JP2007519881A5 - - Google Patents

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JP2007519881A5
JP2007519881A5 JP2006549786A JP2006549786A JP2007519881A5 JP 2007519881 A5 JP2007519881 A5 JP 2007519881A5 JP 2006549786 A JP2006549786 A JP 2006549786A JP 2006549786 A JP2006549786 A JP 2006549786A JP 2007519881 A5 JP2007519881 A5 JP 2007519881A5
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gas
fluid stream
heat
adsorbent
fluid
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JP2007519881A (en
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Priority claimed from PCT/AU2005/000083 external-priority patent/WO2005073644A1/en
Publication of JP2007519881A publication Critical patent/JP2007519881A/en
Publication of JP2007519881A5 publication Critical patent/JP2007519881A5/ja
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Claims (31)

第1及び第2の気体吸着材料を使用して、熱を転送する方法において、第2の材料は第1の材料から熱的に比較的、隔離されているが、連続的に気体を連通しており、
(i)第1の材料に吸着された気体を脱着するように第1の材料を加熱し、それによって生成された気体は第2の材料へ送られて、吸着され、
(ii)気体が第2の材料から脱着して、そこから第1の材料へ再度吸着されるように、第1の材料を冷却し、
それによって第2の材料は、気体をそこから脱着することにより、冷却されるステップを含んでいる熱転送方法。
In the method of transferring heat using the first and second gas adsorbing materials, the second material is thermally relatively isolated from the first material, but the gas is continuously communicated. And
(I) heating the first material to desorb the gas adsorbed on the first material, and the gas generated thereby is sent to the second material and adsorbed;
(Ii) cooling the first material so that the gas desorbs from the second material and is then adsorbed again to the first material;
A heat transfer method whereby the second material is cooled by desorbing a gas therefrom.
ステップ(i)において、第1の材料は、比較的高温の流体流からの熱伝導により加熱される請求項1記載の方法。   The method of claim 1, wherein in step (i), the first material is heated by heat conduction from a relatively hot fluid stream. 比較的高温の流体流は廃棄処理ガスまたは液体である請求項2記載の方法。   The method of claim 2 wherein the relatively hot fluid stream is a waste process gas or liquid. 第1の材料が加熱されている期間中に、第2の材料は、冷却流体流による熱伝導により、第1の材料に関して冷却される請求項1乃至3のいずれか1項記載の方法。   4. A method according to any one of the preceding claims, wherein during the period in which the first material is heated, the second material is cooled with respect to the first material by heat conduction through a cooling fluid stream. 冷却流体流は周囲空気流である請求項4記載の方法。   The method of claim 4, wherein the cooling fluid stream is an ambient air stream. ステップ(ii)において、第1の材料は、周囲への熱伝導により、または冷却流体流による熱伝導により、第2の材料に関して冷却される請求項1乃至5のいずれか1項記載の方法。   6. A method according to any one of the preceding claims, wherein in step (ii) the first material is cooled with respect to the second material by heat conduction to the surroundings or by heat conduction by a cooling fluid stream. 冷却流体流は周囲空気流である請求項6記載の方法。   The method of claim 6, wherein the cooling fluid stream is an ambient air stream. ステップ(ii)において、第2の材料がその材料からのガスの脱着により冷却されているときに、第2の材料は別の流体を冷却するために使用される請求項1乃至7のいずれか1項記載の方法。   8. In step (ii), when the second material is being cooled by desorption of gas from the material, the second material is used to cool another fluid. The method according to claim 1. 前記他の流体流は、冷却を必要とする処理ガスまたは液体である請求項8記載の方法。   9. The method of claim 8, wherein the other fluid stream is a process gas or liquid that requires cooling. 第2の材料からの脱着が完了に到達すると、第2の材料は他の流体流からの熱伝導により僅かに加熱されることを可能にされ、その温度は、気体がそこに吸着される前に、第2の材料がステップ(i)の温度に対応するレベルまでその温度を回復するのに、丁度十分な温度である請求項8または9記載の方法。   When desorption from the second material is complete, the second material is allowed to be slightly heated by heat conduction from the other fluid stream, the temperature of which is before the gas is adsorbed onto it. 10. A method according to claim 8 or 9, wherein the second material is just at a temperature sufficient to restore its temperature to a level corresponding to the temperature of step (i). 第1の気体吸着剤材料は、第2の気体吸着剤材料とは異なる吸着力を有する請求項1乃至10のいずれか1項記載の方法。   The method according to any one of claims 1 to 10, wherein the first gas adsorbent material has an adsorption power different from that of the second gas adsorbent material. 第1の気体吸着剤材料は、第2の気体吸着剤材料とは異なる材料である請求項1乃至11のいずれか1項記載の方法。   The method according to any one of claims 1 to 11, wherein the first gas adsorbent material is a material different from the second gas adsorbent material. 第1の気体吸着剤材料は沸石であり、第2の気体吸着剤材料は活性化された炭素である請求項1乃至12のいずれか1項記載の方法。   The method according to any one of claims 1 to 12, wherein the first gas adsorbent material is zeolite and the second gas adsorbent material is activated carbon. 第1及び第2の材料に吸着される気体は二酸化炭素である請求項1乃至13のいずれか1項記載の方法。   The method according to any one of claims 1 to 13, wherein the gas adsorbed on the first and second materials is carbon dioxide. 気体は周囲圧力に関して加圧される請求項1乃至14のいずれか1項記載の方法。   15. A method according to any one of the preceding claims, wherein the gas is pressurized with respect to ambient pressure. 気体は、約0.5MPaに加圧される請求項15記載の方法。   The method of claim 15, wherein the gas is pressurized to about 0.5 MPa. 開始ステップ(i)の前に、気体および第1及び第2の材料は一般的に、周囲温度である請求項1乃至16のいずれか1項記載の方法。   17. A method according to any one of claims 1 to 16, wherein the gas and the first and second materials are generally at ambient temperature prior to the starting step (i). 第1の吸着剤材料を含む第1の部分と、第2の吸着剤材料を含む第2の部分とを有するチャンバを具備している熱伝導装置において、前記第1及び第2の部分が常に、連続的な気体の連通をその間において可能にするように接続され、相互に熱的に比較的、隔離されていることを特徴とする熱転送装置。   In a heat transfer device comprising a chamber having a first part containing a first adsorbent material and a second part containing a second adsorbent material, the first and second parts are always A heat transfer device connected in such a way as to allow continuous gas communication therebetween and is relatively thermally isolated from each other. 前記第1及び第2の部分は、それらの部分間に連続的な気体連通を可能にしながら、第1の部分と第2の部分との間の伝導熱の伝導を最小にするように構成されているセクションによって接合されている請求項18記載の装置。   The first and second portions are configured to minimize conduction of conduction heat between the first portion and the second portion while allowing continuous gas communication between the portions. The device of claim 18 joined by sections. 前記セクションは、それに隣接する第1及び第2のチャンバ部分の幅に比較して小さい幅を有する導管である請求項19記載の装置。   20. The apparatus of claim 19, wherein the section is a conduit having a width that is small compared to the width of the first and second chamber portions adjacent thereto. 1以上の熱伝導素子が第1及び第2の吸着剤材料と共に、第1及び第2の各チャンバ部分に配置されている請求項18乃至20のいずれか1項記載の装置。   21. Apparatus according to any one of claims 18 to 20, wherein one or more heat conducting elements are disposed in the first and second chamber portions together with the first and second adsorbent materials. 各熱伝導素子は、チャンバ部分の外部とその内部の吸着剤材料との間の熱の連通を高める金属のワイヤメッシュを具備しており、第1及び第2の各吸着剤材料を通して、気体の質量輸送速度を高めている請求項21記載の装置。   Each heat transfer element includes a metal wire mesh that enhances heat communication between the exterior of the chamber portion and the adsorbent material therein, through each of the first and second adsorbent materials. The apparatus of claim 21 wherein the mass transport rate is increased. 第1及び第2のチャンバ部分は、各流体とそれらの部分との間で熱を伝導するように、それぞれの流体の流れの中間流に位置されるようにそれぞれ構成されている請求項18乃至22のいずれか1項記載の装置。   19. The first and second chamber portions are each configured to be positioned in an intermediate flow of a respective fluid flow so as to conduct heat between each fluid and those portions. 23. The apparatus according to any one of items 22. 第1及び第2の材料は、それぞれチャンバのそれぞれの部分に詰められている請求項18乃至23のいずれか1項記載の装置。   24. Apparatus according to any one of claims 18 to 23, wherein the first and second materials are each packed in a respective portion of the chamber. 第1及び第2の材料は請求項12または13で規定されている請求項18乃至23のいずれか1項記載の装置。   24. An apparatus according to any one of claims 18 to 23, wherein the first and second materials are defined in claim 12 or 13. 第1の流体流から熱を連続的に伝導し、第2の流体流を連続的に冷却するためのシステムにおいて、システムは第1及び第2の流体流と熱的に連通することがそれぞれ可能な第1及び第2の装置を具備しており、各装置は、分離された第1及び第2の吸着剤材料を有しているチャンバを具備し、各装置は以下の段階で動作可能であり、即ち、
(1)前記第1の材料は、第1の材料に吸着された気体を脱着するように第1の流体流との熱的連通により加熱され、それによって、気体は第2の材料に送られて、
(2)前記第1の材料は、気体が第2の材料から脱着されるように冷却され、第1の材料へ再度吸着されるように、そこから送られ、第2の材料はそこから気体が脱着されることにより冷却され、第2の流体流は第2の材料との熱的連通により冷却され、
システムは、
前記第1の装置が段階(1)下で、第1の流体流を使用して第1の装置の第1の材料を加熱するように動作されながら、第2の装置が段階(2)下で、気体が第2の装置の第2の材料から脱着することにより第2の流体流を冷却するように動作され、
その後、第1の流体流は第2の装置へ誘導されることができ、第2の装置の段階(1)下で動作され、第2の流体流が第1の装置へ誘導され、第1の装置の段階(2)下で動作されて、
それによって、第1の流体流からの熱の連続的な伝導と、第2の流体流の連続的な冷却を効率的に行うことを特徴とするシステム。
In a system for continuously conducting heat from a first fluid stream and continuously cooling a second fluid stream, the system can be in thermal communication with the first and second fluid streams, respectively. First and second devices, each device comprising a chamber having separated first and second adsorbent materials, each device being operable in the following stages: Yes, that is,
(1) The first material is heated by thermal communication with the first fluid stream so as to desorb the gas adsorbed on the first material, whereby the gas is sent to the second material. And
(2) The first material is cooled so that the gas is desorbed from the second material and sent from there so that it is again adsorbed to the first material, from which the second material is gaseous And the second fluid stream is cooled by thermal communication with the second material,
the system,
While the first device is operated under step (1) to heat the first material of the first device using the first fluid stream, the second device is under step (2). And the gas is operated to cool the second fluid stream by desorbing from the second material of the second device;
Thereafter, the first fluid flow can be directed to the second device, operated under stage (1) of the second device, the second fluid flow directed to the first device, and the first device Operated under stage (2) of the equipment of
Thereby, a system for efficiently conducting continuous conduction of heat from the first fluid stream and continuously cooling the second fluid stream.
複数の第1の装置と複数の第2の装置とを具備している請求項26記載のシステム。   27. The system of claim 26, comprising a plurality of first devices and a plurality of second devices. 第1および第2の装置は並列に動作される請求項26または27記載のシステム。   28. The system of claim 26 or 27, wherein the first and second devices are operated in parallel. さらに、第1の装置と第2の装置との間、および第2の装置と第1の装置との間で、それぞれ第1及び第2の流体流の流動を選択的に切換えるための弁を具備しており、それによって、第1の流体流からの熱の連続的な伝導と、第2の流体流の連続的な冷却を維持する請求項26乃至28のいずれか1項記載のシステム。   And a valve for selectively switching the flow of the first and second fluid flows between the first device and the second device, and between the second device and the first device, respectively. 29. A system according to any one of claims 26 to 28, comprising, thereby maintaining continuous conduction of heat from the first fluid stream and continuous cooling of the second fluid stream. 第1及び第2の装置のそれぞれは請求項18乃至25のいずれか1項に規定されている構成である請求項26乃至29のいずれか1項記載のシステム。   30. The system according to any one of claims 26 to 29, wherein each of the first and second devices is configured as defined in any one of claims 18 to 25. 第1及び第2の装置のそれぞれは請求項1乃至17のいずれか1項で記載されている方法を使用して動作される請求項26乃至30のいずれか1項記載のシステム。   31. A system according to any one of claims 26 to 30, wherein each of the first and second devices is operated using the method described in any one of claims 1 to 17.
JP2006549786A 2004-01-28 2005-01-25 Heat transfer method, heat transfer apparatus and system Pending JP2007519881A (en)

Applications Claiming Priority (2)

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AU2004900376A AU2004900376A0 (en) 2004-01-28 Method, apparatus and system for transferring heat
PCT/AU2005/000083 WO2005073644A1 (en) 2004-01-28 2005-01-25 Method, apparatus and system for transferring heat

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JP2007519881A JP2007519881A (en) 2007-07-19
JP2007519881A5 true JP2007519881A5 (en) 2008-03-13

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US (1) US20080229766A1 (en)
EP (1) EP1711755A4 (en)
JP (1) JP2007519881A (en)
CN (1) CN1961184B (en)
AU (1) AU2005207978B2 (en)
WO (1) WO2005073644A1 (en)

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