where p 3  particulate size  3  are blocked  1010  out of the chopped/pulverized humate—treated water mixture  700 . The third stage particulate filter treated water flush supply pipe  642  conveys third stage particulate filter flush treated water  643  used to flush blocked particulates off of the third stage particulate filter  641 . The third stage particulate filter treated water flush discharge pipe  644  conveys third stage particulate filter flush treated water discharge  645  for discharge processing of one embodiment. The description of the process continues on  FIG. 11 . 
     Fourth Stage Particulate Filter: 
       FIG. 11  shows for illustrative purposes only an example of fourth stage particulate filter of one embodiment.  FIG. 11  shows continuing from  FIG. 10  humate-treated water mixture supply piping  201  continuing the flow  701  to pass through fourth stage particulate filter  651  where p 4  particulate size  4  are blocked  1110  and bact. bacteria microorganism are blocked  1120  out of the chopped/pulverized humate—treated water mixture  700 . The fourth stage particulate filter flush treated water  653  passes through a fourth stage particulate filter treated water flush supply pipe  652  to clean the fourth stage particulate filter  651 . The fourth stage particulate filter treated water flush discharge pipe  654  passes fourth stage particulate filter flush treated water discharge  655  of one embodiment. The description of the process continues on  FIG. 12 . 
     Fifth Stage Particulate Filter: 
       FIG. 12  shows for illustrative purposes only an example of fifth stage particulate filter of one embodiment.  FIG. 12  shows continuing from FIG. lithe flow  701  passing through the humate-treated water mixture supply piping  201  where UV light treatment devices  666  provide a first UV light treatment process sterilization  1220  then flows to and through the fifth stage particulate filter  661 . The mixture is also processed using a continuation of the first UV light treatment process sterilization  1250  after passing through the fifth stage particulate filter  661  where bact. bacteria microorganism and protozoa are killed in the chopped/pulverized humate—treated water mixture  700 . 
     The first UV light treatment process sterilization  1220  includes UV light treatment devices  666  to produce beams of the UV light for penetrating the mixture and killing the bacteria microorganisms and protozoa microorganisms. The plurality of anodes  672  and cathodes  671  are energized to create an electrical charge  676  between an anode  672  and a corresponding cathode  671 . The electrical charge  676  kills any bacteria and microorganisms, not shown, remaining in the fifth stage particulate filtered humate-treated water mixture  670  of one embodiment. The description of the process continues on  FIG. 13 . 
     Second UV Light Treatment Process Sterilization and Dechlorination: 
       FIG. 13  shows for illustrative purposes only an example of second UV light treatment process sterilization and dechlorination of one embodiment.  FIG. 13  shows a continuation from  FIG. 12  a second UV light treatment process sterilization and dechlorination  1310 . A first post filtration chopped/pulverized humate—treated water mixture  1300  is passed through UV light beams created using second UV light treatment devices  1320  to expose the chopped/pulverized humate—treated water mixture  700  flow  701  to a higher intensity than the first UV light treatment process sterilization  1220  of  FIG. 12  to kill any residual microorganism and to break apart chlorine Cl 2  molecules of one embodiment. The description of the process continues on  FIG. 14 . 
     Particulate Filter Settling Tank: 
       FIG. 14  shows for illustrative purposes only an example of a particulate filter settling tank of one embodiment.  FIG. 14  shows a particulate filter settling tank  210  receiving the post filtration flow  1400  from the filtered humate-treated water mixture supply  203 . The mixture  1410  includes pH treated water with suspended s+ soda ash molecules  720 , HA humic acid molecules  730  and FA fulvic acid molecules  740 . After filtration there may be residual suspended particulates p 4  particulate size  4   754  or smaller in the mixture. The post filtration flow  1400  velocity slows when entering the settling tank  210 . The reduced velocity allows residual suspended particulates to settle to the bottom of the settling tank  210  where the particulate waste accumulator funnel  311  accumulates the settled particulates and allows them to flow through the particulate waste disposal discharge pipe  312  and into the particulate disposal container  211 . The remaining post filtration flow that is a settled humic-fulvic suspended mixture free of residual suspended particulates at the top of the settling tank  210  flows out  1430  of a settled humic-fulvic suspended mixture discharge pipe outlet  1420  of one embodiment. 
     Ultraviolet Light Exposure Channels: 
       FIG. 15  shows for illustrative purposes only an example of ultraviolet light exposure channels of one embodiment.  FIG. 15  shows a settled humic-fulvic suspended mixture supply pipe  1530  supplying settled humic-fulvic suspended mixture to ultraviolet light exposure channels  1500 . The ultraviolet light exposure bulbs  1504  are mounted to project UV light beams through the settled humic-fulvic suspended mixture flowing in the ultraviolet light exposure channels  1500 . The ultraviolet light exposure bulbs  1504  and devices can include National Science Foundation (NSF) 
     Certified UV Light Systems. The serpentine channel layout prolongs the time of the exposure to the fluid. The ultraviolet light exposure channels  1500  convey the exposed fluid into the first stage adsorption defluoridation device  230  of one embodiment. 
     UV Light Dechlorination: 
       FIG. 16A  shows for illustrative purposes only an example of UV light dechlorination of one embodiment.  FIG. 16A  shows a UV light dechlorination  1600  process that projects at least one UV light wave beam  1610  into the mixture where chlorine has been detected. A chlorine Cl 2  molecule  1620  is held together by the force of an ion bond  1622 . UV light dechlorination breaks the ion bond  1630  causing the two to separate into two free chlorine CI molecules  1624  that will dissipate more readily of one embodiment. 
     UV Light Sterilization: 
       FIG. 16B  shows for illustrative purposes only an example of UV light sterilization of one embodiment.  FIG. 16B  shows a UV light sterilization  1630  process wherein UV light kills microorganisms  1640 . For example the UV light wave beam intensity can kill the protozoa microorganism  760  and the bact. bacteria microorganism  762  and virus microorganisms of one embodiment. 
     Settled Humic-Fulvic Suspended Mixture: 
       FIG. 17A  shows for illustrative purposes only an example of a humic acid and fulvic acid separation and segregation process overview of one embodiment.  FIG. 17  shows a settled HA-FA suspended mixture storage tank  1700  supplying the settled humic-fulvic suspended mixture to a fulvic acid—humic acid granular activated carbon (GAC) FA-HA GAC separation chamber  1720 . Humic acid molecules adsorb to the granular activated carbon surfaces. When the separation and segregation processes are completed the remaining mixture and fresh flushing treated water are disposed of through discharge pipe and drain  1729  for recycling of one embodiment. 
     The separation process concentrates the fulvic acid molecules and segregates them to the fulvic acid storage tank  252  with temperature and pH control device  241 . After the segregation of the fulvic acid molecules the humic acid molecules are separated from the granular activated carbon and are concentrated at the top of the separation chamber where they are segregated to the humic acid storage tank  264  with temperature and pH control device  241 . A fresh treated water storage tank  240  with temperature control device and pH control device  241  supplies additional treated water when desired. The supplies of the fulvic acid molecules and humic acid molecules are used in the preparation products for human consumption including black colored water beverages  1710 , flavored beverages, soft drinks, alcoholic beverages  1711 , and supplements  1712  and food additives  1713  of one embodiment. 
     Humic-Fulvic Acid Separation Chamber: 
       FIG. 17B  shows for illustrative purposes only an example of a humic-fulvic acid separation chamber of one embodiment.  FIG. 17B  shows a humic-fulvic acid separation chamber  250  with the settled humic-fulvic suspended mixture flowing into the separation chamber through the settled humic-fulvic suspended mixture discharge pipe outlet  1420 . The settled humic-fulvic suspended mixture fills the separation chamber above the fulvic acid segregation vacuum device  1754  and covers the vacuum draw pipe  1752 . A bed  1732  of activated carbon  1730  provides surface area to attract the humic acid molecules. The fulvic acid molecules rise to the top section of the separation chamber where they are drawn out of the separation chamber using the separation vacuum device  1754  to the fulvic acid storage tank  252  of  FIG. 2  with temperature and pH control devices. When the concentration fulvic acid molecules is depleted from the settled humic-fulvic suspended mixture as indicated using a fulvic acid sensor the pH control device  241  is used to draw a sample of the mixture  1740  into a sensor  1741  to detect the pH level of the mixture. 
     A digital processor  1742  is used to calculate the volume of base to inject into the mixture  1745  to adjust the pH level and transmit a signal  1743  using a solenoid  1744  to open a valve to aid in the release of the humic acid molecules from the activated carbon surfaces. Burners  1733  included in a temperature control device  1734  are automatically ignited to raise the temperature of the remaining mixture to further aid in the release of the humic acid molecules from the activated carbon surfaces. The humic acid molecules rise to the top of the separation chamber and are draw out to the humic acid storage tank  264  of  FIG. 2  with temperature and pH control devices. After segregation of the humic acid molecules a valve  1755  is opened to flush the separation chamber with fresh treated water  1751  through an inlet pipe  1750  to regenerate the activated carbon material  1730 . The flushing regeneration water mixture is drained out the disposal discharge pipe  1756  for recycling of one embodiment. 
     Fulvic Acid Separation and Segregation: 
       FIG. 17C  shows for illustrative purposes only an example of fulvic acid separation and segregation of one embodiment.  FIG. 17C  shows the presence of SA+ soda ash molecule  720 , humic acid molecule  730 , fulvic acid molecule  740  in a settled humic-fulvic suspended mixture supply  1701  in a settled HA-FA suspended mixture storage tank  1700 . Piping conveying the mixture  1759  through an opened settled humic-fulvic suspended mixture supply valve  1759  and through an opened humic-fulvic acid separation chamber inlet valve  1773  for an activated carbon HA separation process  1760  of one embodiment. 
     The humic-fulvic acid separation chamber  250  contains a quantity of activated carbon  1730 . When the humic-fulvic acid separation chamber  250  is filled to the top the settled humic-fulvic suspended mixture supply valve  1759  and humic-fulvic acid separation chamber inlet valve  1773  are closed. Humic acid molecules attach to the surfaces of the activated carbon. Fulvic acid molecules rise to the top of the separation chamber. A vacuum segregation of fulvic acid molecules  1762  is performed using a fulvic acid segregation vacuum device  1754 . The fulvic acid segregation vacuum device  1754  draws the concentration fulvic molecules into the fulvic acid storage tank  252 . Fulvic acid molecules suspended in treated water storage tank  1766  show in the fulvic acid storage tank  252 . A fulvic acid detection device  1764  detects and measures the concentration of fulvic acid molecules. When the fulvic acid detection device  1764  measurements indicate the concentration fulvic acid molecules is depleted the fulvic acid segregation process stops of one embodiment. 
     Also showing is a humic acid molecules vacuum device  1770 , humic acid detection device  1772 , humic acid storage tank  264 , pH control device  241 , pH control device injection piping  1764 , burners  1733 , fresh treated water storage tank  240  and a humic-fulvic acid separation chamber discharge valve  1774  closed of one embodiment. 
     Humic Acid Separation and Segregation: 
       FIG. 17D  shows for illustrative purposes only an example of humic acid separation and segregation of one embodiment.  FIG. 17D  shows the presence of SA+ soda ash molecule  720 , humic acid molecule  730 , and fulvic acid molecule  740  in a settled humic-fulvic suspended mixture supply  1701  in a settled HA-FA suspended mixture storage tank  1700 . Piping conveying the mixture  1759  through an opened settled humic-fulvic suspended mixture supply valve  1759  and through an opened humic-fulvic acid separation chamber inlet valve  1773  for an activated carbon HA separation process  1760 . The humic-fulvic acid separation chamber  250  shows the activated carbon  1730  with attached humic acid molecules. The pH control device  241  with pH control device injection piping  1764  begins a process for injecting soda ash to raise pH  710 . The burners  1733  are activated for ignited burners to raise the temperature  1780  of the mixture. Humic acid molecules are desorbed from the activated carbon and humic acid molecules rise to the top of the separation chamber. 
     A humic acid molecules vacuum device  1770  draws the concentrated humic acid molecules into the humic acid storage tank  264 . Humic acid molecules suspended in treated water storage tank  1788  are showing in the humic acid storage tank  264 . The humic acid detection device  1772  detects and measures the concentration of humic acid molecules in the humic acid molecules vacuum device  1770  flow. When the humic acid detection device  1772  measurements indicate the concentration humic acid molecules is depleted the humic acid segregation process stops. Also showing are the vacuum segregation of fulvic acid molecules  1762 , fulvic acid molecules suspended in treated water storage tank  1766 , fulvic acid detection device  1764 , fulvic acid storage tank with temperature and pH control devices  252 , and fulvic acid segregation vacuum device  1754  of one embodiment. 
     The process continues with a flushing process wherein fresh treated water is pumped into the humic-fulvic acid separation chamber  250  from the fresh treated water storage tank  240 . The humic-fulvic acid separation chamber inlet valve  1773  and humic-fulvic acid separation chamber discharge valve  1774  are opened for discharging the remaining mixture and flush treated water for recycling of one embodiment. 
     pH Scale: 
       FIG. 18A  shows for illustrative purposes only an example of a pH scale of one embodiment.  FIG. 18A  shows a pH scale  1870 . The pH scale shows the ranges of pH are from 0 to 14. A humic acid range of solubility pH 7 to 14  1890  is limited to a base pH level. A fulvic acid range of solubility  1880  pH 0 to 14 means it is soluble at any pH level. 
     Titration Curve: 
       FIG. 18B  shows a block diagram of an overview flow chart of titration curve of one embodiment.  FIG. 18B  shows a titration curve  1892 . Sodium hydroxide NaOH also called Soda Ash (SA) is a base material that when various amounts of ml of NaOH added to a solution raises the pH level from pH levels 2 to 12 based on the number of milliliters of NaOH added to the solution. The black water humic and fulvic acids extraction for human consumption and use method and devices uses at least one automated periodic sampling of the humate-treated water mixture at points along the process to check the pH level. If the pH is lower that a desired level NaOH is added to the solution in predetermined amounts to increase the base pH level to the desired level from the sampling detected level. 
     Treating Water Processes: 
       FIG. 19A  shows a block diagram of an overview flow chart of treating water processes of one embodiment.  FIG. 19A  shows flowing chlorinated municipal water  1900 , flowing unchlorinated well water  1902 , flowing stream/spring water  1906 , and flowing ocean water supply  1904  as water sources that may be used for the treating water processes. At least one of the water sources is processed for filtering suspended particulates  1910 . The particulates removed are conveyed for disposing particulate waste  1912 . 
     A next process can include a process for oxygenating water  1911  beginning with a process for detecting a first salinity concentration  1919 . Oxygenating water  1911  can include an electrolysis process of water with a salinity level to promote conductivity of the electrolysis charges through the volume of water. A detecting first salinity concentration  1919  process determines the salinity of the water. Should the water have a total dissolved salt (TDS) concentration where TDS &lt;1,000 ppm  1913  the process continues for adjusting TDS using salt injection for a TDS ≥1,000 ppm ≤3000 ppm  1914  and the water is automatically diverted for oxygenating using electrolysis devices  1916 . If the detecting first salinity concentration  1919  process determines the salinity of the water has TDS ≥1,000 ppm  1915  the water is automatically diverted for oxygenating using electrolysis devices  1916 . After an oxygenating water  1911  process is complete the salinity of the water is reduced to a suitable drinking water concentration level. 
     A next process can include a process for detecting a second salinity concentration  1920  of the water source. Total dissolved salt (TDS) is a measure of the salts suspended in liquid generally measured in parts per million (ppm). The black water humic and fulvic acids extraction for human consumption and use method and devices targets TDS &lt;200 ppm  1921  for human consumption which is a level generally found in drinking water. Automated sampling of the water source is used for obtaining a sample that is fed into an automated chemical analyzer for detecting salinity concentration  1920 . A TDS &lt;200 ppm  1921  automatically initiates a diversion of the flow of the water source to the next process. A TDS ≥200 ppm  1922  automatically initiates a diversion of the flow of the water source for desalinating using reverse osmosis devices  1923  to reduce the salinity to a TDS &lt;200 ppm  1924 . Once the analysis reaches a salinity of a TDS &lt;200 ppm  1921  the flow is automatically diverted to a next process. 
     A next process can include creating distilled water using distilling water devices  1917 . After a distilling water process is complete the process continues to a process for detecting chlorine concentration  1930 . 
     A next process can include a process for detecting chlorine concentration  1930 . A detected chlorine concentration with a yes  1931  or positive for the presence of chlorine (Cl 2 ) initiates an automatic diversion of the water source flow for dechlorinating using ultra-violet devices  1932 . Upon complete of dechlorination the flow is automatically diverted to the next process. A detecting chlorine concentration  1930  with a result of no  1933  or negative detection the presence of chlorine automatically diverted to the additional processes described in  FIG. 19B . 
     Treating Water Additional Processes: 
       FIG. 19B  shows a block diagram of an overview flow chart of treating water additional processes of one embodiment.  FIG. 19B  shows treating water additional processes continuing from  FIG. 19A  including a process for detecting fluoride concentration  1940 . A detecting fluoride concentration  1940  analysis result indication yes  1941  a positive detection of fluoride in the water source automatically diverts the flow of the water source to a process for defluoridating using ultra-violet light devices and activated carbon adsorption devices  1942 . Once an automatic sampling analysis shows the defluoridation process is complete the water source flow is diverted to the next process. The next process uses generating ozone  1945  for disinfecting using ozonation  1944 . An initial detecting fluoride concentration  1940  analysis result indication no  1943  a negative finding that no fluoride is present the water source is diverted to the next process disinfecting using ozonation  1944 . Following ozonation is a process for sterilizing using ultra-violet light  1950 . 
     A first step in the sterilizing using ultra-violet light devices  1950  process is automatically taking a sampling of the water source for detecting pH level  1960 . An automatic detecting pH level  1960  result showing a &lt;8.5 pH ≥10  1961  automatically diverts the flow of the water source flow for adjusting pH level using base injection  1962 . Once a ≥8.5 pH &lt;10  1963  is detected after the adjusting pH level using base injection  1962  process the water source flow is automatically diverted for storing purified water in a tank  1972  for the next process. If the initial automatic detecting pH level  1960  shows a ≥8.5 pH &lt;10  1964  the water source flow is automatically diverted for storing purified water in a tank  1972  for the next process for de-ionizing purified water  1971 . The processing continues for adding de-ionized purified water  1970  for mixing in the mixing tank  1990 . Once the treated water source is injected into the mixing tank  171  of  FIG. 1  a process begins for depositing chopped/pulverized selected humate materials  1980  for mixing in the mixing tank  1990  with the injected treated water. The process descriptions continue in  FIG. 20 . 
     Extraction and Segregation of Humic and Fulvic Acids: 
       FIG. 20  shows a block diagram of an overview flow chart of extraction and segregation of humic and fulvic acids of one embodiment.  FIG. 20  shows the continuation of the processing from  FIG. 19  including conveying humate and treated water mixture into a granular activated carbon separation chamber with pH level and temperature regulating devices  2000 . Adsorbing the humic molecules on the granular activated carbon  2010 . Concentrating suspended fulvic acid molecules near the top of the separation chamber  2020  then segregating suspended aqueous fulvic acid concentrates from the mixture into the fulvic acid storage tank with temperature and pH control devices  2030 . The aqueous fulvic acid concentrate having been removed the process continues by raising the temperature and pH level of the remaining humate and treated water mixture for desorbing the humic acid molecules from the granular activated carbon  2040 . A sampling of the remaining humus and treated water mixture is automatically analyzed to determine the pH level. If the sampling is &lt;8.5 pH ≥10 the pH control device automatically initiates adjusting the pH level in the granular activated carbon separation chamber to be ≥8.5 pH &lt;10 level  2050  and cause the release of the humic acid molecules from the activated carbon materials. Concentrating suspended humic acid molecules near the top of the separation chamber  2060 . Segregating suspended aqueous humic acid concentrate from the mixture into the humic acid storage tank with temperature and pH control devices  2070 . Disposing of the remainder of the mixture for recycling  2080 . Description of the processing continues in  FIG. 21 . 
     Creating Products for Human Consumption and Use: 
       FIG. 21  shows a block diagram of an overview flow chart of creating products for human consumption and use with humic and fulvic acids of one embodiment.  FIG. 21  shows processing continuing from  FIG. 20  with adding suspended aqueous fulvic acid concentrate additive  2100  and adding suspended aqueous humic acid concentrate additive  2110 . Products for human consumption can also be adding flavorings and additives  2120 , spicy black cherry flavoring  2121 , apple grape flavoring  2122 , peach mango flavoring  2123 , citrus mint flavoring  2124 , coffee berry extract  2125 , aloe extract  2126 , cola flavoring  2127 , citrus fruit flavoring  2128 , artificial sweetener  2129 , I-theanine  2130 , ginseng  2131 , caffeine  2132 , guarana  2133 , sage  2134 , basil  2135 , citicoline  2136 , antioxidants  2137 , tropical fruit flavoring  2138 , tea extract  2139 , natural sweetener  2140 , herbal flavoring  2141 , and other flavorings and additives. 
     The ingredients being added include adding vitamins  2150  including A  2151 , B complex  2152 , B 6   2153 , B 12   2154 , C  2155 , D  2156 , E  2157 , K  2158 , and other vitamins. The ingredients being added include adding minerals  2160 , calcium  2161 , folic acid  2162 , iron  2163 , zinc  2164 , chromium  2165 , magnesium chloride  2170 , potassium chloride  2171 , sodium bicarbonate  2172 , calcium chloride  2173  and electrolytes  2174 . Combining predetermined quantities of additive ingredients  2145  is then used in processing described in  FIG. 22 . 
     Products for Human Consumption and Use: 
       FIG. 22  shows a block diagram of an overview flow chart of a continuation of creating products for human consumption and use with humic and fulvic acids of one embodiment.  FIG. 22  shows a continuation of a process from  FIG. 21  for creating products for human consumption. The combining predetermined quantities of additive ingredients  2145  of  FIG. 21  further includes adding de-ionized purified water  2208  and adding carbonation  2209 . Combining ingredients for alcoholic beverages includes segregating ulmic acid from the suspended aqueous humic acid concentrate  2200 , adding alcoholic drink ingredient to the suspended aqueous humic acid concentrate additive  2202 , suspending alcohol soluble ulmic acid in the alcoholic drink ingredient  2204 , and adding alcohol soluble ulmic acid and an alcoholic drink ingredient  2205 . 
     Black water alcoholic beverages will include a flavoring based on the type of alcohol added to the mix including beers and liquor or hard liquor. Humic acids contain an alcohol-soluble portion of the humic fraction named ulmic acid. The ulmic acid will be conveyed to the bottling processes through a separate ulmic acid discharge piping system. Humic and fulvic mineral extraction method and beverage for human consumption alcoholic beverages will be mixed with the ulmic acid and fulvic acids in predetermined volumes of one embodiment. 
     The processes of combining predetermined quantities of additive ingredients  2145  of  FIG. 21  are followed by processes for creating products for human consumption  2206  including black colored water beverages  2210 , flavored beverages  2220 , effervescent flavored beverages  2224 , alcoholic beverages  2230 , supplements  2240 , food additives  2250 , and zero calorie beverages  2280 .  FIG. 22  shows a continuation of a process from  FIG. 21  for creating products for human use  2261  including cosmetics  2260 , and pharmaceuticals  2270 . 
     Combinations of the ingredients can produce different tastes and consumer benefits including improving a consumer&#39;s mood, vitamins and nutrients providing a consumer energy boost, improving a person focus, providing newly focused mental faculties, providing trace minerals that supply electrolytes, antioxidants and amino acids a consumer&#39;s body needs, helps boost a consumer&#39;s immune system and other benefits. Combining quantities of additive ingredients  2145  of  FIG. 21  and selecting some but not all of the ingredients are varied to target specific benefits and taste in the products for human consumption. The black water humic and fulvic acids extraction for human consumption and use method and devices not only removes harmful chemicals in the processing but also does not use other chemicals that can pose a health risk to consumers of products that include humic and fulvic acids extracted using potentially harmful chemicals in the extraction processing. At least annually sample(s) consisting of primary containers of product of unit packages of product shall be tested by an approved competent commercial laboratory and the results of the at least annual test results will be keep on file and logged into a black water bottling process server of one embodiment. 
     Artificial Sweetener Ingredients: 
       FIG. 23A  shows a block diagram of an overview of artificial sweetener ingredients of one embodiment.  FIG. 23A  shows a partial list of the artificial sweetener  2129  additive ingredient used for creating products for human consumption  2206  of  FIG. 22 . The artificial sweetener  2129  additive ingredients include aspartame  2300 , sucralose  2310 , neotame  2320 , and other artificial sweeteners  2330  of one embodiment. 
     Natural Sweetener Ingredients: 
       FIG. 23B  shows a block diagram of an overview of natural sweetener ingredients of one embodiment.  FIG. 23B  shows a partial list of the natural sweetener  2140  additive ingredient used for creating products for human consumption  2206  of  FIG. 22 . The natural sweetener  2140  additive ingredients include stevia leaf extract  2340 , sweet proteins  2341 , synsepalum dulcificum berry  2342 , rebaudioside a  2343 , erythritol  2344 , monk fruit  2345 , inulins  2346 , alcohol sugars  2347 , and other natural sweeteners  2348 . Some of the natural sweetener  2140  additive ingredients have no or low levels of calories. The inulins  2346  group of natural sweetener  2140  additive ingredients includes chicory root  2350 , agave  2351 , Jerusalem artichoke  2352  and other inulin sources  2353 . 
     Inulin is not digested or absorbed in the stomach. It goes to the bowels where bacteria are able to use it to grow. It supports the growth of a special kind of bacteria that are associated with improving bowel function and general health. Inulin decreases the body&#39;s ability to make certain kinds of fats. Inulin received no-objection status as generally recognized as safe (GRAS) from the US Food and Drug Administration (FDA). Inulin is not digested by enzymes in the human alimentary system, contributing to its functional properties: reduced calorie value, dietary fiber and prebiotic effects of one embodiment. 
     Black Water Bottling Process: 
       FIG. 24  shows for illustrative purposes only an example of a black water bottling process of one embodiment. In the following description the terms “bottle” and “bottling” have the meaning of a “beverage container” including a glass bottle, a can including an aluminum can, a food grade plastic bottle, a food grade beverage container that is biodegradable, a beverage container made with an ultraviolet protective tinting or exterior coating, and wherein each type of beverage container may of any volume capacity. The beverage container can include an opening device including a “pop top” opening device, a screw-on cap made of a food grade plastic or aluminum, a crimped cap, a cork, a sealed detection device and other types of capping devices. 
       FIG. 24  shows a black water bottling process beginning with an empty bottle supply bin  2420  where empty bottles are positioned for processing through an empty bottle conveyor alignment  2422  apparatus. The empty bottles are fed in a single row onto a single empty bottle conveyor  2421 . The process includes a de-ionized purified water empty bottle sanitation station  2430  where the bottles are rinsed clean in a bottle cleaning area  2433 . The sanitizing rinse includes de-ionized purified water from an empty bottle sanitation station de-ionized purified water supply tank  2480  and can include heating the de-ionized purified water to a temperature ranging from 110° F. to 180° F. The elevated temperature and de-ionization of the purified water sanitizes the bottle and removes minerals that could remain on the surfaces of the bottles. The minerals that are removed may be some of the same minerals being added later in the processing, but the amount of the minerals in the purified water rinsing cycle may be unknown and may cause a quantity of mineral in the final beverage formulation greater than a predetermined amount to be added. The rinse water used is recycled to the treating water processes described in  FIG. 19A  and  FIG. 19B . 
     All bottling facilities shall apply for and retain on file in the bottling facilities current certificates or notifications of approval issued by the government agency or agencies approving the plant&#39;s source and supply of product water and operations water. All required certificates or notifications of approval shall be available for review at reasonable times. Bottling facilities can include for example an empty bottle filling station  2431  room with tight walls, ceilings, and self-closing doors not shown separate from other bottling operations with double self-closing passage doors that cannot open directly into any room for protection against contamination. Conveyor openings are sized to permit passage of containers. Processing operations can include a sealed system under internal air pressure to prevent infiltration of outside air that may contain particulates and microbial organisms and adequate protection to preclude contamination of the water and the processing system. Adequate ventilation is included to minimize condensation in processing rooms, bottling rooms, and in a bottle cleaning area  2433  for washing and sanitizing bottles. 
     The bottle cleaning area  2433  can include an enclosed room, not shown, for preventing post-sanitizing contamination of the bottles. The empty bottle filling station  2431  can include a sealed room not shown that include double passage doors to prevent contamination from outside air. All double passage door passage ways will include positive air pressure to prevent infiltration of outside air and floor vacuum exhaust apparatus to remove soil, dust and other clothing contaminates possibly on personnel clothing. The floors will include footwear brushing apparatus to permit personnel to brush off any debris on the soles of their footwear. The turbulent positive air pressure blowers will include ultrafiltration and sufficient turbulence to knock lose any particulates on their clothing. Positive air pressure shall be free of oil, dust, rust, excessive moisture, and extraneous materials and shall not affect the bacteriological quality of the water and should not adversely affect the flavor, color, or odor of the water. 
     All product water and operations water supplies are properly located, protected, and operated, easily accessible, adequate, and of a safe, sanitary quality compliant at all times with the applicable laws and regulations of the government agency or agencies having jurisdiction. Finished bottled water must comply with bottled water quality standards. 
     Bottling facilities can include locker and lunchrooms that are separate from plant operations and storage areas and include self-closing doors. Procedures will be established to maintain locker and lunchrooms in a clean and sanitary condition with refuse containers should be provided. Bottling materials and supplies will not be stored in locker or lunchrooms. 
     Next the empty bottles are processed through an empty bottle air cleaner station  2484 . The filter compressed air is injected into the empty bottles from an empty bottle air cleaner station compressed air supply tank  2482 . This dries the empty bottles and prevents any particulates from the air from remaining in the empty bottles. Bottles are then conveyed into an empty bottle filling station  2431 . The black water bottling process includes but is not shown in  FIG. 24  at least one test valve at each supply piping coupled to a supply tank for taking samples of for example waters, liquids and powders. The samples taken are used for testing of microbial and non-organic substances at least weekly. Microbial testing includes for example heterotrophic plate count, coliforms, mold, yeast, pseudomonas aeruginosa, bacteria, protozoa, fungi, viruses, e. coli, and other microorganisms and bacteria. 
     The samples are taken at a predetermined periodic basis. If any coliform organisms are detected, follow-up testing must be conducted to determine whether any of the coliform organisms are E. coli. Sample test results reports are logged into the black water bottling process server including date of sampling, type of product sampled, unit package production code, and results of the analysis and reported to appropriate agencies. While samples are tested in approved laboratories there are also on-site automated testing devices to preform immediate preliminary test results. The on-site automated testing devices are activated by a black water bottling process server signal to each testing device to open the at least one testing valve using a solenoid and process the sample through the on-site automated testing device for detecting microbial and non-organic substances. 
     If the preliminary test results indicate the presence of a targeted microbial organism, the on-site automated testing devices transmit an alert signal to activate a pulsing red light at the location of the at least one test valve, activates an audio alarm and activate a shut-down of the additive supply valve to prevent contamination beyond that point. The automated testing devices transmitted alert signal and test results also is received by a black water bottling process server which relays the signal over a WI-FI communication device to supervisory and management personnel using texting, email and a recorded alert message over a voice communication. 
     Other on-site automated testing devices automatically test a sample for targeted non-organic substances including for example minerals, humic and fulvic acid quantities, a heavy metal assay, arsenic, uranium, antimony, beryllium, cyanide, nickel, thallium, diquat, endothall, glyphosate, dioxin, phosphorus, phosphates, sodium carbonate, sodium bicarbonate, potassium bicarbonate, calcium carbonate, calcium-magnesium carbonate, potassium hydroxide, sodium hydroxide, phosphoric acid, acetic acid, citric acid, hydrochloric acid and sulfuric acid, residual disinfectants and disinfection byproducts, and chemical pesticides. On-site automated testing devices ample test results reports are logged into black water bottling process server including date of sampling, type of product sampled, unit package production code, and results of the analysis and reported to appropriate agencies. 
     The empty bottle filling station  2431  is supplied with a beverage mixture from a beverage mixing tank  2410  for filling the beverage mixture into the bottles in a predetermined volume. Predetermined amounts of ingredients are combined and mixed in the beverage mixing tank  2410 . The ingredients can include predetermined quantities of de-ionized purified water  2400  from a tank, and fulvic acid  2491 , and humic acid  2492  additives. Alcoholic beverages can include ingredients including ulmic acid  2494  in alcohol  2495 . Ulmic acid  2494  is a fraction of humic acid that is soluble in alcohol  2495 . The beverage mixture can also include in predetermined quantities flavorings  2423 , additives  2424 , vitamins  2425 , minerals  2426 , carbonation  2427 , one or more artificial sweetener  2428 , and one or more natural sweetener  2429 . The total predetermined quantities of the ingredients are deposited into the beverage mixing tank  2410  and blended into the final product mixture. 
     After the bottles are filled at the empty bottle filling station  2431  they are conveyed to a bottle capping station  2432  where a cap is coupled to the filled bottle. A bottle volume sensor station  2434  then is used to confirm the predetermined volume has been filled into the bottle. A bottle labeling station  2436  then affixes a label to the bottle. In some instances the bottle or beverage container may be pre-printed with the labeling information including the product name, contents information and other desired and required information. 
     The bottles are conveyed to a bottle quality control station  2440  where one or more inspector and/or automated sensors including scanners, photographic image recognition devices, digital scales and other quality control evaluation test devices can perform quality control inspections to ensure the quality of the bottling processes. The bottles that pass the bottle quality control station  2440  evaluations are then conveyed to a bottle packing station  2450 . During the process of filling, capping or sealing either single-service or multiservice containers, the performance of the filler, capper or sealer shall be monitored and the filled containers visually or electronically inspected using the automated sensors including scanners, photographic image recognition devices, digital scales and other quality control evaluation test devices to assure they are sound, properly capped or sealed, and coded and labeled. Containers that do not pass inspection shall be reprocessed or rejected and not sent to packaging. Bottling electronic monitoring includes bottle quality control devices configured for using automated sensors including scanners, photographic image recognition devices, digital scales and other quality control evaluation test devices to assure bottles and containers are sound, properly capped or sealed, coded and labeled and to physically remove bottles and containers that do not pass inspections of one embodiment. 
     All containers, caps and closures shall be sampled and inspected to ascertain that they are free from microbial organisms and other forms of contamination. Testing for bacteriological contamination shall be performed using approved methods including a bacteriological swab and/or rinse count at least once each 3 months. Testing for bacteriological contamination shall be conducted on not less than four containers, caps and closures selected just prior to filling and sealing. No more than twenty-five percent of the samples may exceed more than one bacteria per milliliter of capacity or one colony per square centimeter of surface area. All samples shall be free of coliform organisms. The procedure and apparatus for these bacteriological tests shall be in conformance with those recognized by the government agency or agencies having jurisdiction. Tests shall be performed either by qualified plant personnel or a competent commercial laboratory. 
     Predetermined packaging for each beverage type and beverage container is positioned at a bottle packing receiving station  2452 . All packaging materials shall be imprinted with a unit package production code. Each unit package from a batch or segment of a continuous production run of bottled drinking water shall be identified by a unit package production code. Imprinting of the unit package production code shall be uniquely codes with unit package production code data including the kind of product, volume produced, date produced, lot code used, and the distribution identification of the finished product to wholesale and retail outlets just prior to packaging of a product. The black water bottling process server shall produce an alphanumeric code and graphic barcode for each finished product batch for each different beverage container type and size. The alphanumeric code and graphic barcode will include codes to distinguish the unit package production code from other batches. The unit package production code shall identify a particular batch or segment of a continuous production run and the day produced. The plant shall record and maintain information as to the kind of product, volume produced, date produced, lot code used, and the distribution of the finished product to wholesale and retail outlets. 
     Predetermined packaging can include a non-corrosive and non-toxic disinfectant agent impregnated into the packaging materials including for example cardboard and plastic rings to prevent growth of bacteria and microorganisms on the beverage containers after packaging and during shipping. A bottle packing folding station  2454  uses the received predetermined packing materials and processes the materials for receiving a predetermined number of bottles. This may include for example folding of packing cartons, drink holders, loading plastic six-pack rings in an application device and other predetermined packing materials preparations. A bottle carton conveyer  2456  is used to convey folded cartons to an unloaded carton staging area  2458 . The unloaded carton staging area  2458  is used for a carton assembly station  2460  for packing the cartons with bottles. An assembled cartons shipping conveyor  2474  is used for grouping and positioning assembled cartons for pick-up for delivery to a shipping area. The above has described an overview of a humic and fulvic black water based beverage for human consumption bottling apparatuses and processes  2490  of one embodiment. 
     Hot Fill: 
     The bottle filling process includes at least one sterilization process. The at least one sterilization process includes a hot fill process. The hot fill apparatus includes heating elements along the metal fill piping. The beverage containers are moved along the conveyor to an adjustable platform. The adjustable platform is automatically adjusted up or down to a fill height determined by a laser sensor that detects the top of the container. A digitally controlled valve of the heated metal fill piping is opened and closed using a signal from the bamboo leaf extraction network computer to dispense a predetermined volume of the heated mixed liquid that will fill the container to a predetermined volume below the top of the container. 
     The hot fill process heats the mixed liquids between  194  and  203  degrees Fahrenheit to ensure sterilization. These heat-up process temperatures can be used with glass and certain types of plastic containers that do not change form at these temperatures. The containers are filled with the heated mixed liquids including non-carbonated beverage and liquid food products such as fruit and vegetable juices, soft drinks, water and teas. The containers are hermetically sealed after filling to preserve the sterilization. The hermetically sealed containers are immediately cooled preserving the product and taste. The hot filling process eliminates the need of preservatives and chemicals while maintaining the same level of shelf life and nutritional properties of the beverage. 
     Cold Fill: 
     The at least one sterilization process includes in another embodiment a cold fill process. The cold fill process pressurizes the container by cooling the product then the cold product is added to the cold container. The cold fill process requires sterilization, which can be either a wet or dry sterilization. The cold fill process includes at least one of three cold fill technologies. 
     A first cold fill technology is Iso-barometric Fillers: Applied to carbonated soft drinks, where the packaging, in PET plastic or glass is filled in iso-barometric fillers, capped and pasteurized in an Iso-barometric tunnel. Filling is made at 3° C. to 4° C. temperatures. 
     A second cold fill technology is Ultra Clean Systems: applied to beverages filling at low temperatures, and where the environmental conditions are very strict. This type of cold fill process is used for products with a short expiring date of about 30 days- and are distributed at low temperature under chilled conditions. The products have high quality, and are flash pasteurized and including a flash pasteurized application to the carton and PET packaging. 
     A third cold fill technology is Steril filling: Sterile filling preserves the product best according to nutritional, organoleptic and shelf life qualities. Sterile filling processing sterilized the container before filling in a sterile environment, sterilizing the container with peroxide or per-acetic acid, then dried to eliminate any traces of it. The sterility of the filling atmosphere is achieved via air filtering and high temperature sterilization. Sterile filling can be used for carton packaging containers and PET bottles. 
     Aseptic Fill: 
     The at least one sterilization process includes in another embodiment Aseptic fill. The aseptic filling process flash pasteurizes the mixed product including the mixed liquid is heated to a temperature between 180° F.-220° F. for a few minutes then cooled and filled at room temperature. Aseptic processing is a process by which a sterile product including at least a food or pharmaceutical, is packaged in a container. Aseptic fill is appropriate for high acid products and the products can last up to  18  months and is great for dairy and beverages in glass, aluminum, or PET. 
     Mixing Tanks: 
     Mixing tanks, sometimes called Blending tanks can include single direction rotating paddles, counter-rotating paddles, multi-speed rotating dual blades and combination homogenizing mixing tanks. 
     Filtration: 
     Filtration is integrated along the flow lines of the liquids at every point where the liquid is being conveyed from one vessel to another. For example when a liquid is pumped from a storage tank to the mixing tank a series of filters of various mesh sizes are incorporated into the piping lines. At least one filter in the series of mesh sizes is 0.2 microns to capture bacteria. Multiple filtration assures clean clear beverages. 
     Computer Controlled Monitoring and Processes: 
       FIG. 25  shows for illustrative purposes only an example of a bottling electronic monitoring and control network of one embodiment.  FIG. 25  shows a humic and fulvic black water based beverage for human consumption bottling electronic monitoring and control network  2599  used for monitoring and controlling a bottling operation. The bottling electronic monitoring and control network  2599  includes at least one digital server  2500 , at least one digital processor  2501 , at least one digital memory device  2502 , at least one Wi-Fi device  2503 , at least one database  2504 , at least one processing algorithm  2505 , and at least one user computer  2510 . The at least one digital server  2500  controls the bottling processes using data and parameters inputted by a user with the at least one user computer  2510  of one embodiment. 
     User inputted data and additional data is stored in the at least one digital memory device  2502  and at least one database  2504  creating a reference file for each beverage. The data includes predetermined quantities of each additive ingredient for each beverage to be formulated, a predetermined pH level range for each beverage, a predetermined temperature range, a bottle or beverage container size for a particular packaging mode, labeling information, and detailed information for each additive ingredient including pH level, calories per unit, a sweetness and taste indicator value, and other additive specific data. The at least one processing algorithm  2505  includes a formulation process to determine for example a projected pH level based on a combination of specific quantities of additive ingredients. The at least one digital processor  2501  is used to calculate the projected pH level based on the volumetric contributions of each additive ingredient of one embodiment. 
     Additional data is communicated to the at least one digital server  2500  using WI-FI communications and data signals from monitoring sensors at various points in the processing. In one embodiment for example, during each process, sensors and tracking devices are connected to each device that processes, mixes, sterilizes, and other operations of the bottles, beverage additive ingredients and bottles to ensure the beginning, intermediate and final processes are controlled to allow the final product to all safety and regulatory standards for human consumption and a desired product quality of one embodiment. 
     In addition a RFID, Bluetooth, NFC, sensors and tracking devices are coupled to the beverage containers  2565  of a beverage product to track the beverage distribution and track the consumption of the beverage product and disposal of the bottle container. A mobile device application is wirelessly coupled to the sensors and devices to allow a user to remotely monitor and observe the distribution, consumption, and disposal of the beverage of one embodiment. 
     An additive supply tank  2520  is equipped to receive an additive quantity control signal  2521  from the at least one digital server  2500 . The signal is received using a predetermined quantity digital meter and monitor controller transceiver  2528 . The additive supply tank  2520  includes a plurality of interior facing waterproof ultraviolet light sanitization fixtures  2523  to prevent bacterial growth and kill any microorganisms that may be present in the additive material prior to being conveyed to the mixing tank  2410 . Coupled to additive bulk supply piping  2522  a metered supply pump  2524  opens a digitally controlled valve to allow the predetermined quantity to flow to the beverage mixing tank  2410  through metered supply piping  2526  of one embodiment. 
     A metered additive temperature control apparatus  2530  can receive a metered additive temperature control signal  2531  from the at least one digital server  2500  using a predetermined digital temperature controller transceiver  2539 . Metered additive supply piping  2532  is equipped with a digital temperature meter  2533 . The digital temperature meter  2533  measures the temperature of the additive flow. 
     The digital temperature meter  2533  transmits digital instructions through the digital temperature meter thermostat cabling  2534  to start the operation of a metered additive supply temperature adjusting apparatus  2536  should the additive flow temperature fall below or above a range determined by a predetermined temperature transmitted by the metered additive temperature control signal  2531 . The predetermined temperature is set to a range for each specific additive to prevent growth of bacteria in the additive. The metered additive supply temperature adjusting apparatus  2536  can operate in a mode to either raise or lower the temperature using a reversible flow of a media in temperature control media piping  2538  to extract or add heat to adjust the additive flow temperature of one embodiment. 
     The beverage mixing tank  2410  includes a beverage mixing tank mixer motor  2542 . The beverage mixing tank  2410  includes a plurality of interior facing waterproof ultraviolet light sanitization fixtures  2523  to prevent bacterial growth and kill any microorganisms that may be present in the additive material prior to being conveyed to the mixing tank  2410 . An additive ingredient mixing tank control signal  2541  is received by the beverage mixing tank  2410  using a plurality of pH metering probe and digital transceiver  2545  coupled to each metered additive supply piping  2544 . At least one pH metering probe and digital transceiver  2545  is coupled to de-ionized purified water supply piping  2546 . The pH metering probe and digital transceiver  2545  measures the actual pH level of the additive ingredient as it flows into the beverage mixing tank  2410 . The actual pH levels are transmitted to the at least one digital server  2500 . This actual data is processed by the at least one processing algorithm  2505  using the at least one digital processor  2501  to determine any pH level adjustment in the combined ingredients of one embodiment. 
     The de-ionized purified water supply tank  2400  can receive a de-ionized purified water supply control signal  2551  from the at least one digital server  2500  using the pH metering probe and digital transceiver  2545 . The de-ionized purified water supply control signal  2551  can include a final pH level adjustment instruction. The final pH level adjustment instruction is transmitted to a soda ash (NaOH) solution injector apparatus  2554  using pH metering probe and digital transmitter signal cabling  2558 . The soda ash (NaOH) solution injector apparatus  2554  can inject into de-ionized purified water supply piping  2546  a predetermined pH level adjustment dose of soda ash to make the adjustment inject that quantity using NaOH injection piping  2556 . The de-ionized purified water supply tank  2400  includes a plurality of interior facing waterproof ultraviolet light sanitization fixtures  2523  to prevent bacterial growth and kill any microorganisms that may be present in the de-ionized purified water prior to being conveyed to the mixing tank  2410  of one embodiment. 
     A bottling conveyor temperature control apparatus  2562  is used to control the temperature of the final beverage product after bottling. The bottling conveyor temperature control apparatus  2562  surround a section of a bottle conveyor  2566  with bottles on a conveyor  2564 . The section of a bottle conveyer  2566  with the bottling conveyor temperature control apparatus  2562  includes in the surrounding structure a plurality of interior facing ultraviolet light fixtures  2563  to prevent bacterial growth and kill any microorganisms that may be present on the exterior of the bottles and caps while being conveyed to the bottle packing station  2450  of  FIG. 24 . 
     A bottling conveyor temperature controller transceiver  2560  can receive a bottling conveyor temperature control signal  2561  with a predetermined temperature. The digital temperature meter  2533  can signal using digital temperature meter thermostat cabling  2534  the metered additive supply temperature adjusting apparatus  2536  to extract or add heat using reversible flow of a media in the temperature control media piping  2538  of one embodiment. The bottling electronic monitoring and control network  2599  is used for metering, monitoring and controlling combining ingredient quantities, regulating ingredient and mixture temperature and pH level of the mixture of one embodiment. 
     Bottling Quality Control Process: 
       FIG. 26  shows for illustrative purposes only an example of a black water bottling quality control process of one embodiment.  FIG. 26  shows a black water bottling quality control process including the bottle quality control station  2440 . Bottling quality control includes a bottling facility physical plant, sanitation inspection procedures and processes including labeling and packaging. The black water beverage method and system bottling apparatuses and processes  2490  includes a black water bottling process server  2600  and computer  2601  to control and regulate black water bottling quality control processes of one embodiment. 
     The bottle quality control station  2440  processes filled, capped, and sealed bottles  2650  for inspections. Qualified personnel conduct physical inspections. Not shown are automated electronic and mechanical sensors and testing devices to inspect for contamination, improper capping and sealing. Inspection results are logged into the black water bottling process server  2600  by physical inspectors using the computer  2601 . Automated electronic and mechanical sensors and testing devices transmit inspection results to the black water bottling process server  2600 . Should a bottle not pass the inspection regimen physical inspectors are alerted by the black water bottling process server  2600  of an inspection rejected bottle  2654  for physically pulling inspection rejected bottle from the conveyor  2652  and transmitting a rejection signal to a robotic gripper  2653  for pulling inspection rejected bottle from the conveyor  2652  and depositing the inspection rejected bottle  2654  in a rejected bottle receptacle  2656  of one embodiment. 
     The bottle packing station  2450  is for receiving a unit package production code  2615  printing instructions  2640  for using a label printer  2642  apparatus and label application apparatus  2644  to affix a unit package production code  2615  includes a barcode  2612  and/or a QR code  2613  label to a bottle and for direct printing on a bottle surface  2643  the unit package production code  2615  data to inform consumers of ingredients, nutritional data and other information including a batch identifying code. The unit package production code  2615  barcode  2612  and/or QR code  2613  is read for example using an application on a users&#39; smart phone of one embodiment. 
     Non-corrosive and non-toxic disinfectant agent impregnated flattened packaging  2610  materials are positioned for using a printer  2604  to print a unit package production code  2615 . The unit package production code  2615  including a barcode  2612  and/or a QR code  2613  on the flattened packaging  2610  materials for providing automated identification of product batch data and packaged product tracking. Flattened packaging  2610  with a printed barcode  2611  passes through a barcode reader scanner  2620  with QR code reading capability to track the numbers of batch indicated product packaging used for a particular batch. The flattened packaging with a printed barcode  2611  is conveyed to the bottle packing receiving station  2452  for processing through the bottle packing folding station  2454 . Folded bottle packing materials are set on the bottle carton conveyer  2456  for movement to the unloaded carton staging area  2458  of one embodiment. 
     The carton assembly station  2460  includes automated processes for robotic (not shown) placing of inspection approved filled, capped and sealed bottles in folded carton packaging. Folded packaging with bottles packed inside  2630  is processed to complete sealing of closed packaging  2632  with a plurality of labeled bottles  2634 . Another barcode reader scanner  2620  registers a sealed closed package of bottles passing through on the assembled cartons shipping conveyor  2474  to identify and track the distribution of the batch identified product of one embodiment. 
     Product Labeling: 
       FIG. 27  shows a block diagram of an overview of product labeling of one embodiment.  FIG. 27  shows one embodiment of product labeling  2700 . Nutritional data from  FIG. 21  is transmitted using the black water bottling process server  2600  of  FIG. 26  and computer  2601  of  FIG. 26  for nutrients included in a product batch mixture. The black water bottling process server  2600  of  FIG. 26  calculates volumes of the nutrients in a batch mixture for inclusion in nutrition facts  2710  data to be included in a product batch label. The nutrition facts  2710  data can include for example a serving size  1  bottle up to 20 fl. oz.  2711 , number of servings per container  2712 , total fat  2713  including saturated fat  2714  and trans fat  2715 , cholesterol  2716 , total carbohydrate  2717 , calories per serving  2720 , a % daily value  2721  calculated using the black water bottling process server  2600  of  FIG. 26 , sodium  2722 , total sugars  2723  including added sugars  2724 , protein  2725 , vitamins  2726  and minerals  2727  of one embodiment. 
     The black water bottling process server  2600  of  FIG. 26  can transmit from  FIG. 21  ingredients  2730  included in a product batch mixture. Each ingredient  2731  is listed in a descending order of predominance  2732  using the calculated volumes from the black water bottling process server  2600  of  FIG. 26  calculated volumes sorted by a descending order of predominance  2732 . The ingredients can for example include a common or usual name  2733 , the presence of any known major food allergen  2734 , an approved chemical preservative  2735  including a function of the preservative  2736 , and certified colors and artificial colors  2737 . The black water bottling process server  2600  of  FIG. 26  can using language databases translate the ingredients, nutrients and other batch mixture data in a desired foreign language to create bilingual labeling with data in English first  2740  of one embodiment. 
     Information from  FIG. 22  for products  2750  is included in creating label data. Label data can include for example a statement of product age  2760  for example of an alcoholic beverage showing “Aged 5 years”. Label data can include for example a health warning statement  2761 , coloring, flavoring and blending materials  2762 , type of alcohol neutral spirits or alcohol and whisky, beer, wine  2763  and name and address of the manufacturer, packer, or distributor  2764  of one embodiment. 
     The foregoing has described the principles, embodiments and modes of operation of the embodiments. However, the embodiments should not be construed as being limited to the particular embodiments discussed. The above described embodiments should be regarded as illustrative rather than restrictive, and it should be appreciated that variations may be made in those embodiments by workers skilled in the art without departing from the scope of the present invention as defined by the following claims.