GB1572682A - Process for the regeneration of an alkanolamine-based absorbent for gases containing co and/or cos - Google Patents
Process for the regeneration of an alkanolamine-based absorbent for gases containing co and/or cos Download PDFInfo
- Publication number
- GB1572682A GB1572682A GB9396/78A GB939678A GB1572682A GB 1572682 A GB1572682 A GB 1572682A GB 9396/78 A GB9396/78 A GB 9396/78A GB 939678 A GB939678 A GB 939678A GB 1572682 A GB1572682 A GB 1572682A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oxazolidone
- fraction
- absorbent
- process according
- reactor
- 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.)
- Expired
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/38—Steam distillation
-
- 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
- B01D53/14—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 absorption
- B01D53/1493—Selection of liquid materials for use as absorbents
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Gas Separation By Absorption (AREA)
- Treating Waste Gases (AREA)
- Heterocyclic Carbon Compounds Containing A Hetero Ring Having Nitrogen And Oxygen As The Only Ring Hetero Atoms (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
(54) PROCESS FOR THE REGENERATION OF AN
ALKANOLAMINE-BASED ABSORBENT FOR
GASES CONTAINING CO2 AND/OR COS
(71) We, SHELL INTERNATION
ALE RESEARCH MAATSCHAPPIJ B.V., a company organised under the laws of the
The Netherlands, of 30 Carel van
Bylandtlaan, The Hague, The Netherlands, do hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement:- The invention relates to a process for the regeneration of an absorbent for the removal of CO2 and/or COS from gases, which absorbent comprises an aqueous solution of an N- (2- hydroxyalkyl) primary and/or secondary amine and is contaminated with an oxazolidone.
N - (2 - hydroxyalkyl) primary and secondary amines, which contains the group ~NH~C~COH~, are found to form oxazolidones where their aqueous solutions are used as absorbent for CO2, possibly according to the following reaction mechanism:
With COS the alkanolamines probably react as follows:
As an example of an absorbent which is often used for absorbing CO2, COS and H2S from gases, and in which oxazolidone formation -can occur, there may be mentioned an aqueous solution of diisopropanolamine. In this case 3 - (2 hydroxypropyl) - 5 - methyl - 2 oxazolidone is formed. Other examples of alkanolamines of the type to which the invention confines itself are monoethanolamine and diethanolamine, which, too, are used in aqueous solution as absorbents.
Since in such absorbents the formation of oxazolidones may be unacceptable (in some cases the conditions are such that 1% w alkanolamine is converted per hour), a regeneration method has previously been proposed in British patent specification No.
1,118,687, whereby potassium hydroxide is added to the absorbent to be regenerated, as a result of which the oxazolidone is converted into the alkanolamine, with the formation of potassium carbonate.
Disadvantages of this method are that the potassium carbonate must be removed, that expensive chemicals are consumed, that the regeneration can hardly be carried out continuously and that a relatively complicated unit is required.
The present invention provides a process, which does not have the above-mentioned disadvantages and with which the alkanolamine can be recovered from the oxazolidone in a simple way.
According to the invention there is provided a process for the regeneration of an absorbent for the removal of CO2 and/or
COS from gases, which absorbent comprises an aqueous solution of an N - (2 - hydroxyalkyl) primary and/or secondary amine and is contaminated with an oxazolidone, in which the absorbent, or an oxazolidone - containing fraction obtained therefrom, is heated to a temperature of at least 200"C at elevated pressure in the presence of water.
It has been found that this heating at elevated pressure converts the oxazolidone into the alkanolamine originally present in the absorbent, with liberation of CO2 and with consumption of water. If the absorbent itself is heated, sufficient water is present for the purpose. If a fraction which is obtained from the absorbent and which does not contain sufficient water is to be heated. some water should be added.
The CO2 formed is preferably removed by
steam stripping during the heating at a
temperature of at least 2000 C. This is an
inexpensive and efficient method, which
does not cause contamination of the
absorbent and with which the required
temperature can easily be reached.
Moreover, steam stripping ensures a
continuous discharge of the CO2 formed.
With an adequate pressure control, the use
of steam permits the desired quantity of
water to be maintained during the
conversion of the oxazolidone.
Good results are obtained at heating
temperatures in the range of 200 to 3000 C, in particular of 200 to 2500 C. At these
temperatures the risk of thermal
degradation of the alkanolamines
concerned is small.
According to a preferred embodiment
heating takes place at a pressure of 1 60 atm. On the one hand, the pressure is then
sufficiently high for a good conversion, on
the other hand the cost of the required
equipment is lower than for much higher
pressures.
Absorbents of the type according to the
invention are often used in a process for the
continuous removal of H2S, COS and CO2 from gases. To this end the gas is often
passed in upflow through a column in which
a number of contact trays are present and in
which absorbent flows from the top
downwards over the trays. At the bottom of
the column, absorbent loaded with CO2 and 112S is discharged and at the top the purified
gas. The loaded absorbent is continuously
passed from the bottom of the said column
to the top of a stripping column in which it
flows downwards and in which it is freed
from the CO2 and H2S either by reducing
the pressure or by stripping with a stripping
gas such as steam. The conditions in the
absorption column and in the stripping
column are such that CO2 and H2S are taken
up and released, respectively. The stripped
solvent is continuously recirculated from
the bottom of the stripping column to the
top of the absorption column. In the
stripping column the temperature is kept in
general below 175"C.
If the oxazolidone formed in the gas
washing column is not removed or
converted, a build-up of the oxazolidone
content takes place and the absorptive
power of the total amount of absorbent
gradually decreases.
Very suitably a bleed stream is taken,
preferably continuously from the absorbent
stream which is recirculated from the
bottom of the stripping column to the top of
the absorption column, and this bleed
stream is regenerated according to the
invention.
Because the regeneration according to the invention will be carried out by heating
(in general for a relatively long period) it is
of advantage to reduce the amount of heat
needed by reducing the amount of liquid to
be heated. For that reason it is of advantage
not to remove oxazolidone from the stream
of absorbent to be recirculated from the
stripping column to the absorption column
as such, but from a fraction of this stream
which contains oxazolidone. Such a fraction
is obtained very suitably by separation
(preferably continuously by means of
distillation into a fraction containing
oxazolidone and a fraction containing
oxazolidone in a lower concentration or not
at all. The oxazolidone-containing fraction
is treated by the process according to the
invention and then recirculated, for
instance to the top of the absorption
column. In this way an ever increasing
oxazolidone content in the total quantity of
absorbant is prevented and the oxazolidone
content of the absorbent can be set at any
desired value without the necessity of
treating large quantities of absorbent at high
pressure and temperature.
The distillation in which a fraction which
contains oxazolidone is obtained is
preferably carried out with steam stripping
at 100 200 C. The N - (2 - hydroxyalkyl)
amine is distilled off and the oxazolidone
containing bottom fraction thus obtained
contains a reduced quantity of water and
alkanolamine as compared with the
absorbent.
The invention is further illustrated by the
following Example.
EXAMPLE
In a number of series of experiments a
mixture of water and 3 - (2 hydroxypropyl) - 5 - methyl - 2
oxazolidone was stripped with steam at
different temperatures and at elevated
pressure for a certain time, samples of the reactor contents being taken during the reaction to be able to determine the course of the conversion of the oxazolidone into diisopropanolamine.
The following procedure was followed:
For each experiment a weighed quantity of water and the oxazolidone was introduced into the reactor, which was subsequently flushed with CO2 to expel the air. Then, the temperature, and consequently the pressure, in the reactor was gradually increased within 15 minutes.
The steam that was passed through during the experiment was always passed from the reactor through a condensation vessel, in which a condensed fraction from it was collected. After the desired temperature has been reached samples were taken at regular intervals via a pipe opening into the reactor, whilst the condensed fraction was at the same time discharged. The time when the first sample was taken was always considered as the starting point of an experiment.
In processing the data obtained from the samples the following effects were taken into account:
The oxazolidone concentration in the reactor is affected in the following three ways:
1. Part of the oxazolidone is converted into diisopropanolamine;
2. The steam blown through may dilute or concentrate the contents of the reactor; and
3. The steam also makes part of the oxazolidone find its way into the condensed fraction.
Because of effects 2 and 3 the fraction of oxazolidone that was converted into diisopropanolamine had to be determined in a special way: the fraction was calculated from a mass balance which was obtained by analysis of the reactor feed, the samples from the reactor and the condensed fractions. In this determination the oxazolidone from the condensed fractions was always taken to belong to the unconverted part of the oxazolidone.
The results are summarized in the following table.
Time, Pressure, Converted Temp.,
min. bar fraction OC 225 0.106
450 12 0.148 200
59 0.137
120 23 0.291 225
179 0.608
59 0.069
120 21 0.124 225
179 0.213
25 0.091
65 36 0.328 250
105 0.542
30 0.103
75 35 0.333 250
135 0.509
15 0.040
45 41 0.167 275
16 0.174
33 55 0.356 275
15 0.181
45 57 0.574 275
90 0.827
40 77 0.461 300
The table shows that at elevated pressure
and temperature-withing the scope of the invention-a considerable part of the
oxazolidone can be convered into amine
within a reasonable time.
WHAT WE CLAIM IS:
1. A process for the regeneration of an
absorbent for the removal of CO2 and/or
COS from gases, which absorbent comprises
an aqueous solution of an N - (2 - hydroxyalkyl) primary and/or secondary
amine and is contaminated with an
oxazolidone, in which the absorbent, or an
oxazolidone - containing fraction obtained
therefrom is heated to a temperature of at
least 200"C at elevated pressure in the
presence of water.
2. A process according to claim 1, in
which the heating temperature is from 200 to 3000 C.
3. A process according to claim 2, in
which the heating temperature is from
2000C to 2500C.
4. A process according to any one of the
preceding claims in which the CO2 formed
during heating is removed by steam
stripping.
5. A process according to any one of the
preceding claims in which the heating takes
place at a pressure of 1060 atm.
6. A process according to any one of the
preceding claims in which an oxazolidone containing fraction is continuously separated from part of the absorbent by
distillation, and in that this fraction is
heated and in that this fraction is then
recirculated.
7. A process according to claim 6 characterized in that the distillation is
carried out with steam stripping at 100- 200"C.
8. A process as claimed in claim 1,
substantially as described with special
reference to the Example.
**WARNING** end of DESC field may overlap start of CLMS **.
Claims (8)
1. A process for the regeneration of an
absorbent for the removal of CO2 and/or
COS from gases, which absorbent comprises
an aqueous solution of an N - (2 - hydroxyalkyl) primary and/or secondary
amine and is contaminated with an
oxazolidone, in which the absorbent, or an
oxazolidone - containing fraction obtained
therefrom is heated to a temperature of at
least 200"C at elevated pressure in the
presence of water.
2. A process according to claim 1, in
which the heating temperature is from 200 to 3000 C.
3. A process according to claim 2, in
which the heating temperature is from
2000C to 2500C.
4. A process according to any one of the
preceding claims in which the CO2 formed
during heating is removed by steam
stripping.
5. A process according to any one of the
preceding claims in which the heating takes
place at a pressure of 1060 atm.
6. A process according to any one of the
preceding claims in which an oxazolidone containing fraction is continuously separated from part of the absorbent by
distillation, and in that this fraction is
heated and in that this fraction is then
recirculated.
7. A process according to claim 6 characterized in that the distillation is
carried out with steam stripping at 100- 200"C.
8. A process as claimed in claim 1,
substantially as described with special
reference to the Example.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL7702650A NL7702650A (en) | 1977-03-11 | 1977-03-11 | PROCESS FOR THE REGENERATION OF AN ALKANOLAMINE-BASED SOLVENT FOR GASES CONTAINING CO2 AND / OR COS. |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1572682A true GB1572682A (en) | 1980-07-30 |
Family
ID=19828153
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9396/78A Expired GB1572682A (en) | 1977-03-11 | 1978-03-09 | Process for the regeneration of an alkanolamine-based absorbent for gases containing co and/or cos |
Country Status (8)
Country | Link |
---|---|
JP (1) | JPS53113290A (en) |
BR (1) | BR7801458A (en) |
CA (1) | CA1104996A (en) |
DE (1) | DE2810249C2 (en) |
FR (1) | FR2382922A1 (en) |
GB (1) | GB1572682A (en) |
NL (1) | NL7702650A (en) |
NO (1) | NO146184C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999021821A1 (en) * | 1997-10-27 | 1999-05-06 | Shell Internationale Research Maatschappij B.V. | Process for the purification of an alkanolamine |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4282194A (en) | 1980-02-19 | 1981-08-04 | Exxon Research & Engineering Co. | Process for converting cyclic urea to corresponding diamine in a gas treating system |
US4282193A (en) | 1980-02-19 | 1981-08-04 | Exxon Research & Engineering Co. | Process for converting cyclic urea to corresponding diamine in a gas treating system |
US4514379A (en) * | 1983-06-28 | 1985-04-30 | Union Oil Company Of California | Catalytic process for converting 2-oxazolidinones to their corresponding alkanolamines |
US5137702A (en) * | 1988-12-22 | 1992-08-11 | Mobil Oil Corporation | Regeneration of used alkanolamine solutions |
US5108551A (en) * | 1990-12-17 | 1992-04-28 | Mobil Oil Corporation | Reclamation of alkanolamine solutions |
CN1035103C (en) * | 1992-12-24 | 1997-06-11 | 四川化工总厂 | Method of removing carbon dioxide from mix gas |
NO20023050L (en) | 2002-06-21 | 2003-12-22 | Fleischer & Co | Process and facilities for carrying out the process |
-
1977
- 1977-03-11 NL NL7702650A patent/NL7702650A/en not_active Application Discontinuation
-
1978
- 1978-02-06 CA CA296,314A patent/CA1104996A/en not_active Expired
- 1978-03-09 GB GB9396/78A patent/GB1572682A/en not_active Expired
- 1978-03-09 DE DE2810249A patent/DE2810249C2/en not_active Expired
- 1978-03-09 NO NO780825A patent/NO146184C/en unknown
- 1978-03-09 FR FR7806800A patent/FR2382922A1/en active Granted
- 1978-03-09 BR BR7801458A patent/BR7801458A/en unknown
- 1978-03-09 JP JP2608678A patent/JPS53113290A/en active Granted
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999021821A1 (en) * | 1997-10-27 | 1999-05-06 | Shell Internationale Research Maatschappij B.V. | Process for the purification of an alkanolamine |
EP0918049A1 (en) * | 1997-10-27 | 1999-05-26 | Shell Internationale Researchmaatschappij B.V. | Process for the purification of an alkanolamine |
US6152994A (en) * | 1997-10-27 | 2000-11-28 | Shell Oil Company | Process for the purification of an alkanolamine |
MY119738A (en) * | 1997-10-27 | 2005-07-29 | Shell Int Research | Process for the purification of an alkanolamine |
Also Published As
Publication number | Publication date |
---|---|
FR2382922A1 (en) | 1978-10-06 |
NO146184B (en) | 1982-05-10 |
DE2810249A1 (en) | 1978-09-14 |
FR2382922B1 (en) | 1983-02-04 |
JPS53113290A (en) | 1978-10-03 |
DE2810249C2 (en) | 1985-09-19 |
NO780825L (en) | 1978-09-12 |
JPS6139092B2 (en) | 1986-09-02 |
NO146184C (en) | 1982-08-18 |
NL7702650A (en) | 1978-09-13 |
CA1104996A (en) | 1981-07-14 |
BR7801458A (en) | 1978-10-10 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |