Patent Publication Number: US-2020276731-A1

Title: Portable cement mixing apparatus with precision controls

Description:
CROSS-REFERENCE TO RELATED APPLICATION 
     This application is a continuation of U.S. application Ser. No. 14/517,085 filed Oct. 17, 2014, now allowed, which is incorporated by reference. 
    
    
     BACKGROUND OF THE INVENTION 
     The present invention is directed to a transportable mixing apparatus for cementitious products transported to and operated on location at a construction site and where accurate control as well as precise qualities, measurements, and performance characteristics of the production processes and of the final cementitious product are required or desired. The present invention is further directed to the described transportable mixing apparatus capable of providing and remotely transmitting a permanent record of all significant parameters of each mixed batch of cementitious product to an off-site location to provide quality assurance. Data recorded during production operations further allow accurate identification of manpower needs of projects and allow owners/operators at job sites to record, control, predict and manage production costs and manpower needs. 
     BRIEF DISCUSSION OF THE RELATED ART 
     Cementitious and other slurry products come in various forms, such as gypsum, cement or lime products and are used in many areas of construction and building, including, without limitation, floor underlayments and other structural and non-structural elements in buildings. For example, gypsum cement underlayments have utility in, among other things, leveling a surface on which flooring products (such as carpet or tile) are to be installed, injecting a fire retardant subfloor, or providing a substrate of sufficient hardness to sustain the applicable surface flooring products or other intended use. 
     Every cementitious product requires exacting measurements and specific ratios of the required ingredients to produce the desired physical characteristics. For example, tile, vinyl planks, and carpet flooring that are laid upon gypsum underlayment require very different and distinct strengths and self-leveling properties of the gypsum or other cement underlayments. Likewise, building codes and architectural plans may require various underlayment strengths and self-leveling properties. These different and distinct physical properties of cementitious products are produced only through precisely measuring and mixing exact ratios of the particular final product&#39;s ingredients. To the extent that these exacting ratios are not mixed into a specific slurry, there is an immediate and irreparable harm. In terms of product quality, the finished product will not meet required performance standards. The economic impact is incurred by the owner and user of the product. For example, an insufficient floor underlayment will begin to crumble and will cause not only an aesthetic issue, but an inability to sustain the intended use of the floor (such as foot traffic or heavy loads on rollers). The only way to repair the floor is to (i) displace the user of the floor, (ii) demolish the floor product, (iii) demolish the failing underlayment, (iv) and reinstall the underlayment and floor product. These costs are high and create a tension between the user, owner, installer, and underlayment manufacturer as they all attempt to place the blame and costs on one of the others. This tension is exacerbated by the fact that there is no current method to test floor underlayments for quality and strength once it has been poured and cured. 
     Cementitious products are formed by mixing two or more ingredients to form slurry that is poured and leveled, as needed, while wet and before hardening. Gypsum underlayment is formed by mixing water, a gypsum cement mix, and sand in the correct proportions to form slurry. 
     For example, and based on the required characteristics of the final product as well as conditions at the site, a certain amount of gypsum cement mix is mixed into a precise amount of water. Typically, an aggregate, commonly referred to as a “filler” in practice and elsewhere herein, is then added (usually fine grain or coarse grain sand) and mixed into these ingredients for a suitable time period. The resulting slurry is then poured, leveled, and left to dry or harden wherever desired. 
     It is necessary to have on-site mixing of certain cementitious products because (as opposed to concrete) once mixing is complete, these certain cementitious slurries&#39; useful lives are short. For example, gypsum underlayment remains a workable slurry for less than 45 minutes. 
     While in theory there should be little difference in the ability of a human operator to control quality between off-site and on-site locations, the realities of human operators at active job sites make it extremely difficult to accomplish accurate measurement of the mixing ingredients. Trying to take precise measurements of bulk products at large scales at an active and fast-moving job site can produce poor results. While precise measurement can be obtained, they come at the cost of speed. Using current technologies, accurate measurements are prohibitively expensive. Conversely, cost effective measurements are unreliable. On-site mixers are operated using high powered engines, which produce systemic vibrations. To transport the mixing apparatus to the site requires the use of a trailer or similar mobile means. The combination of engines and trailer impose significant vibrational and other accuracy-defeating problems in the equipment. 
     As a result, in known art in the field such as U.S. Pat. No. 5,730,523 (the “&#39;523 patent”), the invention therein is directed to transportability, especially in adverse weather conditions. Although the invention of the &#39;523 patent includes basic features of a portable cement mixing apparatus (i.e. ingredient storage bins, delivery means, mixing means, scales and computer controls), the resulting invention allows in practice only “a” slurry to be produced, not “the” slurry required in a given application. Certainly, in practice there is a theoretical possibility that circumstances will allow a specific grade and quality of slurry to be made; however, vibration, human error and the reality of entropy indicate wholly against it. Instead, operators can provide assurances only that apparatus in use on site currently produced a slurry within wide error bars or incur significant costs to ensure constant and time-consuming testing measurements. 
     In a similar fashion, US 2004/0218462 (the “&#39;462 publication”) describes a proposed method of testing the slump of a slurry to determine product quality. If the slump is not accurate, a refinement to the slurry is made. Slump, however, is not a reliable test of a final product&#39;s strength or composition. For example, depending on the quality, size, and dampness of the filler used (such as sand), an operator can have two batches with the exact same slump that produce significantly varied composition and, therefore, final strength determined by multiple factors—meaning that a slurry of a known slump still will have a generally unknown composition. In effect, the &#39;462 publication performs a one variable test of a two (or three) variable problem. It is not possible for the invention of the &#39;462 publication to identify substantive issues with the slump where it cannot look. As a result, the slurry as poured will have unknown properties. 
     By way of metaphor, one might envision a theoretic device for 3-D printing a human organ. If the operator merely requires the 3-D printer to print “an” organ using “muscle” cells, it is not likely to print “the” organ necessary for transplant. By the same token, whereas many mixers of cementitious slurries are capable of mixing slurries within wide error bars, the types of mixers capable of mixing slurries within narrow and controlled limits and under normal operational requirements and time limits are either very limited or nonexistent. They operate either within the realm of guesswork or they operate prohibitively inefficiently. 
     The current, inaccurate on-site human operator practices and the necessity of precision measurements have created a widespread problem in the construction industry, especially when there is an allegation of defective installation. With current technology, a defective installation claim essentially becomes a mere war of words with no strong evidence to support either party&#39;s claims because (i) the installer cannot produce reliable evidence of proper mixing ratios throughout the entire project and (ii) there is no approved method of testing the strength and characteristics of a cementitious product once it has been installed and dried (i.e. core samples do not reproduce a true example of the installed product&#39;s strength). Likewise, there is currently no effective means for both accurately measuring the ingredients in a batch of a cementitious product while it is prepared and then recording that information for later use. Without accurate recordation of the ingredients and other production parameters of the slurry batches that were installed, the quality of the as-poured cementitious product cannot be reliably determined. Thus, there is no effective method for the operator to prove, either concurrently or subsequently to preparation, that each and every batch of cementitious product was properly mixed according to the manufacturer&#39;s or customer&#39;s specifications. 
     There is a need for a device capable of mixing ingredients for a cementitious product to produce the slurry on-site for immediate use. There is a further need for the same device to control the accurate measurement and rate of input of each individual ingredient during the mixing process regardless of operational conditions or operator error. There is a further need to take the control of the measuring and recording of the ingredients for a cementitious product away from the on-site human operator and instead ensure these activities are performed automatically and reliably, as well as record management metrics that can be measured from the data, such as productivity and operating hours. Further still, there is a need to have these precise amounts of each ingredient to be made known, recorded, and remotely transmitted to an off-site database for quality management, third-party investigation (such as by the manufacturer or building owner), and future assurance of proper ratios and mixing. The described apparatus meets these needs. 
     SUMMARY OF THE INVENTION 
     An apparatus for forming a slurry comprising at least one water or other liquid ingredient and at least one, although typically two, flowable, pourable or otherwise conveyable particulate mass or masses, generally one comprising a binding material and one comprising a filler or aggregate material, uses a computer controlled operating system, software, as well as motors and/or valves suitable to deliver a highly accurate amount of each ingredient one at a time into the mixing chamber. For purposes of this specification, the term “slurry” is used for any slurry or slurry-like product, which can be described as any temporary fluid material that requires the mixing of dry and wet ingredients that can then be pumped through a hose, including, but not limited to grout, paste or mortar. The mixing chamber has a system of interconnected scales and associated computer hardware and software that tracks and records in real time the current weight of each of the materials in the mixing chamber, accounting for unweighed infalling ingredients in this process. Software associated with the mixing chamber and the loaded materials therein allows for the tracking and remote transmission of the weight of each individual ingredient in the mixing chamber. The desired amount of each individual ingredient is predetermined and loaded into the computer operating system. This is then reflected in the batch mixed and ultimately installed. 
     While the operator of the apparatus controls the recipe for each batch made, the operator cannot make any batch that is not accurate nor accurately recorded. 
     Ingredients are loaded into the mixing chamber sequentially. As the desired weight of each ingredient is reached within the desired accuracy programmed into the system, the operating system slows down and then shuts off delivery of that ingredient. There can be infinite speeds and/or a slow, curved progression of the speed&#39;s increase and decrease, but typically this is done using two preset delivery speeds. A high rate of speed for inputting each ingredient is used when the ingredient is initially added and while the weight of that ingredient is below an identified threshold. When a predetermined percentage of the total amount of the ingredient is reached, the rate of input is slowed by the operating system to a second rate, which is lower than the first rate of input. This slower rate of input is used until the desired total amount of the ingredient is reached, at which time the input is stopped. The system delivers a preselected weight of the liquid ingredient and then, in succession, a first particulate ingredient and the second particulate ingredient, if the second particulate ingredient is required. Additional ingredients may be added as needed. The system comprises storage and delivery means for each of the ingredients, allowing a start to delivery of each ingredient, continued delivery at different rates, depending on the amount of the ingredient being delivered then in the mixing chamber, and stopping delivery of each ingredient when the desired amount of the ingredient in the mixing chamber is accurately reached. The rate of delivery, further, is fully variable, from a low rate to a high rate and complete shut off. Although in practice only two different speeds are typically used by the operators, the two speeds selected are fully variable within a broad range of possible input speeds or can be delivered on a smooth, gradual increase and decrease in speed. 
     Further, because the weight of each ingredient is measured in the mixing chamber, operators are able to continue to maintain stores of each ingredient by adding additional amounts of each ingredient to the separate storage chambers on a continual basis. 
     It is commonly known in the field that the mixing of ingredients is made more efficient by the retention in the mixing chamber of some amount of the previous batch of cementitious slurry in the mixing chamber, to which are added ingredients, in the proper order and in preselected weights, as described above, to make additional batches of cementitious slurry. By adding additional ingredients to the partial previous batch, the mixing time needed for the additional ingredients to be ready to pour is substantially reduced, while the quality of the batch is substantially improved. The apparatus&#39;s operating system is able to cause the removal from the mixing chamber a specific amount of the mixed batch, retaining a known and desired amount of the previous batch. In the context of the present invention, the software is configured to zero-out the amount of the partial previous batch retained in the mixing chamber before the addition of the ingredients for the next batch. Because of this, only the ingredients for the next batch are measured, resulting in the accurate recording of information as to the qualities of the next batch. 
     Because quality is capable of being retained by the accurate measurement and recording of information as to each batch, while maintaining a high through-put at the mixer, it is generally possible to pump continuously. 
     While the operator of the apparatus maintains a high level of control over all of the operations of the apparatus, such as rate of production and recipes for batches produced, the operator cannot operate the apparatus “off-line.” All production information is automatically saved and stored by the operating system of the apparatus. 
     In an exemplary embodiment, a first, a second, and a third ingredient are separately stored in appropriate storage chambers fixedly integrated into the system. Each separate storage chamber is conveyably connected to the mixing chamber using a connection means suitable for the physical characteristics of each ingredient. The liquid storage means may be conveyably connected to the mixing chamber using a pump, a hose, one or more valves and a nozzle. The separate storage chambers for each of the particulate masses are each conveyably connected to the mixing chamber using a suitable conveyor belt or other means for conveying quantities of particulate masses. The means of conveying the liquid and particulate masses are controlled by valves, pumps or motors, which are controlled by the software system. It is noted that while the number of ingredients, storage chambers and apparatus for conveying is given as three, more or fewer ingredients may be used, with additional storage chambers and conveyance apparatus disposed thereon as needed and with control modifications as needed. 
     Once the human operator has input the recipe for the proportion of ingredients needed, the system software controls the sequential conveyance of all ingredients, including the amount, by weight, of each ingredient to be conveyed to the mixing chamber, the rate of flow of each ingredient into the mixing chamber, and the accuracy of the weight of each ingredient in the mixing chamber. 
     In the exemplary embodiment, a batch of slurry is prepared in the following fashion, showing the primary inventive elements:
         The operator, based on design or construction specifications for a certain type of cementitious product, inputs a recipe for an underlayment slurry into the operating system.   A sufficient quantity of each necessary ingredient is stored in each of the separate storage chambers. The operating system sends a signal causing the liquid ingredients to be pumped into the mixing chamber. During the time that the amount (weight) of the liquid ingredient in the mixing chamber is low, control valves are fully open and the pump is on. The scales connected to the mixing chamber send signals to the operating system in real time as to the weight of the liquid ingredient. When the weight of the liquid ingredient in the mixing chamber reaches a preset limit, which is less than the full amount to be delivered to the mixing chamber, the operating system sends a signal to the valves controlling the rate of flow of the liquid ingredient. The operating system signals the valves to slow the pump a predetermined amount so that the rate of inflow of the liquid ingredient is at a slower rate, still known to the system. When the maximum level is reached, as determined by the scales, the valves are signaled by the operating system to shut completely, stopping the flow of the liquid ingredient. The two rates of inflow are predetermined before mixing begins, but the rates may be altered at any other time to any desired degree.       

     The speed of the rotation of the mixer blades matches the rate of inflow of an ingredient. While an ingredient is added at a high rate, the mixer blades rotate at a fast rate. When the rate of input of an ingredient is slowed, the rate of mixer blade rotation is slowed. However, when input of an ingredient has stopped, the mixer blades rotate at a slow rate. After all the ingredients are added, the mixer blades speed up to a high rate to ensure an adequately mixed batch. 
     It is known in the field that conditions under which mixing devices must operate may vary, depending on location, the nature of the project, the experience of the operating crew and the like. The benefit of the system is the fully adjustable control over the rate of inflow which allows a maximal rate of inflow of an ingredient while providing exact control over the amount of the ingredient in the mixing chamber and in light of external conditions. This allows high accuracy without sacrificing speed. Production rates are thereby maintained at a high level despite the external conditions. 
     In a similar manner, the particulate ingredients are input to the mixing chamber. With the liquid ingredient in the mixing chamber at the correct weight, the operating system sets an initial weight of zero for the second ingredient, a first particulate ingredient (meaning that at first, no first particulate ingredient in is the mixing chamber). The operating system sends a signal to a conveying means connecting the storage chamber for the first particulate ingredient to the mixing chamber. The conveying means inputs the first particulate ingredient at first at a high rate of flow. In the exemplary embodiment, a conveyor belt between the storage chamber and the mixing chamber carries the first particulate ingredient at a known rate. The scales connected to the mixing chamber weigh the amount of first particulate ingredient. At a preset weight, based on the recipe for the desired slurry, the operating system sends a signal to the conveying mean to slow the rate of input of the ingredient. When the desired weight of the first particulate ingredient is reached, the operating system sends a signal to the conveyor belt to stop input of the first particulate ingredient. In the same manner as the liquid ingredient, the rate of input of the first particulate ingredient is maximized while a highly accurate amount of the first particulate ingredient is inputted to the mixing chamber, despite any limitations imposed by external conditions at the work site. Again, mixer blade rotation corresponds to the input rate. 
     Thereafter, the second particulate ingredient is added to the mixing chamber in a similar, precise, and accurate manner. 
     For each added ingredient, the apparatus accurately accounts for ingredients in transit. For example, for water, the software accounts for the amount of water which has left the nozzle but not yet reached the mixing chamber (that is, the amount of water in free fall into the mixing chamber). By accounting for the amount of water in transit, the total amount of water in the mixing chamber remains accurate despite any lag between sending the shut off signal for that ingredient and the time the last water reaches the mixing chamber. Similarly, the apparatus accounts for the amount of any particulate ingredient in free fall into the mixing chamber, having been dropped from the conveying means but not yet in the mixing chamber. 
     The final weight that is recorded for each ingredient is measured with an additional process. Once the system detects the total predetermined weight has been reached (or almost reached), the system closes the valve and then waits to ensure that the predetermined weight holds for a certain time, typically three seconds. The length of time used may be varied by the operator. At the end of three seconds, the weight is recorded. The benefit of the three-second (or other certain time) measuring window is the prevention of recording an erroneous measurement caused by a vibration, jostle, or other environmental effect on or within the apparatus. During the weighing period, the engine powering the apparatus continues to operate. The engine, an approximately 125 BHP diesel engine, typically operates at a sufficiently high rate (1800 RPM +/−) throughout all operations so that errors caused by engine vibration can be eliminated, especially with the ability to calibrate the scale while the engine is running. The extended weighing period for a given ingredient is designed to allow the mixer blades to slow and vibrational and other weighing error sources to dissipate before the final weight of an input ingredient is measured. Similarly, weight over a time period is measured while the mixer blades rotate slowly so as to minimize errors. 
     Further, because the weight of each ingredient is measured in the mixing chamber, operators are able to continue to maintain stores of each ingredient by replenishing the storage chambers on a continual basis as the batches are being weighed and mixed. 
     It is commonly known in the field that the mixing of ingredients is made more efficient by the retention in the mixing chamber of some amount of the previous batch of cementitious slurry in the mixing chamber. By adding a new batch&#39;s ingredients into the mixing chamber that still contains a portion of the previous batch, the mixing time needed for the new batch&#39;s ingredients is substantially reduced and the quality is improved. Once the mixing chamber has fully mixed the ingredients for the requisite time to create properly wetted slurry, the batch is dumped into a holding chamber. The slurry in this holding chamber is then transferred through a hose by a pump for installation. This holding chamber allows simultaneous and continuous mixing and pumping, which increases the speed of the ultimate installation of cementitious slurry. 
     Further, the amount of slurry in the holding chamber is measured by the computer system so that the mixing chamber will not dump a slurry batch into the holding chamber until there is enough room in the holding chamber. This removes the need for a human operator to supervise the relative speeds of the mixing and pumping operations. If the pumping operations have slowed, the mixer will not create new batches until pumping operations have begun again. 
     If desired, the operator of the apparatus can maintain a high level of control over all of the operations of the apparatus through the user control interface, such as rate of production and recipes for batches produced. However, the operator cannot operate the apparatus “off-line.” All production information is irrevocably and automatically saved and remotely transmitted to an off-site database by the operating system. 
     The operating system records all steps of the mixing process, which includes the amounts of each ingredient added to the mixing chamber and may include additional mixing or ingredient parameters, such as the time each ingredient was added to the mixing chamber or the time taken to mix the ingredients, ingredients, jobsites, time records, weights, mix times, dump time, operator number, or the like. 
     The ability of the operating system to transmit the record of each individual batch&#39;s production metrics ensures the quality of installation and provides documentation of the precise ratio and weight of each individual ingredient in each batch installed at any particular job. This allows operators to provide assurances and guarantees that the products installed from the system met the manufacturer&#39;s and/or customer&#39;s design specifications. 
     In addition, the available metrics provide useful management tools, such as measuring productivity, when the apparatus is in operation (and conversely when it is not in operation), and any other related or measurable metric related to the operation of the apparatus. This information can be provided via remote transmission to management, and therefore eliminates the need for certain on-site supervision man hours. 
     The invention is thus able to provide a higher quality final product, both as to the accuracy of the ingredients and the consistency to which the ingredients are mixed, produced at a high rate of production and in which both operator error and operator misconduct are avoided and prevented. Further, the invention provides for the remote transmission of the qualities of the final product, which assures quality and management control. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  depicts a side view of the water tank and mixing chamber of the invention, showing the stand on which the mixing chamber is placed, as well as the hose and nozzle to transfer water to the mixing chamber. 
         FIG. 2  depicts a top view of the same items. 
         FIG. 3  depicts a side view of the assembled apparatus showing primary components of the apparatus. 
         FIG. 4  depicts a perspective view of the mixing chamber, showing two of the strain gauge load cells used to weigh ingredients added to the mixing chamber. 
         FIG. 5  depicts a perspective of one of the strain gauge load cells used to weigh ingredients added to the mixing chamber. 
         FIG. 6  depicts a graph showing an exemplary rate of conveyance of three separate ingredients into the mixing chamber during a representative production run of the invention.  FIG. 6  further depicts a graph of the mixer speed during ingredient conveyance. 
         FIG. 7  depicts a side view of the cement bin, showing in addition the auger system used to deliver cement, gypsum or other binder to the mixing chamber. 
         FIG. 8  depicts a top view of the cement bin, showing additional details of the auger system used to deliver cement, gypsum or other binder to the mixing chamber. 
         FIG. 9  depicts a side view of the sand bin, showing in addition the conveyor used to deliver sand to the mixing chamber. 
         FIG. 10  depicts a top view of the sand bin and conveyor use to deliver sand to the mixing chamber. 
         FIG. 11  depicts a schematic of the major operational components of the operating system. 
         FIG. 12  depicts a flow chart of an exemplary run to make a batch of a cementitious slurry, showing in particular the flow of water using variable speed control, the flow of binder into the mixing chamber and the flow of sand into the mixing chamber. 
     
    
    
     DETAILED DESCRIPTION OF THE DRAWINGS 
     The invention is capable of mixing at a worksite high quality slurry for use in various areas of the construction industry in which it is necessary to know the ingredients of the slurry to a high accuracy as well as to create and maintain a permanent, portable or transmittable record of the manufacturing of the slurry for quality assurances purposes. 
       FIGS. 1 and 2  show aspects of the invention relative to introducing water to the mixing area for forming slurry. A wheeled, hitchable, steel-beam flatbed trailer  100  has affixed to it a steel-beam platform  105  suitable for mounting thereon a mixing chamber  101  known in the industry. A trailer  100  is not mandatory. The apparatus may be equally mounted on a truck, mobile skid or similar transportable base. Similarly, configurations of the components as depicted in the figures are not mandatory, nor is the invention limited to two or three ingredients. The invention may have storage chambers and conveyance apparatus in such numbers, operational configurations and design as needed. Design and configuration variations are determined by the nature of the slurry to be prepared. As better depicted in  FIG. 2 , the mixing chamber  101  has an opening  102  at its top side able to receive a variety of ingredients necessary or useful for making cementitious slurry. Disposed within the mixing chamber  101  are mixing blades  107  for mixing the added ingredients. The trailer  100  also has affixed to it a water-tight tank  103  of suitable volume for storing an adequate and refillable supply of water or other liquids necessary for operations at a work site. One end of a hose  104  is sealably placed through one wall of the tank  103  and is connected to a pump (not depicted) disposed within the tank. The other end of the hose  104  has disposed on it a nozzle  108  suitably designed to allow water or other liquids to be pumped from the tank  103  into the mixing chamber  101  through the top opening  102  without spillage, spraying or other loss. The pump is controlled by an operating system  301 , depicted in  FIG. 3  and  FIG. 11 , which controls and digitally records all aspects of the operation of the apparatus. The rate of water flow into the mixing chamber  101  is limited physically by control of the rate of speed of the pump by opening or closing of the hydraulic valves disposed on the hose between the pump and nozzle  108 . Valves are controlled electronically. The pump and valves used in the invention may be any suitable pump and/or the hydraulic valves of known design and operational parameters in the industry. 
     The hose  104  is fluidly connected from the tank  103  to the opening  102  of the mixing chamber  101 , with the nozzle  108  of the hose removably affixed to the top of the mixing chamber  101  so as to allow water or other liquid to flow into the mixing chamber  101  through the opening  102 . In an alternate embodiment, the nozzle  108  may be placed through a wall of the mixing chamber  101  at any unobstructed position to allow water to be introduced into the mixing chamber  101  as needed. 
     Referring to  FIGS. 3 and 11 , operation of the apparatus is attained by use of a software-based operating system  301  disposed in a suitable work station  302  on the apparatus. During operation, a worker selects from a list of preprogrammed recipes or enters an ingredient list, weights of the ingredients, and mixing time into the operating system  301  to create a new recipe. In practice, this information may be entered manually, as by keyboard  1102 , touchscreen  1101 , portable memory device  1104  or similar method, or remotely, such as by wireless communication  1105 , into the operating system  301 . Software for the operating system  301  is proprietary but is not otherwise disclosed. The operating system  301  is wired by any suitable means to all operative features of the apparatus and controls all operational functions of the apparatus. The operating system  301  further includes memory storage  1103 , a processor  1108  for running operational programming, and wired or wireless data transmission means  1105 . 
     Referring to  FIGS. 1, 3, and 4 , at the start of the operational run of the apparatus in an exemplary embodiment of the invention, a recipe for slurry production is entered into the operating system  301 , and the operating system  301  determines the tare weight of the mixing chamber  101 . In essence, in operation the tare weight is a zero point of the system—that is, with no ingredients in the mixing chamber  101  for a particular batch of slurry. Depending on the circumstances of the operation of the apparatus, the tare weight of the mixing chamber  101  may be the weight of the mixing chamber  101  empty or it may be the mixing chamber  101  with some amount of previously mixed slurry still in the mixing chamber  101 . It can be advantageous to the mixing of a subsequent batch of slurry to retain a predetermined portion of a previous batch of slurry in the mixing chamber  101  to allow for more thorough and faster mixing of the subsequent batch using some portion of the previous batch as a “catalyst” for mixing. It is not necessarily intended that reference to the previously mixed slurry in the mixing chamber  101  as a “catalyst” is used here in a literal or technical sense but as a metaphor for improved mixing time and thoroughness based on the physical characteristics of the previously mixed slurry retained in the mixing chamber  101 . After setting the tare weight, the information is stored in memory  1103 . In addition, the memory  1103  stores the recipe for the slurry to be made along with all other operational information of the production run. 
     During a production run, the operating system typically determines the amount of slurry to be left in the mixing chamber  101 , which may be any amount of the previous batch sufficient to aid subsequent operations. However, in alternate embodiments of the invention, the determination of the amount of slurry left in the mixing chamber  101  from a previous batch may be automatically determined based on environmental conditions or production needs and as determined by sensors, such as temperature sensors, moisture sensors, sensors for determining the density of a slurry or the like. A failure to list a type of sensor or the data a sensor might detect is not a limiting factor in alternative embodiments of the invention. Any suitable sensor measuring any suitable quality of the slurry or the apparatus may be used. 
     Referring to  FIG. 4 , the mixing chamber  101  is affixed to the platform  105  by the use of a set of four strain gauge load cells  401 , commonly referred to as a “scale” when referring to one strain gauge load cell or “scales” when referring to more than one strain gauge load cell, for weighing the amount of each ingredient delivered in the mixing chamber  101 . In  FIG. 4 , only two strain gauges  401  are visible. The other two strain gauges  401  are configured in a like manner on the opposite side of the mixing chamber  101 . A detail depicting a single scale is shown in  FIG. 5 . The scales  401  are interposed between the each one of four feet  402  on the mixing chamber  101 . Each of the scales  401  is wired to a centralized weight computing unit, which is wired to the operating system  301  so as to enable electronic communication between the scales  401  and the operating system  301 . Wiring may be accomplished by any standard method and is not depicted in the figures. 
     In an operational run, a worker either selects a pre-programmed recipe or enters an ingredient list, desired weights, and mixing time into the operating system  301  and starts the operation of the apparatus. The operating system  301  activates the scales  401  to set the tare weight of the mixing chamber  101 . Mixing of slurry begins when the pump in the water tank  103  is activated by the operating system  301 , starting the flow of water into the mixing chamber  101 . While other liquids may be used, water is the typical liquid ingredient and will be described in this exemplary embodiment. At the start of the flow of water, the hydraulic water pump in the water tank  103  is activated by the operating system  301  for a fast flow of water. Valves are opened to permit the pump to cause a high rate of flow of water into the mixing chamber  101 . The operating system  301  measures the weight of water in the mixing chamber  101  using the set of scales  401  in real time. A software algorithm therefrom determines the weight of water accurately. The operating system  301  uses that measurement to determine whether to maintain the rate of water flow into the mixing chamber  101  or to modify it. 
     When the weight of the water in the mixing chamber  101  reaches a preprogrammed, predetermined threshold as set in the operating system  301  software, the operating system  301  sends a signal to the hydraulic control valves controlling the pump to slow the input rate to a slower but still known rate of input. Real time weighing of the water in the mixing chamber  101  by the scales  401  is continuous throughout. When the weight of the water in the mixing chamber  101  reaches a final threshold determined by the recipe, the operating system  301  signals the hydraulic valves to stop the pump. The operating system  301  software is configured to account for the amount of water which has been emitted from the nozzle  108  but which has not yet fallen into the mixing chamber  101  to be weighed. Thus, the operating system  301  can be seen to anticipate this additional amount of water not yet measured in the mixing chamber  101  following shut off of the pump and closing of the valves. The weight of the water in the mixing chamber  101  which causes the signal to shut off the pump is thus: 
       (total weight of water desired as an ingredient)−(weight of water in freefall between nozzle and mixing chamber)=(weight of water sufficient to signal pump shut-off).
 
     By this method, after the shutting off of the pump and the weighing of the water in the mixing chamber  101 , the total weight of water in the mixing chamber  101  will be within a specified, low tolerance of the specified amount programmed into the operating system  301 . 
       FIG. 6  depicts typical rates of flow of ingredients into the mixing chamber. Note that the rate of changes of the weight of each ingredient in the mixing chamber  101  is arbitrary. The horizontal axis of  FIG. 6  represents time. The vertical axis for ingredients (lower graph) represents rate of flow. The vertical axis in the top graph represents mixer blade speed. At point A on the graph, the flow rate of water is 0 gallons per minute, indicating the pump is not activated. When activated, with the pump set for a high rate of flow, the flow rate at point B on the graph quickly reaches Y gallons per minute, an arbitrary rate of flow. This rate is held steady while water flows into the mixing chamber  101 , during which time the weight of the water is weighed in real time. Point C on the graph indicates the time at which the weight of the water in the mixing chamber reaches the pre-set midpoint threshold. At that time, the operating system  301  signals the hydraulic valves to operate the pump at a slower speed to allow a slower input rate, Z gallons per minute, another arbitrary rate of flow and in which Z&lt;Y, reflected at point D on the graph. This slower rate of input continues until the final threshold weight of water is reached, at which time the operating system  301  signals the valves to close, and the pump stops, as reflected at point E on the graph. A small amount of water, the weight of which is known, falls into the mixing chamber, reflected at point F on the graph, showing the full desired amount of water in the mixing chamber. In this exemplary embodiment, Y&gt;&gt;Z. In alternate embodiments, rates of flow may include Y′, in which Y&lt;Y′, or Y″, in which Y&gt;Y″, with similar variability expressed for Z, Z′, Z″ and so forth. 
     As further described in  FIG. 6 , top graph, while the rate of input of the water is fast, the mixing blades  107  rotate slowly. Slow speed X is arbitrary in this representation. 
     It is thus seen that the operating system  301  typically controls the rate of input of an ingredient, currently, water, in a trinary system—off, fast input and slow input rates. It is noted, however, that the operating system  301  allows a fully variable range of speeds for inputted ingredients. The “fast” setting may vary, depending on need, from Y gallons per minute to Y′ gallons per minute, to Y″ gallons per minute, or any rate in-between and with the Y, Y′ and Y″ values determined on conditions such as pump or valve capabilities, worksite conditions, slurry type and so forth. Similarly, lower rates of input for the Z, Z′ and Z″ rates of flow are fully variable except that a given Y value will always be greater than its accompanying Z value. The alternative, in which Y&lt;Z is possible, but of no practical value. Rates of change between a “Y” rate and a “Z” rate may also be controlled by the operating system along any rate of change. 
     The operating system  301  further creates and stores data in memory  1103  relative to each production batch during operation, including a batch identifier, worksite information, the weight of the each ingredient added to the mixing chamber in the batch, the identity of each ingredient in the batch, mixing time and other information useful for quality control. 
     Following completion of the addition of water to the mixing chamber  101 , the amount of water is weighed by the following process: the speed of the engine operating the apparatus is maintained at a constant rate and the mixing blades  107  are maintained at a slow speed. The operating system  301  then measures the weight of the water in the mixing chamber  101  for a predetermined period, typically 3 seconds. By allowing a known level of systemic vibration only to be accounted for, the actual weight of the water is determinable to high precision. Other sources of vibration and weighing error are damped from the system, such that a more accurate measure of the weight is obtained. The weight of the water in the mixing chamber  101  is confirmed to have held steady for the waiting period and then recorded. This process is also depicted in  FIG. 6 . Water is added to the mixing chamber  101  from times A through F. At time F, all input into the mixing chamber  101  is paused. This pause lasts from time F until time A′, the weighing period. Following the weighing, the final weight of the ingredient is assured and recorded to the operating system memory  1103 . 
     Still referring to  FIG. 6 , at time A′, the operating system  301  signals the input of cementitious powder into the mixing chamber  101 . Similar steps to inputting cementitious powder are used, as reflected at times A′ through F′. Between times A′ through C′, the operating system  301  causes the mixing blades  107  to operated at high speed. At time C′, the mixing blades  107  are signaled to operate at slow speed. In a similar fashion, from times F′ through A″, no ingredients are inputted into the mixing chamber  101 , the mixing blades  107  are operated at slow speed and the weight of the cementitious powder in the mixing chamber  107  is assured and recorded in memory  1103 . 
     At time A″, a similar process is followed for the loading of the filler, as depicted from time A″ through time F″, with a suitable period for assuring and recording the weight of the filler in a like manner. 
     The lengths of the pauses have been programmed to allow internal and systemic vibrations to dissipate from the apparatus. In doing so, a far more accurate determination of the weight of each ingredient can be made. Pauses of approximately 2 seconds to approximately 10 seconds are also typical. 
     Having added the water, the next ingredient, typically a binder in the form of a cementitious powder, may be added. Referring to  FIG. 7  and  FIG. 8 , on the steel beam, flatbed trailer  100  previously described also has disposed on it a steel beam platform  705  on which a bin  701  suitable for storing a cementitious powder is affixed. A bin lid  710  is hingedly attached to the bin  701  to control emissions and prevent foreign matter from entering the bin  701 . A grate  810  is further disposed atop the bin  701  below the bin lid  710  when in a closed position to prevent foreign objects from entering the bin  701  and to act as a safety device to prevent workers at the worksite from falling into the bin  701  or otherwise contacting the inner surface of the bin  701  directly. 
     The base of the bin  701  is attached to a coupler  706  for connecting to the bin  701  to a powder delivery tube  704  for delivering the cementitious powder into the mixing chamber  101 . Within the powder delivery tube  704  is an auger  802  of known design powered by a motor and controlled by the operating system  301 . An exit port  708  distal on the powder delivery tube  704  to the coupler  706  allows the cementitious powder to exit the auger  802  from above the mixing chamber opening  102  to allow infall of the cementitious powder into the mixing chamber  101 . 
     The bin  701  may be filled by workers by emptying either bulk or bagged quantities of a desired cementitious powder into the bin. 
     Upon inputting a recipe of ingredients for a batch of slurry into the operating system  301 , and upon completion of inputting water in the mixing chamber  101 , the operating system  301  again sets the tare weight to zero, indicting no amount of the next ingredient, in this case the cementitious powder, has been added to the mixing chamber  101 . Then, the operating system signals the hydraulic valves to operate the motor for the auger  802  to run. The cementitious powder in the bin  701  is carried along the auger  802  disposed within the powder delivery tube  704  and infalls into the mixing chamber  101  via the exit port  708 . As with the water, the operating system  301  weighs the input amount of cementitious powder in real time using the scales  401 . Referring to  FIG. 6 , as with the water, at first the rate of input of the cementitious powder is at a high rate of speed (still identified as an arbitrary Y pounds per minute) until the weight of the cementitious powder in the mixing chamber  101  reaches a pre-set threshold. 
     The arbitrary rate of Y gallons per minute for water does not connote to the arbitrary rate of Y pounds per minute for cementitious powder. The rates are identified for scale only. Any rate of input for any ingredient in a portable mixing apparatus may be used. 
     When the pre-set threshold is reached, the operating system  301  signals the hydraulic valves to operate the motor to slow the auger  802  such that the rate of input of the cementitious powder is slowed to arbitrary rate Z, in which Y&gt;&gt;Z. As with the water input, the operating system  301  software is configured to allow for a known amount of cementitious powder which has fallen from the exit port  708  but not yet landed in the mixing chamber  101  so as to determine an accurate time at which to stop all inflow into the mixing chamber  101 . By this method, the quantity of cementitious powder placed into the bin  701  is known to within a narrow tolerance. When the pre-set final threshold weight of cementitious powder in the mixing chamber  101  is reached, the operating system  301  signals the hydraulic valves to stop the augur  802 . 
     During the process of adding the cementitious powder to the mixing chamber  101 , the operating system  301  directs and controls the movement of the mixing blades  107 , also as depicted in  FIG. 6 . Between times A′ and C′, the mixing blades  107  operate at high speed. From times C′ to A″, the mixing blades  107  operate at slow speed. 
       FIG. 6  depicts the input of cementitious powder into the mixing chamber  101 . Times for the inputting of cementitious powder extend from time A′ through time F′. Again, the weight of the cementitious powder added to the mixing chamber  101  is measured and recorded in the same manner as the water during the programmed system pause between time F′ and time A″. The operating system  301  subtracts from the total weight recorded the weight of the water so that only the weight of the cementitious powder is retained. 
     An inventive element of the invention is the ability to input multiple ingredients for cementitious slurry in which a highly accurate weight of each ingredient is provided while allowing a high rate of input for each ingredient, such that said high rates of input of each ingredient can be separately and variably controlled as to need for an individual batch of cementitious slurry. 
     Referring now to  FIGS. 9 and 10 , aspects of the invention are provided for the input of a second powder ingredient, if desired, and typically a filler, such as an aggregate, into the mixing chamber  101 . On the steel beam, flatbed trailer  100  previously described is disposed a steel beam platform  905  on which is disposed a hopper  901  suitable for storing a filler for cementitious slurry. A typical filler is sand. The base of the hopper  901  contains thereon a variably openable port  1010  through which the filler passes in order to be conveyed into the mixing chamber  101 . Positioned immediately below the variably openable port  1010  is a conveyor belt  908  endlessly rotatably covering a conveyor  904  positioned to convey the filler from the hopper  901  to the mixing chamber opening  101 . The conveyor belt  908  is operated by a motor controlled by the operating system  301 . 
     Upon inputting of the ingredients for a batch of slurry into the operating system  301 , and upon completion of inputting water in the mixing chamber  101 , and upon completion of inputting the cementitious powder into the mixing chamber  101 , the operating system  301  again sets the tare weight to zero, indicting no amount of the next ingredient, in this case the filler, has been added to the mixing chamber  101 . Then, the operating system signals the hydraulic valves to operate the motor for the conveyor belt  908  to start. The filler passes through the variably openable port  1010 , falls upon the conveyor belt  908  and is carried on the conveyor belt  908  until it infalls into the mixing chamber  101 . As with the water, the operating system  301  weighs the input amount of filler in real time using the scales  401 . As with the water, at first the rate of input of the filler is at a high rate of speed (here again identified as an arbitrary Y pounds per minute) until the weight of the filler in the mixing chamber  101  reaches a pre-set threshold. At that time, the operating system  301  signals the motor to slow the conveyor belt  908  such that the rate of input of the aggregate is slowed to arbitrary rate Z, in which Y&gt;&gt;Z. As with the water input, the operating system  301  software is configured to allow for a known amount of filler which has fallen from the conveyor belt  908  into the mixing chamber  101  but not yet landed in the mixing chamber  101  so as to determine an accurate time at which to stop all inflow into the mixing chamber  101  and to ensure that a highly accurate amount of filler is loaded into the mixing chamber  101 . 
     During the process of adding the filler to the mixing chamber  101 , the operating system  301  directs the hydraulic valves to control the movement of the mixing blades  107 . As with the loading of cementitious binder, the loading of filler into the hopper  901  may be performed by workers placing bulk or bagged filler into the hopper  901 . 
       FIG. 6  depicts the input of filler into the mixing chamber  101  as described for the cementitious powder. Further,  FIG. 6  depicts the input times between time A″ and time F″. In the same manner as the weighing of water input and cementitious powder, the operating system  301  weighs and records the amount of filler inputted into the mixing chamber  101  during a pause after time F″. 
     Referring to  FIG. 3  and  FIG. 6 , it is noted that during each stage of input of each ingredient, the operating system  301  provides signals to the hydraulic valves to control the motor driving the mixing blades  107  to turn to mix the ingredients. The rate of rotation for the mixing blades  107  is either predetermined or, if desired, may be input into the operating system  301  by the operator by any known method. Depending upon need at the worksite and the required characteristics of the cementitious slurry to be poured, the mixing blades  107  may operate at any desired speed. 
     Each of the storage containers for the slurry ingredients, i.e. the tank  103 , cementitious powder bin  701  or filler hopper  901 , are configured on the steel beam, flatbed trailer  100  to allow the addition of additional ingredients to be stored for use. As such, during the mixing of a batch of cementitious slurry, as or after water is conveyed from the tank  104  to the mixing chamber  101 , additional water may be pumped to the tank  104  from an external source. Likewise, as or after cementitious powder is conveyed from the bin  701  to the mixing chamber  101 , additional cementitious powder may be added by workers loading bags of cementitious powder from bags or bulk loaded through the top of the bin  701 . Similarly, workers may add additional reserves of filler into the hopper  901  as or after the conveyance of filler from the hopper  901  to the mixing chamber  101 . By this, the invention is enabled, in part, to allow for continual batch processing. 
     The mixing blades continually run while the ingredients are delivered into the mixing chamber  101 . After all ingredients have been delivered, weighed and recorded, the mixing blades  107  in the mixing chamber  101  mix the ingredients at a faster rotation for the predetermined time. A typical mixing time is about 20 seconds, but any suitable time may be used. 
     Referring again to  FIG. 3 , upon completion of each batch mixed in the mixing chamber  101 , some portion of the batch is removed using the mixing blades  107  from the mixing chamber  101  through a port  310  on the side of the mixing chamber  101 . As described above, a portion of the batch is retained in the mixing chamber  101  to aid mixing of the following batch. The portion of the batch removed from the mixing chamber  101  is poured into the wet hopper  305 . A progressive cavity pump  306  located beneath the holding chamber  305  operates the flow of slurry from the holding chamber  305  through the hose used to deliver the final slurry product to the desired location. 
     In determining the amount of slurry to be removed from the mixing chamber  101  to the holding chamber  305 , the operating system uses the scales  401  to weigh the amount of slurry remaining in the mixing chamber  101 . When the pre-set amount of slurry has been removed to the holding chamber  305 , the operating system  301  closes the port on the side of the mixing chamber, stopping removal of slurry. The next batch of slurry may then be prepared following the protocol above. 
     The holding chamber  305  is also placed on a scale (not depicted) to measure its weight in real time. This scale in connected through wiring to the operating system. The operating system  301  will not allow the mixing chamber to dump slurry into the holding chamber  305  until the progressive cavity pump has pumped enough slurry out of the holding chamber  305  to allow enough room for the slurry to be dumped from the mixing chamber  101 . 
     Referring to  FIG. 12 , each of the steps above describing the production of a batch of slurry is set forth in a system flowchart. 
     The operating system  301  stores all information regarding the batch made, including the weight of each ingredient and mixing time in permanent storage. Stored data is maintained in the operating system  301  or can be transmitted or downloaded as needed. For example, and without limitation, a record of each batch for a project can be saved to removable storage. Critically, given the correspondence between ingredients ratios, mixing times and strength or other qualities of the poured slurry, the downloaded information creates a permanent record of the product characteristics of the batches. In the event a problem arises with the as-poured product, the data constitute a permanent quality assurance record suitable to support a warranty on the batches produced. 
     Also, a remote control can be used to remotely transmit a signal to the progressive cavity pump to stop the pump in the middle or end of an application and/or installation of a batch of slurry. 
     In addition to providing information about an individual batch, the data storage capabilities of the operating system allow management oversight at each project worksite. In addition to details of each batch of slurry produced during the workday, extractable and/or storable data includes the times during the day during which the apparatus was used, notification if the system was down or unused for any amount of time during a work day, when each batch was completed during the work day, the total amount of each ingredient, in pounds, bags, gallons or otherwise, used during a day. Other operation data obtained, stored and transmitted can include information concerning power consumption of the apparatus, such as the RPM of the engine providing power to the apparatus or the total amount of product produced by the apparatus each day. 
     By the invention, full control of all aspects of slurry production is established and maintained. Further, by the invention, a permanent, distributable quality assurance record of all production parameters is created and maintained.