Means and methods for selective shelf temperature control
The system addresses frost buildup on freeze-drying shelves by controlling heat exchange fluid flow through a manifold with a stopper mechanism, improving efficiency and reducing maintenance costs.
Patent Information
- Application Number
- CA3093834
- Authority / Receiving Office
- CA · CA
- Patent Type
- Patents
- Current Assignee / Owner
- Priority Date
- 2018-03-14
- Filing Date
- 2019-03-13
- Publication Date
- 2024-10-08
- Estimated Expiration
- Not applicable · inactive patent
AI Technical Summary
Existing freeze-drying systems face issues with frost buildup on shelves during the loading process, which affects heat transfer efficiency and can increase the effort required for automatic loading systems, while current solutions with individual valves for each shelf increase manufacturing and maintenance costs and points of failure.
A system with a fluid manifold and adjustable stopper mechanism that controls heat exchange fluid flow to shelves individually, minimizing frost buildup by cooling 'just in time' and reducing exposure to ambient conditions.
Minimizes frost formation on shelves, enhances heat transfer efficiency, and reduces the mechanical stress on loading systems, while maintaining cost-effectiveness and reliability by minimizing chamber penetrations.
Abstract
Description
<DP=1>²Means and Methods for Selective Shelf Temperature Control²Related Applications ²
[0001] This application claims priority to U.S. Patent Application No. ²62 / 642,767, filed on ²March 14,2018.²Field of Invention²
[0002] The disclosure relates to temperature control of shelves.²BackEround ²
[0003] Freeze-drying (i.e. lyophilization or cryodesiccation) is a process for ²removing ²volatiles such as water or solvents from products. Freeze-drying has many ²applications such ²as preserving perishable materials, allowing for transport of certain ²materials, production of ²ceramics, production of products with short reconstitution times and ²acceptable potency ²levels, and the like. Freeze-drying is employed for a wide variety of ²materials, including, but ²not limited to food, pharmaceuticals and biological specimens.²
[0004] In a typical freeze-drying process, samples, or vials or containers ²containing a sample, ²are loaded onto temperature-controlled shelves within a chamber and are cooled ²to low ²temperature until solidified. The chamber is then subjected to reduced ²pressure and the shelf ²temperature is adjusted to enable removal of a frozen solvent via sublimation ²in a step ²referred to as "primary drying". When sublimation is complete, the shelf ²temperature is ²raised during a "secondary drying" step to remove any additional solvent bound ²to the solid ²product e.g. by adsorption. When sufficient solvent is removed, the process is ²concluded. If ²samples are contained in vials or containers, the vials or containers are ²sealed, typically under ²sub-ambient pressure of inert gas.²
[0005] Freeze-dryers generally contain a plurality of shelves onto which ²samples are loaded. ²The shelves may be cooled to below ambient temperature via flow of a heat ²exchange fluid ²through the shelves. Shelves may be cooled to temperatures for instance of ²from about 5 C ²to about -55 C or colder. Cooling of a plurality of shelves during a loading ²process in which ²the shelves are exposed to ambient conditions of a loading area may result in ²undesired frost ²buildup on some or all shelves. Frost will act as an insulator and prevent ²proper heat transfer ²to a product vial or container. In addition, frost build-up can increase the ²amount of effort ²required to push product vials or trays onto a shelf. Increased force needed ²to move product²1²Date Recue / Date Received 2023-07-19²<DP=2>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²onto shelves may adversely affect the performance of automatic loading ²systems. While ²there have been some designs that utilize valves for each shelf and fluid ²connection, these ²designs require a connection for each valve be extended through the pressure ²chamber in ²order to maintain process boundaries and cleanliness. Such methods increase ²the ²manufacturing cost and maintenance cost, while also add to the number of ²points of potential ²failure of the device. Desired are methods to cool shelves "just in time" ²before they are ²loaded, thereby reducing exposure time of a cold shelf to the atmosphere and ²minimizing the ²potential for frost buildup, while also doing so with fewer chamber ²penetrations.²Summary ²
[0006] Accordingly, disclosed is a system comprising a housing defining a ²chamber;²a plurality of horizontal shelves arranged vertically within the chamber, each ²shelf ²comprising an inlet, an outlet and a flow passageway disposed between the ²inlet and the ²outlet; a fluid manifold having a length and a width and in fluid ²communication with a ²respective flow passageway of each shelf; and an article comprising an element ²disposed ²within the manifold and adapted for adjustable lengthwise movement along the ²length of the ²manifold.²
[0007] Also disclosed is a method of controlling a shelf temperature in a ²system comprising a ²housing defining a chamber; a plurality of horizontal shelves arranged ²vertically within the ²chamber, each shelf containing a flow passageway, an inlet and an outlet; a ²fluid manifold ²having a length and a width and in fluid communication with each shelf; and an ²article ²comprising an element disposed within the manifold and adapted for adjustable ²lengthwise ²movement in the manifold; the method comprising adjustably moving the element ²lengthwise ²within the manifold.²
[0008] Also disclosed is a system comprising a fluid manifold having a length ²and a width ²and a plurality of inlet or outlet ports and an article comprising an element ²disposed within ²the manifold adapted for adjustable lengthwise movement within the manifold.²
[0009] Also disclosed is a method of controlling fluid flow through a fluid ²manifold, the ²manifold having a length and a width and a plurality of inlet or outlet ports, ²wherein an ²element is disposed within the manifold and adapted for adjustable lengthwise ²movement²2²<DP=3>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²within the manifold; the method comprising adjustably moving the element ²lengthwise within ²the manifold.²Brief Description of the Drawings ²
[0010] The disclosure described herein is illustrated by way of example and ²not by way of ²limitation in the accompanying figures. For simplicity and clarity of ²illustration, features ²illustrated in the figures are not necessarily drawn to scale. For example, ²the dimensions of ²some features may be exaggerated relative to other features for clarity. ²Further, where ²considered appropriate, reference labels have been repeated among the figures ²to indicate ²corresponding or analogous elements.²[00111 FIG. I shows a freeze-drying system according to disclosed embodiments.²[00121 FIG. 2 shows the freeze-drying system of FIG. 1 in another stage of ²operation ²in accordance with disclosed embodiments.²100131 FIG. 3 shows the freeze-drying system of FIG. 1 in another stage of ²operation ²in accordance with disclosed embodiments.²[00141 FIG. 4 shows the freeze-drying system of FIG. 1 in another stage of ²operation ²in accordance with disclosed embodiments.²Detailed Description ²
[0015] This disclosure, in one example, relates to systems and methods for ²minimizing ²undesired frost formation on cooled shelves during loading of a freeze-drying ²process.²
[0016] A freeze-drying process includes at least a freezing stage, a primary ²drying (i.e. ²sublimation) stage and a secondary drying (i.e. desorption) stage. During the ²freezing stage, ²a product is frozen and solvent crystals are formed in the product. During the ²primary drying ²stage, solvent is removed from the product by sublimation of free solvent by ²an increase in ²temperature and reduced pressure. During the secondary drying stage, the ²temperature is ²raised higher to remove bound solvent from the product. The solvent, or ²volatiles, in general ²comprise water.²
[0017] Chambers of freeze-dryers in general contain a plurality of shelves, ²which are adapted ²with a cavity, i.e. flow passageway, to pass through a heat exchange fluid for ²temperature²3²<DP=4>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²adjustment. Embodiments of the invention relate to systems and methods for ²control of shelf ²temperatures.²
[0018] FIG. 1 is a depiction of a freeze-drying system 100 according to an ²embodiment of the ²invention. The system contains a housing 101 defining a chamber 102 containing ²a plurality ²of horizontal, vertically arranged shelves 103. While only eleven shelves 103 ²are shown in ²the figure, it should be understood that more or less shelves 103 may be used. ²Each shelf ²103 contains a flow passageway 104, an inlet 105 and an outlet 106. The shelf ²inlet 105 and ²outlet 106 locations are shown for some of the shelves 103, but it should be ²understood that ²each shelf 103 will have an inlet 105 and an outlet 106 for a respective flow ²passageway 104 ²even though they are not explicitly shown here. Shelf inlets 105 and outlets ²106 may be ²aligned with each other as shown here, but need not be. The inlets 105 and ²outlets 106 may ²be at any location along the flow passageways 104 in fluid communication with ²each other ²and the flow passageways 104, respectively. For example, the 105 may be on an ²opposite ²site of the shelf 103 from inlet 106. The system contains an article 115 ²comprising an ²element having a rod 107 affixed with a stopper 108, a means 109 of moving the ²rod and ²stopper and a seal 110. The rod 107 affixed with the stopper 108 is disposed ²in a fluid ²manifold 111. The manifold 111 has ports 112, each associated and in fluid ²communication ²with a corresponding shelf 103 through tubes 113, which may also be any other ²type of ²piping of a suitable material and size to carry a heat exchange fluid. The ²stopper 108, as ²shown in FIG. 1, is in a fully retracted position. In this stopper 108 ²position, heat exchange ²fluid flow is allowed through only a top shelf 103 and an upper portion of ²manifold 111. The ²manifold 111 is in fluid communication with the shelves.²
[0019] FIG. 1 depicts the manifold 111 being connected through tubes 113 to ²outlets ²106, such that fluid flows from inlets 105 through the flow passageways 104 in ²the shelves ²103 to the outlets 106 and then to the manifold 111 exiting at 114. Not shown ²is a tube or ²fluid connection from heat transfer fluid pump 120 (discussed below) to inlets ²105. In an ²alternative embodiment, the manifold 111 may be connected through tubes 113 to ²inlets 105, ²such that fluid flows from 114 (reversing the 114 arrow), through the manifold ²111, through ²the tubes 113, through the inlets 105, through the flow passageways 104 to ²outlets 106, which ²would then flow back heat transfer fluid pump 120.²4²<DP=5>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²
[0020] FIG. 2 depicts the freeze-drying system 100, for example that shown in ²FIG. 1, ²according to an embodiment of the invention. In FIG. 2, the stopper 108 is in ²a partially ²inserted position. In this stopper position, flow of a heat exchange fluid is ²permitted through ²the top two shelves 103 and the manifold 111. Flow of a heat exchange fluid ²through the ²remaining shelves and the bottom portion of the manifold is blocked by the ²stopper 108.²
[0021] FIG. 3 depicts the freeze-drying system 100, for example that shown in ²FIGS. 1 and ²2, according to an embodiment of the invention. In FIG. 3, the stopper 108 is ²in a partially ²inserted position, which is more fully inserted than as shown in FIG. 2. In ²this stopper ²position, flow of a heat exchange fluid is permitted through all shelves 103 ²and the manifold ²111 except the bottom shelf 103, shelf N. Flow of a heat exchange fluid ²through the bottom ²shelf 103 and the bottom portion of the manifold is blocked by the stopper ²108.²
[0022] FIG. 4 depicts the freeze-drying system 100, for example that shown in ²FIGS. 1 - 3, ²according to an embodiment of the invention. In FIG. 4, the stopper 108 is in ²a fully inserted ²position. In this stopper 108 position, flow of a heat exchange fluid is ²permitted through all ²shelves 103 and the entirety of the flow portion of the manifold 111.²
[0023] The freeze-drying system 100 of FIGS. 1-4 may have additional elements ²in addition ²to a plurality of shelves 103 and a chamber 102, for instance a refrigeration ²unit, a vacuum ²system, fluid lines or hoses, gas lines, etc. The chamber may be accessible ²via a door or ²doors which may seal the chamber and allow it to sustain vacuum conditions. ²The chamber ²may comprise one or more inlets and / or outlets to facilitate gas flow, liquid ²flow or to ²connect to a vacuum source.²
[0024] In some embodiments, the freeze-drying system may be adapted to perform ²steam ²sterilization cycles. The freeze-drying system may be adapted to perform clean-²in-place ²(CIP) and / or a steam sterilization (SIP) cycle after each use to ensure a ²product is not ²contaminated by a previously lyophilized material. For example, in certain ²embodiments, the ²freeze-drying system may include one or more inlets for introducing cleaning ²media and / or ²steam into a chamber. The chamber may contain a drain to remove excess water.²
[0025] The chamber may include one or more orifices for connecting to various ²valves and ²gauges. For instance, a gauge, such as a Pirani gauge, may be coupled to a ²chamber to ²measure the pressure within the chamber.²<DP=6>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²
[0026] In some embodiments, the shelves may be thermally coupled to a heating ²element. A ²heating element may be an electric heating device. In some embodiments, a ²heating element ²may be one or more fluid lines thermally coupled to the shelves.²
[0027] In certain embodiments, the freeze-drying system may include a ²condenser, which ²may be contained within the housing. In other embodiments, the system may ²comprise an ²external condenser. In such embodiments, condensing plates or coils may be ²disposed ²proximate within chamber 102, a separate condensing chamber or a conduit ²connecting the ²chamber 102 to the condensing chamber. If the orifices are on the condensing ²chamber or in ²a conduit between an isolation valve and the condensing chamber, then the ²isolation valve ²separating chamber 102 and the condensing chamber will be opened to achieve ²identical ²pressures between the two. In some embodiments, more than one chamber 102 may ²be ²connected to a single condensing chamber and vice versa.²
[0028] In some embodiments, the freeze-drying system may include a control ²interface, ²which may allow a user to program a series of steps and cause the steps to be ²executed. The ²freeze-drying system may include various control hardware (e.g., one or more ²processing ²devices) and software systems adapted to command and coordinate the various ²elements of ²the system / apparatus and carry out a pre-programmed freeze-drying cycle. ²Various control ²hardware and software systems may also provide documentation, data logging, ²alarms and ²system security capabilities as well. In addition, auxiliary systems to the ²freeze-dryer system ²may include a leak check system, performance check system and various ²subsystems to clean ²and sterilize the product chamber and / or auto-load / unload the product in the ²product ²chamber, as well as associated mechanical or cryogenic refrigeration system ²accessories such ²as refrigeration skids, compressors, condensers, heat exchangers, heat ²transfer fluid systems, ²pumps, heaters, expansion tanks, cryogen tanks, piping, flow ²controllers / regulators, valves, ²sensors, etc.²
[0029] Disclosed herein are methods of controlling shelf temperatures in a ²system such as ²freeze-drying system 100. The product to be chilled is first loaded onto the ²shelves, e.g., ²shelves 103 (FIG. 1). During the loading of the product, the present system ²may minimize ²frost buildup on the product shelves. Shelves generally are loaded starting ²with the topmost ²(first) usable shelf (the very top shelf generally is for radiant heat ²transfer only). During the ²loading of the first shelf, the stopper 108 is positioned to allow heat ²transfer fluid flow ²through the radiant (very top shelf 103) and first shelves 103 only. Upon ²completion of²6²<DP=7>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²loading of the first shelf (or at a point during the loading of the first ²shelf), the stopper ²element moves or is moved to allow fluid flow through the second shelf. This ²process ²repeats until all shelves have been loaded. By limiting the duration that an ²unloaded shelf is ²chilled, frost buildup can be minimized, which leads to increased heat ²transfer efficiency.²
[0030] After the product has been loaded, the shelves generally are held at ²the cold ²temperature and / or cooled further to induce nucleation of the product ²(freezing). The shelf ²temperature may be held at relatively cold values (e.g. about -50 C) for a ²period of time to ²ensure that all of the product has frozen completely. However, the temperature ²at which the ²product is held may depend on the specific product and desired cooling.²100311 After freezing of the sample is complete, drying steps are initiated ²which include a ²primary drying step and secondary drying step. Primary drying involves ²activating a vacuum ²pump and condenser refrigeration system to establish the desired sublimation ²and condensing ²conditions in the chamber 102. In some embodiments, a small bleed flow of a ²gas (e.g., an ²inert gas) may be fed into the chamber throughout the drying process to help ²control the ²vacuum level. After the vacuum pressure conditions are attained, the shelves ²are warmed ²(e.g., using an electric heater) to the desired primary drying temperature, ²which is dictated by ²the thermal, mechanical, chemical and / or biological properties of the material ²undergoing ²freeze-drying. Primary drying is completed when all the unbound water has been ²removed ²by sublimation, as determined by one or more of product temperature ²measurements, ²humidity measurements, comparison of capacitance manometer and Pirani gauge ²measurements, analysis of samples obtained with a sample thief, or other ²techniques. Once ²primary drying is complete, the freeze-dryer shelf temperatures are further ²warmed at a ²desired warming rate until the product or materials reach a temperature where ²desorption of ²bound water may be adequately achieved. This final product temperature depends ²on product ²composition and could be about 20 C or higher. After drying is complete, the ²product or ²material is removed from the chamber 102. At any time during the process, the ²freeze-drying ²system may be capable of emergency stop or shutdown, which would close ²pressurization ²and depressurization control valves while the chamber remains under vacuum.²
[0032] Shelves 103 are adapted with a cavity, i.e. flow passageway 104, to ²pass through it a ²heat exchange fluid for temperature adjustment. The flow passageway may ²advantageously ²have a serpentine shape or other shape to increase the heat transfer area ²between the fluid and²7²<DP=8>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²the shelves 103. The fluid may be an aqueous or non-aqueous, for instance ²water, glycol, a ²glycol / water mixture or a silicone oil. Glycol includes ethylene glycol and ²propylene glycol.²
[0033] The manifold 111, whether it be configured as an inlet manifold or an ²outlet manifold, ²will have a length L and a width W, the width being the longest radii of the ²manifold, e.g, ²near the ports 112. In some embodiments, the manifold may have a shape that is ²cylinder-²like or rectangular box-like. The manifold 111 will have a number of ports ²112, which ²function as an inlet or outlet for the manifold depending on the configuration ²of the manifold ²111. Each port 112 is associated with a shelf outlet 106 or an inlet 105 via, ²for example a ²tube, hose, or a pipe 113. The manifold inlets or outlets are orifices or ²ports 112 for fluid ²flow. A fluid manifold 111 may have from 2 to 25 or 30 ports or more, for ²example 2, 3, 4, ²5, 6, 7, 8, 9, 10, 20, 25 or 30 ports depending on the number of shelves 103 ²in the system 100. ²The inlet or outlet manifold ports 112 may or may not be uniformly spaced ²apart.²
[0034] The article 115 includes, in one example, an element or rod 107 with ²stopper 108, ²disposed in the manifold is adapted for adjustable lengthwise movement in the ²manifold 111. ²In some embodiments, the article 115 comprises a rod 107 with a stopper 108 or ²"plunger" ²fixed to the end of the rod 107 within the manifold 111. This arrangement is ²not unlike a ²piston in a cylinder. The stopper 108 may have any shape suitable to produce ²the desired ²effect of preventing fluid flow through the manifold 111 at the location of ²the stopper. In ²some embodiments, the stopper 108 may have a disc shape, a ball shape, a ²spheroid shape, a ²piston shape, etc. In some embodiments, a diameter of the stopper 108 is ²slightly smaller ²than the interior diameter of the manifold 111, enabling the stopper 108 to be ²adjustably ²moved within the manifold 111 and also prevent fluid flow in the manifold 111. ²As the ²stopper 108 is moved up or down (or sideways if the manifold was similarly ²mounted) within ²the manifold, that is, retracted or inserted, fluid flow is enabled (allowed) ²or is prevented ²(disallowed) through one or more particular shelves 103. In one example ²embodiments, the ²system 100 comprises an article 115 disposed in an outlet manifold, in an ²inlet manifold, or in ²both manifolds.²
[0035] In one example the system 100 will include an inlet manifold and an ²outlet manifold, ²with the inlet manifold coupled to the shelf inlets and with the outlet ²manifold coupled to the ²shelf outlets. One or both of the inlet and outlet manifolds may be like ²manifold 111 having ²an article 115.²8²<DP=9>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²
[0036] When fluid flow is prevented through one or more particular shelves ²103, those ²shelves 103 remain in fluid communication with the manifold 111, but the ²liquid cannot flow ²through those shelves 103. This is illustrated in the figures. As the stopper ²108 travels ²farther into the manifold 111, flow is enabled to each shelf 103 one-by-one. ²For example, for ²an system 100 containing 5 shelves 103, in a fully retracted position, flow is ²enabled to only a ²first (top) shelf 103. The stopper 108 may be partially inserted to a next ²position to enable ²flow to the first two shelves 103. The stopper 108 may be partially inserted ²to allow liquid ²flow to the first three or the first four shelves 103. The stopper 108 may be ²fully inserted to ²allow flow to all 5 shelves 103.²
[0037] The element disposed within the manifold may be associated with a ²suitable means of ²actuation 109. That is, the article 115 comprising the element also comprises ²a means of ²actuation 109, e.g. pneumatic or electric actuator, electric or hydraulic ²piston, rack and ²pinion, work gear, or other suitable device including manual means. The means ²of actuation ²109 may be any suitable means adapted to move a rod 107 in a linear motion. ²The means of ²actuation may be in communication, e.g. electrical communication, with an ²automated ²loading device. The allowance of flow may be programmed to be timed to ²coincide with ²automatic sample loading through sub-doors or through a single door (not ²shown).²
[0038] As fluid is not compressible, in one example the system 100 is designed ²to allow fluid ²to escape from below the stopper 108 as it is inserted past a bottom shelf's ²103 connection ²port 112 to a manifold. This may be accomplished, for instance, by increasing ²the diameter ²of the manifold at a connection point for the last (bottom) shelf, for example ²at 124 (FIG. 4), ²such that the width of the manifold at 124 is greater than width W. In other ²stopper 108 ²positions, fluid may escape back through a shelf or shelves whose connection ²is below the ²stopper 108 position. All of the aforementioned are means of allowing escape ²of a fluid from ²below the element when the element is in an inserted position.²
[0039] There might also be a change in flow path resistance as a stopper 108 ²is retracted or ²inserted; which change may be compensated for by any suitable means. In some ²embodiments, with reference to FIG. 1, this may be compensated by having a ²variable ²frequency drive 118 on a heat transfer liquid pump 120 and / or a bypass line ²122 with or ²without suitable valve(s) or other fluid flow control devices. These are means ²of allowing ²escape of a fluid from below the element when the element is in an inserted ²position.²9²<DP=10>²CA 03093834 2020-09-11²WO 2019 / 178201 ²PCT / US2019 / 022013²
[0040] Present systems may therefore also comprise a means to adjust the flow ²rate of fluid ²supplied to a shelf or shelves. The means may comprise a bypass line 122 ²and / or a variable ²frequency drive 118 on a heat transfer fluid pump 120, or other fluid flow ²control device(s). ²An adjustable variable flow rate will allow for maintenance of heat transfer ²equilibrium (i.e. ²constant heat transfer fluid velocity in each shelf) among the shelves as each ²shelf is ²"opened" to the liquid. Maintaining consistent heat transfer fluid velocity ²will provide ²temperature uniformity across a shelf surface.²
[0041] In some embodiments, the apparatus may contain from 2 to 25 or 2 to 30 ²shelves or ²more, for example 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 20, 25 or 30 shelves or ²more. The shelves ²may in general be uniformly spaced apart, or not.²
[0042] Present systems and methods are not limited to freeze-dryers or freeze-²drying ²methods. For example, disclosed systems and methods are equally applicable to ²refrigerators ²and freezers without a separate vacuum or drying system. Disclosed systems may ²also be ²utilized in any other temperature control systems, including heating systems.²
[0043] The term "system" may be synonymous with "apparatus" or "device" and ²may ²include an associated collection of elements, for instance elements selected ²from hardware, ²software and electronics. The terms "element", "article" and "member" may be ²synonymous ²and may themselves consist of a single element or may comprise more than one ²element. In ²general, a system may comprise one or more articles and an article may ²comprise one or ²more elements.²
[0044] In some embodiments, vacuum conditions may be less than 1 millibar up ²to about ²1000 millibar.²
[0045] The term "configured" as used in the description and claims is intended ²to be an open-²ended term as are the terms "comprising" or "containing". The term ²"configured" is not ²meant to exclude other possible articles or elements. The term "configured" ²may be ²equivalent to "adapted".²
[0046] The term "associated" means for instance "equipped with", "coupled to", ²"connected ²to" or in "communication with", for example "electrically connected" or in ²"fluid ²communication with" or otherwise connected in a way to perfoini a function. ²The term²<DP=11>²"associated" may mean directly associated with or indirectly associated with, ²for instance ²through one or more other articles or elements.²
[0047] The articles "a" and "an" herein refer to one or to more than one (e.g. ²at least one) of ²the grammatical object. Any ranges cited herein are inclusive. The term ²"about" used ²throughout is used to describe and account for small fluctuations. For ²instance, "about" may ²mean the numeric value may be modified by 5%, 4%, 3%, 2%, 1 %, ²0.5%, ²0.4%, 0.3%, 0.2%, 0.1% or 0.05%. All numeric values are modified by ²the term ²"about" whether or not explicitly indicated. Numeric values modified by the ²term "about" ²include the specific identified value. For example, "about 5,0" includes 5.0. ²In addition, a ²feature discussed with one figure or embodiment may also be used in ²combination with or in ²the alternative of another disclosed feature or embodiment as applicable.²
[0048] Unless otherwise indicated, all parts and percentages are by weight. ²Weight percent ²(wt%), if not otherwise indicated, is based on an entire composition free of ²any volatiles, that ²is, based on dry solids content.²
[0049] What is claimed as new and desired to be protected by Letters Patent ²is:²11²Date Recue / Date Received 2023-07-19²
Claims
<DP=1>²CLAIMS²1. A system comprising²a housing defining a chamber;²a plurality of horizontal shelves arranged vertically within the chamber, each ²shelf ²comprising an inlet, an outlet and a flow passageway disposed between the ²inlet and the ²outlet;²a fluid manifold having a length and a width and in fluid communication with a ²²respective flow passageway of each shelf; and²an element disposed within the manifold and adapted for adjustable lengthwise ²movement along the length of the manifold, wherein the element comprises a rod ²connected ²to a stopper, wherein the stopper is sized to prevent a flow of a heat ²exchange fluid through ²one or more of the shelves.²2. The system according to claim 1, wherein the manifold is an outlet fluid ²manifold that ²is coupled to the outlets of each shelf²3. The system according to claim 1, wherein the manifold is an inlet fluid ²manifold that is ²coupled to the inlets of each shelf²4. The system according of claim 1, wherein the adjustable movement serves ²to allow or ²prevent flow of a heat exchange fluid through one or more of the shelves.²5. The system according to claim 1, wherein the element is connected to a ²means of ²actuation.²6. The system according to claim 1, wherein²if the element is in a fully retracted position, the flow of the heat exchange ²fluid is ²permitted through only a first of the plurality of horizontal shelves;²if the element is in a fully inserted position, the flow of the heat exchange ²fluid is ²permitted through all of the plurality of horizontal shelves; or²12²Date Recue / Date Received 2023-07-19²<DP=2>²if the element is in a partially inserted position, the flow of the heat ²exchange fluid is ²permitted through more than one of the plurality of horizontal shelves and ²fewer than all of ²the plurality of horizontal shelves.²7. The system according to claim 1, wherein the element is adapted to being ²actuated ²into a position so as to prevent the flow of heat exchange fluid through a ²desired number of ²the plurality of shelves and to permit the flow of heat exchange fluid through ²the remaining ²number of the plurality of shelves.²8. The system according to claim 7, wherein the plurality of shelved is ²from 2 to 30 ²shelves, inclusive.²9. The system according to claim 5, wherein the element is associated with ²an automated ²or a manual sample positioning device.²10. The system according to claim 1, further comprising at least one of ²bypass line, a ²variable frequency drive on a liquid pump, and a fluid flow control device.²11. The system according to claim 1, further comprising a vacuum source.²12. The system according to claim 1, wherein the system is a freeze-drying ²system.²13. A method of controlling a shelf temperature in a system comprising a ²housing ²defining a chamber;²a plurality of horizontal shelves arranged vertically within the chamber, each ²shelf ²containing a flow passageway, an inlet and an outlet;²a fluid manifold having a length and a width and in fluid communication with ²each ²shelf; and²an element disposed within the manifold and adapted for adjustable lengthwise ²movement in the manifold;²the method comprising adjustably moving the element lengthwise within the ²manifold ²wherein the element comprises a rod connected to a stopper, wherein the ²stopper is sized to ²prevent a flow of a heat exchange fluid through one or more of the shelves.²13²Date Recue / Date Received 2023-07-19²<DP=3>²14. The method ²according to claim 13, further comprising controlling fluid flow rate²through the shelves by at least one of bypassing fluid around one or more ²shelves and ²adjusting a pump rate of the fluid.²14²Date Recue / Date Received 2023-07-19²
