EP3261748A1 - Verfahren zum herstellen eines horizontal durchströmten adsorbers und trennwandmodul zur verwendung in diesem verfahren - Google Patents
Verfahren zum herstellen eines horizontal durchströmten adsorbers und trennwandmodul zur verwendung in diesem verfahrenInfo
- Publication number
- EP3261748A1 EP3261748A1 EP16703713.4A EP16703713A EP3261748A1 EP 3261748 A1 EP3261748 A1 EP 3261748A1 EP 16703713 A EP16703713 A EP 16703713A EP 3261748 A1 EP3261748 A1 EP 3261748A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- partition
- vertical
- module
- partition wall
- adsorber
- 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.)
- Withdrawn
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0431—Beds with radial gas flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0423—Beds in columns
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28052—Several layers of identical or different sorbents stacked in a housing, e.g. in a column
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/3092—Packing of a container, e.g. packing a cartridge or column
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/002—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor with a moving instrument
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
- B01J8/0214—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0403—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0403—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal
- B01J8/0407—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds
- B01J8/0411—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds the beds being concentric
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/414—Further details for adsorption processes and devices using different types of adsorbents
- B01D2259/4141—Further details for adsorption processes and devices using different types of adsorbents within a single bed
- B01D2259/4145—Further details for adsorption processes and devices using different types of adsorbents within a single bed arranged in series
- B01D2259/4146—Contiguous multilayered adsorbents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00752—Feeding
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00769—Details of feeding or discharging
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00823—Mixing elements
- B01J2208/00831—Stationary elements
- B01J2208/0084—Stationary elements inside the bed, e.g. baffles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00938—Flow distribution elements
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
- B01J2208/023—Details
- B01J2208/024—Particulate material
- B01J2208/025—Two or more types of catalyst
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/56—Use in the form of a bed
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/66—Other type of housings or containers not covered by B01J2220/58 - B01J2220/64
Definitions
- Partition module for use in this method
- the invention relates to a method according to the preamble of patent claim 1.
- a horizontal flow adsorber contains an adsorption bed and can be constructed as a horizontal or vertical container; that is, it is either longer than high or higher than wide. It is designed so that the adsorption bed is flowed through horizontally during operation.
- a special type of standing adsorber is formed by a radial adsorber. It has long been known to use radial adsorbers for adsorptive separation and purification processes, for example for cleaning feed air for a cryogenic air separation plant. Such a
- Essentially cylindrical symmetry and contains at least two cylindrical baskets in a container, which define an annular adsorption bed.
- External space between the outermost basket and the container wall serve for the inflow and outflow of a fluid that is to be cleaned or separated.
- the container height of a radial adsorber is significantly larger than its diameter. Typical values are 3 to 25 m for the height and 2 to 8 m for the diameter.
- the invention has for its object to find a manufacturing method of the type mentioned above and suitable tools that a filling of a Allow horizontally flowed adsorber with two or more directly adjacent beds with relatively little effort.
- no one-piece ring as a separating ring or - in a flat boundary layer - no one-piece wall is used as a flat partition, but the separating ring / the flat partition wall consists of a plurality of partition modules horizontally strung together the separating ring / the flat Form partition.
- the number of partitioning modules for a separating ring / flat partition wall is, for example, 3 to 25, preferably 6 to 18.
- Their height is for example between 0.3 m and 1 m, preferably between 0.4 m and 0.6 m. While a massive dividing ring or a massive flat dividing wall one
- the individual partition modules are much easier to handle. They can be moved up by hand.
- no special filling devices or other auxiliary devices are necessary, which would have to be introduced into the container.
- the production process according to the invention is particularly variable; For example, the partition modules may even be removed from the container after filling. It should be noted that the
- Containers with catalyst beds are particularly advantageous.
- Radial adsorber and the partition are formed by a circular separator ring, wherein the container of the radial adsorber has a cylindrical outer wall and two cylindrical baskets that limit the adsorption.
- Spacers are arranged, which connect the partition module temporarily to the outer basket, and these spacers are removed at the beginning of the next step (b) and reattached after moving the partition module.
- at least two spacers are used for each partition wall module.
- the spacers allow a precise adjustment of the partition wall modules and thus of the entire separating ring.
- the layer thickness of the beds can be kept very precisely constant.
- the spacers allow compliance with the layer thickness, even if on the inside of the outer basket in certain vertical distances reinforcing rings or similar installations are present. The fixation of the spacers then takes place just above these reinforcing rings.
- the spacers are preferably connected by hooking on the outer basket with the outer basket.
- the outer end of the spacers is designed so that it can engage in one of these slots.
- the spacers can be engaged with one handle in the basket and released from it again and it still creates a stable connection.
- each partition module has a means for sealing
- This means can be formed in particular by an angle bar along one of the two vertical edges of the partition module.
- the opening angle of the angle bar is between 30 and 120 °.
- an effective seal can be achieved, which prevents the unwanted mixing of both adsorbents. This can be a clear and clean interface between the two beds are generated.
- the angle bar can be formed by an angle plate.
- the angle bar is arranged so that the vertical edge of the adjacent
- Partition module is guided in the angle. This hinders this
- FIG. 1 shows a cross section through a partially filled radial adsorber
- Figure 3 is a perspective view of a partition module and Figures 4 and 5 a spacer in detail.
- the horizontal image plane of Figure 1 cuts through the cylindrical outer wall 1 of the container of a Radialadsorber.
- This contains in the embodiment, two baskets, an outer basket 2 and an inner basket 3, which are also intersected by the image plane.
- This opens the view for a plan view of two already partially filled beds, a first, outer bed 4 and a second, inner bed 5.
- the separating ring is adjusted by means of spacers 7.01 a to 7.1 1 b relative to the outer basket 2.
- the spacers engage in the slots that has the outer basket.
- the inner basket also has such slots to be gas-permeable and elastic in the axial direction, see details
- EP 402783 A2 US 5827485)
- a first adsorbent - in the example Alugel - is filled via a hose between the outer basket 2 and the separator ring 6 until about 80% of the height of the partition wall elements is reached.
- the introduced first adsorbent forms a first part of a first bed 4.
- a second adsorbent-in the example a molecular sieve of the 13X type- is likewise introduced via a hose into the adjacent space between separating ring 6 and inner basket 3, as a rule up to approximately the same height as the first adsorbent. Then the partially filled
- step (b) is then repeated until the desired filling level is reached. Subsequently, the partition modules can be completely out of the beds
- the partition modules Before the start of the filling, the partition modules can be reversed over the manhole; it is not necessary to introduce them - like a solid separating ring - before the container is welded together.
- Figure 2 shows a section of the height of the container in longitudinal section along the cylinder axis 8 in the partially filled state.
- the Partition module 6.01 is the step (b) already for both beds 4, 5
- a single partition module is shown in detail in FIG. Its essential component is a solid metal wall 10, which has the shape of a circular arc section.
- the upper edge is reinforced by a likewise correspondingly bent angle plate.
- two handles 1 1 a, 11 b are attached, which facilitate the removal from the beds much easier and faster.
- holes 12 in the upper edge At both ends are holes 12 in the upper edge. In this a U-shaped connecting element 12a is inserted, which allows a secure coupling with the adjacent partition module 6.02 (see Figure 1).
- the bending edge is connected to the edge of the metal wall, preferably by a welded joint.
- the interior angle of the angle bar is oriented towards the adjacent partition wall module.
- This guide also causes a seal against the particles of the bed, so that no unwanted mixing of the two adsorbents occurs when pulling out.
- FIG. 3 also shows the spacers 7.01a and 7.01b, the structure and function of which will now be explained in greater detail on the basis of the detailed illustration in FIGS. 4 and 5.
- the spacer has an angled portion 15 which engages in the mounted state in one of the slots of the basket.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Separation Of Gases By Adsorption (AREA)
- Fencing (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102015002260.1A DE102015002260A1 (de) | 2015-02-25 | 2015-02-25 | Verfahren zum Herstellen eines horizontal durchströmten Adsorbers und Trennwandmodul zur Verwendung in diesem Verfahren |
| EP15000897.7A EP3061514A1 (de) | 2015-02-25 | 2015-03-26 | Verfahren zum herstellen eines horizontal durchströmten adsorbers und trennwandmodul zur verwendung in diesem verfahren |
| PCT/EP2016/000130 WO2016134816A1 (de) | 2015-02-25 | 2016-01-26 | Verfahren zum herstellen eines horizontal durchströmten adsorbers und trennwandmodul zur verwendung in diesem verfahren |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP3261748A1 true EP3261748A1 (de) | 2018-01-03 |
Family
ID=53016428
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP15000897.7A Withdrawn EP3061514A1 (de) | 2015-02-25 | 2015-03-26 | Verfahren zum herstellen eines horizontal durchströmten adsorbers und trennwandmodul zur verwendung in diesem verfahren |
| EP16703713.4A Withdrawn EP3261748A1 (de) | 2015-02-25 | 2016-01-26 | Verfahren zum herstellen eines horizontal durchströmten adsorbers und trennwandmodul zur verwendung in diesem verfahren |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP15000897.7A Withdrawn EP3061514A1 (de) | 2015-02-25 | 2015-03-26 | Verfahren zum herstellen eines horizontal durchströmten adsorbers und trennwandmodul zur verwendung in diesem verfahren |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US20180126319A1 (de) |
| EP (2) | EP3061514A1 (de) |
| JP (1) | JP2018512266A (de) |
| KR (1) | KR20170120663A (de) |
| CN (1) | CN107405562A (de) |
| BR (1) | BR112017016786A2 (de) |
| CA (1) | CA2982967A1 (de) |
| CL (1) | CL2017002102A1 (de) |
| DE (1) | DE102015002260A1 (de) |
| RU (1) | RU2017133118A (de) |
| TW (1) | TW201637705A (de) |
| WO (1) | WO2016134816A1 (de) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10576455B2 (en) | 2018-03-22 | 2020-03-03 | Air Products And Chemicals, Inc. | Particle loading method and apparatus for a radial flow vessel |
| PL3542894T3 (pl) | 2018-03-22 | 2025-05-19 | Air Products And Chemicals, Inc. | Sposób i urządzenie do ładowania cząstek do zbiornika o przepływie promieniowym |
| FR3093009B1 (fr) | 2019-02-21 | 2021-07-23 | Air Liquide | Procédé et installation de purification d’un flux gazeux de débit élevé |
| FR3093008B1 (fr) * | 2019-02-21 | 2021-01-22 | Air Liquide | Installation et procédé de séparation des gaz de l’air à basse pression |
| FR3093169B1 (fr) | 2019-02-21 | 2021-01-22 | Air Liquide | Installation et procédé de séparation des gaz de l’air mettant en œuvre un adsorbeur de forme parallélépipèdique |
| EP3901606A1 (de) * | 2020-04-20 | 2021-10-27 | Catalytic Instruments GmbH & Co. KG | Thermodenuder und verfahren zur entfernung von halbflüchtigem material und von halbflüchtigen partikeln aus einem aerosol |
| CN113959180A (zh) * | 2021-10-28 | 2022-01-21 | 上海二十冶建设有限公司 | 一种空分装置制氧工艺快速联调试车方法 |
| CN114191934A (zh) * | 2021-11-18 | 2022-03-18 | 上海二十冶建设有限公司 | 一种分子筛填充工装及其使用方法 |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2541588B1 (fr) * | 1983-02-28 | 1985-07-05 | Air Liquide | Recipient et installation d'epuration par adsorption |
| DE3919750A1 (de) | 1989-06-16 | 1990-12-20 | Linde Ag | Reaktor |
| US5837021A (en) | 1994-12-09 | 1998-11-17 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Installation for the treatment of at least one fluid, by passage through two adjacent masses of material |
| FR2727875B1 (fr) * | 1994-12-09 | 1997-03-21 | Air Liquide | Installation de traitement d'au moins un fluide, applications au traitement d'un flux d'air et procede de chargement d'une masse de materiau particulaire d'une telle installation |
| US5836362A (en) * | 1997-07-15 | 1998-11-17 | Praxair Technology, Inc. | Multiple adsorbent loading method and apparatus for a radial flow vessel |
| US6379433B1 (en) * | 2000-10-25 | 2002-04-30 | Delbert C. Scranton, Jr. | Device for use in filtering contaminated air |
-
2015
- 2015-02-25 DE DE102015002260.1A patent/DE102015002260A1/de not_active Withdrawn
- 2015-03-26 EP EP15000897.7A patent/EP3061514A1/de not_active Withdrawn
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2016
- 2016-01-26 JP JP2017545394A patent/JP2018512266A/ja active Pending
- 2016-01-26 KR KR1020177026922A patent/KR20170120663A/ko not_active Withdrawn
- 2016-01-26 WO PCT/EP2016/000130 patent/WO2016134816A1/de not_active Ceased
- 2016-01-26 EP EP16703713.4A patent/EP3261748A1/de not_active Withdrawn
- 2016-01-26 RU RU2017133118A patent/RU2017133118A/ru not_active Application Discontinuation
- 2016-01-26 US US15/551,798 patent/US20180126319A1/en not_active Abandoned
- 2016-01-26 BR BR112017016786A patent/BR112017016786A2/pt not_active Application Discontinuation
- 2016-01-26 CN CN201680012380.8A patent/CN107405562A/zh active Pending
- 2016-01-26 CA CA2982967A patent/CA2982967A1/en not_active Abandoned
- 2016-02-24 TW TW105105535A patent/TW201637705A/zh unknown
-
2017
- 2017-08-17 CL CL2017002102A patent/CL2017002102A1/es unknown
Also Published As
| Publication number | Publication date |
|---|---|
| BR112017016786A2 (pt) | 2018-04-17 |
| EP3061514A1 (de) | 2016-08-31 |
| CL2017002102A1 (es) | 2018-05-18 |
| CN107405562A (zh) | 2017-11-28 |
| WO2016134816A1 (de) | 2016-09-01 |
| KR20170120663A (ko) | 2017-10-31 |
| RU2017133118A (ru) | 2019-03-25 |
| JP2018512266A (ja) | 2018-05-17 |
| RU2017133118A3 (de) | 2019-04-15 |
| CA2982967A1 (en) | 2016-09-01 |
| US20180126319A1 (en) | 2018-05-10 |
| DE102015002260A1 (de) | 2016-08-25 |
| TW201637705A (zh) | 2016-11-01 |
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