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US4048413A Expired / Lapsed US ⏱️ 0.0 years remaining

High-conversion drift-free batch-type addition copolymerization

Assignee: SCM Corp
•
Filing: 1975-12-08
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Granted: 1977-09-13
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Expires: 1995-12-08
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Abstract

Abstract Copolymer substantially free from compositional drift can be produced in a batch-type addition copolymerization process to a high degree of conversion by initiating the reaction in a monomer-containing phase (optionally dispersed in another phase of a reaction mixture) containing the monomers at mole ratios f i such that the monomers will initially be incorporated into copolymer at the desired mole ratios F i and sustaining the reaction while simultaneously controlling the addition each monomer to the phase in which the copolymerization reaction is continuing according to the relation Q.sub.i = f.sub.i Q.sub.0 + (F.sub.i - f.sub.i Q.sub.0 /Q.sub.∞)Z, where Q i is the running cumulative moles of monomer i added to the phase in which reaction is occurring (including that initially present), Q 0 is the total moles of all monomers initially present in that phase, Q.sub.∞ is the total moles of all monomers ultimately to be added to that phase, and Z is the running cumulative moles of all monomers converted to copolymer. Q 0 /Q.sub.∞ must not substantially exceed the smallest ratio F i /f i for any of the monomers and in the preferred mode is made substantially equal to that smallest ratio, thereby eliminating the corresponding monomer from the continuing addition.

Inventors

  • 👤 James B. Wilkens

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 00:11
CPC Classifications
C; C08; C08F; C08F2/00; C08F291/00

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 288 words
A non-azeotropic batch-type addition copolymerization process for producing copolymer of substantially uniform composition from a plurality of mutually copolymerizable ethylenically unsaturated monomers, each of said monomers designated herein by a different value of the index i other than 0 or ∞, said process comprising a. forming a reaction mixture comprising a monomer-containing phase in which said monomers are present in substantially those mole ratios f i of the moles of each of said monomers to the moles of all of said monomers required to initially produce copolymer in which said monomers are incorporated in substantially the desired mole ratios F i of the moles of each of said monomers incorporated to the moles of all said monomers incorporated, the moles Q 0 of all of said monomers initially present in said monomer-containing phase not substantially exceeding that value which would make the ratio Q O /Q.sub.∞ equal to the smallest of the ratios F i /f i for any of said monomers, where Q∞ is the total moles of all of said monomers to be copolymerized; b. initiating an addition copolymerization reaction of said monomers in said monomer-containing phase; and c. sustaining said reaction in said monomer-containing phase under substantially constant conditions, while simultaneously introducing into said reaction mixture a monomer feedstream which controls the cumulative molar addition of each of said monomers to said monomer-containing phase to have substantially the values given by Q.sub.i = f.sub.i Q.sub.O + (F.sub.i - f.sub.i Q.sub.O /Q.sub.28 )Z when the cumulative moles of all of said monomers converted in said monomer-containing phase to said copolymer is Z, at least until the total unreacted moles of all of said monomers present in said monomer-containing phase is reduced to about Q O /2.
Claim 2
Dependent Claim 288 words
A non-azeotropic batch-type addition copolymerization process for producing copolymer of substantially uniform composition from a plurality of mutually copolymerizable ethylenically unsaturated monomers, each of said monomers designated herein by a different value of the index i other than 0 or ∞, said process comprising a. forming a reaction mixture comprising a monomer-containing phase in which said monomers are present in substantially those mole ratios f i of the moles of each of said monomers to the moles of all of said monomers required to initially produce copolymer in which said monomers are incorporated in substantially the desired mole ratios F i of the moles of each of said monomers incorporated to the moles of all said monomers incorporated, the moles Q 0 of all of said monomers initially present in said monomer-containing phase not substantially exceeding that value which would make the ratio Q O /Q.sub.∞ equal to the smallest of the ratios F i /f i for any of said monomers, where Q∞ is the total moles of all of said monomers to be copolymerized; b. initiating an addition copolymerization reaction of said monomers in said monomer-containing phase; and c. sustaining said reaction in said monomer-containing phase under substantially constant conditions, while simultaneously introducing into said reaction mixture a monomer feedstream which controls the cumulative molar addition of each of said monomers to said monomer-containing phase to have substantially the values given by Q.sub.i = f.sub.i Q.sub.O + (F.sub.i - f.sub.i Q.sub.O /Q.sub.28 )Z when the cumulative moles of all of said monomers converted in said monomer-containing phase to said copolymer is Z, at least until the total unreacted moles of all of said monomers present in said monomer-containing phase is reduced to about Q O /2.
Claim 3
Dependent Claim 14 words
The process of claim 1 wherein said addition copolymerization reaction is a free-radical reaction.
Claim 4
Dependent Claim 14 words
The process of claim 1 wherein said addition copolymerization reaction is an ionic reaction.
Claim 5
Dependent Claim 13 words
The process of claim 1 wherein said monomer-containing phase is a continuous phase.
Claim 6
Dependent Claim 21 words
The process of claim 1 wherein said monomer-containing phase is dispersed in another phase in which said monomers are substantially insoluble.
Claim 7
Dependent Claim 13 words
The process of claim 5 wherein said other phase is an aqueous phase.
Claim 8
Dependent Claim 15 words
The process of claim 1 wherein said reaction mixture contains no added polymer or copolymer.
Claim 9
Dependent Claim 44 words
The process of claim 1 wherein said monomer-containing phase contains or is in intimate contact with an added polymer or copolymer and a substantial proportion of the copolymer produced in said process is chemically bonded to said added polymer or copolymer during said process.
Claim 10
Dependent Claim 78 words
The process of claim 1 wherein said monomer feedstream is added to said reaction mixture substantially according to the schedule defined by said Q i and substantially all of the monomers added to said reaction mixture as part of said monomer feedstream are either directly added to said monomer-containing phase or promptly transferred to said monomer-containing phase from any other phase of said reaction mixture to which any portion of said monomer feedstream may have been directly added.
Claim 11
Dependent Claim 25 words
The process of claim 9 wherein said ratio Q O /Q.sub.∞ is substantially equal to the smallest of said ratios F i /f i .
Claim 12
Dependent Claim 127 words
The process of claim 1 wherein said process is a continuous or semi-continuous batch-type process in which, after said addition copolymerization reaction is initiated, said reaction mixture moves a. continuously or intermittently through a signle reactor vessel or b. semi-continuously through a series of reactor vessels by intermittent transfer of substantially all of said reaction mixture fro one to another of said series of reactor vessels; said monomer feedstream is added to said reaction mixture at suitable physically spaced intervals during the progress of said reaction mixture through said reactor vessel or vessels; and said reaction mixture is immediately preceded and/or followed through said reactor vessel or vessels or a substantially identical reaction mixture in a substantially identical process without substantial intermixing between such successive reaction mixtures.
Claim 13
Dependent Claim 32 words
The process of claim 1 wherein, after initiation of said addition copolymerization reaction, said reaction mixture remains in the reactor vessel in which said initiation took place until said process is completed.
Claim 14
Dependent Claim 25 words
The process of claim 1 wherein said ratio Q O /Q.sub.∞ is substantially equal to the smallest of said ratios F i /f i .
Claim 15
Dependent Claim 15 words
The process of claim 13 wherein said plurality of monomers consists of only two monomers.
Claim 16
Dependent Claim 15 words
The process of claim 1 wherein said plurality of monomers comprises more than two monomers.

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-09-12 1981-03-14 1981-09-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-09-12 1985-03-14 1985-09-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-09-12 1989-03-14 1989-09-13 $7700.00 Window Closed / Lapsed

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