Adsorber for two-component recovery and method of operating same

An adsorber for the cleaning of air or natural gas by the removal of water as a first component and carbon dioxide and/or a hydrocarbon as a second component from the gas stream to be treated utilizes two distinct adsorber beds traversed in succession by the gas stream, at least one of these beds being vertically oriented so that the gas stream and the regenerating gas pass horizontally through it.

FIELD OF THE INVENTION 
Our present invention relates to an adsorber unit for two recoverable 
components, i.e. for the removal of two distinct components from a 
multicomponent gas stream, and to a method of operating such an adsorber. 
More particularly, the invention relates to an adsorber of the type in 
which two separated absorber beds are traversed in succession by a 
multicomponent gas stream for the componentwise removal of two distinct 
components from the gas stream which, in addition, can contain other 
components or substances. The invention is especially directed to an 
adsorber of this type which, upon regeneration, evolves one of the two 
adsorbed components in a liquid state and the other of these components in 
a gaseous state. 
BACKGROUND OF THE INVENTION 
In the adsorptive purification of the gases, the adsorptive separation of 
gases and in the adsorptive recovery selectively of components from gases, 
it is known to provide an adsorber having two separated beds which are 
traversed in succession by the multicomponent gas stream for the selected 
removal of the two different components therefrom. 
Examples of the removal of two components from a gas mixture include the 
treatment of moist air prior to separation of the air into the low-boiling 
components so as to remove water and carbon dioxide, the treatment of 
natural gas to remove water and higher hydrocarbons and other systems 
which, upon regeneration of the adsorber beds, produce one of the 
components, e.g. water in a liquid form, while the other component is 
discharged from its adsorber bed in a gaseous form. 
After adsorption operation for a period sufficient to result in the 
saturation of one of these beds, the adsorber is regenerated, usually by 
the treatment of the beds in succession with a regenerating or adsorption 
gas. It is during this regeneration that one of the components is evolved 
in a liquid state or phase while the other component is evolved in a 
gaseous state or phase. 
For efficient operation of the adsorber, it is imperative that not only the 
gaseous desorbed component be discharged completely, but also that the 
liquid component be removed to the greatest possible extent. 
To this end, in German Patent Document--Open Application DE-OS No. 27 46 
673, a substantially horizontal adsorber bed is provided which is 
traversed by the gas to be treated in a vertical direction and which rests 
upon a gas-permeable grate through which the liquid component upon 
regeneration can trickle. 
An adsorber having horizontal beds of this type is found to have large 
amounts of free space which cannot effectively be utilized and to require 
considerable area in a plant where floor space may be at a premium. 
Furthermore, these adsorbers do not operate fully effectively, frequently 
cannot assure complete discharge of the liquid phase produced during 
regeneration and, with respect to their size, are comparatively expensive 
to construct and maintain. 
OBJECTS OF THE INVENTION 
It is the principal object of the present invention to provide an adsorber 
for the selective removal of two components from a multicomponent gas 
stream in the manner described but which is free from disadvantages of 
earlier systems and, especially, for a given degree of operational 
reliability, has a reduced volume and occupies less space, or for a given 
volume has higher adsorptive capacity for greater efficiency. 
Another object of this invention is to provide an improved method of 
operating a selective adsorber of the type described. 
Another object of this invention is to provide an adsorber unit for the 
purposes described which can be fabricated at lower cost than earlier 
adsorbers of a similar capacity. 
SUMMARY OF THE INVENTION 
We have discovered that these objects can be attained and the operations of 
a two-component adsorber greatly improved over earlier systems when at 
least one of the two beds is an upright bed and is traversed horizontally 
by the fluids associated therewith, i.e. the gas to be treated and the 
regenerating gas. 
According to the invention, therefore, an adsorber is provided which 
includes the usual adsorber shell or housing but which may be vertically 
elongated and is provided with two spaced-apart beds, successively 
traversed by the gases passing through this housing, the beds being 
designed to extract respective components from a multicomponent gas stream 
to be treated and, upon regeneration, to evolve one of these components in 
a liquid and another of these selectively adsorbed components in a gas 
phase, one of these beds at least being vertically oriented or upright and 
traversed by the gas streams in a substantially horizontal direction. 
We have found, most surprisingly, that this arrangement, in which at least 
one of the beds is vertically oriented, can greatly reduce the free space 
or unused volume of the adsorber by comparison with an adsorber having 
only horizontal beds and operated with the same performance so that the 
overall volume of the adsorber can be markedly reduced. Conversely, for a 
given volume, the separating capacity or efficiency can be markedly 
increased. 
According to the invention, the first adsorber bed is the adsorber bed 
which evolves its adsorbed components in a liquid state upon desorption 
while the second adsorber bed evolves its adsorbed component in a gaseous 
state, the first and second adsorber beds being traversed in this order or 
reverse order by the gas stream to be treated. 
We have found it to be especially advantageous when at least the second 
adsorber bed, which upon regeneration evolves its component in a gaseous 
state, or in which its adsorbed component is trapped in a gaseous state, 
is the upright and vertically elongated bed. 
In a preferred embodiment of the invention, the first adsorber bed is a 
horizontal or recumbent bed and is traversed by the gases in the vertical 
direction. 
In another preferred embodiment of the invention, the first adsorber bed is 
also upright. The combination of two upright adsorber beds in a common 
housing has been found to be especially advantageous because of the small 
area occupied by the adsorber, the simplicity of the construction and the 
reduced volume of the apparatus. 
It has also been found to be desirable to provide the second adsorber bed 
above the first adsorber bed, thereby simplifying the discharge of the 
component which is released in the liquid phase from the housing. The 
second adsorber bed can have the configuration of an upright cylinder with 
a circular horizontal cross section and surrounding a vertical axis, the 
cylinder being hollow so that its cross section is annular. In this case, 
the interior or hollow of the cylinder can be provided with gas flow 
means, i.e. means for feeding gas to the cylindrical bed or recovering gas 
from this bed. This fitting can be connected to or formed in the housing 
wall. 
The hollow cylindrical configuration of the bed has been found to be 
especially space-saving and permits simplification of the means for 
introducing the adsorbent, for controlling the height of the adsorbent bed 
and hence for adjusting the level of the adsorbent for various purposes. 
The gas mixture traverses the cylindrical body of an adsorbent in a 
horizontal direction. The second adsorber bed, in a variation of this 
them, can be subdivided into a plurality of spaced-apart vertically 
oriented sections which can be parallel to one another and to the axis or 
vertical wall of the housing and which can be internally provided with the 
means for feeding the gas to and discharging the gas from the adsorbent, 
while being connected to the housing wall. In this embodiment as well, 
each section of the second adsorber bed can be traversed horizontally by 
the gases and can be disposed within a respective compartment of the 
housing, the compartments of the housing being separated by partitions on 
one or more sides. The housing itself may be subdivided into compartments 
by the planar or arcuate vertically oriented sections of the second bed. 
It has been found to be advantageous to provide a partition between 
adsorber beds, e.g. between the first and second adsorber beds, so that it 
has a frustoconical or wedge-shaped profile whose half apex angle 
corresponds to the maximum piling angle of the adsorbent thereabove so 
that it can allow adsorbent above this partition to slide downwardly. When 
the apparatus is also provided with an opening in the region of or aligned 
with the end of the partition, filling of the beds is simplified since the 
material for the lower bed can be introduced first and can pass the 
partition as a result of the fact that the angle of inclination of the 
partition does not impede the flow of the material thereabove. When the 
first bed is completely filled in this manner, the adsorbent of the second 
bed is introduced and stacks above the first bed. 
It has been found to be advantageous to provide the first absorber bed with 
a drying gel and the second absorber bed with molecular sieve. 
In the method of the invention, we provide that the gas stream to be 
treated and the regenerating gas stream pass through at least one of the 
two beds in a horizontal direction. 
According to one embodiment of the method, the first adsorber bed is 
traversed vertically upwardly by the gas mixture although at another 
embodiment of the invention both beds are traversed in the horizontal 
direction by the gas mixture. Preferably, moreover, water is removed from 
the gas mixture in the first absorber bed while in the second adsorber bed 
carbon dioxide and/or a higher carbon then methane, e.g. ethane, is 
removed.

SPECIFIC DESCRIPTION AND EXAMPLE 
As can be seen from FIGS. 1 and 2, an adsorber for the purposes of the 
present invention can comprise a cylindrical housing 1 which can be formed 
at its upper and lower ends with fittings 2 and 3 for passing the gas to 
be treated and the regenerating gas through the housing in the axial and 
vertical directions. These fittings 2 and 3 represent means for feeding 
gas to and discharging gas from the beds which are disposed within the 
housing and are axially aligned, i.e. are disposed along the axis of the 
housing 1. 
The adsorber housing 1 is vertically elongated and upright and thus has a 
vertical axis. 
In the lower portion of the housing 1, a first adsorber bed 4 is provided, 
this adsorber bed consisting, for example, of a drying gel capable of 
trapping water from moist air or natural gas which may be processed 
through the adsorber. 
As can be seen from FIG. 1a, the first adsorber bed 4 rests upon a 
gas-permeable grate 4', is horizontal and extends over the full cross 
section of the housing 1. 
Above the adsorber bed 4 within the housing 1, a second adsorber bed 5 is 
provided, this adsorber bed consisting of a second adsorbent, e.g. a 
molecular sieve dimensioned to retain carbon dioxide and and/or ethane 
from the gas to be treated. 
In the embodiments of FIGS. 1 and 2, the second adsorber bed 5 is divided 
into the two partial beds or bed sections 5a and 5b which are planar, 
mutually parallel and disposed symmetrically on opposite sides of the 
housing axis, these beds being enclosed in gas-permeable walls which run 
to the top of the housing and are connected to the upper and lateral walls 
thereof as should be apparent from FIG. 2. At the bottom ends of these 
adjoining beds, a horizontal partition 6 interconnects the partial beds to 
define a space 7 above the partition 6 and between the two parallel beds. 
The fitting 2 opens into this space. 
As will be apparent from FIG. 1a, a pair of parallel walls 5a' and 5a" 
vertically enclose the partial bed 5a and the latter is supported at the 
bottom by a gas impermeable wall 5a'". 
The operation of the adsorber unit of the invention will be described by 
way of example for the cleaning of air which may be subjected to low 
temperature air rectification, i.e. separation of nitrogen and oxygen for 
the Linde Process. The air is cleaned to eliminate moisture and carbon 
dioxide as well as hydrocarbons from the air before such air 
rectification. 
The adsorbent for each of the sections 5a and 5b is introduced through 
hatches 1a and 1b while a hatch 1c is provided for the housing to permit 
replacement of the adsorbent of the bed 4. Once the beds are in place in a 
first operating step, air is passed through the adsorber from the opening 
3 to the fitting 2 and is dried in vertically traversing the drying gel 
forming the bed 4. The moisture-free air then passes horizontally through 
the bed sections 5a and 5b of a second adsorbent bed 5 which is a 
molecular sieve and removes carbon dioxide and hydrocarbons. The cleaned 
air is discharged via the fitting 2. 
When the adsorber is fully charged, i.e. one of the two beds is saturated 
or both are saturated, the second phase of the operating cycle is 
effected, i.e. the supply of air is cut off and a regenerating gas, e.g. 
nitrogen, is passed through the adsorber in the opposite direction. 
The nitrogen entering through fitting 2, thus first traverses the second 
adsorber bed 5 substantially horizontally to entrain the gaseous products, 
e.g. the carbon dioxide and hydrocarbons adsorbed thereby. Then the 
nitrogen flows vertically through the adsorber bed 4 to entrain the 
moisture therefrom. At least a portion of this moisture condenses and, as 
liquid, rapidly and unimpededly is permitted to flow downwardly and is 
discharged together with the regenerating gas through the opening 3. 
The system thus operated with a high degree of reliability and efficiency, 
allowing the two adsorber beds to be provided in a very compact 
configuration with the adsorber having relatively small dimensions. The 
adsorber occupies a minimum of space and allows, for example, four times 
as much adsorbent to be used for the removal of carbon dioxide as the 
adsorbent which is required for the removal of moisture. 
The embodiment shown in FIGS. 3 and 4 differs from that of FIGS. 1 and 2 in 
that the second adsorber bed 8 has a cylindrical configuration and is of 
an annular cross section, as will be apparent from FIG. 4. The upper end 
of the cylindrical bed is connected to the housing wall and the interior 
of the cylinder is closed at its lower end by a partition 6. The fitting 2 
thus opens into the space enclosed by the cylinder. Otherwise this 
arrangement operates in the manner previously described in connection with 
FIGS. 1 and 2. 
FIG. 5 shows an adsorber in which both adsorber beds 9 and 10 can be 
upright. Here the two adsorber beds are of cylindrical configuration and 
annular cross section. The outer perimeter is defined by a cylindrical 
sieve 12 while the inner perimeter is defined by a pair of axially spaced 
cylindrical sides 12a and 12b, the former being provided for the upper bed 
9 while the latter is provided for the lower bed 10. 
Between the two sieve sections 12a and 12b a partition 13 is provided with 
a frustoconical configuration such that the half angle of the frustocone 
corresponds to the flow angle of the adsorbent in the lower bed, i.e. is 
about 30.degree.. In the region of the end of this partition, a gap is 
provided between the partition and the sieve 12. 
When the adsorbent of the lower bed is thus introduced through the hatches 
14, the adsorbent flows readily via the partition through the gap to 
completely fill the lower bed in a gapless or fully packed manner. Once 
the lower bed is filled, the material for the upper adsorbent bed can be 
introduced. Hatches 15 have been provided for discharging the adsorbents 
of the two beds. The hatches can be closed with cuts as has been shown in 
FIG. 1. 
The fittings for gas flow have been shown at 16 and 17 and the gas flow 
path by the arrows 18. In this embodiment the gases traverse both beds 
substantially horizontally.