Patent Grant
11059029
The present invention relates to a method for manufacturing an adsorption agent for treating compressed gas, more specifically an adsorption agent that can be used for drying compressed gas, for example compressed air.
Adsorption devices are already known in the form of drying devices for compressed gas, whereby these drying devices comprise a vessel in which a drying agent, or desiccant, is placed. The vessel concerned is provided with an inlet for supplying a compressed gas to be dried, and an outlet for removing dried gas.
The drying agent concerned is generally realised in the form of a regeneratable drying agent, or in other words a drying agent that can be regenerated after reaching a certain degree of saturation. It is indeed the case that as the drying agent extracts moisture from the gas to be dried, this drying agent will become increasingly saturated with adsorbed moisture. Hence, it is usual, after using the drying agent for a certain time to dry compressed gas, to regenerate this drying agent, for example by exposing it to a regeneration gas flow that extracts the moisture from the drying agent. Such a regeneration gas flow can consist of a fraction of the dried gas and/or hot gas for example whose relative humidity is sufficiently low to be able to realise the regeneration of the drying agent.
In some embodiments of drying devices for compressed gas, use is made of two or more vessels of drying agent. With two vessels this principle of drying device is also referred to as a twin tower dryer. In such a type of drying device a compressed gas, for example originating from a compressor, can be passed through the first of the aforementioned vessels for example, where it will be dried by the drying agent in the vessel concerned, after having passed through an after cooler and a condensate separator (which may or may not form part of the after cooler concerned). This vessel consequently acts as a drying vessel.
At the same time, a regeneration gas flow can be guided through a second aforementioned vessel in order to regenerate the drying agent in that second vessel by extracting the moisture from this drying agent. This can be done by making use of a gas that has already been dried, for example, that is tapped off downstream from the drying vessel for example and/or by supplying a gas flow that has been heated, for example by recovering the heat generated in the compressor during the compression. In this last case it is called a “heat of compression” or HOC dryer.
When the drying agent in the drying vessel has reached a certain degree of saturation, the gas flows through the first and the second vessel can be changed over, such that the drying agent in the first vessel will now be regenerated by a regeneration gas flow while the second vessel will take on the role of drying vessel. In this way the two or more vessels will alternately operate as a drying pressure vessel and a regenerating pressure vessel, such that continuity in the drying process can be realised. Examples of such drying devices with a number of vessels are described for example in US 2003/023.941, U.S. Pat. No. 4,783,432, U.S. Pat. No. 6,375,722, EP 1.776.171 and WO 2006/050.582.
The drying agent that is used in such drying devices with a number of vessels often consists of grains of silica gel, activated alumina or a molecular sieve material, or a combination thereof. As is known activated alumina is produced by thermal dehydration or activation of aluminium hydroxide Al(OH)3, while molecular sieves consist of synthetic zeolites (crystalline aluminosilicates).
A limitation of such a type of drying device that comprises a drying agent in a granular form, consists of the gas speeds through the vessels having to be limited in order to counteract grains moving against one another or even fluidisation. Indeed, due to the grains being set in motion friction will occur between them, which in turn leads to dust formation and a reduced drying capacity. Other causes of such dust formation are for example pressure variations and/or thermal shocks. Moreover, the pressure drop across a twin tower dryer is relatively high and the desiccant grains have a rather high thermal mass.
Alternative drying devices are known for compressed gas, whereby the drying agent is placed in a rotating drum, while a drying zone and regeneration zone extend in the vessel. During the operation of such a drying device, the drying drum will be made to rotate by drive means provided to this end, such that the drying agent in this drying drum will alternately be taken through the drying zone and the regeneration zone. The compressed gas to be dried will be guided through the drying zone, while the regeneration gas flow is guided through the regeneration zone, in order to realise simultaneous drying of compressed gas in the drying zone and regeneration of the drying agent in the regeneration zone.
Examples of such drying devices that are provided with a rotating drying drum are described for example in WO 00/033.943, WO 00/074.819, WO 01/078.872, WO 01/087.463, WO 02/038.251, WO 2007/079533, WO 2005/070.518, WO 2006/012.711, GB 1.226.348, GB 1.349.732, GB 1.426.292, U.S. Pat. No. 3,490,201, U.S. Pat. No. 5,385,603 and U.S. Pat. No. 8,349,054.
The drying agent or desiccant that is used in the known drying devices for drying compressed gas consists of silica gel, molecular sieves, activated alumina or a combination thereof, for example. As is known, the drying agent can be affixed on a support such as a corrugated structure of glass fibres or ceramic fibres that are rolled up for example to form a honeycomb structure in the vessel, for example as described in U.S. Pat. No. 5,683,532.
In practice it turns out that with the known drying devices for drying compressed gas, under certain conditions such as in the event of insufficient regeneration of the drying agent and oversaturation thereof, the drying agent goes through a complex breakdown process that in some cases can ultimately result in the failure of the drying device, for example in the case of silica gel as a drying agent in a rotor, because the binder function of the silica gel decreases, which leads to a loss of structural strength of the supporting glass fibre matrix, and also because the adsorbing function of the silica gel decreases as a result of hydrolisation and breakdown of the silica gel structure.
Thus the adsorption behaviour and adsorption capacity of a silica gel rotor, in heavy conditions of high moisture and high temperature will substantially change during the useful life of the rotor.
The purpose of the present invention is to provide a method for manufacturing an improved adsorption agent for treating compressed gas, whereby this adsorption agent provides a solution to one or more of the disadvantages attached to the conventional, known adsorption agents.
To this end the invention concerns a method for manufacturing an adsorption agent for treating compressed gas, whereby this method comprises the following steps:
An advantage of the adsorption agent obtained with this method is that there is no risk of grains moving against one another or even fluidisation of such an adsorption agent during use in an adsorption device for treating compressed gas, as loose grains of adsorption agent are not used. As a result dust formation is prevented, while a relatively high flow speed of the compressed gas to be dried through the drying device is possible.
In addition the drying agent thus obtained enables it to be affixed in a drying device in whatever spatial orientation during use, such as vertical, sloping or even horizontal, which is not possible with conventional drying agents that are granular, as the horizontal use of such granular drying agents can lead to a rearrangement of the grains and the formation of internal leakage paths and consequently reduced dryer performance.
According to a preferred characteristic of the invention, the aforementioned monolithic supporting structure comprises one or more of the following materials: ceramic material, metal foil, a fibre structure and a polymer. Particularly good results are obtained with the use of a ceramic structure that contains cordierite.
Preferably the aforementioned adsorbent contains one or more of the following materials: a zeolite, silica gel, activated alumina, activated carbon, metal organic frameworks, carbon molecular sieve (CMS), an impregnated adsorbent and a hybrid. In particular a hydrophilic zeolite support is preferable. Good results are obtained by making use of faujasite zeolite type X, in which the silicon/aluminium ratio is between 2 and 3.
The present invention also relates to an adsorption agent obtained with the method according to claim 1, whether or not in combination with the characteristics of one or more of the claims following on from it.
The invention also relates to an adsorption device for drying compressed gas, whereby this adsorption device comprises an adsorption agent obtained with the method according to the invention.
With the intention of better showing the characteristics of the present invention, a few preferred variants of a method according to the invention for manufacturing an adsorption agent for treating compressed gas are described hereinafter by way of an example, without any limiting nature, with reference to the accompanying drawings, wherein:
Essentially the method according to the invention for the manufacture of an adsorption agent for treating compressed gas consists of a step 1A of providing a monolithic supporting structure and a step 1B consisting of the production of a coating suspension that contains an adsorbent.
In the next step 2 the aforementioned coating suspension is applied to the aforementioned supporting structure to form a coating and, finally, in step 3 a thermal treatment is applied to the resulting supporting structure with the coating obtained after step 2, in order to sinter the aforementioned coating in order to finally obtain an improved adsorption agent.
According to a preferred, but not necessary, characteristic of the invention a ceramic structure that contains cordierite, for example Celcor© by Corning, is selected for the monolithic supporting structure.
Alternatively, according to the invention, other materials can also be used for the manufacture of the supporting structure concerned, such as:
It goes without saying that the aforementioned list is not exhaustive and the use of other materials is not excluded.
According to the invention, it is not excluded either that the monolithic supporting structure is made of a combination of two or more of the aforementioned and/or other materials.
According to a preferred characteristic of the invention the material from which the supporting structure is made preferably contains between 200 and 1200 CPSI (cells per square inch), and more preferably between 350 and 450 CPSI.
The wall thickness of the supporting structure is preferably between 2 and 11 mil (milli-inch), and more preferably between 3 and 9 mil, and even more preferably between 5 and 7.5 mil. In a most preferred embodiment, the wall thickness is between 6 and 7 mil, preferably approximately 6.5 mil.
The porosity of the wall of the supporting structure is preferably greater than 5%, and more preferably greater than 10%, and even better greater than 20%.
The cells formed preferably have a square shape, but can present other shapes such as triangular, sinusoidal, circular, hexagonal and similar.
Step 1B of the production of the coating suspension preferably comprises the following sub-steps:
In sub-step 1BY preferably one or more of the following and/or other materials are selected as an adsorbent:
The above list is not exhaustive and other materials are also possible according to the invention. The choice of adsorbent depends on what treatment the gas to be treated must go through, such as drying or the selective removal of other molecules such as oxygen or carbon dioxide for example, when using the adsorption means in a nitrogen generator or similar, whereby the gas to be treated can be compressed air for example.
The distribution of the particle size of the adsorbent is preferably such that D50 is less than 10 μm and more preferably less than 4 μm.
The aforementioned binder material that is added in the third sub-step 1BZ preferably contains an inorganic binder material such as:
Moreover, if need be use can be made of an organic binder material such as:
According to a possible characteristic of the invention, step 1B of the production of the coating suspension comprises the addition of one or more additives, such as an additive to affect the acidity (pH value), for example hydrogen chloride (HCl) to decrease the pH or ammonia (NH3) to increase the pH, and/or an additive to counteract foam formation. For example, but not strictly necessary, the pH value is brought between 9 and 11 and more preferably between 9.5 and 10.5.
The second sub-step 1BY of the addition of an adsorbent to the aforementioned solvent to form a mixture preferably comprises:
According to an additional preferred aspect of the invention, after mixing the adsorbent in the solvent, the adsorbent particles are reduced in size in order to obtain the aforementioned preferred particle size, for example by wet milling. Examples of wet milling are attrition milling, roll milling or immersion milling.
The coating suspension obtained after step 1B is preferably a shear thinning liquid, which upon the action of shear stress presents a reduced viscosity.
Step 2 of the method according to the invention, consisting of the application of the aforementioned coating suspension on the aforementioned supporting structure, preferably consists of flushing or perfusing the supporting structure with the coating suspension concerned.
Preferably the perfusion of the supporting structure is done from bottom to top or in other words in the opposite direction to gravity, for example by pumping means provided to this end that either pump the coating suspension upwards through the supporting structure or sucks up the coating suspension through the supporting structure, preferably until all channels through the supporting structure have been filled with coating material.
Then the pumping means can be switched off in order to let the surplus coating material flow out of the channels. Alternatively the operating direction of the pumping means concerned can be reversed such that an active evacuation of surplus coating material from the channels is obtained.
According to a particular preferred aspect of the invention, a part of the surplus coating material can be evacuated from the supporting structure by applying one or more pressure pulses of a purge gas through the channels of the supporting structure. An example of such a purge gas is air.
Good results are obtained in particular when using a shear thinning coating suspension with such active evacuation of the channels in the supporting structure.
After any removal of surplus coating material the coated supporting structure may be left to dry, for example in ambient conditions, until the solvent has largely evaporated. When water is used as a solvent, for example, this drying can be done in the surrounding air.
In a last step 3 of the method according to the invention the resulting supporting structure with coating, as obtained after step 2, is subject to a thermal treatment in order to sinter the coating.
During this thermal treatment the aforementioned resulting supporting structure is exposed to a temperature of preferably more than 400° C., and even more preferably more than 500° C., and in a most preferred embodiment a temperature of 550° C.
Of course numerous variant temperature variations may be applied during this thermal treatment. A non-limiting example is shown in
At the start time t0 of step three, the temperature is equal to the ambient temperature, in this example 20° C. The temperature is raised slowly, in this case at a rate of 50° C. per hour, and in this example for a period of 10 hours 36 minutes. At time t1, i.e. 10 hours and 36 minutes after time t0, in this case the temperature will consequently have risen to 550° C.
Preferably the period of increasing temperature is followed by a period in which the temperature is kept constantly high, preferably above 400° C. and better above 500° C. In this non-exhaustive example the time interval in which the temperature is kept high is 1 hour. At the end of this time interval in which in this example the temperature is kept at 550° C. for 1 hour, the temperature will be reduced again, in this example at a higher rate than the temperature increase at the beginning of the heat treatment. The temperature can be decreased for example at a rate of 150° C. per hour, which in the example shown means that the time interval between t2 at the end of the period in which the temperature is kept practically constantly high, and t3 at the end of the temperature decrease to ambient temperature (in this example 20° C.), is only 3 hours and 32 minutes.
Starting with an ambient temperature of 20° C. and by adhering to the temperature variations as shown in
As a method according to the invention yields a coating material with a very high mass density of adsorbent material and with a very good adhesion to the supporting structure (250 kg per cubic metre or more), such an adsorption agent obtained with the method according to the invention is extremely suitable for application in a drying device for drying compressed gas, as the increased dryer efficiency even enables the flow rate of gas to be dried that is guided through the drying device to be tripled. In other words, for the same flow rate of gas to be dried, a substantially smaller drying device can be used, which presents important ecological and economic benefits.
In order to be able to make the layer thickness bigger, according to a preferred aspect of the invention, the steps of applying the coating suspension and the thermal treatment of the whole of the supporting structure with the coating thereon is repeated one or more times, until the desired coating thickness on the supporting structure is reached.
The invention relates to a method for manufacturing an adsorption agent, either in the form of a drying agent for the adsorption of moisture or in the form of a different adsorption agent that can be used for selective adsorption, for example, such as in nitrogen generators or similar, because the adsorption agent is able to adsorb certain gas molecules such as oxygen, carbon dioxide and similar. By removing such gas molecules from compressed air for example, as is known, nitrogen can be generated.
The present invention is by no means limited to the embodiments described as an example and shown in the drawings, but a method according to the invention for manufacturing an adsorption agent can be realised in many ways, without departing from the scope of the invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2015/5724 | Nov 2015 | BE | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/BE2016/000032 | 7/7/2016 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
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| WO2017/015728 | 2/2/2017 | WO | A |
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