WO2014158500A1 - Heat transfer in distillation columns - Google Patents
Heat transfer in distillation columns Download PDFInfo
- Publication number
- WO2014158500A1 WO2014158500A1 PCT/US2014/017439 US2014017439W WO2014158500A1 WO 2014158500 A1 WO2014158500 A1 WO 2014158500A1 US 2014017439 W US2014017439 W US 2014017439W WO 2014158500 A1 WO2014158500 A1 WO 2014158500A1
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- WO
- WIPO (PCT)
- Prior art keywords
- trays
- region
- heat pipe
- distillation column
- tray
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/42—Regulation; Control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/007—Energy recuperation; Heat pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
- B01D3/324—Tray constructions
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/4935—Heat exchanger or boiler making
- Y10T29/49353—Heat pipe device making
Definitions
- an apparatus comprises a distillation column including at least three trays, a pressure mechanism operably connected to the distillation column to control respective pressures of the at least three trays, and at least one heat pipe operably connected to each of the at least three trays to thermally connect each of the at least three trays.
- an apparatus comprises a distillation column including at least one tray and a heat pipe having a first section and a second section, wherein the first section of the heat, pipe is located in a first region proximate to the at least one tray and the second section of the heat pipe is located in a second region proximate to the at, least one tray, the first region being different from the second region, and wherein the heat pipe is configured to transfer heat, between the first and second sections responsive to a temperature differential between the first and second regions.
- a method comprises changing respective pressures of at least three trays in a distillation column and thermally connecting the at least three trays, wherein the thermal connection is selected to substantially isothermalize the at least three trays.
- a method comprises thermally connecting a first region proximate to a tray in a distillation column to a second region proximate to the tray with a heat pipe and transferring heat between the first region and the second region with the heat pipe.
- FIG. 1 is a schematic of a distillation column.
- FIG. 2 is a schematic of a distillation column.
- FIG. 3 is a schematic of a distillation column.
- FIG. 4 is a schematic of a distillation column.
- FIG. 5 is a schematic of two distillation columns.
- FIG. 6 is a schematic of a distillation column and circuitry.
- FIGS. 7-10 are flow charts depicting a method.
- an apparatus comprises a distillation column 100 including at least three trays 102, a pressure mechanism 104 operably connected to the distillation column 100 to control respective pressures of the at least three trays 102, and at least one heat pipe 506 operably connected to each of the at least three trays 102 to thermally connect each of the at least three trays 102.
- the pressure mechanism 104 is a pump.
- Figure 5 shows the pressure mechanism 104 being operably connected to the distillation column 500 to control respective pressures Pi, Pa, and P 3 of three trays 102 (where, in Figure 1 , the regions 108, 1 10, and 1 12 each include one of the at least three trays 1 02 and are configured to support different pressures), however in other embodiments the pressure mechanism 104 is operablv connected to more than three trays 102. Further, although the pressure mechanism 104 is shown in Figure 1 as bei g one unit, in other embodiments the pressure mechanism 104 may comprise more than one unit. For example, in some embodiments each tray 102 is operablv connected to a separate device configured to maintain and/or alter the pressure of the tray 102,
- the at least one heat pipe 106 is shown as being a single heat pipe, other embodiments may include more than one heat pipe 106 depending on the particular embodiment.
- the heat pipe 106 is shown as branched, other embodiments may include an unbranched configuration in which the heat pipe thermally couples to each of the three or more trays.
- the heat pipe 106 is shown as being a branch structure made substantially of tubular-shaped pipes, in other embodiments the spatial extent of the heat pipe may have a different configuration.
- the heat pipe may be configured in a different way than shown in Figure 1 , such as an embodiment where one or more portions of the heat pipe is/are configured to extend spatially along two dimensions defined by one or more of the trays 102.
- portions of the heat pipes that are operably connected to individual trays 102 may be connected together by a substantially one-dimensional structure (such as the pipes shown in Figure 1), a two dimensional structure such as a plane, or a different structure.
- the heat pipes 106 as shown herein show exemplary embodiments of the configuration of a heat pipe 106 that is selected for clarity in the drawings, however the actual configuration of the heat pipe depends on the particular embodiment.
- the term "heat pipe” as used herein includes a device for heat transfer whose spatial distribution is determined by the particular application and may be substantially two or three dimensional, and need not actually resemble a "pipe" in appearance.
- heat pipe 106 and pressure mechanism 104 are shown in Figure 1 as being operably connected to three trays, in other embodiments one or both elements 104, 106 may be operably connected to more than three trays.
- the pressure mechanism 104 is operablv connected to the distillation column 100 to maintain substantially different pressures for each of the at least three trays 102.
- the pressures may be maintained differently in order to adjust the vaporization temperatures of the at least three trays,
- the at least three trays 102 are arranged sequentially, and wherein the pressure mechanism 104 is operablv connected to the distillation column 500 to maintain a substantially mono tonic variation in pressure of the sequential arrangement.
- the lowest tray 102 may have the lowest pressure
- the tray above it may have a slightly higher pressure
- the tray above it may have an even slightly higher pressure, producing a substantially monotonic variation in pressure of the trays 102.
- the pressure variation may be opposite that described previously, with pressure decreasing with increasing height in the column.
- the trays 102 are not arranged vertically but horizontally, i.e., side by side, or they may have a different spatial arrangement. In such an embodiment the sequence of the trays 102 is determined by the flow of fluid/vapor in the distillation column 100.
- the apparatus further comprises a flow assembly operably connected to at least two of the at least three trays 102 to transfer material from a first of the at least three trays 102 to a second of the at least three trays 102.
- the trays may be sealed off such that the fluid in the distillation column is pumped between trays 102 instead of flowing by gravity.
- the flow assembly is selected to transfer material responsive to a pressure differential.
- the flow assembly includes at least one of a pump, a valve, and a nozzle.
- the trays 102 in the distillation column 100 may be arranged horizontally instead of vertically, as shown in Figure 2,
- An embodiment such as Figure 2 may include the elements as shown in Figure 1, including, but not limited to, the pressure mechanism 104 and/or the heat pipes 106.
- fluid flow between adjacent trays 102 can be controlled by adjusting the pressure at each tray.
- the heat pipe 106 may be branched (as illustrated in Figure 2) or may be unbranched, and/or may have a different configuration entirely as described with respect to Figure 1.
- an apparatus comprises a distillation column 100 including at least one tray 102 and a heat pipe 106 having a first, section 302 and a second section 304, wherein the first section 302 of the heat pipe 106 is located in a first region 306 proximate to the at least one tray 102 and the second section 304 of the heat pipe 106 is located in a second region 308 proximate to the at least one tray 102, the first region 306 being different from the second region 308, and wherein the heat pipe 106 is configured to transfer heat between the first and second sections 302, 304 responsive to a temperature differential between the first and second regions 306, 308,
- Such an embodiment may be employed to maintain a substantially even temperature within the tray 102, i.e. to substantially isothermalize the first and second regions 306, 308 and/or the entire tray 102.
- this isothermalization may increase the homogeneity of distillation products within the fray 102.
- the first and second regions 306, 308 are examples of regions that are substantially isothermalized with the heat pipe 106, however these regions are exemplar ⁇ ' and the regions affected by the heat pipe 106 may be larger or smaller than those shown in Figure 3. Further, due to the nature of heat flow the regions affected by the heat pipe 106 are not necessarily clearly defined having a hard boundary as indicated by the regions 306, 308, and the regions 306, 308 are merely shown as an example of what may be considered a region affected by the heat pipe 106. Although Figure 3 is shown having a single heat pipe 106, other embodiments include more than one heat pipe 106. Although the first and second regions 306, 308 are shown as being partially overlapping in Figure 3, in some embodiments the regions are not overlapping.
- heat pipe 106 is shown in Figure 3 as being branched into first and second sections 302, 304, other layouts may be used.
- heat pipe 106 in unbranched, with first section 302 and second section 304 occupying different portions along the length of the heat pipe.
- the heat pipe 106 is located along a length of tray 102, thermally transferring heat to/from regions of tray 102 along the length.
- the heat pipes can have plate-like configurations and may be configured to match the shape or dimensions of the tray.
- the heat pipe may be built-in to the tray (e.g., integrally forming the base of the tray). Further, as described with respect to Figure 1 , the spatial distribution of the heat pipe 106 may have many different configurations according to a particular embodiment.
- the heat pipe 106 has a third section 310 different from the first and second sections 302, 304, and wherein the third section 310 of the heat pipe 106 is located in a source region 312 different from the first and second regions 306, 308, the source region 312 including a temperature source, and wherein the heat pipe 106 is configured to transfer heat between the third section 310 and the first and second sections 302, 304 responsive to a temperature differential between the source region 312 and at least one of the first and second regions 306, 308.
- the source region 312 may be located outside of the distillation column and may be, for example, a liquid having a temperature that is controllable by one or more heating and/or refrigeration elements, where the temperatures of the first and second regions 306, 308 may be controlled by controlling the temperature of the source region 312.
- the heat source and/or coolant, thermometers, and other control and/or measurement devices are, in some embodiments, operably connected to circuitry (explained in more detail with respect to Figure 6) configured to control the temperature of the source region 312 in response to one or more measurements of the source region 312, the first and second regions 306, 308, and/or a different region.
- an apparatus comprises a distillation column 100, a heat pipe 106 having a first section 302 and a second section 304, the first section 302 being located in a first region 306 proximate to a first tray 402 of the distillation column 100, and a temperature source 404, wherein the second section 304 of the heat pipe 106 is located in a source region 312 that includes the temperature source 404, and wherein the heat pipe 106 is configured to transfer heat between the first and second sections 302, 304 responsive to a temperature differential between the first region 306 and the source region 312.
- the temperature source 404 is explained in greater detail with respect to Figure 3, where the source region 312 includes a temperature source.
- the heat pipe 106 is configured to substantially isothermalize the first region 306 with the source region 312.
- the apparatus further comprises circuitry 406 operabiy connected to the temperature source 404 to control the temperature of the source region 312.
- the apparatus may further comprise a thermometer 408 configured to determ ine the temperature of the first region 306 and/or the source region 312 and operabiy connected to the circuitry 406 to control the temperature of the source region 312.
- a thermometer 408 is shown as a way of
- other embodiments include other mechanism for indirectly determining temperature, such as a device for measuring pressure.
- the heat pipe 106 may comprise a variable conductance heat pipe.
- the heat pipe 106 has adjustable thermal conditions, for example, an adjustable internal pressure and/or an adjustable fluid composition.
- Some embodiments further comprise circuitry 406 operabiy connected to the heat pipe 106 to control the adjustable thermal conditions.
- the circuitry 406 is further receptive to a signal indicative of a condition of the temperature source 404 to control the adj ustable thermal conditions of the heat pipe 106.
- an apparatus comprises first and second distillation columns 502, 504 having substantially equivalent parts and a heat pipe 106 operably connected to a first tray 506 of the first distillation column 502 and a second tray 508 of the second distillation column 504, wherein the first and second trays 506, 508 are substantially equivalent parts.
- first and second distillation columns 502, 504 having substantially equivalent parts are substantially identical having the same number of trays.
- first and second distillation columns 502, 504 having substantially equivalent parts may include one or more portions of the distillation columns 502, 504 that are
- the distillation columns 502, 504 have substantially equivalent parts up to a certain height of the distillation columns 502, 504, and parts above that height are not substantially equivalent.
- Figure 5 shows an embodiment having two distillation columns 502, 504 with substantially equivalent parts, other embodiments may include three or more distillation columns having substantially equivalent parts.
- first and second distillation columns 502, 504 having substantially equivalent parts are each configured to produce one or more products 510, 512, the products 10, 552 being substantially the same for both the first and second distillation columns 502, 504.
- an apparatus comprises circuitry 602 configured to receive a first signal 604 corresponding to a condition of a first region 306 of a first distillation column 100, circuitry 602 configured to process the first signal 604 and to determine a second signal 606 corresponding to an altered condition of the first region 306 of the first distillation column 100, and circuitry 602 configured to produce the second signal 606, the second signal 606 being indicative of a change in a condition of a thermal connection between the first region 306 and a source region 608 outside the distillation column 100.
- condition of the first region 306 includes a temperature of the first region 306, and in some embodiments the second signal 606 is indicative of a change in temperature of the so urce region 608, In some embodiments the condition of the first region 306 includes an amount of a product 610 produced in the first region 306 and/or a pressure of the first region 306. In some embodiments the second signal 606 is indicative of a change in temperature of the source region 608. In some embodiments the second signal 606 is indicative of a change in a thermal condition of a heat pipe 612 connecting the first and source regions 306, 608, where the thermal condition includes a pressure and/or a fluid composition in different embodiments.
- distillation columns 100 shown in Figures 1 -6 are shown with 6 trays 102 each for clarity. However, the number of trays 102 of a distillation column depends on the particular embodiment, and a distillation column 100 may have more or fewer than 6 trays depending on the particular embodiment.
- the heat pipes 106 are generally shown in Figures 1 ⁇ 6 as elongated tubes.
- the heat pipes can be tubular with a circular cross-section, a rectilinear cross-section, a cross-section having a different spatial distribution, and/or some combination of cross-sections depending on the particular embodiment.
- the heat pipe cross section may vary along the length of the heat pipe, for example, the cross-section may have substantially circular geometry in one section and have substantially rectilinear geometry in another.
- one or more sections of the heat pipes may include one or more portions having a cross-section that is large compared to the length of the heat pipe (i.e., that portion of the heat pipe may be substantially two- or three-dimensional in its spatial extent), and may be configured to match the shape or dimensions of the tray and/or temperature source.
- the evaporation and the condensation sections of the heat pipe are physically separate from each other.
- the heat pipe may be built-in to the tray (e.g., integrally forming the base of the tray).
- the heat pipes 106 may comprise substantially tubular heat pipes, vapor chambers, variable conductance heat pipes, loop heat pipes, or similar sealed heat transfer devices utilizing reversible liquid-vapor phase changes of a contained working fluid.
- the selection, working fluids, and operational principles of heat pipes are discussed in reference books such as, "Heat Pipes, Fifth Edition: Theory, Design, and Applications", by David Reay, Ryan McGlen, and Peter ew, Butterworth- Heinemann, 2006, as well as in technical papers such as, "Heat Pipe, Selection of Working Fluid” by Per W allin, each of which is incorporated herein by reference.
- the working fluid may be chosen based on the temperature range over which the heat pipe will be used,
- a hydrocarbon distillation column may use heat pipes having different working fluids for different trays, i.e., based on the boiling point of the distillation product handled by a given tray.
- heat pipes used for trays processing naptha might use methanol, acetone, or water
- heat, pipes used for trays processing gasoline or diesel might use water, thermex, or flutec
- heat pipes used for trays processing lubricating oils or fuel oils might use mercury, cesium, or sulfur/iodine mixtures.
- heat pipe working fluids may be used, for instance: nitrogen or ammonia for cryogenic distillation; or potassium, sodium or lithium for high temperature distillation.
- a method comprises (702) changing respective pressures of at least three trays 102 in a distillation column 100 and (704) thermally connecting the at least three trays 102 (for example, with the heat pipe 106), wherein the thermal connection 106 is selected to substantially isothermalize the at least three trays 102.
- changing respective pressures of at least three trays 102 in a distillation column includes maintaining substantially different pressures for each of the at least three trays 102.
- the method further comprises transferring material from a first of the at least three trays 102 to a second of the at least three trays 102, where in some embodiments transferring material includes pumping material, and in some embodiments transferring material includes establishing a. pressure differential between at least two of the at least three trays 102.
- a method comprises (802) thermally connecting a. first region proximate to a.
- tray in a distillation column for example, the first region 306 to a second region 308 proximate to the tray (for example, the second region 308) with a heat pipe 106 and (804) transferring heat between the first region 306 and the second region 308 with the heat pipe 106.
- transferring heat between the first region 306 and the second region 308 with the heat pipe 106 includes substantially isothermalizing the distillation column tray 102.
- the method may further comprise thermally connecting the first and second regions 306, 308 to a source region 312 with the heat pipe 106, wherein the source region 312 includes a temperature source.
- the source region 312 is located outside the distillation column 100.
- the first region 306 overlaps at least partially with the second region 308.
- a method comprises thermally connecting a first region 306 proximate to a tray in a distillation column 100 to a source region 352 with a heat pipe 106, wherein the thermal connection substantially isothermalizes the first region 306 and the source region 312, and changing the temperature of the first region 306 with the thermal connection 106.
- changing the temperature of the first region 306 with the thermal connection 106 includes heating the source region 312, cooling the source region 312, and/or receiving a first signal indicative of a temperature and changing the temperature of the source region 312 in response to the first signal.
- the first signal is indicative of a. temperature of the first region 306 and/or a temperature of the source region 312.
- changing the temperature of the first region 306 with the thermal connection 106 includes changing a thermal condition of the thermal connection 106, which, in some embodiments, further includes changing a pressure of the thermal connection 106, changing a fluid composition of the thermal connection 106, and/or receiving a. signal and changing the thermal condition of the thermal connection 106 responsive to the signal, where in some embodiments the signal includes information related to a. condition of the temperature source.
- a method comprises thermally connecting a first region 514 of a first distillation column 502 to a second region 516 of a second distillation column 504, wherein the first region 514 and the second region 516 are substantially equivalent regions, and substantially isotherrnalizing the first and second regions 514, 516 with the thermal connection.
- first region 514 corresponds to a first tray 506 in the first distillation column 502 and the second region 516 corresponds to a second tray 508 in the second distillation column 504, and wherein the first and second trays 506, 508 are substantially equivalent.
- each of the first and second distillation columns 502, 504 includes an array of trays, wherein the array of trays in the first distillation column 502 is substantially equivalent to the array of trays in the second distillation column 504, and the method further comprises thermally connecting each of the trays in the first distillation column 502 with an equivalent tray in the second distillation column 504 and substantially isotherrnalizing each of the trays in the first distillation column 502 with the equivalent tray in the second distillation column 504.
- the impiementer may opt for a mainly hardware and/or firmware vehicle: alternatively, if flexibility is paramount, the implementer may opt for a mainly software implementation; or, yet again alternatively, the implementer may opt for some combination of hardware, software, and/or firmware.
- any vehicle to be utilized is a choice dependent upon the context in which the vehicle will be deployed and the specific concerns (e.g., speed, flexibility, or predictability) of the implementer, any of which may vary.
- optical aspects of implementations will typically employ optically-oriented hardware, software, and or firmware.
- logic and similar implementations may include software or other control structures.
- Electronic circuitry may have one or more paths of electrical current constructed and arranged to implement various functions as described herein.
- one or more media may be configured to bear a device-detectable implementation when such media hold or transmit a device detectable instructions operable to perform as described herein.
- implementations may include an update or modification of existing software or firmware, or of gate arrays or programmable hardware, such as by performing a reception of or a transmission of one or more instructions in relation to one or more operations described herein.
- an implementation may include special-purpose hardware, software, firmware components, and/or general-purpose components executing or otherwise invoking special-purpose components.
- Specifications or other implementations may be transmitted by one or more instances of tangible transmission media as described herein, optionally by packet transmission or otherwise by passing through distributed media at various times.
- implementations may include executing a special-purpose instruction sequence or invoking circuitry for enabling, triggering, coordinating, requesting, or otherwise causing one or more occurrences of virtually any functional operations described herein.
- operational or other logical descriptions herein may be expressed as source code and compiled or otherwise invoked as an executable instruction sequence.
- implementations may be provided, in whole or in part, by source code, such as C++, or other code sequences.
- source or other code implementation using commercially available and/or techniques in the art, may be compiled/ .
- a logical expression e.g., computer programming language implementation
- HDL Hardware Description Language
- VHDL Very High Speed Integrated Circuit Hardware Descriptor Language
- Those skilled in the art will recognize how to obtain, configure, and optimize suitable transmission or computational elements, material supplies, actuators, or other structures in light of these teachings,
- Examples of a signal bearing medium include, but are not limited to, the following: a recordable type medium such as a floppy disk, a hard disk drive, a Compact Disc (CD), a Digital Video Disk (DVD), a digital tape, a computer memory, etc.; and a transmission type medium such as a digital and/or an analog
- a communication medium e.g., a fiber optic cable, a waveguide, a wired
- a wireless communication link e.g., transmitter, receiver, transmission logic, reception logic, etc., etc.
- electro-mechanical system includes, but is not limited to, electrical circuitry operably coupled with a transducer (e.g., an actuator, a motor, a.
- piezoelectric crystal a Micro Electro Mechanical System (MEMS), etc.
- electrical circuitry having at least one discrete electrical circuit, electrical circuitry having at least one integrated circuit, electrical circuitry having at least one application specific integrated circuit, electrical circuitry forming a general purpose computing device configured by a computer program (e.g., a general purpose computer configured by a computer program which at least partially carries out processes and/or devices described herein, or a microprocessor configured by a computer program which at least partially carries out processes and/or devices described herein), electrical circuitry forming a memory device (e.g., forms of memory (e.g., random access, flash, read only, etc,)), electrical circuitry forming a communications device (e.g., a modem, communications switch, optical-electrical equipment, etc.), and/or any non-electrical analog thereto, such as optical or other analogs.
- a memory device e.g., forms of memory (e.g., random access, flash, read only, etc,)
- electro-mechanical as used herein is not necessarily limited to a system that has both electrical and mechanical actuation except as context may dictate otherwise.
- electrical circuitry includes, but is not limited to, electrical circuitry having at least one discrete electrical circuit, electrical circuitry having at least one integrated circuit, electrical circuitry having at least one application specific integrated circuit, electrical circuitry forming a general purpose computing device configured by a computer program (e.g., a general purpose computer configured by a computer program which at least partially carries out processes and/or devices described herein, or a microprocessor configured by a computer program which at least partially carries out processes and/or devices described herein), electrical circuitry forming a memory device (e.g., forms of memory (e.g., random access, flash, read only, etc.)), and/or electrical circuitry forming a communications device (e.g., a modem, communications switch, optical- electrical equipment, etc.).
- a memory device e.g., forms of memory (e.g., random access, flash, read only, etc.)
- communications device e.g., a modem, communications switch, optical- electrical equipment, etc.
- typical image processing system generally includes one or more of a system unit housing, a video display device, memory such as volatile or non-volatile memory, processors such as microprocessors or digital signal processors, computational entities such as operating systems, drivers, applications programs, one or more interaction devices (e.g., a touch pad, a touch screen, an antenna, etc.), control systems including feedback loops and control motors (e.g., feedback for sensing lens position and/or velocity; control motors for moving/distorting lenses to give desired focuses).
- An image processing system may be implemented utilizing suitable commercially available components, such as those typically found in digital still systems and/or digital motion systems.
- a data processing system generally includes one or more of a system unit housing, a video display device, memory such as volatile or non-volatile memory, processors such as microprocessors or digital signal processors, computational entities such as operating systems, drivers, graphical user interfaces, and applications programs, one or more interaction devices (e.g., a touch pad, a touch screen, an antenna, etc.), and/or control systems including feedback loops and control motors (e.g., feedback for sensing position and/or velocity; control motors for moving and/or adjusting components and/or quantities).
- a data processing system may be implemented utilizing suitable commercially available components, such as those typically found in data
- examples of such other devices and/or processes and/or systems might include - as appropriate to context and application— all or part of devices and/or processes and/or systems of (a) an air conveyance (e.g., an airplane, rocket, helicopter, etc.), (b) a ground conveyance (e.g., a car, truck, locomotive, tank, armored personnel carrier, etc.), (c) a building (e.g., a home, warehouse, office, etc.), (d) an appliance (e.g., a refrigerator, a washing machine, a dryer, etc.), (e) a communications system, (e.g., a networked system, a telephone system, a Voice over IP system, etc.), (f) a business entity (e.g., an Internet Service Provider (ISP) entity such as Comcast Cable, Qwest,
- ISP Internet Service Provider
- a wired/wireless services entity e.g., Sprint, Cingular, Nextel, etc.
- use of a system or method may occur in a territory even if components are located outside the territory.
- use of a distributed computing system may occur in a territory even though parts of the system may be located outside of the territory (e.g., relay, server, processor, signal-bearing medium, transmitting computer, receiving computer, etc. located outside the territory).
- a sale of a system or method may likewise occur in a territory even if components of the system or method are located and/or used outside the territory.
- implementation of at least part of a system for performing a method in one territory does not preclude use of the system in another territory.
- user is shown/described herein as a single illustrated figure, those skilled in the art will appreciate that user may be representative of a human user, a robotic user (e.g., computational entity), and/or substantially any combination thereof (e.g., a user may be assisted by one or more robotic agents) unless context dictates otherwise.
- a robotic user e.g., computational entity
- substantially any combination thereof e.g., a user may be assisted by one or more robotic agents
- Those skilled in the art will appreciate that, in general, the same may be said of "sender” and/or other entity-oriented terms as such terms are used herein unless context dictates otherwise.
- any two components herein combined to achieve a particular functionality can be seen as “associated with” each other such that the desired functionality is achieved, irrespective of architectures or intermedial components.
- any two components so associated can also be viewed as being “operably connected”, or “operably coupled,” to each other to achieve the desired functionality, and any two components capable of being so associated can also be viewed as being “operably couplable,” to each other to achieve the desired functionality.
- operably couplable include but are not limited to physically mateable and'or physically interacting components, and/or wirelessly intera.cta.ble, and ' or wirelessly interacting components, and/or logically interacting, and'or logically interactable components.
- one or more components may be referred to herein as “configured to,” “configured by,” “configurable to,” “operable/operative to,”
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Abstract
Description
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Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/829,468 | 2013-03-14 | ||
| US13/829,468 US20140262741A1 (en) | 2013-03-14 | 2013-03-14 | Heat transfer in distillation columns |
| US13/836,294 US20140262729A1 (en) | 2013-03-14 | 2013-03-15 | Heat transfer between a distillation column and a temperature source |
| US13/836,294 | 2013-03-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2014158500A1 true WO2014158500A1 (en) | 2014-10-02 |
Family
ID=51522576
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2014/017448 Ceased WO2014158501A1 (en) | 2013-03-14 | 2014-02-20 | Heat transfer between a distillation column and a temperature source |
| PCT/US2014/017439 Ceased WO2014158500A1 (en) | 2013-03-14 | 2014-02-20 | Heat transfer in distillation columns |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2014/017448 Ceased WO2014158501A1 (en) | 2013-03-14 | 2014-02-20 | Heat transfer between a distillation column and a temperature source |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US20140262729A1 (en) |
| WO (2) | WO2014158501A1 (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4234391A (en) * | 1978-10-13 | 1980-11-18 | University Of Utah | Continuous distillation apparatus and method |
| US5783047A (en) * | 1994-08-29 | 1998-07-21 | Kimura Chemical Plants Co., Ltd. | Heat integrated distillation column |
| US20050121303A1 (en) * | 2002-01-25 | 2005-06-09 | Technische Universiteit Delft | Heat integrated distillation column |
| US20120085126A1 (en) * | 2010-10-06 | 2012-04-12 | Exxonmobil Research And Engineering Company | Low energy distillation system and method |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3575007A (en) * | 1968-03-26 | 1971-04-13 | Treadwell Corp | Isothermal fractional distillation of materials of differing volatilities |
| US3603767A (en) * | 1969-09-03 | 1971-09-07 | Dynatherm Corp | Isothermal cooking or heating device |
| US4787843A (en) * | 1987-06-22 | 1988-11-29 | Thermo Electron Corporation | Pressure balanced heat pipe |
| CA2654508C (en) * | 2006-06-08 | 2014-07-29 | Yale University | Multi stage column distillation (mscd) method for osmotic solute recovery |
| JP2008051389A (en) * | 2006-08-24 | 2008-03-06 | Asahi Kasei Fibers Corp | Heat pipe type heat transfer device |
| WO2010033675A1 (en) * | 2008-09-17 | 2010-03-25 | Sylvan Source, Inc. | Large-scale water purification and desalination |
| JP4803470B2 (en) * | 2009-10-05 | 2011-10-26 | 独立行政法人産業技術総合研究所 | Heat exchange type distillation equipment |
-
2013
- 2013-03-15 US US13/836,294 patent/US20140262729A1/en not_active Abandoned
-
2014
- 2014-02-20 WO PCT/US2014/017448 patent/WO2014158501A1/en not_active Ceased
- 2014-02-20 WO PCT/US2014/017439 patent/WO2014158500A1/en not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4234391A (en) * | 1978-10-13 | 1980-11-18 | University Of Utah | Continuous distillation apparatus and method |
| US5783047A (en) * | 1994-08-29 | 1998-07-21 | Kimura Chemical Plants Co., Ltd. | Heat integrated distillation column |
| US20050121303A1 (en) * | 2002-01-25 | 2005-06-09 | Technische Universiteit Delft | Heat integrated distillation column |
| US20120085126A1 (en) * | 2010-10-06 | 2012-04-12 | Exxonmobil Research And Engineering Company | Low energy distillation system and method |
Also Published As
| Publication number | Publication date |
|---|---|
| US20140262729A1 (en) | 2014-09-18 |
| WO2014158501A1 (en) | 2014-10-02 |
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