Device for the adsorption treatment of a fluid or fluid stream
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
B01D-053/04
H01M-008/06
B01D-053/02
F16L-037/60
출원번호
US-0640861
(2011-04-13)
등록번호
US-9149756
(2015-10-06)
우선권정보
DE-10 2010 014 890 (2010-04-14); DE-20 2010 014 363 U (2010-04-14); DE-20 2010 016 522 U (2010-04-14)
국제출원번호
PCT/EP2011/055785
(2011-04-13)
§371/§102 date
20121213
(20121213)
국제공개번호
WO2011/128363
(2011-10-20)
발명자
/ 주소
Anfang, Hans-Georg
Hamel, Christian
Modl, Norbert
출원인 / 주소
Clariant Produkte (Deutschland) GmbH
대리인 / 주소
Bisulca, Anthony A.
인용정보
피인용 횟수 :
0인용 특허 :
9
초록▼
A device for adsorption treatment of a fluid or fluid stream, comprising a container for receiving adsorber material, wherein the container has a fluid inlet opening and a fluid outlet opening, and two fluid connection devices, wherein one of the fluid connection devices is provided at the fluid inl
A device for adsorption treatment of a fluid or fluid stream, comprising a container for receiving adsorber material, wherein the container has a fluid inlet opening and a fluid outlet opening, and two fluid connection devices, wherein one of the fluid connection devices is provided at the fluid inlet opening and the other one of the fluid connection devices is provided at the fluid outlet opening, wherein the fluid connection devices are locked in a fluid-tight manner and are designed in such a way that they can each be connected to a fluid line connector and unlocked and, if they are connected to the respective fluid line connector they can be unlocked or are unlocked.
대표청구항▼
1. A device for the adsorption treatment of a fluid or fluid stream, comprising: a container for receiving adsorber material, wherein the container has a fluid inlet and a fluid outlet, and two fluid connection devices, wherein one of the fluid connection devices is provided at the fluid inlet and t
1. A device for the adsorption treatment of a fluid or fluid stream, comprising: a container for receiving adsorber material, wherein the container has a fluid inlet and a fluid outlet, and two fluid connection devices, wherein one of the fluid connection devices is provided at the fluid inlet and the other fluid connection device is provided at the fluid outlet, wherein the fluid connection devices are locked fluid-tight and are formed such that they can each be connected to a fluid line connection piece and unlocked, and on condition that they are connected to the respective fluid line connection piece, can be or are unlocked, wherein: the fluid connection devices each have a fluid throughflow duct and a moveable closure body, wherein the closure body closes the fluid throughflow duct fluid tight, wherein the fluid connection devices are formed such that the respective closure body is moved by connecting the fluid connection device to the fluid line connection piece and the fluid throughflow duct opens and/or is moved by detaching the fluid line connection piece, and closes the fluid throughflow duct, and a gas-tight connection of the gas pipe to the gas connector is produced; and wherein the fluid connection devices are formed such that the fluid line connection pieces are secured when the fluid connection devices are unlocked. 2. The device according to claim 1, wherein the unlocked fluid connection devices secure the fluid line connection pieces; and/or wherein the fluid connection devices are formed such that they can be manually or automatically locked by means of the respective fluid line connection pieces; and/orwherein at least one of the fluid connection devices is formed such that it can be successively or simultaneously connected to and unlocked from the respective fluid line connection piece. 3. The device according to claim 1, further comprising two fluid line connection pieces which are formed such that they can each be connected to one of the fluid connection devices and a fluid line. 4. The device according to claim 1, wherein the container contains one or more adsorber materials; and/or the container contains one or more adsorber materials for desulfurizing liquid gas, gas, natural gas or other hydrocarbons; and/orthe container contains several adsorber materials and the adsorber materials are present in a mixed bed or as multi-component adsorber material. 5. The device according to claim 1, further comprising a thermally activating fluid shutoff apparatus and/or a fluid flow controller. 6. The device according to claim 1, wherein for reversible filling with the adsorber material the container comprises an opening and closing element which has a safety device to prevent manipulations by unauthorized persons, selected from: a cover for the opening and closing element and a special screw connection which can be opened exclusively by a special tool. 7. The device according to claim 1, wherein the container is formed such that it can be installed vertically and have, adjoining the fluid inlet, a cavity, or a cavity with a filling or bounding of porous and/or flexible inert material or plastic foam filling, for trapping condensate; and/or wherein the device and/or the adsorber material used are formed such that they can be used at temperatures of from −10 to +90° C. and a pressure range of from −500 mbar over atmospheric pressure to +10 bar over atmospheric pressure. 8. The device according to claim 1, wherein the container has a feedstock length-to-feedstock diameter ratio of from 0.1 to 40; and/or wherein a space velocity of <10.000 h−1 relative to the total quantity of the adsorber material is set in the container; and/orwherein the feedstock-to-particle diameter ratio is greater than 10. 9. The device according to claim 1, wherein the outer length of the container between the fluid inlet and the fluid outlet is in a range of from 700 to 800 mm or 729 mm. 10. The device according to claim 1, wherein the device including the fluid connection devices is in the range of from 850 mm to 900 mm, or 871 mm, long. 11. The device according to claim 1, wherein the container has an external diameter of 110 mm and/or an internal diameter of 90 mm. 12. The device according to claim 1, wherein the container is 717 mm long and a first opening selected from the fluid inlet and the fluid outlet comprises a tube piece 33 mm long; and/or wherein a press connector is provided in the tube section and this is connected to the associated fluid connection device. 13. The device according to claim 1, wherein in a second opening selected from the fluid inlet and the fluid outlet a screw connection or bulkhead connection is provided; and/or wherein the bulkhead connection extends the container by 6 mm. 14. The device according to claim 1, wherein the fluid connection devices each have a shape bent at a 90° angle; and/or wherein the fluid connection devices each have, at their respective free end, a connection opening for connection to the respective fluid line connection piece, wherein the distance between the centres of the connection openings is between 835 and 850 mm or is 839 mm. 15. A method of desulfurizing a combustion fluid, in particular natural gas or liquefied gas, for fuel cells, comprising subjecting a fluid or fluid stream to an adsorption treatment with the device according to claim 1. 16. A method for regenerating and/or disposing of, filling and/or installing a device for the adsorption treatment of a fluid or fluid stream according to claim 1, comprising at least one of the steps: removing the device for the adsorption treatment of a fluid or fluid stream according to claim 1, the container of which contains adsorber material to be regenerated and/or disposed of, from an apparatus at or in which an adsorption treatment has been carried out, by detaching the fluid connection devices from the fluid line connection pieces which are connected to the apparatus;transporting the container with the adsorber material to be regenerated and/or disposed of and locked fluid line connection pieces while the container is filled with fluid which has been treated or is to be treated; transporting the container with the adsorber material to be regenerated and/or disposed of and locked fluid connection devices to a regeneration and/or disposal station;flushing the container which contains adsorber material to be regenerated and/or disposed of, with gas, protective gas, inert fluid, inert gas or air; emptying the container of the adsorber material to be regenerated and/or disposed of;removing and/or regenerating the adsorber material to be regenerated and/or disposed of;filling the container with regenerated or unused adsorber material;flushing the container with protective gas, inert fluid, inert gas or the fluid which no longer contains an adsorbate to be removed by the adsorption treatment, during and/or after filling the container with the regenerated or unused adsorber material; carrying out a pressure and/or leak test to check the tightness of the filled container with locked fluid connection devices;transporting the container with the regenerated or unused adsorber material and locked fluid connection devices while the container is filled with protective gas, inert fluid or inert gas;transporting the container with the regenerated or unused adsorber material and locked fluid connection devices to an apparatus at or in which an adsorption treatment is to be carried out; connecting fluid line connection pieces to the apparatus at or in which an adsorption treatment is to be carried out;installing the device for the adsorption treatment of a fluid or fluid stream according to claim 1 at or in an apparatus at or in which an adsorption treatment is to be carried out while the container is filled with regenerated or unused adsorber material and an element selected from protective gas, inert fluid, inert gas or the fluid which no longer contains an adsorbate to be removed by the adsorption treatment by connecting the fluid connection devices to fluid line connection pieces which are connected to the apparatus. 17. The method according to claim 16, wherein the apparatus is a fuel cell or a gas compressor of a fuel cell; and/or wherein the device for the adsorption treatment of a fluid or fluid stream or the apparatus is an adsorbate detector or sulfur detector, and the regeneration and/or disposing of the device for the adsorption treatment of a fluid or fluid stream is carried out according to whether an adsorbate or sulfur compounds have been detected; and/or wherein the apparatus is provided with at least one shutoff valve which is installed in flow direction before or after the device for the adsorption treatment of a fluid or fluid stream. 18. A method for the adsorption treatment of a fluid or fluid stream, in particular for desulfurizing natural gas or liquefied gas for fuel cells, comprising: providing a device for the adsorption treatment of a fluid or fluid stream according to claim 1, wherein the container has been or is filled with an adsorber material for the adsorption treatment of a fluid or fluid stream, connecting a fluid feed pipe to a first fluid line connection piece and a fluid drainage pipe to a second fluid line connection piece,connecting the first and second fluid line connection piece to the two fluid connection devices of the device for the adsorption treatment of a fluid or fluid stream and thereby unlocking the fluid connection devices, andintroducing a fluid in or passing a fluid through the device for the adsorption treatment of the fluid. 19. The method according to claim 18, wherein the fluid is passed vertically from bottom to top through the device for the adsorption treatment of a fluid or fluid stream. 20. The method according to claim 18, wherein the device for the adsorption treatment of a fluid or fluid stream is operated in combination with an adsorbate detector or sulfur detector and a replacement or a regeneration and/or disposing of the device is carried out according to whether an adsorbate or sulfur compounds have been detected; and/orwherein the device for the adsorption treatment of a fluid or fluid stream is operated in combination with a shutoff valve which is installed in flow direction in front of or after the container. 21. The method according to claim 18, wherein the fluid has a purity of <50 ppb residual sulfur after being passed through the device. 22. The method according to claim 18, wherein the fluid is passed through the device at temperatures of from −10 to +90° C. and a pressure in a pressure range of from −500 mbar over atmospheric pressure to +10 bar over atmospheric pressure. 23. The method according to claim 18, wherein the container has a feedstock length-to-feedstock diameter ratio of from 0.1 to 40; and/or wherein a space velocity of <10.000 h-1 relative to the total quantity of the adsorber material is set in the container; and/orwherein the feedstock-to-particle diameter ratio is greater than 10.
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