Patent Publication Number: US-9849433-B2

Title: Elastomeric hydrogen reactor with clog-less filter

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
     This application is a Continuation of International Patent Application No. PCT/US2015/025652, filed Apr. 14, 2015, which claims full priority to Provisional Patent Application 61/979,951 filed Apr. 15, 2014, Provisional Patent Application 61/983,947 filed Apr. 24, 2014, and Provisional Patent Application 62/030,551, filed Jul. 29, 2014, the disclosures of which are incorporated by reference in their entirety. 
    
    
     FIELD OF THE DISCLOSURE 
     This disclosure relates to portable reactors which produce hydrogen. 
     BACKGROUND 
     With the increased use of mobile electronic devices, including, but not limited to, smart phones, laptop computers, and tablet computers, demand for portable power systems has increased. A popular solution is the use of rechargeable batteries, such as lithium-ion or lithium polymer batteries. For many mobile electronic devices, rechargeable batteries, even when replaceable by a user, are left in the device during use and charging of the battery. 
     Despite advances in battery designs leading to reduced size and increased capacity, rechargeable batteries impose a number of restrictions on users. First, battery capacity is often only enough to provide for a few hours of active use for many mobile electronic devices. For example, many laptop computers include batteries sufficient for around 5 hours of use, and many smartphones include batteries sufficient for approximately a full day&#39;s use. Second, rechargeable batteries must be recharged, which generally requires multiple hours to fully recharge a battery. The combined need to have an appropriate charging device on hand, access to an electrical outlet for the charging device, and adequate time to leave the mobile device attached to the charger for charging, imposes a significant inconvenience on users. Although some devices feature user-replaceable rechargeable batteries, and in theory a user might have an extra charged battery on hand, in practice users rarely find this to be a convenient solution. 
     Fuel cell technologies have advanced, in terms of size, reliability, and cost, to where fuel cell based power systems can replace or supplement conventional rechargeable battery based solutions. One advantage of fuel cell systems is increased energy density over rechargeable battery technologies. For example, a hydrogen fuel based fuel cell system, including the weight of hydrogen fuel, a storage canister for the fuel, a fuel cell stack, and a “balance of plant” for a fuel cell subsystem, can offer approximately a 1-fold increase in energy density over a lithium-based battery solution. As a result, in comparison to battery-based counterparts, fuel cell based power allows for lighter designs and/or greater run time. 
     However, fuel cell based power imposes a significant requirement: ensuring there is adequate fuel on hand. The fuel is volatile, and often compressed at a significant pressure, meaning that appropriate storage must be provided for the fuel. For example, the use of cartridges for storing compressed hydrogen is known in the art, and provides a safe and reliable mechanism for supplying fuel to fuel cell powered devices. However, a convenient mechanism for controlled distribution and reuse of such cartridges is required in order to achieve successful commercial application of fuel cell power technologies. 
     BRIEF DESCRIPTION 
     The file of this patent or application contains at least one drawing/photograph executed in color. Copies of this patent or patent application publication with color drawing(s)/photograph(s) will be provided by the Office upon request and payment of the necessary fee. 
     Disclosed herein are aspects of a reactor having a fuel core within a containment vessel and the vessel having an exit nozzle; around the vessel and to supply compressive force are at least one elastomeric winding; and, a water line to deliver fluid to the core and to produce hydrogen gas. 
     Disclosed herein are aspects of a hydrogen production cartridge and reactor having a body enclosing a fuel core within a containment vessel and the vessel having an exit nozzle; around the vessel and to supply compressive force are at least one elastomeric winding; a water line to deliver fluid to the core; an expanded PTFE tube having a sealed end and an open end fluidly connected to a valve; and, wherein fluid delivered to the core via the water line urges the core to produce hydrogen via a reaction and the hydrogen permeates the e-PTFE tube and is delivered to the valve. Becasue the e-PTFE tube is permeable to hydrogen it is in fluid connection with a hydrogen supply if it is exposed to such hydrogen. In some instances the cartridge reactor includes a desiccant placed within the e-PTFE tube. In some instances the cartridge reactor includes a hydrogen filter placed around the e-PTFE tube. In some instances the cartridge reactor includes NaOH within the body wherein the NaOH at least one of reduces the rate of reaction and reduces pressure. 
     Disclosed herein are aspects of a clog-less hydrogen filter unit having an envelope containing a separator material with a tube guide formed therein wherein an expanded PTFE tube, filled with a desiccant and having a sealed end and an open end is contained in the guide; and the e-PTFE tube is fluidly connected to a valve. In some instance desiccant material is also around the e-PTFE tube. In the clog-less filter the separator may either be at least in partial contact with the e-PTFE tube or not in contact with the e-PTFE tube. 
     Disclosed herein are aspects of a method of producing hydrogen from a cartridge with an elastomeric reactor and clog-less filter, the method includes placing a fuel pellet in a containment vessel which is wound with an elastomeric winding, the wound combination placed inside a wrapping in a sealed fuel cartridge, then adding at least water to the fuel pellet within the containment; whereby hydrogen gas and other products are produced from the water and fuel pellet reaction. 
     Disclosed herein are aspects of a method of producing hydrogen from a cartridge with an elastomeric reactor and clog-less filter, the method includes placing a fuel pellet in a containment vessel which is wound with an elastomeric winding, the wound combination placed inside a wrapping in a sealed fuel cartridge, then adding at least water to the fuel pellet within the containment; whereby hydrogen gas and other products are produced from the water and fuel pellet reaction and the gases produced are filtered with a clog-less filter to yield substantially pure hydrogen. In some instances the clog-less filter is connected to an e-PTFE tube containing at least desiccant; and output. In some instances additional desiccant material is placed around and in contact with the e-PTFE tube. 
     In the above methods the addition of a clog-less filter provides for less clogging and provides about twice the run time of a traditional filter system. 
     In the above methods the addition of a clog-less filter provides for less clogging and provides more than twice the run time of a traditional filter system. 
     In the above methods the addition of a clog-less filter provides for less clogging and provides more than two and ½ times the run time of a traditional filter system. 
    
    
     
       DRAWINGS 
         FIG. 1  illustrates aspects of an elastomeric hydrogen reactor device and system; 
         FIG. 2  illustrates aspects of an elastomeric hydrogen reactor; 
         FIG. 3  illustrates some components of an unassembled elastomeric hydrogen reactor; 
         FIG. 4  illustrates an assembled elastomeric hydrogen reactor; 
         FIG. 5A  illustrates the Hydrogen output pathway for fluid communication with an elastomeric hydrogen reactor; 
         FIGS. 5B and 5C  are assembly drawing showing aspects of hydrogen filter encasements and placement; 
         FIGS. 5D and 5E  show charts of operational time which corresponds to output of H 2  of an elastomeric reactor with and without a clog-less filter arrangement; 
         FIG. 6  illustrates aspects of the assembly of the elastomeric hydrogen reactor; 
         FIG. 7A-D  illustrate aspects of the cartridge assembly with an adapter and some aspects of mechanical/electrical portions of some fluid management; and, 
         FIG. 8  illustrates an assembly of the elastomeric hydrogen reactor with an adapter. 
     
    
    
     All callouts, figures, descriptions in the attached figures are hereby incorporated by this reference as if fully set forth herein. 
     It should be appreciated that, for simplicity and clarity of illustration, elements shown in the figures have not necessarily been drawn to scale. For example, the dimensions of some of the elements are exaggerated, relative to each other, for clarity. Further, where considered appropriate, reference numerals have been repeated among the Figures to indicate corresponding elements. While the specification concludes with claims defining the features of the present disclosure that are regarded as novel, it is believed that the present disclosure&#39;s teachings will be better understood from a consideration of the following description in conjunction with the figures and appendix in which like reference numerals are carried forward. 
       FIG. 1-8  disclose aspects of exemplary implementations of a reactor and cartridge for supplying hydrogen gas. The cartridge may be a unitary system or a hybrid. The cartridge  10  has a bottom  11  affixed to a lower body  12  which is generally hollow. The bottom  11  closes off a first end of the generally hollow lower body  12 . An upper body  13  is affixed to the second end of the lower body  12 . The lower body  12 , bottom and upper body are bonded or sonically welded to seal them and prevent hydrogen leakage (via seals—see  FIG. 6 . An adapter  14  (which may be reusable) mates with the upper body  13  (via seals—see  FIG. 6, 7A-7D ). Hydrogen produced by the reactor within the cartridge is fed to a pressure valve  15  formed on the adapter  14 . The valve is in fluid communication with gaseous hydrogen produced via a reactor  20  within the cartridge  10 . Via the fluid communication hydrogen is supplied for use as a fuel source. Other balance of plant “BOP” components include, but are not limited to, a fuel pellet or core  22 , elastomeric winding(s)  25  affixed around a containment “COT”  27  which surrounds the core  22 . An exit nozzle  28  is within the COT  27 . A woven bag or wrapping  29  such as nylon is placed around the reactor to limited exposure of the hydrogen collection means to waste products. A water or fluid input line  30  connection  55  for water or other fluid to pass into the reactor  20  to the core  22  is in fluid connection to a fluid reservoir  60 . Water or other fluid reservoir(s)  60 . A water line  100  provides fluid or water to the reactor. The water line  100  may be connected to a wicking  101  region to control water or fluid flow. 
     An expanded PTFE (e-PTFE) tube unit  200  is the fluid communication means to deliver hydrogen produced by the reactor to the valve  15 . The e-PTFE tube unit  200  is sealed at a distal end  201  and open at its proximal end  202 . PTFE is permeable to hydrogen. The proximal end  202  is connected to a connection fitting  203 . Within the e-PTFE tube  210  is a desiccant material  204  through which hydrogen gas passes as it is transported from the reactor to the valve  15 . The e-PTFE tube  210  may also be wrapped in a Hydrogen filter material  206  which is permeable to hydrogen and may filter out other non-hydrogen fluids.  FIGS. 5B and 5C  are assembly views of several clog-less hydrogen filter exemplars for the output portion of the elastomeric hydrogen reactor. Those of ordinary skill in the art will recognize that this clog-less filter arrangement has application to an output of hydrogen wherein non-hydrogen gas or vapor substances need to be removed prior to supply the hydrogen gas to a fuel cell. 
     We have determined that the performance of the elastomeric reactor can be increased by preventing filter clogging during use.  FIG. 5D  shows a chart of the run time of an elastomeric hydrogen reactor with a traditional filter surrounding the e-PTFE hydrogen output as shown in  FIG. 5A . The filter material  206  will become clogged thereby reducing the output and eventually shutting down the reactor due to increased internal pressure build up. The run time is under  6000  seconds and both the output pressure  270  of hydrogen gas and the water flow  280  drop off steeply as time runs out. Because the elastomeric reactor is producing hydrogen at 6000 seconds the inability to output filtered hydrogen causes a pressure build up which in turn could rupture the cartridge. To prevent rupture the hydrogen gas may be vented and/or the water pump will be shut down. In both instances hydrogen is lost and fuel wasted. A reactor that shuts down prematurely is less efficient and more costly. Conversely,  FIG. 5E  shows a chart of the run time of an elastomeric hydrogen reactor with a clog-less filter  207  surrounding the e-PTFE tube  210 . The clog-less filters  207  is formed via capturing a separator in an envelope having a first side  208  and a second side  208 ′ which is then sealed  216  at the bottom and the side edges. A porous “L” shaped separator  220  which may be a mesh structure is connected to the e-PTFE tube  210 . Material that may be used for the separator include but are not limited to polyethylene, poly propylene, woven materials, nonwoven materials, battery separators, PTFE membranes, Tyvek type material, fabrics and other flexible material which are non-reactive to hydrogen gas. The length “l”  222  of the mesh may be varied and the height  224  “h” of the mesh may also be varied to form the alternate exemplary shown in  FIG. 5B  “W-Z”. The shaped separator may also be rectangular  220 ′. In some instances the e-PTFE tube is placed in a tube guide  230  formed inbetween the first side  208  and a second side  208 ′ and the separator  220  wraps partially around the e-PTFE tube  210  (see “W”) in other instances the separator  220  wraps partially around the e-PTFE tube  210  (see “X”). In other instances the tube guide is formed by circling the e-PTFE tube with the clog-less filter  207  (see “Z”). 
     The clog-less filter  207  is preferably formed of a cellulose based material, the cellulose ha the properties of being porous enough to allow hydrogen to easily pass through and absorbent enough to scavenge some of the water vapour produced during the reaction without closing off the flow of hydrogen gas to the e-PTFE tube  210 . The envelope  207  is positioned in the cartridge body to provide maximum surface area for hydrogen collection. By utilizing this type of extended filter surface area can be increased by a factor of 10-15 times or more. By separating the sides  208  and  208 ″ of the envelope clogging, primarily due to water vapour is reduced. The e-PTFE tube  210  is sealed  232  to the envelope  207  at or near the connection fitting  203 . The envelope is preferably loosely packaged within the cartridge wherein most of the surfaces are exposed to the gaseous environment in the cartridge as opposed to being in physical contact with themselves. It is preferred that the filter material not wrap or fold on itself. 
     During assembly, the separator  220 / 220 ′ is inserted in the filter envelope  207  having two generally planar sides  208 / 208 ′ open at the top and sealed  216  around the bottom and sides forming a cavity to accept the separator  220 / 220 ′. After insertion of the separator the envelope is sealed  217  forming a tube guide  230  wherein the e-PTFE output tube  200  is later inserted. Prior to inserting the e-PTFE tube, or commensurate with inserting the e-PTFE tube  210  into a tube guide  230  a quantity of desiccant material  235  which should be contiguous to the e-PTFE tube  210  is added. The region of the envelope that forms the around the outside of the tube guide may be referred to as the tube region  240 . 
     The separator may be shaped in the tube guide  230  to surround the tube  251 , or to partially surround the tube  253  in both cases the separator is against at least a portion of the e-PTFE tube  210 . When utilizing a mesh like separator the mesh can also support at least some of the added desiccant material  235 . In other cases the separator may end prior to the tube guide  255 . Finally, the separator—envelope combination may have the separator fill the entire envelope and the tube region  240  is then rolled in on itself to form a tube guide  230 ′ wherein the separator  220 / 220 ′ is separated from the e-PTFE tube  210  by at least a layer of envelop  FIG. 5E  illustrates the second run time of an elastomeric reactor which has a clog-less filter  207 . The run time is over 16000 seconds and both the output pressure  270  of hydrogen gas and the water flow  280  are substantially steady as time runs. Because of the longer run time all or at least more of the fuel is utilized, pressure build up is reduced, the chance of a critical failure such as a burst is reduced and the reactor will run longer and provide more hydrogen from the same amount of fuel as a traditional reactor would. 
       FIG. 6  illustrates an assembly view of the elastomeric reactor in housing for use in a cartridge. A fluid container or bag  300  in some exemplary implementations is filled with De-ionized water and a Catalyst mix. The upper body  13  provides one or more sealed valves  310  fluidly connected to the e-PTFE tube for delivering hydrogen to the adapter  14 . The valves  310  are protected by a sealed foil-like member  350 . 
     Reactor Design and Aspects of Features within the Reactor and Cartridge. 
     1. Use of Elastomeric Winding  25 . 
     a. Description: Elastomers are wound around the fuel pellet  22  and its wrapping COT  27 . 
     b. Actions, method of action: 
     i. The elastomeric winding(s) force reaction products from reaction site and exposes fresh reactants 
     ii. The elastomeric winding(s) reduce pooling of products and reaction fluid (pooling causes poor performance, low utilization, requires excessive water, sluggish H2 control, uncontrollable H2 after shut down) 
     iii. The elastomeric winding(s) reduce compression set which is inherent in other designs such as the stretched silicon bag and others 
     iv. The elastomeric winding(s) are adapted to apply variable force if desired (i.e. more force in back of pellet than in front)—stretched bag designs cannot! Such windings need not be a unitary piece. Several windings of different stretch and force properties may be combined. Variations in thickness, length and elasticity may be applied to shape or control the compression. Elastic and rubber-like materials are used. 
     v. The elastomeric winding(s) provide compression until pellet  22  is fully dehydrogenated. Conversely a traditional bagged or compression tube will stop compressing once it reaches its starting diameter 
     vi. The elastomeric winding(s) provide assembly advantages via a winding machine which winds after the core  22  is placed in the COT  27 . 
     2. Use of Reaction Products to Dehumidify  112  Stream 
     a. As disclosed in  FIGS. 1-8  and appendices A and B the reaction products can, in some exemplary implementations, be routed to form at least a partial wall between the reacting pellet and the H2 out port. The reaction products are hydroscopic and will tend to dry out the H2 stream provided the H2 is forced to pass through them. Accordingly, this method of flow reduces the amount of desiccant required thereby reducing volume and/or costs. 
     3. Exit Nozzle  28  Dictate Characteristics of Reaction Products 
     a. Description: Size, design, and location of the exit nozzle can be used to customize the characteristics of the reaction products. Smaller nozzles and/or nozzle placement where it is more difficult for reaction products to flow toward will increase residence time in the reactor and result in increased fuel utilization, lower water ratios, much dryer products, less unreacted material and thus quicker H2 flow response to water pump shut down. Larger nozzles and/or nozzle placement at a location where products can find the nozzle quickly will result in a more liquid product and with less initial volume per unit mass. 
     b. Benefits 
     i. Nozzle location and size allows the reactor designer to optimize the reactor design and containment of the products 
     ii. Can result in improved characteristics both performance and energy density 
     4. COT  27  is a Thin Latex or Rubber-Like Material 
     a. Description: Natural rubber or latex material can be used as either a wrap around the pellet. 
     b. Benefits 
     i. Such COT  27  material is thin and durable and results in more energy dense systems vs thicker walled materials. 
     ii. Easier to assemble when using preformed finger cots (since one end is already sealed) 
     iii. Significantly less expensive than silicon rubber 
     iv. Reduced compression set 
     5. Use of a Woven Bag  29  to Protect Ports and  112  Filter  206   
     a. Description: a thin woven nylon bag loosely encloses the reactor. When reaction products are expelled from the reactor, the majority of the products clump inside the nylon bag and are kept away from the H2 filter and ports to help prevent clogging. Even if products expand to the point of contacting the ports or filter they typically will not fully surround then due to restriction by the bag material. 
     b. Benefits: 
     i. Reduced clogging of the ports—able to put more fuel in the cartridge without it clogging 
     ii. Eliminates the need for other filtration material 
     6. Use of Hydrophobic,  112  Permeable Membrane  206  to Protect the—ePTFE H2 Filter. 
     a. Description: A membrane material with adhesive on one side and which is both hydrophobic and permeable to H2 is one of wrapped around the e-PTFE H2 filter and connected to the e-PTFE H2 filter with the envelope loosely placed inside the cartridge. 
     b. Benefits: 
     i. The membrane (which is found on some types of Band-Aids) helps prevent the H2 filter from clogging. 
     ii. Fluid beads off the surface and keeps the H2 filter open and exposed to H2 gas in the cartridge. 
     iii. Also provides a secondary physical barrier to products 
     Fuel/Chemistry 
     1. Use of hybrid chemistry (catalyst plus acid) as fluid 
     a. Description: It was found that the use of catalyst alone or acid alone resulted in variable performance each with particular draw backs. A system was designed where both could be used in the same system but added in different ways resulting in ideal reaction characteristics 
     b. Benefits 
     i. Catalyst alone resulted in: Relatively high activity but because catalyst level is variable through reaction due to catalyst sites being blocked and then exposed, H2 variability was high. In addition when sites were blocked unreacted material would move out of the reactor too soon and result in continuous H2 generation outside the reactor resulting in slow response to water pump shut down. 
     ii. Acid alone results in: More stable H2 flow but less active overall and more water was required to carry out the reaction so lower energy density. 
     iii. Combination of the two: 
     (a) Dehydrogenation activity much higher than either by itself 
     (b) Requirement of significantly less water to generate the same amount of H2 
     (c) Quicker start up than either on its own (30 seconds) 
     (d) Quicker shutdown when pump shuts off than either on their own 
     (e) More stable H2 flow than either by itself 
     2. Use of NaOH or other caustic to neutralize reactants after leaving the reactor to minimize residual H2 production and allow for passage of the regulatory testing which calls for no more than 16 mg/hr of H2 to be vented upon shut down. 
     a. Description: NaOH or other neutralizing material can be applied to the reaction by products in different forms and locations to 1) increase the pH of the reaction by-products and 2) displace the catalyst. Both avenues of neutralization support quicker reactor shutdown. 
     i. Method 1) in some instances NaOH or other neutralizing material pellets or powder are applied outside the reactor and near the exit. When products which are partially liquid exit, the residual liquid dissolves the solid NaOH, which increases the pH and displaces the catalyst and expedites reaction shutdown. 
     ii. Method 2) in some instances NaOH or other neutralizing material is pressed as a separate part of the pellet or core  22 . For instance NaOH would be loaded first into a press, then pressed, the ram removed from the die, then the fuel material loaded, then the fuel material would be pressed on top of the NaOH material. This would form a two phase pellet with fuel on one end and neutralization material on the other end. A second discrete pellet could also be pressed and added to the reactor separately. In this application water would be applied to the fuel side, then reaction products would be formed and travel to the neutralization side where the residual fluid in the by-products would dissolve some of the NaOH and neutralize the reaction. 
     iii. Method 3) in some instances the NaOH or other neutralizing material is encapsulated. In this instance the NaOH would be encapsulated with a time released material that would only allow the NaOH to be exposed after a specific time delay after coming in contact with water or other activating agent. Specifically in our reactor, the encapsulated NaOH material would be blended and mixed with the fuel blend and pressed together homogenously. When water is dispensed onto the fuel pellet the encapsulated material is activated and after a certain time delay the NaOH would be exposed. The time delay would be engineered such that the NaOH would not be exposed prior to leaving the reactor. Therefore if it took 5 minutes on average for fuel by-products to leave the reactor after first being exposed to water, then the time delay would be set for 5 min or longer. This allows the NaOH to be added directly to the reactor without adversely affecting the primary H2 generating reaction until after leaving the chamber. 
     b. Benefits: 
     i. Selectively providing NaOH or other neutralizing material is useful in maintaining desired pressure controls. 
     ii. Adds another safety factor to the cartridge. For instance if the water bag breaks for some reason, the NaOH can neutralize the water prior to entering the reactor, thus, preventing or limit a runaway reaction. 
     iii. NaOH is hydroscopic and can help prevent humidity getting to the fuel pellet prematurely. 
     3. Addition of 12% HCL to the water 
     a. Description: in some instances about 12% HCL is added to the water to lower the freezing point to below 20 C. 
     Fuel Examples: TestS showed that a balance of purity and percentages of components achieve a fuel with a high efficiency controlled release and with a moderate amount of water. Aspects of such a mix include a reactor chemical mix, chemical type and percentage as follows: 70% Sodium Borohydride “NaBH 4 ” (SBH), 30% Oxalic Acid (in powder form) Liquid/powder etc. The liquid portion is made up of 86% distilled or deionized water, 12% HCL, and 2% Cobalt chloride hexahydrate “CoCl 2 .6H 2 O”. The HCL is currently added to the water in liquid form The CoCl2 comes in pellet form and dissolved readily in a matter of seconds with moderate stirring/mixing. 
     In the above mixture the NaBH 4  should be at least 50% pure. Oxalic acid should be at least 10% pure, The CoCl 2 .6H 2 O should be at least 1% pure. In the above mixture it is preferred that the NaBH 4  should be greater than 50% pure. Oxalic acid should be greater than 10% pure, The CoCl 2 .6H 2 O should greater than 1% pure. In the above mixture it is more preferred that the NaBH 4  should be at least about 90% pure. Oxalic acid should be at least about 50% pure, The CoCl 2 .6H 2 O should at least about 20% pure. 
     In the above mixture it is most that NaBH4 should be at least about 98% pure. Oxalic acid should be at least about 99.6% pure, The CoCl 2 .6H 2 O should be at least about 98% pure. The above mixture has been shown to yield a water to SBH molar ratio of about 3.7:1. The ratio is significant in that less water equates to less mass in the cartridge form. Other formulations which we have tested show that SBH and acid alone result in molar ratios of SBH to acid in the range of above 5:1. The reactor tested containing about 23.9 g total weight of the above mixture produced about 27 L of H 2 . 
     Fuel Mix Process Requirements and Environmental Controls 
     During blending operation fuel mix should be under inert conditions. When powder components are exposed, they should be kept in an inert environment or at a minimum in an environment with RH&lt;10%. Powders should only be mixed for the minimum amount of time (currently 5 min) and without any media or any component that applies friction to the powders. Extended processing time or any process or blending aids could result in a more active fuel mixture that would be increasing sensitive to air and moisture. Process controls should be in place to ensure these situations are avoided. As with many powders, process controls should be in place to avoid dust explosions. Static controls should be in place as sparks could initiate the powder materials individual or while in a mixture. All equipment and tools that come into contact with the fuel mix should be thoroughly dry at all times. 
       FIGS. 7A through 8  illustrated aspects of the cartridge assembly with an adapter  14  and some aspects of mechanical/electrical portions of some fluid management.  FIG. 8  also illustrates the connection of a reusable adapter  14  over an upper and lower body  12 / 13  combination. Within the adapter  14  is a motor  401 , pump and pump head  402  to drive a peristaltic pump  420 . Also within the adapter is a poppet pinch valve  410  and pressure relief valve  15 . 
     Those of ordinary skill in the art will appreciate that the above disclosure, in which particular methods or techniques may be described in relation to particular items illustrated in  FIG. 1 , is merely for the purpose of illustration, and that it is within the ordinary skills of the art to alternatively perform such methods or techniques with other items illustrated in  FIG. 1 . Such alternatives merely illustrate the ease with which, particularly where systems can exchange data with each other, programmed functionality can be moved and/or distributed among a plurality of programmable processors. 
     It is to be understood that any feature described in relation to any one aspect may be used alone, or in combination with other features described, and may also be used in combination with one or more features of any other of the disclosed aspects, or any combination of any other of the disclosed aspects. Furthermore, equivalents and modifications not described above may also be employed without departing from the scope of the disclosed subject matter. 
     The many features and advantages of the disclosed subject matter are apparent from the detailed specification, and thus, it is intended by the appended claims to cover all such features and advantages of the disclosed subject matter which fall within the true spirit and scope of the disclosed subject matter. Further, since numerous modifications and variations will readily occur to those skilled in the art, it is not desired to limit the disclosed subject matter to the exact construction and operation illustrated and described, and accordingly, all suitable modifications and equivalents may be resorted to, falling within the scope of the disclosed subject matter. 
     Further, each of the various elements of the disclosure and claims may also be achieved in a variety of manners. This disclosure should be understood to encompass each such variation, be it a variation of an implementation of any apparatus implementations, a method or process implementations, or even merely a variation of any element of these. 
     Particularly, it should be understood that as the disclosure relates to elements of the disclosure, the words for each element may be expressed by equivalent apparatus terms or method terms—even if only the function or result is the same. 
     Such equivalent, broader, or even more generic terms should be considered to be encompassed in the description of each element or action. Such terms can be substituted where desired to make explicit the implicitly broad coverage to which this disclosure is entitled. 
     It should be understood that all actions may be expressed as a means for taking that action or as an element which causes that action. 
     Similarly, each physical element, disclosed, should be understood to encompass a disclosure of the action which that physical element facilitates. 
     To the extent that insubstantial substitutes are made, to the extent that the applicant did not in fact draft any claim so as to literally encompass any particular exemplary implementations, and to the extent otherwise applicable, the applicant should not be understood to have in any way intended to or actually relinquished such coverage as the applicant simply may not have been able to anticipate all eventualities; one skilled in the art, should not be reasonably expected to have drafted a claim that would have literally encompassed such alternative exemplary implementations. 
     Further, the use of the transitional phrase “comprising” is used to maintain the “open-end” claims herein, according to traditional claim interpretation. Thus, unless the context requires otherwise, it should be understood that the term “comprise” or variations such as “comprises” or “comprising”, are intended to imply the inclusion of a stated element or step or group of elements or steps but not the exclusion of any other element or step or group of elements or steps. 
     Such terms should be interpreted in their most expansive forms so as to afford the applicant the broadest coverage legally permissible.