Activity monitoring and polymerization process control
View Patent ↗The present invention relates to a method to control a liquid feed stream carried out by measuring at least one spectrum of the liquid feed stream comprising an initiator or catalyst, determining its activity using a predictive model on the basis of said spectrum and adjusting the feed streams and/or the preparation conditions of the feed stream comprising the initiators or catalysts in order to attain or maintain a desired level of total activity. In a further aspect the invention relates to a controlled process for the preparation of polymers in a polymerization reactor by contacting liquid feed streams comprising monomers and initiators or catalysts, whereby the control of the feed streams entering the polymerization reactor and/or the initiator or catalyst preparation is carried out by measuring at least one spectrum of the liquid feed stream comprising an initiator or catalyst, determining its activity using a predictive model on the basis of said spectrum and adjusting the feed streams and/or the preparation conditions of the feed stream comprising the initiators or catalysts in order to attain or maintain a desired level of total activity within the polymerization reactor. More particularly, the invention relates to a method for controlling the activity of aluminum containing initiators in a process for the co-polymerization of isolefins and multiolefins, in particular isobutylene and isoprene. The present invention further to device and a chemical plant suitable to operate said process.
1. A controlled process for the preparation of polymers, the process comprising:
a) preparing an active first liquid medium comprising at least one polymerisation catalyst or at least one polymerisation initiator;
b) contacting in a polymerization reactor
a volume of a first feed stream of the active first liquid medium, with
a volume of a second feed stream of a second liquid medium comprising an amount of at least one polymerizable monomer,
to form a reaction medium, wherein the at least one polymerizable monomer polymerizes within the reaction medium to form a product medium comprising a polymer, and
during the contacting, controlling at least one of the first feed stream and the second feed stream by:
i) measuring at least one spectrum of the active first liquid medium;
ii) determining the specific activity (a specific ) of the active first liquid medium using a predictive model;
iii) determining a desired volume ratio (R desired ) of the active first liquid medium and the second liquid medium necessary to obtain a desired ratio of total activity a Total (=a specific ×V 1 ) and the amount of monomer contained in the second feed stream, wherein V 1 is the volume of the first feed stream; and
iv) controlling
the volume V 1 of the first feed stream, or
the volume V 2 of the second feed stream, or
both volumes V 1 and V 2
entering the polymerization reactor in such a manner, that the volume ratio of V 1 and V 2 at least converges to R desired ; and
whereby the predictive model is generated by a process comprising:
A) measuring spectra for a plurality of active liquid media having different activity;
B) determining the specific activity (a specific ) for the plurality of active liquid media by their employment in a polymerisation reaction with known volumes V 1 and V 2 and a known amount of the at least one monomer and analysis of the polymer formed thereby, whereby the polymerisation reaction proceeds substantially via the same mechanism as the polymerisation in step b); and
C) correlating the spectra of the active liquid media measured in step A) with their specific activity (a specific ) determined in step B).
2. A method to control the feed streams of a process for the production of polymers comprising the contacting of a first feed stream of an active liquid medium comprising a polymerization initiator or catalyst and a second feed stream of a second liquid medium comprising an amount of at least one polymerizable monomer within a polymerization reactor, the method comprising:
1) measuring at least one spectrum of an active liquid medium comprising an initiator or catalyst to be employed in the polymerization process;
2) determining the specific activity (a specific ) of the active liquid medium using a predictive model; and
3) controlling the volume or the volume flow rate of at least one of the first feed stream and the second feed stream;
whereby the predictive model is generated by a process comprising:
A) measuring spectra for a plurality of active liquid media having different activity;
B) determining the specific activity (a specific ) for the plurality of active liquid media by their employment in a polymerisation and analysis of the polymer formed thereby, whereby the polymerisation reaction proceeds substantially via the same mechanism as the polymerisation for which the feed stream of the active liquid medium is intended to be used; and
C) correlating the spectra of the active liquid media measured in step A) with their specific activity (a specific ) determined in step B).
3. The process according to claim 1 or the method according to claim 2 , wherein the active liquid medium comprises the at least one polymerisation initiator or the at least one polymerisation catalyst, and an organic solvent.
4. The process or method according to claim 3 , wherein the polymerisation initiator is selected from cationic initiators.
5. The process or method according to claim 4 , wherein the cationic initiators are selected from
reaction products of
at least one lewis acid or at least one organometal compound or a mixture of lewis adds and organometal compounds, and
at least one proton source;
carbocationic compounds of formula (I)
[CR 1 R 2 R 3 ] + An − (I)
wherein R 1 , R 2 and R 3 are independently hydrogen, C 1 -C 20 -alkyl or C 5 -C 20 -aryl with the proviso that either one or none of R 1 , R 2 and R 3 is hydrogen and An − denotes a monoanion or 1/p equivalent of a p-valent anion;
silylium compounds of formula (II)
[SiR 1 R 2 R 3 ] + An − (II)
wherein R 1 , R 2 and R 3 and An − have the same meaning as set forth above for formula (I); or
mixtures of the aforementioned compounds and reaction products.
6. The process or method according to claim 3 , wherein the organic solvent is selected from C 2 -C 20 alkanes and C 1 -C 20 haloalkanes and mixtures thereof.
7. The process according to claim 1 or the method according to claim 2 , wherein the second liquid media comprises a mixture of 70.0 to 99.5 wt.-% of a C 4 -C 16 monoolefin and 0.5 to 30.0 wt.-% of a C 4 -C 16 monoolefin of at least one conjugated C 4 -C 16 multiolefin.
8. The process according to claim 1 or the method according to claim 2 , wherein the second liquid media comprises a mixture of 92.0 to 99.0 wt.-% of a C 4 -C 16 monoolefin and 1.0 to 8.0 wt.-% of a C 4 -C 16 monoolefin of at least one conjugated C 4 -C 16 multiolefin.
9. The process according to claim 1 or the method according to claim 2 , wherein the second liquid media comprises a mixture of 90.0 to 98.5 wt.-% of isobutene, 1.0 to 8.0 wt.-% of isoprene, and 0.5 to 9 wt.-% of a monomer selected from the group consisting of 2-, 3- or 4-methylstyrene, styrene, 2-, 3- or 4-chlorostyrene, p-methoxystyrene, cyclopentadiene, methylcyclopentadiene, and indene.
10. The process according to claim 1 or the method according to claim 2 , wherein the second liquid media comprises a mixture of 91.0 to 98.5 wt.-% of isobutene, 1.0 to 8.0 wt.-% of isoprene, and 0.5 to 3 wt.-% of at least one non-conjugated C 4 -C 16 multiolefin.
11. The process according to claim 1 or the method according to claim 2 , wherein the second liquid media comprises 0.1 to 100 wt.-% of at least one polymerizable monomer.
12. The process according to claim 1 wherein step b) is carried out continuously.
13. The process according to claim 1 , wherein V 1 and V 2 are functions of volume flow rates.
14. The process according to claim 1 or the method according to claim 2 , wherein the measuring is made at-line or in-line.
15. The process according to claim 1 or the method according to claim 2 , wherein the spectrum is an infrared spectrum.
16. The process according to claim 1 or the method according to claim 2 , further comprising measuring the spectrum using a fourier-transform-infrared spectrometer (FT-IR).
17. The process according to claim 1 or the method according to claim 2 , wherein the control of the at least one feed stream is effected by a valve or pump.
18. The process according to claim 1 or the method according to claim 2 , wherein the correlation according to step C) includes either correlation of the whole spectrum measured for the active liquid media with their specific activity or the correlation of at least one part of the spectrum.