CA1171022A - Solvent recovery process - Google Patents
Solvent recovery processInfo
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- CA1171022A CA1171022A CA000358395A CA358395A CA1171022A CA 1171022 A CA1171022 A CA 1171022A CA 000358395 A CA000358395 A CA 000358395A CA 358395 A CA358395 A CA 358395A CA 1171022 A CA1171022 A CA 1171022A
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- liquid waste
- residue
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- organic solvent
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Abstract
ABSTRACT OF THE INVENTION
Solvent Recovery Process This process provides a means of re-claiming useful materials from liquid waste products comprising solutions or dispersions of polymer in organic solvents. The liquid waste is dispersed in particulate form in water and that dispersion distilled to recover the organic solvent. A
feature of the process is that the residue is a free-flowing slurry of solid particles which is readily discharged from the processing equipment and can be re-cycled in suitable products. To achieve this the liquid waste must be adapted to be heat convertible by the processing conditions, to the point where it is insoluble in acetone on curing for 60 mins at 100°C.
Solvent Recovery Process This process provides a means of re-claiming useful materials from liquid waste products comprising solutions or dispersions of polymer in organic solvents. The liquid waste is dispersed in particulate form in water and that dispersion distilled to recover the organic solvent. A
feature of the process is that the residue is a free-flowing slurry of solid particles which is readily discharged from the processing equipment and can be re-cycled in suitable products. To achieve this the liquid waste must be adapted to be heat convertible by the processing conditions, to the point where it is insoluble in acetone on curing for 60 mins at 100°C.
Description
~ ~ 71 02~ `
This invention relates to a process of recovering organic solvents from liquid waste products comprising such solvents in which polyme~ic materials are dispersed or dissolved.
The chemical processing industry accu~ulates each year large tonnages of liquid waste products which are basically solutions or dispersions of polymer in organic solvent. We use the word "solvent" herein in the context in which it is co~monly understood in the paint, adhesive and allied industries; that is, a relatively volatile organic liquid which has the property of dissolving other less volatile organic compounds, especially film-forming polymers and resins.
These liquid waste products are not nonmally useable in their existing form, but their disposal by dumping or încineration is ecologically unacceptable and is rapidly becoming an option denied by legislation. Destructive disposal methods are wasteful of chemical resources, the solven~ content in particular being a potentially valuable asset i~ it can be recovered economi2ally.
Conventional recovery processes, for exam~le, the recovery of volatiles by direct distillation, are only a partial answer to the problem. For example 9 ~he e~ficiency of release of volatiles from the non-volatile components may fall well short of theoretical and a typical end-product in the still is a tarry residue which has no intrinsic value, but the removal of which can be a difficult and expensi~e exercise.
We have now found that it is possible to treat many such wastes in a process which not only gives a good yield of organic solvent, but also leaves a 0 ~ ~
residue which is solid, relatively innocuous and readily discharged rom ~he processing vessel.
The particular liquid waste products useful in our process are "heat convertible" materials, by which we mean that when they are subjected ~o a temperature of 100C for 60 mins under the test conditions described hereinunder, they yield a solid residue which is insoluble at 25C in acetone.
The process involves forming a particulate dispersion in water of the liquid waste, stripping water and organic solvent from the dispersion by distillation and separating the organic solvent from the water in the distillate. The residue consists of a free-flowing slurry in water of solid, granular particles.
We therPfore provide, according to the present in~ention, a process of recovering organic solvent from a liquid heat-convertible waste product as herein defined by the steps of:
(a~ dispersing the liquid waste product in ~ .
particulate form in water in the presence of a suspending agent for the particles;
(b) heating the dispersion to boiling point to strip off ste~m and organic solvent va~ouri (c) condensing the evolved steam and organic solvent vapour and separating the water therefrom; and (d) recovering the residue as an aqueous free-flowing slurry of solid granular particles.
Optionally the water can be evaporated from the slurry to give a residue of dry, solid particles.
The organic solvent can also be further refined by conventional means, for example by fractional distillation, when it contains a mixture o solvents.
~ ,~
. ~
~ 17:~2 Our test for heat convertibility is performed in the following manner. The liquid waste product to be tested ls poured or spread on a horizontal test plate, e.g. a sheet of gl$ss or a flat steel panel, so that a film of up to 1-2 mm thick is formed thereon.
The test plate is then heated in air to 100C and held at that te~perature ~or 60 mins It is cooled to 25C and then moistened with droplets of acetone.
If the required degree of heat convertibility has been achieved, the residue on the test plate will not dissolve in the acetone. The effect of the acetone is sometimes more readily assessed by gently rubbing the moistened residue with a glass test probe. The appearance of a satisfactory test area will vary somewhat depending on the actual composition of the liquid waste. For example, a satisfactory material may not be entirely unaEfected by acetone. When moistf~ned and rubbed with the probe, it may lose adhesion to the substrate or even break up into irregular lumps or flakes. In extreme cases it may even show some wrinkling or swe-lling, but no dissolution. However, an unsatisfactory test sample will show definite evidence of d-Lssolution in the acetone, notably a streaking or smearing on the test probe or subs~rate and an obvious loss of film integrity.
We associate the property of heat convertibility as measured by our acetone solubility test with the ability of the disperse particles of liquid waste to form solid, discrete particles during the stPam stripping stage of our process. This gives rîse to a slurry of granular particles which is readily dischaxged ~rom the reaction vessel.
I 1 7~0 As we understand it, the heat convertibility is derivQd from cross-linking of polymeric components o~ the liquid waste. This characteristic may be inherent in the materials to be treated. For 5 example, paint residues are a form of liquid waste to which our process is particularly well suited.
One well-known class o~ paints, the "thermosetting"
compositions, have the property of curing from a liquid to a solid form by a cross-linking chemical reaction between polymer components thereo. The cross-linking reaction can be initiated and controlled by well-known means, for example by the application of heat, a catalyst or a so-called cross-linking agent.
Many mechanisms of this kind are known and are discussed in various authoritative texts such as, for example, "The Chemistry of Organic Film Formers"
Solomon, D.H., Krieger Publishing Co., New York U.S.A. When the liquid waste comprises such a the~mosetting composition and the reaction conditions required to cause cross-linking to take place are present during the steam stripping cycle of our process, a satisfactory granular residue is produced.
The cross-linking reaction may require some acceleration other than by heat alon~. For example, the above reference discloses other mechanisms, ~.g.
the additiDn to polymers of acid ca~alysts to achieve heat convertibility. The catalyst addit~o~ is made to the liquid waste before subjecting it to our above-described cross-linking test. However, in carrying out the actual process the catalyst is ~ot necessarily added to the liquid waste; it may alternati~ely be added to the dispersion of liquid waste in water, or to the water in which the disper~ion is to be made provided this is consistent with the nature of the required cross-linking reaction.
... .
~ 3 71022 Liquid wastes which cross-link in the presence of an acid catalyst include, for example, wastes comprising mixtures o hydroxylated acrylic polymers, e.g. copolymers of methyl metha~rylate and hydroxy-ethyl methacrylate, and butylated melamine-formaldehyde resins. The added catalyst might then be, for example, p-toluene sulphonic acid or phosphoric acid.
We have observed that a surprising number of liquid waste products, including some which are normally acid catalysed, will pass our acetone solubility test for heat convertibility when made alkaline by the addition of an inorganic base, for example sodium and potassium hydroxides, before they are tested. It appears that such mixtures, especially when usPd in conju~ction with an inorganic suspending agent, are particularly satisfaotory materials for use in our process. They typically provide free-flowing slurries which show little, if any, tendency to lea~e solid deposits on the walls of the process equipment.
Alternatively, a liquid waste which is not inherently able to take part in a cross-linkîng reaction may be adapted to the requirements of our process by blending it wi~h hea~-convertible constituents. For exam~e, thermoplastic lacquer comprislng polymethyl methacrylate produces a residue soluble in acetone when subjected to our above-described cross-linking test. However, the necessary heat-convertibility can be imparted to it by adding thereto sufficient carboxylated styrene-maleic anhydride co~oIymer, difunctional epoxy resin and tertiary amine catalyst.
A useful practical method of dealing with waste con~aining essentially thermoplastic polymer, is to blend that waste with a known heat convertible waste until a composition is reached which does satisy our cross-linking test. The proportions to be blended depend on the compositions o~ the wastes to be treated and are readily determined by experiment.
The dispersion of the liquid waste in particulate form in water can be made, for example, by pouring the waste into water which is kept agitated by a mechanical stirrer. The water may be at ambient room temperature or preferably it may be heated to boiling before the liquid waste is added to it.
Alterna~ively, if the water is heated by direct injection o steam, the agitation set up by the steam sparg~ may be sufficient to break the liquid waste up into discrete disperse particles.
The suspending agent, which may be present in either ~he water or in the liqui.d waste may be chosen ~rom the large number of such ag~nts known to stabilise liquid dispersions in water; our process will tolerate most types of agent in common use.
However, because the nature bf the waste acceptable to this process can vary widely in composition and the di~persion must remain stable during the steam stripping cycle, some degree of trial may be necessary to determine the most suitable suspending agent for use with a particular liquid waste.
We have found that inorganic materials such as Wyoming bentonite and activated clays of the Hectorite type can be satisfactory suspending agents. Other suitable materials are, for example, poly(vinyl alcohol), gelatine and amphipathic polymeric surface active agents, eg. triethanolamine oLeate, sorbitol monostearate, lauryl alcohol ethoxylate and nonyl ~, phenol ethoxylate.
The requir d coneentration of suspending agent also varies with bo~h the type o ~uspending age~t used and the nature of the liquid was~e being treated. r~i~h orga~ic suspending agents a typical concentration is 2-5% based on the weight of liquid waste, while or inorganic suspending agents t~e corresponding igure is ~ypically 5 10%.
The size of the disperse`particles is not particularly critical in so far as the recovery process is concerned. Factors which influence the disperse particle size distribution in such sy~tems are well known to the art and include, for example, the relative viscositle~ of each phase and the shear force~ generated in the dispersion equipment.
The nature and ~mount of solid material dissolved .or dispersed in the liquid waste will, in turn, affect the vi~cosity of the disperse phase. If, for example, the solid constituents are polymeric and very viscous, the disperse particles tend -~ to be coarser than wh~n m~re fluid materials are us d. Some agglomeration of primary particles ma~
take place, but this is usually a reversible ac~ion and ~he fi~al slur~y rernains free flowing.
In general, the iner the dispersion the more ~ree-2S flowing the residue left in the process vessel aterthe steam ~tripping stage.
Typical dispersions we have used successully in our process have differed quite mar~edly in average particle diameter, the extremities lying at 30 about a . l ~m and 5 mm.
Ihe dispersion may be raised to boiling point by e~ternally applied heat or, for example, by steam injected direc~ly into the proces~ vessel. The condensed mix~ure of stea~ and organic solvent ~apour is ~reated by normal phase separation techniques to recover the organlc ~oLvent, less some losses of water-soluble fractions which will partition into .
71~2 _ 9 _ the aqu~ous phase. As menLioned hereinabove, the organic solv~nt may be further refined, if desired by, for example, a further fractional distillation range.
The actual processing cycle is dependent on ~he ~hoice of equipment and limi~ing factors such a~
the tendency of ~he dispersion to fo~m excessively i~ too-rapid processing is attempted and the desirability of producing a suitably solid, free-flowing residue. Typical cycle times are of the order of 40-90 minu~es.
At the comple~ion of the steam stripping ~ycle~
the solid residue is discharged, preferably by gravity, from ~he process vessel. It can be readily dewatered by, for exam~Le, ~iltration. In its dew~tered f~r~, although still containing an appreciable quantity of water, l:he granular residue packs do~ to a ~irm mass and, subj ec~ to ruling environmental protectiorl laws, is in a suitable form for disposal as solid fill.
I:E desired, it may be completely dried.
The process is broadly applicable to a wide range of material~ such as, for example, paint residues, adhesives and dispersions or solu~ions of polymers u~ed as in~ermediates in the preparation o~
pai~ts and adheRives. Care must be exercised, however, in using liquid wastes comprising ~aterials which have a significant reactivity with water~
A par~icularly useful fea~ure of our process is tha~ if the average particle diameter is held to the appropria~e dimensions, the residue can be re-cycled as a iller in products such as, for example, surface coating~, putties, caulking compounds, fillers and adhesives. For thls purpose the average particle diameter is preferably less than about 35 mm.
Dried residue, provided it is suitably chemicall~ inert, is also poten~ially useful as a filler in moulded plastic~ ware.
7~2~
The invention is illustrated by the following e~amples, in which all parts are expressed in weight.
E ~ ~PLE 1 Recovery of solvent from a liquid thermosetting acrylic enamel.
The enamel treated by the process comprised a hydroxylated acrylic polymer and a butylated melamine-formaldehyde resin. The material was inherently hea~-convertible when catalysed by an acid.
A sample of the liquid waste, catalysed by the addition thereto o l~/o by weight of 80% phosphoric acid, gave a residue insoluble in acetone when -~
subjected to our test for heat convertib~lity.
A mixture of:
water 900 parts -poly(vinyl alcohol)~ solution 300 "
80% phosphoric acid 3 "
was heated to boiling point in a still fitted wi~h reflsux condenser and water separator and 500 par~s of the liquid waste added to it over a period of 30 min~
Organic solvent~was separat d off from condensed distillate and the water fxa tion, which in the initial stage of the process, contained approximately 7% solvent in solution, was recycled to the batch.
Steam stripping was continued for a further 90 min.
at which time 95%~by wt.o the~solvent, as determined by analysis o~ the liquld waste charged to the process9 had been collected. Distillation ~as stopped at that point.
* A 7.5% solution by weight in water of an 85%
hydrolysed grade of poly(vinyl alcohol).
A satlsfactory product is"Poval"(Trade Mark) 224G.
,i :
" ' ' ~ ' "' . ~ ' The non-volatile residue consisted of hard, discrete particles with a maximum diameter of about 300 ~m. A slurry o~ these particles in the water remaining in the still flowed readily when discharged.
Recovery of solvent from a liquid thermosetting alkyd enamel.
The enamel treated by the process comprised a hydroxylated coconut oil-modified alkyd resin and a butylated melamine-ormaldehyde resin. The material was inherently heat-convertible when catalysed by an acid.
A sample of the liquid waste, catalysed by the addition thereto of 1% by weight of 80%
phosphoric acid, gave a residue insoluble in acetone when subjec~ed to our test for heat convertibility.
A steam jacketed reaction vessel fitted with a reflux condenser and water separator was charged with the following:
water ~ 32 parts poly(vinyl alcohol) solution 8 (as example 1) 80~/o phosphoric acid 0.13 parts liquid waste 30 The charge~was stirred mechanically and brought slowly to ~he boil, then held at reflux for 2.25 hr.
Solvent was stripped off continuously and water from the reflux condensate re-cycled to the batch. The yield of solvent against analysed content of the liquid waste was 95% by wt.
.
~ ~7102~
The residue in the reaction vessel was a free-flowing aqueous slurry of solid particulates with a maximum particle diameter o about 200 ~m. The flash point o the slurry was higher than 61C, compared with 26 or the original liquid residue.
The Biological Oxygen Demand of a sample of the slurry was 10 p.p.m. The residue thus presented significantly less of a disposal problem than the original liquid waste.
Use of bentonite as a suspending agent in the recovery o solvent from a liquid thermosetting acrylic enamel.
The process o~ example 1 was repeated, but with the fQllowing substitutions made to the reactants.
The water ~poly(vinyl alcohol) ~phosphoric acid mixture was replaced by a mixture of 1200 parts of water and 72 parts of Wyoming bentonite. ThP
phosphoric acid was omitted and its function as catalyst achieved by dissolving 50 parts of a styrene-maleic anhydride polymer (acid value 480 mg KOH per~gm and molecular weight 1600) in the 5~0 parts of liquid was~e. (A suitable polymer is S.M.A 1000 ex Arco Chemicals Co., U.5.A.~. The catalysed liquid waste passed our acetone tes~ for heat convertibility.
The yield of organic solvent was 90% by wt. of the content estimated by analysis of the original liquid waste. The disperse particles o rPsidue were of the order of 5-10 mm.diameter.
This invention relates to a process of recovering organic solvents from liquid waste products comprising such solvents in which polyme~ic materials are dispersed or dissolved.
The chemical processing industry accu~ulates each year large tonnages of liquid waste products which are basically solutions or dispersions of polymer in organic solvent. We use the word "solvent" herein in the context in which it is co~monly understood in the paint, adhesive and allied industries; that is, a relatively volatile organic liquid which has the property of dissolving other less volatile organic compounds, especially film-forming polymers and resins.
These liquid waste products are not nonmally useable in their existing form, but their disposal by dumping or încineration is ecologically unacceptable and is rapidly becoming an option denied by legislation. Destructive disposal methods are wasteful of chemical resources, the solven~ content in particular being a potentially valuable asset i~ it can be recovered economi2ally.
Conventional recovery processes, for exam~le, the recovery of volatiles by direct distillation, are only a partial answer to the problem. For example 9 ~he e~ficiency of release of volatiles from the non-volatile components may fall well short of theoretical and a typical end-product in the still is a tarry residue which has no intrinsic value, but the removal of which can be a difficult and expensi~e exercise.
We have now found that it is possible to treat many such wastes in a process which not only gives a good yield of organic solvent, but also leaves a 0 ~ ~
residue which is solid, relatively innocuous and readily discharged rom ~he processing vessel.
The particular liquid waste products useful in our process are "heat convertible" materials, by which we mean that when they are subjected ~o a temperature of 100C for 60 mins under the test conditions described hereinunder, they yield a solid residue which is insoluble at 25C in acetone.
The process involves forming a particulate dispersion in water of the liquid waste, stripping water and organic solvent from the dispersion by distillation and separating the organic solvent from the water in the distillate. The residue consists of a free-flowing slurry in water of solid, granular particles.
We therPfore provide, according to the present in~ention, a process of recovering organic solvent from a liquid heat-convertible waste product as herein defined by the steps of:
(a~ dispersing the liquid waste product in ~ .
particulate form in water in the presence of a suspending agent for the particles;
(b) heating the dispersion to boiling point to strip off ste~m and organic solvent va~ouri (c) condensing the evolved steam and organic solvent vapour and separating the water therefrom; and (d) recovering the residue as an aqueous free-flowing slurry of solid granular particles.
Optionally the water can be evaporated from the slurry to give a residue of dry, solid particles.
The organic solvent can also be further refined by conventional means, for example by fractional distillation, when it contains a mixture o solvents.
~ ,~
. ~
~ 17:~2 Our test for heat convertibility is performed in the following manner. The liquid waste product to be tested ls poured or spread on a horizontal test plate, e.g. a sheet of gl$ss or a flat steel panel, so that a film of up to 1-2 mm thick is formed thereon.
The test plate is then heated in air to 100C and held at that te~perature ~or 60 mins It is cooled to 25C and then moistened with droplets of acetone.
If the required degree of heat convertibility has been achieved, the residue on the test plate will not dissolve in the acetone. The effect of the acetone is sometimes more readily assessed by gently rubbing the moistened residue with a glass test probe. The appearance of a satisfactory test area will vary somewhat depending on the actual composition of the liquid waste. For example, a satisfactory material may not be entirely unaEfected by acetone. When moistf~ned and rubbed with the probe, it may lose adhesion to the substrate or even break up into irregular lumps or flakes. In extreme cases it may even show some wrinkling or swe-lling, but no dissolution. However, an unsatisfactory test sample will show definite evidence of d-Lssolution in the acetone, notably a streaking or smearing on the test probe or subs~rate and an obvious loss of film integrity.
We associate the property of heat convertibility as measured by our acetone solubility test with the ability of the disperse particles of liquid waste to form solid, discrete particles during the stPam stripping stage of our process. This gives rîse to a slurry of granular particles which is readily dischaxged ~rom the reaction vessel.
I 1 7~0 As we understand it, the heat convertibility is derivQd from cross-linking of polymeric components o~ the liquid waste. This characteristic may be inherent in the materials to be treated. For 5 example, paint residues are a form of liquid waste to which our process is particularly well suited.
One well-known class o~ paints, the "thermosetting"
compositions, have the property of curing from a liquid to a solid form by a cross-linking chemical reaction between polymer components thereo. The cross-linking reaction can be initiated and controlled by well-known means, for example by the application of heat, a catalyst or a so-called cross-linking agent.
Many mechanisms of this kind are known and are discussed in various authoritative texts such as, for example, "The Chemistry of Organic Film Formers"
Solomon, D.H., Krieger Publishing Co., New York U.S.A. When the liquid waste comprises such a the~mosetting composition and the reaction conditions required to cause cross-linking to take place are present during the steam stripping cycle of our process, a satisfactory granular residue is produced.
The cross-linking reaction may require some acceleration other than by heat alon~. For example, the above reference discloses other mechanisms, ~.g.
the additiDn to polymers of acid ca~alysts to achieve heat convertibility. The catalyst addit~o~ is made to the liquid waste before subjecting it to our above-described cross-linking test. However, in carrying out the actual process the catalyst is ~ot necessarily added to the liquid waste; it may alternati~ely be added to the dispersion of liquid waste in water, or to the water in which the disper~ion is to be made provided this is consistent with the nature of the required cross-linking reaction.
... .
~ 3 71022 Liquid wastes which cross-link in the presence of an acid catalyst include, for example, wastes comprising mixtures o hydroxylated acrylic polymers, e.g. copolymers of methyl metha~rylate and hydroxy-ethyl methacrylate, and butylated melamine-formaldehyde resins. The added catalyst might then be, for example, p-toluene sulphonic acid or phosphoric acid.
We have observed that a surprising number of liquid waste products, including some which are normally acid catalysed, will pass our acetone solubility test for heat convertibility when made alkaline by the addition of an inorganic base, for example sodium and potassium hydroxides, before they are tested. It appears that such mixtures, especially when usPd in conju~ction with an inorganic suspending agent, are particularly satisfaotory materials for use in our process. They typically provide free-flowing slurries which show little, if any, tendency to lea~e solid deposits on the walls of the process equipment.
Alternatively, a liquid waste which is not inherently able to take part in a cross-linkîng reaction may be adapted to the requirements of our process by blending it wi~h hea~-convertible constituents. For exam~e, thermoplastic lacquer comprislng polymethyl methacrylate produces a residue soluble in acetone when subjected to our above-described cross-linking test. However, the necessary heat-convertibility can be imparted to it by adding thereto sufficient carboxylated styrene-maleic anhydride co~oIymer, difunctional epoxy resin and tertiary amine catalyst.
A useful practical method of dealing with waste con~aining essentially thermoplastic polymer, is to blend that waste with a known heat convertible waste until a composition is reached which does satisy our cross-linking test. The proportions to be blended depend on the compositions o~ the wastes to be treated and are readily determined by experiment.
The dispersion of the liquid waste in particulate form in water can be made, for example, by pouring the waste into water which is kept agitated by a mechanical stirrer. The water may be at ambient room temperature or preferably it may be heated to boiling before the liquid waste is added to it.
Alterna~ively, if the water is heated by direct injection o steam, the agitation set up by the steam sparg~ may be sufficient to break the liquid waste up into discrete disperse particles.
The suspending agent, which may be present in either ~he water or in the liqui.d waste may be chosen ~rom the large number of such ag~nts known to stabilise liquid dispersions in water; our process will tolerate most types of agent in common use.
However, because the nature bf the waste acceptable to this process can vary widely in composition and the di~persion must remain stable during the steam stripping cycle, some degree of trial may be necessary to determine the most suitable suspending agent for use with a particular liquid waste.
We have found that inorganic materials such as Wyoming bentonite and activated clays of the Hectorite type can be satisfactory suspending agents. Other suitable materials are, for example, poly(vinyl alcohol), gelatine and amphipathic polymeric surface active agents, eg. triethanolamine oLeate, sorbitol monostearate, lauryl alcohol ethoxylate and nonyl ~, phenol ethoxylate.
The requir d coneentration of suspending agent also varies with bo~h the type o ~uspending age~t used and the nature of the liquid was~e being treated. r~i~h orga~ic suspending agents a typical concentration is 2-5% based on the weight of liquid waste, while or inorganic suspending agents t~e corresponding igure is ~ypically 5 10%.
The size of the disperse`particles is not particularly critical in so far as the recovery process is concerned. Factors which influence the disperse particle size distribution in such sy~tems are well known to the art and include, for example, the relative viscositle~ of each phase and the shear force~ generated in the dispersion equipment.
The nature and ~mount of solid material dissolved .or dispersed in the liquid waste will, in turn, affect the vi~cosity of the disperse phase. If, for example, the solid constituents are polymeric and very viscous, the disperse particles tend -~ to be coarser than wh~n m~re fluid materials are us d. Some agglomeration of primary particles ma~
take place, but this is usually a reversible ac~ion and ~he fi~al slur~y rernains free flowing.
In general, the iner the dispersion the more ~ree-2S flowing the residue left in the process vessel aterthe steam ~tripping stage.
Typical dispersions we have used successully in our process have differed quite mar~edly in average particle diameter, the extremities lying at 30 about a . l ~m and 5 mm.
Ihe dispersion may be raised to boiling point by e~ternally applied heat or, for example, by steam injected direc~ly into the proces~ vessel. The condensed mix~ure of stea~ and organic solvent ~apour is ~reated by normal phase separation techniques to recover the organlc ~oLvent, less some losses of water-soluble fractions which will partition into .
71~2 _ 9 _ the aqu~ous phase. As menLioned hereinabove, the organic solv~nt may be further refined, if desired by, for example, a further fractional distillation range.
The actual processing cycle is dependent on ~he ~hoice of equipment and limi~ing factors such a~
the tendency of ~he dispersion to fo~m excessively i~ too-rapid processing is attempted and the desirability of producing a suitably solid, free-flowing residue. Typical cycle times are of the order of 40-90 minu~es.
At the comple~ion of the steam stripping ~ycle~
the solid residue is discharged, preferably by gravity, from ~he process vessel. It can be readily dewatered by, for exam~Le, ~iltration. In its dew~tered f~r~, although still containing an appreciable quantity of water, l:he granular residue packs do~ to a ~irm mass and, subj ec~ to ruling environmental protectiorl laws, is in a suitable form for disposal as solid fill.
I:E desired, it may be completely dried.
The process is broadly applicable to a wide range of material~ such as, for example, paint residues, adhesives and dispersions or solu~ions of polymers u~ed as in~ermediates in the preparation o~
pai~ts and adheRives. Care must be exercised, however, in using liquid wastes comprising ~aterials which have a significant reactivity with water~
A par~icularly useful fea~ure of our process is tha~ if the average particle diameter is held to the appropria~e dimensions, the residue can be re-cycled as a iller in products such as, for example, surface coating~, putties, caulking compounds, fillers and adhesives. For thls purpose the average particle diameter is preferably less than about 35 mm.
Dried residue, provided it is suitably chemicall~ inert, is also poten~ially useful as a filler in moulded plastic~ ware.
7~2~
The invention is illustrated by the following e~amples, in which all parts are expressed in weight.
E ~ ~PLE 1 Recovery of solvent from a liquid thermosetting acrylic enamel.
The enamel treated by the process comprised a hydroxylated acrylic polymer and a butylated melamine-formaldehyde resin. The material was inherently hea~-convertible when catalysed by an acid.
A sample of the liquid waste, catalysed by the addition thereto o l~/o by weight of 80% phosphoric acid, gave a residue insoluble in acetone when -~
subjected to our test for heat convertib~lity.
A mixture of:
water 900 parts -poly(vinyl alcohol)~ solution 300 "
80% phosphoric acid 3 "
was heated to boiling point in a still fitted wi~h reflsux condenser and water separator and 500 par~s of the liquid waste added to it over a period of 30 min~
Organic solvent~was separat d off from condensed distillate and the water fxa tion, which in the initial stage of the process, contained approximately 7% solvent in solution, was recycled to the batch.
Steam stripping was continued for a further 90 min.
at which time 95%~by wt.o the~solvent, as determined by analysis o~ the liquld waste charged to the process9 had been collected. Distillation ~as stopped at that point.
* A 7.5% solution by weight in water of an 85%
hydrolysed grade of poly(vinyl alcohol).
A satlsfactory product is"Poval"(Trade Mark) 224G.
,i :
" ' ' ~ ' "' . ~ ' The non-volatile residue consisted of hard, discrete particles with a maximum diameter of about 300 ~m. A slurry o~ these particles in the water remaining in the still flowed readily when discharged.
Recovery of solvent from a liquid thermosetting alkyd enamel.
The enamel treated by the process comprised a hydroxylated coconut oil-modified alkyd resin and a butylated melamine-ormaldehyde resin. The material was inherently heat-convertible when catalysed by an acid.
A sample of the liquid waste, catalysed by the addition thereto of 1% by weight of 80%
phosphoric acid, gave a residue insoluble in acetone when subjec~ed to our test for heat convertibility.
A steam jacketed reaction vessel fitted with a reflux condenser and water separator was charged with the following:
water ~ 32 parts poly(vinyl alcohol) solution 8 (as example 1) 80~/o phosphoric acid 0.13 parts liquid waste 30 The charge~was stirred mechanically and brought slowly to ~he boil, then held at reflux for 2.25 hr.
Solvent was stripped off continuously and water from the reflux condensate re-cycled to the batch. The yield of solvent against analysed content of the liquid waste was 95% by wt.
.
~ ~7102~
The residue in the reaction vessel was a free-flowing aqueous slurry of solid particulates with a maximum particle diameter o about 200 ~m. The flash point o the slurry was higher than 61C, compared with 26 or the original liquid residue.
The Biological Oxygen Demand of a sample of the slurry was 10 p.p.m. The residue thus presented significantly less of a disposal problem than the original liquid waste.
Use of bentonite as a suspending agent in the recovery o solvent from a liquid thermosetting acrylic enamel.
The process o~ example 1 was repeated, but with the fQllowing substitutions made to the reactants.
The water ~poly(vinyl alcohol) ~phosphoric acid mixture was replaced by a mixture of 1200 parts of water and 72 parts of Wyoming bentonite. ThP
phosphoric acid was omitted and its function as catalyst achieved by dissolving 50 parts of a styrene-maleic anhydride polymer (acid value 480 mg KOH per~gm and molecular weight 1600) in the 5~0 parts of liquid was~e. (A suitable polymer is S.M.A 1000 ex Arco Chemicals Co., U.5.A.~. The catalysed liquid waste passed our acetone tes~ for heat convertibility.
The yield of organic solvent was 90% by wt. of the content estimated by analysis of the original liquid waste. The disperse particles o rPsidue were of the order of 5-10 mm.diameter.
2 ç~
EXA~LE 4 ___ Use of Hectorite as a suspending agent in the recovery of solvent from a liquid thermosetting acrylic enamel.
Example 3 was repeated, but replacing the Wyoming bentonite of that example with an equal weight of a swellable synthetic clay (Hectorite~
known by the ~rade name "Laponite".
The same weight of solvent was recovered and the disperse particles of residue had a mean diameter of approximately 200 ~m.
EXAMPLE _ The use of amphipathic organic suspending agents in the recovery of organic solvents from a liquid thermosetting acrylic enamel.
The enamel used in this e~ample was the same as that used in example 1 but catalysed by dispersing therein 1% of p-toluene sulphonie acid. The catalysed liquid enamel gave a residue insoluble in acetone when tested by our test for heat convert-ibility.
A charge o~ 1200 part~ of water was added to a still fltted with a reflux condenser and water separator, then heated to boiling point. A mixture of:
liquid thermosetting acryIic enamel (as e~ample 1) 500 parts p~toluene sulphonic acid 5 "
sorbitan monopalmitate/
polyoxy ethylene (20 units) 1.5 parts sorbitan monostearate 1.5 "
`` l ~7102~
was added t~ the boiling water and steam stripping as generally described in example 1 continued for 90 mins. A yield against analysis of 95% by weight was recorded. The discrete particles of residue were somewhat fibrous in nature with an average length of about S mm.
Recovery of solvent from a liquid thermoplastic acrylic lacquer.
The lacquer used in this example was essentially a pigmented solution in organic solvents of a poly(methyl methacrylate), which under the conditions of our test for heat convertibility gave a residue which was readily solvated by acetone.
To 600 parts of the liquid waste was added 14.4 parts of a styrene-maleic copolymer as used in example 3, (S.M.A 1000 ex Arco Corp., U.S.A.) 32.4 parts of a liquid epo~y resin("Epikote"828 ex Shell Chemicals) and 0.5 parts of a tertiary amine (''Armeen"DMCD ex Armor-Hess CorpO, U.S.A.), dissolved in 40 parts of a 30:10 (by weight) mixture of toluene and acetone.
A sample of the liquid waste so modified gave a residue insoluble in acetone when subjected to our test for heat convertibility The 600 parts of modified liquid waste was added over a period of 30 min. to the following mixture held at boiling point in a still fitted with reflux condenser and water separator.
water 900 parts poly(vinyl alcohol~ solution as example 1 300 "
sodium carbonate, anhydrous 6 Steam stripping and re-cycling of aqueous condensate was continued for a further 90 min.to give a yield of solvent, based on analysis of the liquid waste, of 95%.
The svlid residue was in the form of friable, gritty aggregates with an average diameter of about 5 ~m.
Recovery of organic solvent rom a mixed thermoplastic~thermosetting paint system.
A thermosetting acrylic lacquer as used in example 1 was added to a thermoplastic acrylic lacquer as used in example 6 until the blend, when catalysed by the addition of 1% by weight of 80%
phosphoric acid, gave a residue insoluble in acetone, when subjected to our test for heat convertibility.
By the general method of example 1, that blend as tested was steam stripped to yield about 90% by weight of the availabLe organic solvent.
The solid residue consisted of coarse, f~iable crumbs with average diameters o~ the order of 1-10 mm.
~XArrLL 8 Recovery of organic solvent from a thermosetting acrylic lacquer using steam injection.
The liquid waste used in this example comprised a copolymer of styrene and hydroxypropyl methacrylate and a butylated melamine-formaldehyde resin.
When catalysed by the addition there~o o~ 1% by weight of 80% phosphoric acid and subjected to our heat convertibility test, the liquid waste yielded a solid residue insoluble in acetone.
,...
~ 3 ~V22 A mixture of:
water 400 parts poly(vinyl alcohol) solution as example 1 180 "
~0% phosphoric acid 3 "
was loaded into a still ~itted with a reflux condenser and water separator. Steam was injected into the batch, which reached boiling point in 1 hr. The steam injection was continued and 540 parts of liquid waste added ~o the batch at a uniform rate over a period of 1 hr. Aqueous condensate was re-cycled continuously to the batch during the steam stripping, which conti.nued for a further 2~ hr. The recovery of organic solvent corresponded to 99% by weight of theoretical. The residue discharæed from the still was an aqueous slurry of friable aggregates of solid particles. The aggrPgates had diameters of up to 1 cm.
Reeovery of organic solvent from an air-drylng 0 enamel.
e waste liquid of this example was a solution in mineral spir~its of an air-dr~ing oil-modified alkyd resin pigmented with alumirlium powder. The poLymeric alkyd~resin dld not give a solid residue 2S insoluble in acetone, when subjected to our heat co~ertibility test. When subjected to the process as described in example 1, organic solvent was recoverable from the was~e liquid but a glutinous mass, dificult to remove from the still, formed before the theoretical yield of organic solvPnt was realised.
.
. :
, ~
~ 1 7~(~22 The waste liquid was then blended with increments of the thermosetting acrylic enamel used in example 1 (catalysed with the corresponding amount of 80%
phosphoric acid) until under the conditions of our test a solid, acetone-insoluble residue was obtained.
The acceptable blend contained approximately equal par~s by weight of the two liquids.
This blend7 when subjected to the process described in example l, yielded about 90~/O of the theoretical content of organic solvent and a slurry of crum~ly, but somewhat soft, disperse particles, loosely aggregated into secondary particles of mean diameter up to 1-2 cm. The slurry discharged readily fro~ the still.
_ E~AMPLE 10 Recovery of organic solvent from a mixed thermoplastic/thermosetting pain~ system.
A thermosetting acrylic Lacquer (comprising a hydroxylated aerylic pol~mer and a butylated melamine-formaldehyde resin) and a thermoplastic acrylic lacquer (a pigmented solution of poly(methyl methacryl-ate? ) were mixed in the weight ratio of 1:1. After addition of 1% by weight of sodium hydroxide (in the form of a ~oLution in ethanol, this mixture gave a residue which w~s essentially insoluble in acetone when subjected to our test for heat convertibility.
A mixture of ~ia er 1200 parts sodium bentonite 15 "
sodium hydroxlde 6 l ~71G22 was heated to boiling in a still fitted with stirrer, reflux condenser and water separator and 600 parts of the 1:1 liquid waste mixture previously described was added thereto over a period of 30 minutes.
Organic solvent was separated off from the condensed distillate and the water fraction, which in the initial stage of the process eontained approximately 7% solvent in solution, was recycled to the batch.
Steam stripping was continued for a further 3 hours at which time 98% by weight of the solvent present in the waste as determined by analysis had been collected. Distillation was stopped at that point.
The non-volatile residue ronsisted of hard discrete particles with a maximum diameter of 6 mm.
A slurry of these particles in the water remaining in the still flowed readily when discharged.
EXAMæLE 11 Use of verniculite as a suspending agen~ in the recovery of solvent from a mixed thexmoplastic/
thermosetting paint system.
Example 10 was repeated but replacing the sodium bentonite of that example with an equal weight o~
vermiculite, the particle size of which was such that 10% was retainPd on a 52 mesh BSS sieve and 70%
maximum on a 100 mesh BSS sieve.
The same weight of solvent was recovered and the solid particles had a mean diameter of approximately 5 mm.
. . .
EXA~LE 4 ___ Use of Hectorite as a suspending agent in the recovery of solvent from a liquid thermosetting acrylic enamel.
Example 3 was repeated, but replacing the Wyoming bentonite of that example with an equal weight of a swellable synthetic clay (Hectorite~
known by the ~rade name "Laponite".
The same weight of solvent was recovered and the disperse particles of residue had a mean diameter of approximately 200 ~m.
EXAMPLE _ The use of amphipathic organic suspending agents in the recovery of organic solvents from a liquid thermosetting acrylic enamel.
The enamel used in this e~ample was the same as that used in example 1 but catalysed by dispersing therein 1% of p-toluene sulphonie acid. The catalysed liquid enamel gave a residue insoluble in acetone when tested by our test for heat convert-ibility.
A charge o~ 1200 part~ of water was added to a still fltted with a reflux condenser and water separator, then heated to boiling point. A mixture of:
liquid thermosetting acryIic enamel (as e~ample 1) 500 parts p~toluene sulphonic acid 5 "
sorbitan monopalmitate/
polyoxy ethylene (20 units) 1.5 parts sorbitan monostearate 1.5 "
`` l ~7102~
was added t~ the boiling water and steam stripping as generally described in example 1 continued for 90 mins. A yield against analysis of 95% by weight was recorded. The discrete particles of residue were somewhat fibrous in nature with an average length of about S mm.
Recovery of solvent from a liquid thermoplastic acrylic lacquer.
The lacquer used in this example was essentially a pigmented solution in organic solvents of a poly(methyl methacrylate), which under the conditions of our test for heat convertibility gave a residue which was readily solvated by acetone.
To 600 parts of the liquid waste was added 14.4 parts of a styrene-maleic copolymer as used in example 3, (S.M.A 1000 ex Arco Corp., U.S.A.) 32.4 parts of a liquid epo~y resin("Epikote"828 ex Shell Chemicals) and 0.5 parts of a tertiary amine (''Armeen"DMCD ex Armor-Hess CorpO, U.S.A.), dissolved in 40 parts of a 30:10 (by weight) mixture of toluene and acetone.
A sample of the liquid waste so modified gave a residue insoluble in acetone when subjected to our test for heat convertibility The 600 parts of modified liquid waste was added over a period of 30 min. to the following mixture held at boiling point in a still fitted with reflux condenser and water separator.
water 900 parts poly(vinyl alcohol~ solution as example 1 300 "
sodium carbonate, anhydrous 6 Steam stripping and re-cycling of aqueous condensate was continued for a further 90 min.to give a yield of solvent, based on analysis of the liquid waste, of 95%.
The svlid residue was in the form of friable, gritty aggregates with an average diameter of about 5 ~m.
Recovery of organic solvent rom a mixed thermoplastic~thermosetting paint system.
A thermosetting acrylic lacquer as used in example 1 was added to a thermoplastic acrylic lacquer as used in example 6 until the blend, when catalysed by the addition of 1% by weight of 80%
phosphoric acid, gave a residue insoluble in acetone, when subjected to our test for heat convertibility.
By the general method of example 1, that blend as tested was steam stripped to yield about 90% by weight of the availabLe organic solvent.
The solid residue consisted of coarse, f~iable crumbs with average diameters o~ the order of 1-10 mm.
~XArrLL 8 Recovery of organic solvent from a thermosetting acrylic lacquer using steam injection.
The liquid waste used in this example comprised a copolymer of styrene and hydroxypropyl methacrylate and a butylated melamine-formaldehyde resin.
When catalysed by the addition there~o o~ 1% by weight of 80% phosphoric acid and subjected to our heat convertibility test, the liquid waste yielded a solid residue insoluble in acetone.
,...
~ 3 ~V22 A mixture of:
water 400 parts poly(vinyl alcohol) solution as example 1 180 "
~0% phosphoric acid 3 "
was loaded into a still ~itted with a reflux condenser and water separator. Steam was injected into the batch, which reached boiling point in 1 hr. The steam injection was continued and 540 parts of liquid waste added ~o the batch at a uniform rate over a period of 1 hr. Aqueous condensate was re-cycled continuously to the batch during the steam stripping, which conti.nued for a further 2~ hr. The recovery of organic solvent corresponded to 99% by weight of theoretical. The residue discharæed from the still was an aqueous slurry of friable aggregates of solid particles. The aggrPgates had diameters of up to 1 cm.
Reeovery of organic solvent from an air-drylng 0 enamel.
e waste liquid of this example was a solution in mineral spir~its of an air-dr~ing oil-modified alkyd resin pigmented with alumirlium powder. The poLymeric alkyd~resin dld not give a solid residue 2S insoluble in acetone, when subjected to our heat co~ertibility test. When subjected to the process as described in example 1, organic solvent was recoverable from the was~e liquid but a glutinous mass, dificult to remove from the still, formed before the theoretical yield of organic solvPnt was realised.
.
. :
, ~
~ 1 7~(~22 The waste liquid was then blended with increments of the thermosetting acrylic enamel used in example 1 (catalysed with the corresponding amount of 80%
phosphoric acid) until under the conditions of our test a solid, acetone-insoluble residue was obtained.
The acceptable blend contained approximately equal par~s by weight of the two liquids.
This blend7 when subjected to the process described in example l, yielded about 90~/O of the theoretical content of organic solvent and a slurry of crum~ly, but somewhat soft, disperse particles, loosely aggregated into secondary particles of mean diameter up to 1-2 cm. The slurry discharged readily fro~ the still.
_ E~AMPLE 10 Recovery of organic solvent from a mixed thermoplastic/thermosetting pain~ system.
A thermosetting acrylic Lacquer (comprising a hydroxylated aerylic pol~mer and a butylated melamine-formaldehyde resin) and a thermoplastic acrylic lacquer (a pigmented solution of poly(methyl methacryl-ate? ) were mixed in the weight ratio of 1:1. After addition of 1% by weight of sodium hydroxide (in the form of a ~oLution in ethanol, this mixture gave a residue which w~s essentially insoluble in acetone when subjected to our test for heat convertibility.
A mixture of ~ia er 1200 parts sodium bentonite 15 "
sodium hydroxlde 6 l ~71G22 was heated to boiling in a still fitted with stirrer, reflux condenser and water separator and 600 parts of the 1:1 liquid waste mixture previously described was added thereto over a period of 30 minutes.
Organic solvent was separated off from the condensed distillate and the water fraction, which in the initial stage of the process eontained approximately 7% solvent in solution, was recycled to the batch.
Steam stripping was continued for a further 3 hours at which time 98% by weight of the solvent present in the waste as determined by analysis had been collected. Distillation was stopped at that point.
The non-volatile residue ronsisted of hard discrete particles with a maximum diameter of 6 mm.
A slurry of these particles in the water remaining in the still flowed readily when discharged.
EXAMæLE 11 Use of verniculite as a suspending agen~ in the recovery of solvent from a mixed thexmoplastic/
thermosetting paint system.
Example 10 was repeated but replacing the sodium bentonite of that example with an equal weight o~
vermiculite, the particle size of which was such that 10% was retainPd on a 52 mesh BSS sieve and 70%
maximum on a 100 mesh BSS sieve.
The same weight of solvent was recovered and the solid particles had a mean diameter of approximately 5 mm.
. . .
Claims (3)
1. A process of recovering organic solvent from a liquid waste product comprising a dispersion or solution in that solvent of polymeric material, which is heat convertible in that a film of the liquid waste not more than 2 mm thick when heated in air at 100°C for 60 mins yields a residue insoluble in acetone, the process consisting of the steps of:
(a) dispersing the liquid waste product in particulate form in water in the presence of an inorganic suspending agent forte particles;
(b) heating the dispersion to boiling point to strip off steam and organic solvent vapour;
(c) condensing the evolved steam and organic solvent vapour and separating the water therefrom; and (d) recovering the residue as an aqueous free-flowing slurry of solid granular particles.
(a) dispersing the liquid waste product in particulate form in water in the presence of an inorganic suspending agent forte particles;
(b) heating the dispersion to boiling point to strip off steam and organic solvent vapour;
(c) condensing the evolved steam and organic solvent vapour and separating the water therefrom; and (d) recovering the residue as an aqueous free-flowing slurry of solid granular particles.
2. A process according to claim 1 in which the liquid waste product is made alkaline with an inorganic base selected from sodium and potassium hydroxides.
3. A process according to claim 1 in which the slurry is dried to yield a dry, granular residue.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000358395A CA1171022A (en) | 1980-08-15 | 1980-08-15 | Solvent recovery process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000358395A CA1171022A (en) | 1980-08-15 | 1980-08-15 | Solvent recovery process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1171022A true CA1171022A (en) | 1984-07-17 |
Family
ID=4117662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000358395A Expired CA1171022A (en) | 1980-08-15 | 1980-08-15 | Solvent recovery process |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1171022A (en) |
-
1980
- 1980-08-15 CA CA000358395A patent/CA1171022A/en not_active Expired
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