WO2007108023A1 - Method for purifying a contaminated solvent and concurrently producing a semi-finished product for use in the production of panels - Google Patents
Method for purifying a contaminated solvent and concurrently producing a semi-finished product for use in the production of panels Download PDFInfo
- Publication number
- WO2007108023A1 WO2007108023A1 PCT/IT2006/000176 IT2006000176W WO2007108023A1 WO 2007108023 A1 WO2007108023 A1 WO 2007108023A1 IT 2006000176 W IT2006000176 W IT 2006000176W WO 2007108023 A1 WO2007108023 A1 WO 2007108023A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- plastic material
- mass
- semi
- panels
- production
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C70/00—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts
- B29C70/04—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts comprising reinforcements only, e.g. self-reinforcing plastics
- B29C70/28—Shaping operations therefor
- B29C70/54—Component parts, details or accessories; Auxiliary operations, e.g. feeding or storage of prepregs or SMC after impregnation or during ageing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/003—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor characterised by the choice of material
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/04—Reinforcing macromolecular compounds with loose or coherent fibrous material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/30—Vehicles, e.g. ships or aircraft, or body parts thereof
- B29L2031/3005—Body finishings
- B29L2031/3041—Trim panels
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/44—Furniture or parts thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/751—Mattresses, cushions
Definitions
- the present invention refers to a method for purifying a contaminated solvent and concurrently production a semi-finished product for use in the production of panels.
- the panels of the last-mentioned kind are produced starting from wood fragments, generally known as chips in the art, which are first of all caused to undergo grinding processes and then added with sawdust, glue and additives such as urea resins. After drying, the material is placed into proper moulds so as to obtain a kind of mattress that is then pressed, squared, cut into plates and submitted to smoothing.
- a need that is markedly and concretely felt within the woodworking industry in general is therefore the ability of developing production processes that do not only allow alternative materials to be produced for use instead of wood-based raw materials of known kind, but also enable processing solvents to be recovered along with the residues contained therein, as well as waste and scraps of fibres that have already gone through various production processes.
- the need is felt for the binding power, which - as noted hereinbefore - is still to be found in the residues of resins and glues suspended in the solvents to be purified, to be recovered in order to advantageously make use of this resource in the production of a semi-finished product for use in manufacturing panels that normally involve or require the use of such substances.
- These alternative materials to wood-based raw materials must of course have mechanical properties similar, if not even superior to the ones typically ensured by currently used wood-based raw materials of known kind.
- Yet another purpose of the present invention is to provide a method for purifying a contaminated solvent and concurrently producing a semi- finished product for use in the production of panels, which allows for used and potentially polluting materials to be effectively and safely recycled, thereby considerably reducing energy usage and requirements as compared to traditional prior- art processes.
- the inventive method for purifying a contaminated solvent and concurrently producing a semi-finished product for use in the production of panels calls for a first mass of fibrous material to be used.
- This material may be comprised of a single type of fibres, such as for instance lignocellulose fibres, or a mix of fibres of different nature.
- a fibre mix suitable for use in the inventive method is comprised of various synthetic textile and vegetable fibres.
- the fibrous material includes fibres derived from processing waste and scraps, recovered materials or residues from production processes, such as for instance paper-mill sludge, in which fibres are generally too short to be suitable for re-use in the production of paper.
- the mass of fibrous material may furthermore be provided in the form of layers of agglomerated fibres.
- the fibrous materials has a high water content, such as in the case of paper-mill sludge, appropriate drying operations, in which said sludge is for instance pressed and dehydrated, may be duly provided. Pressing enables the aqueous component in the sludge to be reduced down to anywhere between 30 and 40 wt%, while the subsequent dehydration operation enables said aqueous content to be further brought down to approx. 5 wt%. At such water content, sludge and slurries are generally defined as "dry".
- the resulting dry sludge is in the form of small cylindrical blocks that, at the moment of their use, must be first ground, or fiberized, using corresponding machines provided with adjacent rotating disks, the relative position of which can be properly adjusted to modify both the length and the diameter of the fibres accordingly.
- a second mass of plastic material comprising one or several types or grades of thermoplastic polymers, such as for instance ABS (Acrylonitrile- Butadiene-Styrene), polystyrene, and the like, is impregnated with a contaminated solvent that is due to be purified.
- thermoplastic polymers such as for instance ABS (Acrylonitrile- Butadiene-Styrene), polystyrene, and the like
- thermosetting polymers such as phenol-formaldehyde resins, epoxy resins and polyurethanes.
- the contaminated solvent is recovered as a by-product or waste from such processes as the ones used to clean painting installations, tools and equipment.
- the contaminated solvent may therefore be comprised of a mixture of chemical substances of a different nature, such as for instance ketone- based solvents, benzines, or the like, and will generally contain a suspension of solid residues, such as for instance resins and/ or glues of various nature.
- a solvent suitably selected among the recovered ones, or by providing or arranging a suitable composition of the mass of plastic material it will therefore be possible for the latter to be caused to at least partially dissolve, so that the plastic material impregnated with contaminated solvent is induced to properly soften as a whole. The extent to which this materials will actually soften depends on.
- the plastic material upon having been so softened, the plastic material will have the consistency of a malleable paste.
- part of the mass of plastic material that cannot be treated with the solvent may therefore be micronized so as to enable it to be more readily mixed with the portion of said mass of plastic material that it was the contrary possible to submit to the softening treatment.
- the fibrous material is available in a powder or similar form, mixing it with the mass of softened plastic material originates a compound that is adapted to be evenly spread over a plane so as to form a mat, or mattress, of a homogeneous consistence.
- This mattress formed with such compound i.e. the mat of aggregated fibres mixed with plastic material, is then hot-pressed in a press, wherein the pressing temperature is greater than or equal to the temperature needed to cause the plastic material to melt. In particular, this temperature is of at least 180 0 C.
- Hot-pressing this mat of mixed materials i.e. the layer of aggregated fibres impregnated with plastic material
- This semi-finished product comes out in the form of a thick sheet or mat made up by a fibre aggregate.
- Hot-pressing will also cause the volatile components of the contaminated solvent that has impregnated the fibrous material to evaporate. Solid residues contained in the solvent remain on the contrary trapped in the fibres of the semi-finished product, thereby favouring the aggregation thereof by boosting the binding effect produced by melting the plastic materials.
- the fraction of evaporated solvent is duly collected and condensed in a distillation apparatus so as to purify the solvent.
- the semi-finished product obtained with the above-described method is in a form that is most suitable in view of its utilization as cladding or lining panels to sound deadening or heat insulation purposes. In this case, no need arises for the semi-finished product itself to be submitted to any further processing, apart from a simple cutting-to-size operation required to give it dimensions suiting the particular application.
- the semi-finished product can however be sent to further processing in view of producing panels of various kinds for application in a plurality of manufacturing and industrial sectors in general, such as the furniture- making industry, the building industry and everywhere there are surfaces to be lined, clad or covered.
- the semi-finished mat is transferred onto an impregnation station, where it is permeated by a binding agent in liquid form.
- a suitable substance in this connection is sodium silicate in the form that is generally known as water-glass in the art.
- other water-soluble glues or binders can be used, as well.
- the binding agent is forced through the interstices of the mat by submitting the latter to a pressure gradient between the upper surface and the lower surface thereof.
- the impregnation of the mat with water-glass imparts fire-resistant and self-extinguishing properties to the treated product.
- the semi-finished product so impregnated with binding agent is then sent into a drying tunnel, or kiln, or onto a hot-pressing press to dry off the aqueous component of the binder and obtain a finished construction- grade panel.
- a drying tunnel or kiln
- a hot-pressing press to dry off the aqueous component of the binder and obtain a finished construction- grade panel.
- the carbon dioxide used to favour hardening of sodium silicate can be taken from ambient air, thereby contributing to a reduction in the presence of this compound in the atmosphere under a clear improvement in the quality thereof.
- Such chemical reaction can also take place at ambient temperature (conventionally set at 20 0 C), so that, should any amount of sodium silicate that failed to take part in the chemical reaction be still present in the semi-finished mat after the latter has been dried, this amount will take part in such reaction even after the finished panel has eventually been formed.
- processing scraps that may result when the panel is cut-to-size and/ or further processed can be used as a material adapted to reduce the presence of carbon dioxide in ambient air.
- An amount situated anywhere between 550 and 650 kg of fibrous material such as for instance paper-mill sludge in a dry state or with a moisture content lower than or equal to 5wt% of the mass, is mixed with at least 120 kg of plastic material that has been preliminarily impregnated and softened with the use of an amount of contaminated solvent ranging from 200 to 500 kg.
- the resulting compound in powder form is evenly poured and spread over a plane so as to form a kind of mattress.
- This mattress is then pressed at a temperature of at least 18O 0 C, thereby forming a semi-finished mat having a density of approx. 700 kg/m 3 . Pressing the mattress in this way causes the solvent contained in the plastic material to evaporate.
- an amount of purified solvent can be produced, which corresponds to approximately 60% of the total amount of contaminated solvent used in the process.
- the purified solvent does not contain any suspended solid residues, which are in fact retained within the semi-finished mat.
- the semi-finished mat is impregnated with a binding agent, as this may for instance consist of an aqueous solution of sodium silicate (water-glass) having a solid content of up to 30 to 35%.
- a binding agent as this may for instance consist of an aqueous solution of sodium silicate (water-glass) having a solid content of up to 30 to 35%.
- the amount of binder used in the application depends on the mechanical and workability properties that the finished panel should desirably have.
- the impregnated semi-finished mat is then submitted to a drying process in view of drying off the aqueous portion of the binding agent. This drying operation can be carried out in a drying tunnel, or kiln, or in a hot press.
- a panel produced in this way, and having a thickness of 20 millimeters, has following least characteristics: ⁇ Screw extraction resistance (EN 320/93):
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Health & Medical Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Composite Materials (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Reinforced Plastic Materials (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP06745242A EP1996646A1 (en) | 2006-03-21 | 2006-03-21 | Method for purifying a contaminated solvent and concurrently producing a semi-finished product for use in the production of panels |
PCT/IT2006/000176 WO2007108023A1 (en) | 2006-03-21 | 2006-03-21 | Method for purifying a contaminated solvent and concurrently producing a semi-finished product for use in the production of panels |
US12/225,153 US20090111939A1 (en) | 2006-03-21 | 2006-03-21 | Method for Purifying a Contaminated Solvent and Concurrently Producing a Semi-Finished Product for Use in the Production of Panels |
BRPI0621435-5A BRPI0621435A2 (en) | 2006-03-21 | 2006-03-21 | method for purifying a contaminated solvent and concomitantly producing a semifinished product for use in the production of panels, and unfinished panel for furniture parts |
CA002641470A CA2641470A1 (en) | 2006-03-21 | 2006-03-21 | Method for purifying a contaminated solvent and concurrently producing a semi-finished product for use in the production of panels |
CNA2006800538889A CN101432344A (en) | 2006-03-21 | 2006-03-21 | Method for purifying polluted solvent and simultaneously producing semi-finished product used in panel production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/IT2006/000176 WO2007108023A1 (en) | 2006-03-21 | 2006-03-21 | Method for purifying a contaminated solvent and concurrently producing a semi-finished product for use in the production of panels |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007108023A1 true WO2007108023A1 (en) | 2007-09-27 |
Family
ID=37059625
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/IT2006/000176 WO2007108023A1 (en) | 2006-03-21 | 2006-03-21 | Method for purifying a contaminated solvent and concurrently producing a semi-finished product for use in the production of panels |
Country Status (6)
Country | Link |
---|---|
US (1) | US20090111939A1 (en) |
EP (1) | EP1996646A1 (en) |
CN (1) | CN101432344A (en) |
BR (1) | BRPI0621435A2 (en) |
CA (1) | CA2641470A1 (en) |
WO (1) | WO2007108023A1 (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2439929A (en) * | 1942-06-17 | 1948-04-20 | Westinghouse Electric Corp | Electrical insulation |
US2605205A (en) * | 1946-10-25 | 1952-07-29 | American Cyanamid Co | Protective overlay sheets and process of preparing same |
US4022942A (en) * | 1972-02-17 | 1977-05-10 | Monsanto Company | Process of preparing fibrous sheet from high-ortho phenolic resole resin varnish |
FR2672537A1 (en) * | 1991-02-08 | 1992-08-14 | Cray Valley Sa | Method of manufacturing moulded components from materials preimpregnated with thermosetting resin |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5445659A (en) * | 1993-10-04 | 1995-08-29 | Texaco Inc. | Partial oxidation of products of liquefaction of plastic materials |
US5670574A (en) * | 1995-01-25 | 1997-09-23 | Hill; Joe C. | Salt-resin plastic products and process |
KR20030061675A (en) * | 2002-01-11 | 2003-07-22 | 뉴 아이스 리미티드 | Biodegradable or compostable containers |
US20090209667A1 (en) * | 2008-02-15 | 2009-08-20 | Helen Mackin Thompson | Recycled Poly(vinyl butyral) |
-
2006
- 2006-03-21 EP EP06745242A patent/EP1996646A1/en not_active Withdrawn
- 2006-03-21 CN CNA2006800538889A patent/CN101432344A/en active Pending
- 2006-03-21 US US12/225,153 patent/US20090111939A1/en not_active Abandoned
- 2006-03-21 WO PCT/IT2006/000176 patent/WO2007108023A1/en active Application Filing
- 2006-03-21 BR BRPI0621435-5A patent/BRPI0621435A2/en not_active IP Right Cessation
- 2006-03-21 CA CA002641470A patent/CA2641470A1/en not_active Abandoned
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2439929A (en) * | 1942-06-17 | 1948-04-20 | Westinghouse Electric Corp | Electrical insulation |
US2605205A (en) * | 1946-10-25 | 1952-07-29 | American Cyanamid Co | Protective overlay sheets and process of preparing same |
US4022942A (en) * | 1972-02-17 | 1977-05-10 | Monsanto Company | Process of preparing fibrous sheet from high-ortho phenolic resole resin varnish |
FR2672537A1 (en) * | 1991-02-08 | 1992-08-14 | Cray Valley Sa | Method of manufacturing moulded components from materials preimpregnated with thermosetting resin |
Also Published As
Publication number | Publication date |
---|---|
BRPI0621435A2 (en) | 2011-12-13 |
CN101432344A (en) | 2009-05-13 |
EP1996646A1 (en) | 2008-12-03 |
CA2641470A1 (en) | 2007-09-27 |
US20090111939A1 (en) | 2009-04-30 |
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